Chemical Properties of Ethanol (CAS 64-17-5)

InChI

InChI=1S/C2H6O/c1-2-3/h3H,2H2,1H3

InChI Key

LFQSCWFLJHTTHZ-UHFFFAOYSA-N

Formula

C2H6O

SMILES

CCO

Molecular Weight¹

46.07

CAS

64-17-5

Other Names

• Absolute alcohol
• Absolute ethanol
• Aethanol
• Aethylalkohol
• Alcare Hand Degermer
• Alcohol
• Alcohol anhydrous
• Alcohol, dehydrated
• Alcool ethylique
• Alcool etilico
• Algrain
• Alkohol
• Alkoholu etylowego
• Anhydrol
• C2H5OH
• Cologne spirit
• Cologne spirits
• Denatured alcohol
• Denatured alcohol CD-10
• Denatured alcohol CD-5
• Denatured alcohol CD-5a
• Denatured alcohol SD-1
• Denatured alcohol SD-13a
• Denatured alcohol SD-17
• Denatured alcohol SD-23a
• Denatured alcohol SD-28
• Denatured alcohol SD-30
• Denatured alcohol SD-39b
• Denatured alcohol SD-39c
• Denatured alcohol SD-3a
• Denatured alcohol SD-40m
• Denatured ethanol
• EtOH
• Etanolo
• Ethanol 200 proof
• Ethanol, silent spirit
• Ethyl alc
• Ethyl alcohol
• Ethyl alcohol anhydrous
• Ethyl hydrate
• Ethyl hydroxide
• Ethylol
• Etylowy alkohol
• Fermentation alcohol
• Grain alcohol
• Jaysol
• Jaysol S
• Methylcarbinol
• Molasses alcohol
• NCI-C03134
• Potato alcohol
• Punctilious ethyl alcohol
• SD 3A
• SD Alchol 23-hydrogen
• SD alcohol 23-hydrogen
• Spirits of wine
• Spirt
• Tecsol
• Tecsol C
• UN 1170

• ω : Acentric Factor.
• PAff : Proton affinity (kJ/mol).
• T_ig : Autoignition Temperature (K).
• BasG : Gas basicity (kJ/mol).
• Δ_cH°_gas : Standard gas enthalpy of combustion (kJ/mol).
• Δ_cH°_liquid : Standard liquid enthalpy of combustion (kJ/mol).
• C_p,gas : Ideal gas heat capacity (J/mol×K).
• C_p,liquid : Liquid phase heat capacity (J/mol×K).
• μ : Dipole Moment (debye).
• η : Dynamic viscosity (Pa×s).
• σ_cond : Electrical conductivity (S/m).
• LFL : Lower Flammability Limit (% in Air).
• UFL : Upper Flammability Limit (% in Air).
• T_flash,cc : Flash Point (Closed Cup Method) (K).
• T_flash,oc : Flash Point (Open Cup Method) (K).
• Δ_fG° : Standard Gibbs free energy of formation (kJ/mol).
• R_g : Radius of Gyration.
• Δ_fH°_gas : Enthalpy of formation at standard conditions (kJ/mol).
• Δ_fH°_liquid : Liquid phase enthalpy of formation at standard conditions (kJ/mol).
• Δ_fusH° : Enthalpy of fusion at standard conditions (kJ/mol).
• Δ_fusH : Enthalpy of fusion at a given temperature (kJ/mol).
• Δ_vapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
• Δ_vapH : Enthalpy of vaporization at a given temperature (kJ/mol).
• IE : Ionization energy (eV).
• ν : Kinematic viscosity (m²/s).
• log₁₀WS : Log10 of Water solubility in mol/l.
• logP_oct/wat : Octanol/Water partition coefficient.
• McVol : McGowan's characteristic volume (ml/mol).
• NFPA Fire : NFPA Fire Rating.
• P_c : Critical Pressure (kPa).
• P_vap : Vapor pressure (kPa).
• n₀ : Refractive Index.
• ρ_l : Liquid Density (kg/m³).
• I_np : Non-polar retention indices.
• I : Polar retention indices.
• Δ_fusS : Entropy of fusion at a given temperature (J/mol×K).
• S°_liquid : Liquid phase molar entropy at standard conditions (J/mol×K).
• c_sound,fluid : Speed of sound in fluid (m/s).
• γ : Surface Tension (N/m).
• T_boil : Normal Boiling Point Temperature (K).
• T_boil : Boiling point at given pressure (K).
• T_c : Critical Temperature (K).
• λ : Liquid thermal conductivity (W/m×K).
• T_fus : Normal melting (fusion) point (K).
• V_c : Critical Volume (m³/kmol).
• V_m : Molar Volume (m³/mol).
• Z_c : Critical Compressibility.
• Z_ra : Rackett Parameter.
• ¹: Molecular weight from the IUPAC atomic weights tables.

Contents

1. Physical Properties
2. Temperature Dependent Properties
3. Pressure Dependent Properties
4. Datasets
5. Correlations
6. Similar Compounds
7. Mixtures
8. Sources

Physical Properties

Property	Value	Unit	Source
ω	0.6440		KDB
PAff	[776.40; 779.40]	kJ/mol
PAff	776.40	kJ/mol	NIST
PAff	779.40 ± 0.80	kJ/mol	NIST
Tig	638.15	K	KDB
BasG	746.00	kJ/mol	NIST
ΔcH°gas	-1366.30 ± 0.40	kJ/mol	NIST
ΔcH°liquid	[-1370.90; -1367.00]	kJ/mol
ΔcH°liquid	-1367.60 ± 0.30	kJ/mol	NIST
ΔcH°liquid	-1367.00 ± 0.42	kJ/mol	NIST
ΔcH°liquid	-1370.90	kJ/mol	NIST
ΔcH°liquid	-1368.34	kJ/mol	NIST
ΔcH°liquid	-1368.60	kJ/mol	NIST
μ	1.70	debye	KDB
η	[0.0010930; 0.0011120]	Pa×s
η	0.0010930	Pa×s	Speeds ...
η	0.0011050	Pa×s	Dynamic...
η	0.0011120	Pa×s	Densiti...
LFL	3.30	% in Air	KDB
UFL	19.00	% in Air	KDB
Tflash,cc	290.93	K	KDB
Tflash,oc	285.93	K	KDB
ΔfG°	-168.40	kJ/mol	KDB
Rg	2.2500		KDB
ΔfH°gas	-235.00	kJ/mol	KDB
ΔfH°liquid	[-277.60; -274.70]	kJ/mol
ΔfH°liquid	-277.00 ± 0.30	kJ/mol	NIST
ΔfH°liquid	-277.60 ± 0.42	kJ/mol	NIST
ΔfH°liquid	-277.60	kJ/mol	NIST
ΔfH°liquid	-274.70	kJ/mol	NIST
ΔfH°liquid	-276.20 ± 5.00	kJ/mol	NIST
ΔfH°liquid	-275.90 ± 5.00	kJ/mol	NIST
ΔfusH°	5.02	kJ/mol	Joback Calculated Property
ΔvapH°	36.73	kJ/mol	Joback Calculated Property
IE	[10.04; 10.70]	eV
IE	10.48 ± 0.07	eV	NIST
IE	10.41 ± 0.05	eV	NIST
IE	10.40	eV	NIST
IE	10.47 ± 0.07	eV	NIST
IE	10.30	eV	NIST
IE	10.50	eV	NIST
IE	10.70	eV	NIST
IE	10.49 ± 0.01	eV	NIST
IE	10.46 ± 0.02	eV	NIST
IE	10.65	eV	NIST
IE	10.46	eV	NIST
IE	10.47 ± 0.02	eV	NIST
IE	10.48 ± 0.05	eV	NIST
IE	10.64	eV	NIST
IE	10.64	eV	NIST
IE	10.65	eV	NIST
IE	10.61	eV	NIST
IE	10.65 ± 0.03	eV	NIST
IE	10.59	eV	NIST
IE	Outlier 10.04	eV	NIST
IE	10.62	eV	NIST
IE	10.64	eV	NIST
log10WS	[1.10; 1.10]
log10WS	1.10		Aq. Sol...
log10WS	1.10		Estimat...
logPoct/wat	-0.001		Crippen Calculated Property
McVol	44.910	ml/mol	McGowan Calculated Property
NFPA Fire	3		KDB
Pc	[6129.00; 12060.00]	kPa
Pc	6137.00	kPa	KDB
Pc	6270.00	kPa	Critica...
Pc	6140.00 ± 20.00	kPa	NIST
Pc	6170.00	kPa	NIST
Pc	6140.00 ± 20.00	kPa	NIST
Pc	6140.00 ± 20.00	kPa	NIST
Pc	6137.00	kPa	NIST
Pc	6324.75 ± 5.00	kPa	NIST
Pc	6129.00 ± 10.00	kPa	NIST
Pc	6148.00	kPa	NIST
Pc	6131.00	kPa	NIST
Pc	6391.44 ± 68.94	kPa	NIST
Pc	6380.00 ± 80.00	kPa	NIST
Pc	6380.00	kPa	NIST
Pc	6313.00 ± 162.12	kPa	NIST
Pc	6360.00	kPa	NIST
Pc	6796.00	kPa	NIST
Pc	6586.00	kPa	NIST
Pc	6536.00	kPa	NIST
Pc	6292.00	kPa	NIST
Pc	Outlier 12060.00	kPa	NIST
Inp	[396.00; 496.00]
Inp	463.60		NIST
Inp	459.20		NIST
Inp	457.40		NIST
Inp	463.60		NIST
Inp	459.20		NIST
Inp	457.40		NIST
Inp	415.00		NIST
Inp	Outlier 496.00		NIST
Inp	413.00		NIST
Inp	397.00		NIST
Inp	396.00		NIST
Inp	396.00		NIST
Inp	427.00		NIST
Inp	435.00		NIST
Inp	423.00		NIST
Inp	437.00		NIST
Inp	427.00		NIST
Inp	403.00		NIST
Inp	400.00		NIST
Inp	439.00		NIST
Inp	410.00		NIST
Inp	422.00		NIST
Inp	409.00		NIST
Inp	396.00		NIST
Inp	400.00		NIST
Inp	440.00		NIST
Inp	414.40		NIST
Inp	443.20		NIST
Inp	443.80		NIST
Inp	443.00		NIST
Inp	444.70		NIST
Inp	444.70		NIST
Inp	436.00		NIST
Inp	446.00		NIST
Inp	416.00		NIST
Inp	432.00		NIST
Inp	446.00		NIST
Inp	446.00		NIST
Inp	427.00		NIST
Inp	411.00		NIST
Inp	415.00		NIST
Inp	411.00		NIST
Inp	406.00		NIST
Inp	443.00		NIST
Inp	410.00		NIST
Inp	412.00		NIST
Inp	408.00		NIST
Inp	462.00		NIST
Inp	405.00		NIST
Inp	421.00		NIST
Inp	458.00		NIST
Inp	454.00		NIST
Inp	459.00		NIST
Inp	426.00		NIST
Inp	429.00		NIST
Inp	477.00		NIST
Inp	482.00		NIST
Inp	444.00		NIST
Inp	440.00		NIST
Inp	445.00		NIST
Inp	427.00		NIST
Inp	440.00		NIST
Inp	450.00		NIST
Inp	427.40		NIST
Inp	450.00		NIST
Inp	440.00		NIST
Inp	436.00		NIST
Inp	440.00		NIST
Inp	448.00		NIST
Inp	Outlier 489.00		NIST
Inp	472.00		NIST
Inp	Outlier 493.00		NIST
Inp	472.00		NIST
Inp	Outlier 493.00		NIST
Inp	462.00		NIST
Inp	482.00		NIST
Inp	439.00		NIST
Inp	440.00		NIST
Inp	455.00		NIST
Inp	443.00		NIST
Inp	427.00		NIST
Inp	443.00		NIST
Inp	443.00		NIST
Inp	428.00		NIST
Inp	427.00		NIST
Inp	421.00		NIST
Inp	446.00		NIST
Inp	440.00		NIST
Inp	421.00		NIST
Inp	414.40		NIST
Inp	446.00		NIST
I	[883.00; 972.00]
I	944.00		NIST
I	952.00		NIST
I	924.00		NIST
I	Outlier 972.00		NIST
I	942.00		NIST
I	939.00		NIST
I	922.00		NIST
I	941.00		NIST
I	931.00		NIST
I	921.00		NIST
I	951.00		NIST
I	926.00		NIST
I	925.00		NIST
I	900.00		NIST
I	905.00		NIST
I	940.70		NIST
I	933.00		NIST
I	934.00		NIST
I	939.00		NIST
I	937.00		NIST
I	933.00		NIST
I	941.00		NIST
I	934.00		NIST
I	Outlier 888.00		NIST
I	947.00		NIST
I	955.00		NIST
I	900.00		NIST
I	948.80		NIST
I	935.00		NIST
I	930.00		NIST
I	956.00		NIST
I	932.00		NIST
I	925.00		NIST
I	944.00		NIST
I	947.00		NIST
I	947.00		NIST
I	929.00		NIST
I	936.00		NIST
I	930.00		NIST
I	930.00		NIST
I	944.00		NIST
I	938.00		NIST
I	944.00		NIST
I	929.00		NIST
I	Outlier 893.00		NIST
I	920.00		NIST
I	918.00		NIST
I	908.00		NIST
I	Outlier 897.00		NIST
I	934.00		NIST
I	932.00		NIST
I	934.00		NIST
I	937.00		NIST
I	937.00		NIST
I	945.00		NIST
I	944.00		NIST
I	Outlier 960.10		NIST
I	935.00		NIST
I	910.00		NIST
I	926.00		NIST
I	936.00		NIST
I	932.00		NIST
I	927.00		NIST
I	910.00		NIST
I	Outlier 890.00		NIST
I	917.00		NIST
I	944.00		NIST
I	Outlier 883.00		NIST
I	939.00		NIST
I	913.00		NIST
I	Outlier 883.00		NIST
I	938.00		NIST
I	938.00		NIST
I	932.00		NIST
I	937.00		NIST
I	928.00		NIST
I	922.00		NIST
I	922.00		NIST
I	930.00		NIST
I	955.00		NIST
I	900.00		NIST
I	942.00		NIST
I	913.00		NIST
I	926.00		NIST
I	930.00		NIST
I	946.00		NIST
I	934.00		NIST
I	934.00		NIST
I	932.00		NIST
I	926.00		NIST
I	927.00		NIST
I	944.00		NIST
I	937.00		NIST
I	934.00		NIST
I	931.00		NIST
I	924.00		NIST
I	924.00		NIST
I	913.00		NIST
I	926.00		NIST
I	913.00		NIST
I	913.00		NIST
I	934.00		NIST
I	940.00		NIST
I	900.00		NIST
I	908.00		NIST
I	950.00		NIST
I	922.00		NIST
I	959.00		NIST
I	921.00		NIST
I	913.00		NIST
I	946.00		NIST
I	932.00		NIST
I	925.00		NIST
I	930.00		NIST
I	930.00		NIST
I	925.00		NIST
I	915.00		NIST
I	900.00		NIST
I	927.00		NIST
I	927.00		NIST
I	927.00		NIST
I	936.00		NIST
I	940.00		NIST
I	940.00		NIST
I	900.00		NIST
I	900.00		NIST
I	923.00		NIST
I	951.00		NIST
I	942.00		NIST
I	929.00		NIST
I	939.00		NIST
I	943.00		NIST
I	935.00		NIST
I	932.00		NIST
I	923.00		NIST
I	912.00		NIST
I	928.00		NIST
I	910.00		NIST
I	932.00		NIST
I	937.00		NIST
I	924.00		NIST
I	934.00		NIST
I	929.00		NIST
I	932.00		NIST
I	930.00		NIST
I	929.00		NIST
I	929.00		NIST
I	910.00		NIST
I	927.00		NIST
I	905.00		NIST
I	905.00		NIST
I	932.00		NIST
I	916.00		NIST
I	930.00		NIST
I	932.00		NIST
I	941.00		NIST
I	922.00		NIST
I	940.00		NIST
I	932.00		NIST
I	936.00		NIST
I	936.00		NIST
I	950.00		NIST
I	926.00		NIST
I	936.00		NIST
I	925.00		NIST
I	934.00		NIST
I	934.00		NIST
I	944.00		NIST
I	900.00		NIST
I	940.00		NIST
I	919.00		NIST
I	923.00		NIST
I	943.00		NIST
I	928.00		NIST
I	934.00		NIST
I	929.00		NIST
I	932.00		NIST
I	922.00		NIST
I	950.00		NIST
I	944.00		NIST
I	939.00		NIST
I	951.00		NIST
S°liquid	[159.86; 177.00]	J/mol×K
S°liquid	159.86	J/mol×K	NIST
S°liquid	161.21	J/mol×K	NIST
S°liquid	160.70	J/mol×K	NIST
S°liquid	177.00	J/mol×K	NIST
Tboil	[350.15; 351.91]	K
Tboil	351.44	K	KDB
Tboil	351.44	K	Isobari...
Tboil	351.43	K	Vapor l...
Tboil	351.44	K	Vapor l...
Tboil	351.44	K	Isobari...
Tboil	351.43	K	Study o...
Tboil	351.41	K	Isobari...
Tboil	351.30	K	Vapor l...
Tboil	351.55	K	Isobari...
Tboil	351.55	K	Liquid-...
Tboil	351.55	K	Isobari...
Tboil	351.45	K	Phase e...
Tboil	351.45	K	Separat...
Tboil	351.45	K	Isobari...
Tboil	351.70	K	Phase d...
Tboil	351.40	K	Isobari...
Tboil	351.65	K	Vapor-l...
Tboil	351.45	K	Isobari...
Tboil	351.55	K	Solubil...
Tboil	351.45	K	Vapour-...
Tboil	Outlier 350.15	K	Measure...
Tboil	351.38	K	Isobari...
Tboil	351.45	K	Isobari...
Tboil	351.55	K	Investi...
Tboil	351.65	K	Investi...
Tboil	351.45	K	Measure...
Tboil	351.44	K	Low-Pre...
Tboil	351.45	K	Measure...
Tboil	351.49	K	Isobari...
Tboil	351.41	K	Measure...
Tboil	351.46	K	Vapor-L...
Tboil	351.41	K	Isobari...
Tboil	351.46	K	Vapor-L...
Tboil	351.46	K	Vapor-L...
Tboil	351.45	K	Vapor-L...
Tboil	351.30	K	Effect ...
Tboil	351.44	K	Liquid-...
Tboil	351.55	K	Isobari...
Tboil	351.35	K	Isobari...
Tboil	351.45	K	Vapor L...
Tboil	351.20	K	Isobari...
Tboil	351.51	K	Measure...
Tboil	351.45	K	Vapor L...
Tboil	Outlier 351.91	K	Evaluat...
Tboil	351.65	K	Isobari...
Tboil	351.14	K	Vapor L...
Tboil	351.44	K	Vapor-L...
Tboil	351.46	K	Vapor L...
Tboil	351.44	K	Vapor-L...
Tc	[506.90; 531.90]	K
Tc	514.00	K	KDB
Tc	514.00	K	Measure...
Tc	514.20	K	Measure...
Tc	514.20	K	Measure...
Tc	514.00 ± 0.20	K	NIST
Tc	515.00	K	NIST
Tc	514.10 ± 0.60	K	NIST
Tc	514.10 ± 0.60	K	NIST
Tc	514.10	K	NIST
Tc	516.15 ± 0.20	K	NIST
Tc	513.90 ± 0.20	K	NIST
Tc	513.90 ± 0.20	K	NIST
Tc	513.90 ± 0.20	K	NIST
Tc	513.90 ± 0.20	K	NIST
Tc	513.90 ± 0.20	K	NIST
Tc	513.90	K	NIST
Tc	513.91 ± 0.10	K	NIST
Tc	516.00 ± 8.00	K	NIST
Tc	513.88	K	NIST
Tc	516.20	K	NIST
Tc	518.90 ± 0.70	K	NIST
Tc	516.00	K	NIST
Tc	514.00	K	NIST
Tc	516.48 ± 2.77	K	NIST
Tc	514.20	K	NIST
Tc	516.70	K	NIST
Tc	516.20	K	NIST
Tc	514.90	K	NIST
Tc	516.20 ± 2.00	K	NIST
Tc	Outlier 523.00	K	NIST
Tc	516.30	K	NIST
Tc	518.60 ± 5.00	K	NIST
Tc	514.00 ± 1.00	K	NIST
Tc	507.50	K	NIST
Tc	516.80	K	NIST
Tc	508.60	K	NIST
Tc	513.80	K	NIST
Tc	506.90 ± 8.00	K	NIST
Tc	507.80	K	NIST
Tc	507.50	K	NIST
Tc	507.50	K	NIST
Tc	Outlier 531.90	K	NIST
Tfus	[159.00; 159.02]	K
Tfus	159.02	K	Aq. Sol...
Tfus	159.00	K	KDB
Vc	[0.168; 0.168]	m3/kmol
Vc	0.168	m3/kmol	KDB
Vc	0.168	m3/kmol	NIST
Vm	5.87e-05	m3/mol	Excess ...
Zc	0.2412490		KDB
Zra	0.25		KDB

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[51.38; 107.00]	J/mol×K	[200.00; 591.25]
Cp,gas	51.38 ± 0.50	J/mol×K	200.00	NIST
Cp,gas	62.30 ± 0.54	J/mol×K	279.00	NIST
Cp,gas	62.09 ± 0.42	J/mol×K	280.00	NIST
Cp,gas	73.15	J/mol×K	350.01	NIST
Cp,gas	75.70 ± 1.10	J/mol×K	356.55	NIST
Cp,gas	74.57	J/mol×K	360.00	NIST
Cp,gas	76.40 ± 1.10	J/mol×K	361.75	NIST
Cp,gas	75.52	J/mol×K	367.90	NIST
Cp,gas	76.00	J/mol×K	370.01	NIST
Cp,gas	77.70 ± 1.10	J/mol×K	371.85	NIST
Cp,gas	77.46	J/mol×K	380.00	NIST
Cp,gas	79.80 ± 1.10	J/mol×K	387.25	NIST
Cp,gas	80.00 ± 1.10	J/mol×K	388.85	NIST
Cp,gas	80.40	J/mol×K	400.08	NIST
Cp,gas	82.01	J/mol×K	410.16	NIST
Cp,gas	83.39	J/mol×K	422.00	NIST
Cp,gas	84.10	J/mol×K	425.09	NIST
Cp,gas	85.90 ± 1.10	J/mol×K	433.25	NIST
Cp,gas	87.99	J/mol×K	437.00	NIST
Cp,gas	87.30 ± 1.10	J/mol×K	443.35	NIST
Cp,gas	87.65	J/mol×K	450.08	NIST
Cp,gas	91.11	J/mol×K	475.12	NIST
Cp,gas	91.21	J/mol×K	476.00	NIST
Cp,gas	92.20 ± 1.10	J/mol×K	480.45	NIST
Cp,gas	99.40 ± 1.10	J/mol×K	534.35	NIST
Cp,gas	101.30 ± 1.10	J/mol×K	548.75	NIST
Cp,gas	104.50 ± 1.10	J/mol×K	572.25	NIST
Cp,gas	107.00 ± 1.10	J/mol×K	591.25	NIST
Cp,liquid	[97.53; 160.70]	J/mol×K	[250.00; 318.15]
Cp,liquid	97.53	J/mol×K	250.00	NIST
Cp,liquid	106.30	J/mol×K	270.00	NIST
Cp,liquid	102.40	J/mol×K	271.40	NIST
Cp,liquid	106.53	J/mol×K	283.15	Excess ...
Cp,liquid	108.27	J/mol×K	288.15	Excess ...
Cp,liquid	108.07	J/mol×K	288.15	NIST
Cp,liquid	110.06	J/mol×K	293.15	Excess ...
Cp,liquid	111.30	J/mol×K	293.15	Excess ...
Cp,liquid	109.87	J/mol×K	294.31	NIST
Cp,liquid	112.06	J/mol×K	297.36	NIST
Cp,liquid	114.70	J/mol×K	297.80	NIST
Cp,liquid	111.70	J/mol×K	298.00	NIST
Cp,liquid	112.26	J/mol×K	298.00	NIST
Cp,liquid	103.30	J/mol×K	298.00	NIST
Cp,liquid	113.40	J/mol×K	298.00	NIST
Cp,liquid	112.10	J/mol×K	298.00	NIST
Cp,liquid	160.70	J/mol×K	298.10	NIST
Cp,liquid	111.96	J/mol×K	298.15	NIST
Cp,liquid	112.68	J/mol×K	298.15	NIST
Cp,liquid	110.51	J/mol×K	298.15	NIST
Cp,liquid	115.90	J/mol×K	298.15	NIST
Cp,liquid	112.67	J/mol×K	298.15	NIST
Cp,liquid	112.40	J/mol×K	298.15	NIST
Cp,liquid	113.75	J/mol×K	298.15	NIST
Cp,liquid	113.30	J/mol×K	298.15	Excess ...
Cp,liquid	112.30	J/mol×K	298.15	NIST
Cp,liquid	112.50	J/mol×K	298.15	NIST
Cp,liquid	112.30	J/mol×K	298.15	NIST
Cp,liquid	112.33	J/mol×K	298.15	NIST
Cp,liquid	112.09	J/mol×K	298.15	NIST
Cp,liquid	111.81	J/mol×K	298.15	NIST
Cp,liquid	112.36	J/mol×K	298.15	NIST
Cp,liquid	111.53	J/mol×K	298.15	NIST
Cp,liquid	112.03	J/mol×K	298.15	Excess ...
Cp,liquid	112.00	J/mol×K	298.15	Volumet...
Cp,liquid	112.15	J/mol×K	298.15	NIST
Cp,liquid	115.10	J/mol×K	303.00	NIST
Cp,liquid	114.01	J/mol×K	303.15	Excess ...
Cp,liquid	114.00	J/mol×K	303.15	Volumet...
Cp,liquid	115.30	J/mol×K	303.15	Excess ...
Cp,liquid	117.50	J/mol×K	308.15	Excess ...
Cp,liquid	116.00	J/mol×K	308.15	Volumet...
Cp,liquid	118.72	J/mol×K	313.15	NIST
Cp,liquid	118.00	J/mol×K	313.15	Volumet...
Cp,liquid	119.70	J/mol×K	313.15	Excess ...
Cp,liquid	118.40	J/mol×K	313.20	NIST
Cp,liquid	118.80	J/mol×K	316.00	NIST
Cp,liquid	122.10	J/mol×K	318.15	Excess ...
η	[0.0005120; 0.0019750]	Pa×s	[268.10; 348.15]
η	0.0019750	Pa×s	268.10	Density...
η	0.0017750	Pa×s	273.10	Density...
η	0.0016290	Pa×s	278.10	Density...
η	0.0016292	Pa×s	278.15	Density...
η	0.0016123	Pa×s	278.15	Density...
η	0.0014680	Pa×s	283.10	Density...
η	0.0014735	Pa×s	283.15	Density...
η	0.0014750	Pa×s	283.15	Density...
η	0.0014179	Pa×s	283.15	Density...
η	0.0014483	Pa×s	283.15	Density...
η	0.0013185	Pa×s	288.15	Density...
η	0.0013370	Pa×s	288.15	Densiti...
η	0.0013410	Pa×s	288.15	Density...
η	0.0012811	Pa×s	288.15	Density...
η	0.0013325	Pa×s	288.15	Density...
η	0.0013130	Pa×s	288.15	Densiti...
η	0.0013370	Pa×s	288.15	Densiti...
η	0.0012160	Pa×s	293.15	Densiti...
η	0.0011800	Pa×s	293.15	Viscosi...
η	0.0012070	Pa×s	293.15	Density...
η	0.0011960	Pa×s	293.15	Density...
η	0.0011617	Pa×s	293.15	Density...
η	0.0011700	Pa×s	293.15	Viscosi...
η	0.0011600	Pa×s	293.15	Density...
η	0.0012110	Pa×s	293.15	Densiti...
η	0.0011880	Pa×s	293.15	Viscosi...
η	0.0012220	Pa×s	293.15	Volumet...
η	0.0011946	Pa×s	293.15	Density...
η	0.0012097	Pa×s	293.15	Density...
η	0.0011870	Pa×s	293.15	Dynamic...
η	0.0011770	Pa×s	293.15	Densiti...
η	0.0011802	Pa×s	293.15	Densiti...
η	0.0011870	Pa×s	293.15	Density...
η	0.0011890	Pa×s	293.15	Densiti...
η	0.0012103	Pa×s	293.15	Viscosi...
η	0.0011870	Pa×s	293.15	Viscosi...
η	0.0011600	Pa×s	293.15	Density...
η	0.0011870	Pa×s	293.15	Dynamic...
η	0.0012107	Pa×s	293.15	Densiti...
η	0.0011407	Pa×s	293.15	Viscosi...
η	0.0010950	Pa×s	298.15	Densiti...
η	0.0011320	Pa×s	298.15	Densiti...
η	0.0010830	Pa×s	298.15	Excess ...
η	0.0011170	Pa×s	298.15	Viscosi...
η	0.0010820	Pa×s	298.15	Dynamic...
η	0.0010371	Pa×s	298.15	Viscosi...
η	0.0010569	Pa×s	298.15	Density...
η	0.0010880	Pa×s	298.15	Density...
η	0.0010911	Pa×s	298.15	Densiti...
η	0.0010900	Pa×s	298.15	Tempera...
η	0.0010740	Pa×s	298.15	Densiti...
η	0.0010859	Pa×s	298.15	Density...
η	0.0010991	Pa×s	298.15	Viscosi...
η	0.0010964	Pa×s	298.15	Measure...
η	0.0010970	Pa×s	298.15	Densiti...
η	0.0011050	Pa×s	298.15	Densiti...
η	0.0011020	Pa×s	298.15	Density...
η	0.0011090	Pa×s	298.15	Volumet...
η	0.0010820	Pa×s	298.15	Dynamic...
η	0.0011050	Pa×s	298.15	Densiti...
η	0.0010840	Pa×s	298.15	Densiti...
η	0.0010820	Pa×s	298.15	Viscosi...
η	0.0010912	Pa×s	298.15	Densiti...
η	0.0010780	Pa×s	298.15	Viscosi...
η	0.0010990	Pa×s	298.15	Density...
η	0.0010820	Pa×s	298.15	Density...
η	0.0011050	Pa×s	298.15	Density...
η	0.0009462	Pa×s	303.15	Viscosi...
η	0.0009575	Pa×s	303.15	Densiti...
η	0.0010100	Pa×s	303.15	Density...
η	0.0009645	Pa×s	303.15	Density...
η	0.0009790	Pa×s	303.15	Densiti...
η	0.0009810	Pa×s	303.15	Viscosi...
η	0.0009971	Pa×s	303.15	Density...
η	0.0010191	Pa×s	303.15	Densiti...
η	0.0009820	Pa×s	303.15	Viscosi...
η	0.0010030	Pa×s	303.15	Densiti...
η	0.0010095	Pa×s	303.15	Measure...
η	0.0009770	Pa×s	303.15	Densiti...
η	0.0009870	Pa×s	303.15	Viscosi...
η	0.0009890	Pa×s	303.15	Viscosi...
η	0.0009835	Pa×s	303.15	Density...
η	0.0010090	Pa×s	303.15	Volumet...
η	0.0009870	Pa×s	303.15	Dynamic...
η	0.0009680	Pa×s	303.15	Density...
η	0.0010858	Pa×s	303.15	Densiti...
η	0.0009977	Pa×s	303.15	Densiti...
η	0.0009940	Pa×s	303.15	Density...
η	0.0009986	Pa×s	303.15	Densiti...
η	0.0009680	Pa×s	303.15	Density...
η	0.0009980	Pa×s	303.15	Densiti...
η	0.0009870	Pa×s	303.15	Density...
η	0.0009900	Pa×s	303.15	Excess ...
η	0.0010100	Pa×s	303.15	Densiti...
η	0.0009960	Pa×s	303.15	Density...
η	0.0009870	Pa×s	303.15	Dynamic...
η	0.0009350	Pa×s	308.15	Viscosi...
η	0.0009732	Pa×s	308.15	Densiti...
η	0.0008653	Pa×s	308.15	Viscosi...
η	0.0008950	Pa×s	308.15	Density...
η	0.0009120	Pa×s	308.15	Tempera...
η	0.0008950	Pa×s	308.15	Excess ...
η	0.0009020	Pa×s	308.15	Densiti...
η	0.0008970	Pa×s	308.15	Density...
η	0.0008880	Pa×s	308.15	Densiti...
η	0.0009170	Pa×s	308.15	Measure...
η	0.0008877	Pa×s	308.15	Densiti...
η	0.0009140	Pa×s	308.15	Densiti...
η	0.0009210	Pa×s	308.15	Densiti...
η	0.0009210	Pa×s	308.15	Densiti...
η	0.0009080	Pa×s	308.15	Densiti...
η	0.0009200	Pa×s	308.15	Density...
η	0.0008758	Pa×s	308.15	Densiti...
η	0.0009139	Pa×s	308.15	Densiti...
η	0.0008827	Pa×s	308.15	Density...
η	0.0009083	Pa×s	308.15	Density...
η	0.0008387	Pa×s	313.15	Densiti...
η	0.0008320	Pa×s	313.15	Densiti...
η	0.0008400	Pa×s	313.15	Density...
η	0.0008100	Pa×s	313.15	Density...
η	0.0008420	Pa×s	313.15	Density...
η	0.0008450	Pa×s	313.15	Densiti...
η	0.0008220	Pa×s	313.15	Viscosi...
η	0.0008450	Pa×s	313.15	Viscosi...
η	0.0007933	Pa×s	313.15	Viscosi...
η	0.0008596	Pa×s	313.15	Densiti...
η	0.0008086	Pa×s	313.15	Densiti...
η	0.0008240	Pa×s	313.15	Densiti...
η	0.0008184	Pa×s	313.15	Density...
η	0.0008319	Pa×s	313.15	Densiti...
η	0.0008100	Pa×s	313.15	Density...
η	0.0008424	Pa×s	313.15	Densiti...
η	0.0007915	Pa×s	313.15	Densiti...
η	0.0008100	Pa×s	313.15	Density...
η	0.0008979	Pa×s	313.15	Measure...
η	0.0008280	Pa×s	313.15	Density...
η	0.0008190	Pa×s	313.15	Densiti...
η	0.0008400	Pa×s	313.15	Volumet...
η	0.0007670	Pa×s	318.15	Density...
η	0.0007560	Pa×s	318.15	Densiti...
η	0.0008284	Pa×s	318.15	Densiti...
η	0.0007710	Pa×s	318.15	Densiti...
η	0.0007218	Pa×s	318.15	Densiti...
η	0.0008172	Pa×s	318.15	Measure...
η	0.0007451	Pa×s	318.15	Density...
η	0.0007335	Pa×s	318.15	Densiti...
η	0.0007720	Pa×s	318.15	Density...
η	0.0007740	Pa×s	318.15	Tempera...
η	0.0007650	Pa×s	318.15	Densiti...
η	0.0007298	Pa×s	318.15	Viscosi...
η	0.0007530	Pa×s	318.15	Densiti...
η	0.0007710	Pa×s	318.15	Densiti...
η	0.0006727	Pa×s	323.15	Viscosi...
η	0.0006868	Pa×s	323.15	Density...
η	0.0007130	Pa×s	323.15	Density...
η	0.0006876	Pa×s	323.15	Densiti...
η	0.0006677	Pa×s	323.15	Densiti...
η	0.0007040	Pa×s	323.15	Densiti...
η	0.0007081	Pa×s	323.15	Densiti...
η	0.0006880	Pa×s	323.15	Densiti...
η	0.0007493	Pa×s	323.15	Densiti...
η	0.0006939	Pa×s	323.15	Viscosi...
η	0.0007050	Pa×s	323.15	Volumet...
η	0.0006970	Pa×s	323.15	Densiti...
η	0.0007490	Pa×s	323.15	Viscosi...
η	0.0006323	Pa×s	323.15	Densiti...
η	0.0006340	Pa×s	328.15	Densiti...
η	0.0006104	Pa×s	328.15	Densiti...
η	0.0006219	Pa×s	328.15	Viscosi...
η	0.0006344	Pa×s	328.15	Density...
η	0.0006640	Pa×s	328.15	Tempera...
η	0.0005762	Pa×s	333.15	Viscosi...
η	0.0005806	Pa×s	333.15	Densiti...
η	0.0005872	Pa×s	333.15	Density...
η	0.0005810	Pa×s	333.15	Densiti...
η	0.0005970	Pa×s	333.15	Volumet...
η	0.0005890	Pa×s	338.15	Tempera...
η	0.0005120	Pa×s	348.15	Tempera...
σcond	[3.00e-05; 7.11e-04]	S/m	[298.15; 318.15]
σcond	4.13e-04	S/m	298.15	Electri...
σcond	3.00e-05	S/m	298.15	Viscosi...
σcond	5.04e-04	S/m	303.15	Electri...
σcond	5.84e-04	S/m	308.15	Electri...
σcond	6.44e-04	S/m	313.15	Electri...
σcond	7.11e-04	S/m	318.15	Electri...
ΔfusH	[0.66; 5.02]	kJ/mol	[111.40; 159.00]
ΔfusH	3.14	kJ/mol	111.40	NIST
ΔfusH	0.66	kJ/mol	127.50	NIST
ΔfusH	4.63	kJ/mol	156.20	NIST
ΔfusH	5.02	kJ/mol	158.50	NIST
ΔfusH	4.96	kJ/mol	158.70	NIST
ΔfusH	4.64	kJ/mol	158.80	NIST
ΔfusH	4.64	kJ/mol	158.80	NIST
ΔfusH	4.97	kJ/mol	159.00	NIST
ΔfusH	4.93	kJ/mol	159.00	NIST
ΔvapH	[14.20; 54.10]	kJ/mol	[208.00; 503.00]
ΔvapH	44.00	kJ/mol	208.00	NIST
ΔvapH	45.60	kJ/mol	240.50	NIST
ΔvapH	42.40	kJ/mol	318.00	NIST
ΔvapH	54.10	kJ/mol	318.50	NIST
ΔvapH	41.00 ± 0.10	kJ/mol	320.00	NIST
ΔvapH	40.90	kJ/mol	320.00	NIST
ΔvapH	42.90	kJ/mol	322.00	NIST
ΔvapH	42.50	kJ/mol	322.50	NIST
ΔvapH	42.20	kJ/mol	324.50	NIST
ΔvapH	40.70	kJ/mol	326.00	NIST
ΔvapH	40.40	kJ/mol	328.00	NIST
ΔvapH	42.50	kJ/mol	329.50	NIST
ΔvapH	41.70	kJ/mol	331.00	NIST
ΔvapH	40.00 ± 0.10	kJ/mol	335.00	NIST
ΔvapH	40.20	kJ/mol	335.00	NIST
ΔvapH	41.30	kJ/mol	339.50	NIST
ΔvapH	41.30	kJ/mol	339.50	NIST
ΔvapH	39.30	kJ/mol	340.00	NIST
ΔvapH	39.40	kJ/mol	344.00	NIST
ΔvapH	40.50	kJ/mol	349.50	NIST
ΔvapH	40.00	kJ/mol	351.00	NIST
ΔvapH	38.70 ± 0.10	kJ/mol	351.00	NIST
ΔvapH	38.80	kJ/mol	351.00	NIST
ΔvapH	38.56	kJ/mol	351.50	NIST
ΔvapH	38.74	kJ/mol	351.50	KDB
ΔvapH	40.10	kJ/mol	361.50	NIST
ΔvapH	35.20	kJ/mol	393.00	NIST
ΔvapH	39.10	kJ/mol	417.00	NIST
ΔvapH	30.60	kJ/mol	423.00	NIST
ΔvapH	25.70	kJ/mol	453.00	NIST
ΔvapH	21.80	kJ/mol	473.00	NIST
ΔvapH	36.10	kJ/mol	486.50	NIST
ΔvapH	17.30	kJ/mol	493.00	NIST
ΔvapH	14.20	kJ/mol	503.00	NIST
ν	[0.0000008; 0.0000015]	m2/s	[293.15; 323.15]
ν	0.0000015	m2/s	293.15	Density...
ν	0.0000014	m2/s	298.15	Density...
ν	0.0000012	m2/s	303.15	Density...
ν	0.0000011	m2/s	308.15	Density...
ν	0.0000010	m2/s	313.15	Density...
ν	0.0000009	m2/s	318.15	Density...
ν	0.0000008	m2/s	323.15	Density...
Pvap	[2.18; 4760.00]	kPa	[278.15; 498.30]
Pvap	2.26	kPa	278.15	Total v...
Pvap	2.18	kPa	278.60	A milli...
Pvap	3.15	kPa	283.15	Total v...
Pvap	3.11	kPa	283.50	A milli...
Pvap	4.33	kPa	288.15	Total v...
Pvap	5.59	kPa	292.33	Vapor p...
Pvap	5.88	kPa	293.15	Total v...
Pvap	5.95	kPa	293.40	A milli...
Pvap	6.70	kPa	295.25	Thermop...
Pvap	7.88	kPa	298.15	Study o...
Pvap	7.88	kPa	298.15	Thermod...
Pvap	7.80	kPa	298.15	Total v...
Pvap	7.92	kPa	298.15	Vapor-P...
Pvap	7.96	kPa	298.30	A milli...
Pvap	9.07	kPa	301.10	Thermog...
Pvap	10.43	kPa	303.15	Solubil...
Pvap	10.42	kPa	303.15	Isother...
Pvap	10.41	kPa	303.15	Total v...
Pvap	10.47	kPa	303.15	Thermod...
Pvap	10.47	kPa	303.15	Thermod...
Pvap	10.47	kPa	303.15	Study o...
Pvap	10.47	kPa	303.15	Thermod...
Pvap	10.54	kPa	303.15	Vapor-P...
Pvap	10.52	kPa	303.20	A milli...
Pvap	10.86	kPa	303.83	Vapor p...
Pvap	11.32	kPa	303.95	Measure...
Pvap	10.94	kPa	305.47	Thermog...
Pvap	11.69	kPa	305.54	Thermog...
Pvap	11.08	kPa	305.63	Thermog...
Pvap	11.85	kPa	305.68	Thermog...
Pvap	13.30	kPa	307.45	Thermop...
Pvap	13.19	kPa	307.52	Investi...
Pvap	13.84	kPa	308.10	A milli...
Pvap	13.84	kPa	308.15	Vapor-P...
Pvap	13.77	kPa	308.15	Study o...
Pvap	13.77	kPa	308.15	Thermod...
Pvap	13.71	kPa	308.15	Total v...
Pvap	15.05	kPa	309.89	Investi...
Pvap	15.36	kPa	310.23	Measure...
Pvap	16.15	kPa	311.14	Vapor p...
Pvap	17.00	kPa	312.17	Vapor-L...
Pvap	17.13	kPa	312.21	Investi...
Pvap	17.77	kPa	313.07	Vapour ...
Pvap	17.87	kPa	313.10	A milli...
Pvap	17.98	kPa	313.15	Vapor-P...
Pvap	17.91	kPa	313.15	Study o...
Pvap	17.89	kPa	313.15	(Vapour...
Pvap	17.84	kPa	313.15	Solubil...
Pvap	17.93	kPa	313.15	Thermod...
Pvap	17.90	kPa	313.15	Total v...
Pvap	18.00	kPa	313.20	High pr...
Pvap	18.15	kPa	313.43	Vapor-L...
Pvap	20.00	kPa	315.05	Thermop...
Pvap	20.00	kPa	315.24	Investi...
Pvap	21.32	kPa	315.75	Measure...
Pvap	21.07	kPa	316.30	Vapor-L...
Pvap	21.90	kPa	317.00	Phase e...
Pvap	22.84	kPa	317.90	Vapor p...
Pvap	22.98	kPa	318.10	A milli...
Pvap	23.06	kPa	318.15	Total v...
Pvap	23.07	kPa	318.15	Study o...
Pvap	23.02	kPa	318.15	Isother...
Pvap	23.17	kPa	318.15	Vapor-P...
Pvap	23.07	kPa	318.15	Vapor-L...
Pvap	23.18	kPa	318.24	Vapor-L...
Pvap	23.45	kPa	318.42	Investi...
Pvap	23.82	kPa	318.81	Measure...
Pvap	24.00	kPa	319.50	Vapor-L...
Pvap	25.72	kPa	320.31	Investi...
Pvap	26.39	kPa	320.87	Vapor-L...
Pvap	26.41	kPa	321.00	Isobari...
Pvap	26.41	kPa	321.00	Isobari...
Pvap	26.70	kPa	321.05	Thermop...
Pvap	28.12	kPa	322.13	Investi...
Pvap	29.05	kPa	322.90	A milli...
Pvap	29.41	kPa	323.09	Vapor p...
Pvap	29.40	kPa	323.14	Vapor L...
Pvap	29.46	kPa	323.15	Study o...
Pvap	29.37	kPa	323.15	Vapor-L...
Pvap	29.57	kPa	323.15	Thermod...
Pvap	29.46	kPa	323.15	Total v...
Pvap	29.57	kPa	323.15	Thermod...
Pvap	29.58	kPa	323.15	Vapor-P...
Pvap	29.48	kPa	323.15	Vapor-L...
Pvap	29.27	kPa	323.17	Isother...
Pvap	30.00	kPa	323.46	Measure...
Pvap	31.32	kPa	323.50	Measure...
Pvap	30.53	kPa	324.00	Isobari...
Pvap	30.85	kPa	324.10	Investi...
Pvap	31.10	kPa	324.28	Measure...
Pvap	32.02	kPa	325.00	Isobari...
Pvap	32.50	kPa	325.12	Phase e...
Pvap	33.00	kPa	325.48	Using 1...
Pvap	33.30	kPa	325.65	Thermop...
Pvap	33.68	kPa	325.96	Investi...
Pvap	33.90	kPa	326.03	Using 1...
Pvap	34.00	kPa	326.13	Vapor-L...
Pvap	34.02	kPa	326.16	Vapor-L...
Pvap	34.60	kPa	326.48	Using 1...
Pvap	34.61	kPa	326.49	Vapor-L...
Pvap	35.11	kPa	326.80	Vapor p...
Pvap	35.30	kPa	326.93	Using 1...
Pvap	35.19	kPa	327.00	Isobari...
Pvap	36.00	kPa	327.33	Using 1...
Pvap	36.20	kPa	327.52	Investi...
Pvap	36.80	kPa	327.80	Using 1...
Pvap	36.73	kPa	327.90	A milli...
Pvap	37.34	kPa	328.14	Vapor-L...
Pvap	37.46	kPa	328.15	Vapor-P...
Pvap	37.39	kPa	328.17	Vapor-L...
Pvap	37.60	kPa	328.26	Using 1...
Pvap	38.40	kPa	328.73	Using 1...
Pvap	39.20	kPa	329.18	Using 1...
Pvap	41.33	kPa	329.35	Measure...
Pvap	39.76	kPa	329.53	Measure...
Pvap	40.00	kPa	329.55	Thermop...
Pvap	40.00	kPa	329.57	Investi...
Pvap	40.00	kPa	329.58	Investi...
Pvap	40.00	kPa	329.62	Using 1...
Pvap	40.00	kPa	329.62	Isobari...
Pvap	40.00	kPa	329.67	Isobari...
Pvap	40.44	kPa	330.00	Isobari...
Pvap	40.44	kPa	330.00	Isobari...
Pvap	40.90	kPa	330.11	Using 1...
Pvap	41.30	kPa	330.28	Phase e...
Pvap	41.76	kPa	330.56	Vapor p...
Pvap	41.90	kPa	330.62	Using 1...
Pvap	41.90	kPa	330.65	Vapor-L...
Pvap	42.90	kPa	331.16	Using 1...
Pvap	43.49	kPa	331.49	Investi...
Pvap	43.90	kPa	331.66	Using 1...
Pvap	44.67	kPa	332.06	Vapor L...
Pvap	44.90	kPa	332.17	Using 1...
Pvap	45.90	kPa	332.68	Using 1...
Pvap	46.15	kPa	332.80	A milli...
Pvap	46.70	kPa	332.85	Thermop...
Pvap	46.34	kPa	333.00	Isobari...
Pvap	46.95	kPa	333.15	Vapor-P...
Pvap	46.63	kPa	333.15	Isother...
Pvap	46.90	kPa	333.15	Using 1...
Pvap	46.94	kPa	333.16	Vapor-L...
Pvap	47.00	kPa	333.20	High pr...
Pvap	50.00	kPa	333.20	High pr...
Pvap	47.09	kPa	333.26	Measure...
Pvap	47.62	kPa	333.45	Investi...
Pvap	48.40	kPa	333.86	Using 1...
Pvap	48.61	kPa	333.94	Vapor p...
Pvap	51.33	kPa	334.05	Measure...
Pvap	49.90	kPa	334.55	Using 1...
Pvap	50.67	kPa	335.00	Isobari...
Pvap	51.22	kPa	335.03	Vapor-L...
Pvap	51.36	kPa	335.16	Investi...
Pvap	51.30	kPa	335.17	Using 1...
Pvap	52.00	kPa	335.45	Phase e...
Pvap	52.80	kPa	335.84	Using 1...
Pvap	53.30	kPa	335.95	Thermop...
Pvap	53.33	kPa	335.99	Isobari...
Pvap	52.96	kPa	336.00	Isobari...
Pvap	53.33	kPa	336.06	Isobari...
Pvap	53.47	kPa	336.10	Vapor-L...
Pvap	53.56	kPa	336.14	Vapor-L...
Pvap	53.85	kPa	336.28	Using 1...
Pvap	53.32	kPa	336.50	Vapor-L...
Pvap	54.67	kPa	336.63	Measure...
Pvap	55.12	kPa	336.76	Investi...
Pvap	55.13	kPa	336.81	Using 1...
Pvap	56.06	kPa	337.18	Vapor p...
Pvap	56.32	kPa	337.31	Using 1...
Pvap	57.69	kPa	337.86	Using 1...
Pvap	61.33	kPa	338.05	Measure...
Pvap	58.58	kPa	338.15	Vapor-P...
Pvap	58.48	kPa	338.16	Vapor-L...
Pvap	58.87	kPa	338.32	Using 1...
Pvap	60.00	kPa	338.65	Thermop...
Pvap	59.97	kPa	338.70	Vapor-L...
Pvap	60.00	kPa	338.72	Measure...
Pvap	60.05	kPa	338.72	Investi...
Pvap	60.00	kPa	338.73	Investi...
Pvap	60.49	kPa	338.97	Using 1...
Pvap	60.35	kPa	339.00	Isobari...
Pvap	61.82	kPa	339.47	Using 1...
Pvap	62.30	kPa	339.58	Phase e...
Pvap	62.42	kPa	339.71	Measure...
Pvap	63.20	kPa	339.97	Vapor p...
Pvap	63.19	kPa	339.99	Using 1...
Pvap	63.00	kPa	340.00	Isobari...
Pvap	63.84	kPa	340.19	Investi...
Pvap	64.47	kPa	340.47	Using 1...
Pvap	65.48	kPa	340.82	Using 1...
Pvap	66.70	kPa	341.15	Thermop...
Pvap	66.45	kPa	341.18	Using 1...
Pvap	66.66	kPa	341.20	Isobari...
Pvap	66.66	kPa	341.23	Isobari...
Pvap	67.56	kPa	341.50	Investi...
Pvap	71.33	kPa	341.65	Measure...
Pvap	67.91	kPa	341.68	Using 1...
Pvap	68.60	kPa	342.00	Isobari...
Pvap	68.92	kPa	342.01	Using 1...
Pvap	69.73	kPa	342.30	Vapor p...
Pvap	70.00	kPa	342.32	Phase e...
Pvap	70.11	kPa	342.45	Measure...
Pvap	70.35	kPa	342.53	Using 1...
Pvap	70.90	kPa	342.65	Vapor-L...
Pvap	71.88	kPa	343.05	Using 1...
Pvap	72.10	kPa	343.06	Investi...
Pvap	72.24	kPa	343.15	Vapor-P...
Pvap	72.30	kPa	343.15	Vapor-L...
Pvap	73.00	kPa	343.43	Vapor-L...
Pvap	73.35	kPa	343.54	Using 1...
Pvap	74.68	kPa	343.97	Using 1...
Pvap	75.37	kPa	344.11	Vapor-L...
Pvap	75.99	kPa	344.37	Investi...
Pvap	76.08	kPa	344.41	Using 1...
Pvap	76.84	kPa	344.57	Vapor-L...
Pvap	81.33	kPa	344.75	Measure...
Pvap	77.68	kPa	344.93	Using 1...
Pvap	77.77	kPa	345.00	Isobari...
Pvap	77.77	kPa	345.00	Isobari...
Pvap	77.95	kPa	345.00	Measure...
Pvap	78.95	kPa	345.30	Using 1...
Pvap	79.75	kPa	345.48	Vapor-L...
Pvap	79.99	kPa	345.59	Isobari...
Pvap	79.99	kPa	345.60	Isobari...
Pvap	79.99	kPa	345.69	Investi...
Pvap	80.00	kPa	345.69	Investi...
Pvap	80.44	kPa	345.77	Using 1...
Pvap	80.90	kPa	345.79	Phase e...
Pvap	81.82	kPa	346.17	Using 1...
Pvap	83.77	kPa	346.68	Vapor-L...
Pvap	83.74	kPa	346.75	Using 1...
Pvap	84.41	kPa	346.94	Measure...
Pvap	84.65	kPa	347.10	Investi...
Pvap	85.17	kPa	347.17	Using 1...
Pvap	86.38	kPa	347.51	Using 1...
Pvap	91.33	kPa	347.55	Measure...
Pvap	87.78	kPa	347.91	Using 1...
Pvap	87.96	kPa	348.00	Isobari...
Pvap	88.77	kPa	348.14	Vapor-L...
Pvap	88.59	kPa	348.15	Measure...
Pvap	88.59	kPa	348.15	Measure...
Pvap	88.66	kPa	348.15	Vapor-P...
Pvap	88.58	kPa	348.15	Measure...
Pvap	89.17	kPa	348.29	Using 1...
Pvap	89.52	kPa	348.31	Vapor-L...
Pvap	90.20	kPa	348.45	Phase e...
Pvap	89.37	kPa	348.51	Investi...
Pvap	90.00	kPa	348.56	Measure...
Pvap	90.34	kPa	348.62	Using 1...
Pvap	91.55	kPa	348.87	Vapor-L...
Pvap	91.82	kPa	349.03	Using 1...
Pvap	92.48	kPa	349.19	Measure...
Pvap	93.08	kPa	349.36	Using 1...
Pvap	93.32	kPa	349.38	Isobari...
Pvap	93.32	kPa	349.42	Isobari...
Pvap	93.88	kPa	349.49	Vapor-L...
Pvap	94.24	kPa	349.67	Using 1...
Pvap	94.48	kPa	349.83	Investi...
Pvap	93.33	kPa	349.94	Vapour-...
Pvap	95.35	kPa	350.00	Isobari...
Pvap	95.68	kPa	350.05	Using 1...
Pvap	101.33	kPa	350.15	Measure...
Pvap	97.16	kPa	350.44	Using 1...
Pvap	98.66	kPa	350.82	Isobari...
Pvap	98.63	kPa	350.82	Using 1...
Pvap	99.24	kPa	351.00	Isobari...
Pvap	99.74	kPa	351.03	Isobari...
Pvap	101.30	kPa	351.14	Vapor L...
Pvap	100.02	kPa	351.17	Using 1...
Pvap	101.30	kPa	351.20	Isobari...
Pvap	100.00	kPa	351.21	Isobari...
Pvap	101.40	kPa	351.31	Phase e...
Pvap	101.30	kPa	351.35	Isobari...
Pvap	101.18	kPa	351.36	Vapor-L...
Pvap	101.11	kPa	351.38	Vapor-L...
Pvap	101.23	kPa	351.42	Vapor-L...
Pvap	101.30	kPa	351.44	Low-Pre...
Pvap	101.30	kPa	351.44	Vapor-L...
Pvap	101.30	kPa	351.45	Measure...
Pvap	101.33	kPa	351.45	Vapor-L...
Pvap	101.33	kPa	351.45	Phase e...
Pvap	101.30	kPa	351.45	Vapour-...
Pvap	101.30	kPa	351.45	Isobari...
Pvap	101.30	kPa	351.45	Vapor L...
Pvap	101.30	kPa	351.45	Isobari...
Pvap	101.30	kPa	351.45	Isobari...
Pvap	101.38	kPa	351.51	Using 1...
Pvap	101.30	kPa	351.51	Measure...
Pvap	101.32	kPa	351.55	Isobari...
Pvap	101.31	kPa	351.55	Investi...
Pvap	101.30	kPa	351.65	Investi...
Pvap	102.37	kPa	351.76	Using 1...
Pvap	102.80	kPa	351.85	Measure...
Pvap	101.30	kPa	351.91	Evaluat...
Pvap	103.64	kPa	352.07	Using 1...
Pvap	105.17	kPa	352.45	Using 1...
Pvap	106.59	kPa	352.79	Using 1...
Pvap	108.14	kPa	353.15	Isother...
Pvap	108.08	kPa	353.15	Using 1...
Pvap	109.08	kPa	353.15	Measure...
Pvap	108.42	kPa	353.15	Vapor L...
Pvap	108.00	kPa	353.20	High pr...
Pvap	110.00	kPa	353.20	High pr...
Pvap	109.58	kPa	353.50	Using 1...
Pvap	110.80	kPa	353.79	Using 1...
Pvap	111.70	kPa	354.00	Isobari...
Pvap	112.36	kPa	354.14	Using 1...
Pvap	113.75	kPa	354.46	Using 1...
Pvap	115.35	kPa	354.82	Using 1...
Pvap	116.13	kPa	355.00	Isobari...
Pvap	116.81	kPa	355.15	Using 1...
Pvap	118.44	kPa	355.51	Using 1...
Pvap	120.01	kPa	355.85	Using 1...
Pvap	121.30	kPa	356.11	Isobari...
Pvap	121.68	kPa	356.22	Using 1...
Pvap	123.23	kPa	356.54	Using 1...
Pvap	124.46	kPa	356.81	Using 1...
Pvap	125.44	kPa	357.00	Isobari...
Pvap	126.16	kPa	357.16	Using 1...
Pvap	127.68	kPa	357.48	Using 1...
Pvap	129.67	kPa	357.89	Using 1...
Pvap	135.37	kPa	359.00	Isobari...
Pvap	135.37	kPa	359.00	Isobari...
Pvap	156.04	kPa	363.15	Isother...
Pvap	161.30	kPa	363.55	Isobari...
Pvap	201.30	kPa	369.55	Isobari...
Pvap	224.37	kPa	373.15	Measure...
Pvap	224.37	kPa	373.15	Measure...
Pvap	224.31	kPa	373.15	Measure...
Pvap	224.00	kPa	373.20	High pr...
Pvap	225.00	kPa	373.20	High pr...
Pvap	572.00	kPa	403.20	High pr...
Pvap	585.00	kPa	403.20	High pr...
Pvap	600.00	kPa	405.53	Isobari...
Pvap	3040.00	kPa	473.20	A novel...
Pvap	2970.00	kPa	473.20	A novel...
Pvap	3030.00	kPa	473.20	A novel...
Pvap	4690.00	kPa	498.20	A novel...
Pvap	4760.00	kPa	498.30	A novel...
Pvap	4710.00	kPa	498.30	A novel...
n0	[1.34827; 1.36600]		[283.15; 328.15]
n0	1.36546		283.15	Thermop...
n0	1.36342		288.15	Densiti...
n0	1.36344		288.15	Refract...
n0	1.36300		288.15	Excess ...
n0	1.36320		288.15	Liquid ...
n0	1.36342		288.15	Densiti...
n0	1.36351		288.15	Densiti...
n0	1.36138		293.15	Mixing ...
n0	1.36162		293.15	Liquid ...
n0	1.36160		293.15	Vapor-L...
n0	1.36600		293.15	Solubil...
n0	1.36190		293.15	Solubil...
n0	1.36160		293.15	Liquid ...
n0	1.36090		293.15	Isobari...
n0	1.36600		293.15	Solubil...
n0	1.36120		293.15	Vapour ...
n0	1.35920		293.15	Vapor l...
n0	1.36100		293.15	Solubil...
n0	1.36130		293.15	Solid-L...
n0	1.36160		293.15	Liquid-...
n0	1.36180		293.15	A novel...
n0	1.36144		293.15	Refract...
n0	1.36160		293.15	Density...
n0	1.36160		293.15	Liquid-...
n0	1.36160		293.15	Measure...
n0	1.36160		293.15	Measure...
n0	1.36180		293.15	Isother...
n0	1.36140		293.15	Vapor l...
n0	1.36130		293.15	Isobari...
n0	1.36600		293.15	Solubil...
n0	1.36200		293.15	Vapor-l...
n0	1.36138		293.15	Study o...
n0	1.36120		293.20	Vapor L...
n0	1.36000		293.20	Vapor l...
n0	1.36160		293.20	Isobari...
n0	1.36000		298.00	Determi...
n0	1.35930		298.00	Vapor-L...
n0	1.35920		298.10	PHYSICA...
n0	1.36068		298.15	Isobari...
n0	1.35917		298.15	Isother...
n0	1.35929		298.15	Study o...
n0	1.35929		298.15	Mixing ...
n0	1.36023		298.15	Synthes...
n0	1.35920		298.15	Excess ...
n0	1.35930		298.15	Density...
n0	1.36023		298.15	Physica...
n0	1.36023		298.15	Excess ...
n0	1.35935		298.15	Thermop...
n0	1.35937		298.15	Viscosi...
n0	1.35900		298.15	Volumet...
n0	1.35830		298.15	Applica...
n0	1.36250		298.15	(Vapor ...
n0	1.35929		298.15	Effect ...
n0	1.35950		298.15	Densiti...
n0	1.35950		298.15	Tempera...
n0	1.35928		298.15	Physica...
n0	1.35940		298.15	Propert...
n0	1.35907		298.15	Effect ...
n0	1.35910		298.15	Ternary...
n0	1.35910		298.15	Thermod...
n0	1.35929		298.15	Ternary...
n0	1.35928		298.15	Isother...
n0	1.35940		298.15	(Vapor ...
n0	1.36023		298.15	Synthes...
n0	1.35910		298.15	Thermod...
n0	1.35922		298.15	Refract...
n0	1.35947		298.15	Sucrose...
n0	1.36068		298.15	Vapor-L...
n0	1.36080		298.15	Physico...
n0	1.35930		298.15	Excess ...
n0	1.36160		298.15	Liquid ...
n0	1.35920		298.15	Experim...
n0	1.35940		298.15	(Vapor ...
n0	1.36068		298.15	Vapor-l...
n0	1.35959		298.15	Vapor-l...
n0	1.36068		298.15	Experim...
n0	1.35926		298.15	Isobari...
n0	1.35984		298.15	Thermop...
n0	1.36000		298.15	Bubble ...
n0	1.35920		298.15	Experim...
n0	1.35916		298.15	Density...
n0	1.35928		298.15	Isother...
n0	1.35910		298.15	Excess ...
n0	1.35920		298.15	Geometr...
n0	1.35933		298.15	Isother...
n0	1.35910		298.15	Liquid ...
n0	1.35939		298.15	Isobari...
n0	1.35929		298.15	A study...
n0	1.35930		298.15	Density...
n0	1.35949		298.15	Densiti...
n0	1.35928		298.15	Isother...
n0	1.35924		298.15	Densiti...
n0	1.35949		298.15	Vapor l...
n0	1.35910		298.15	Excess ...
n0	1.35935		298.15	Densiti...
n0	1.35950		298.15	Density...
n0	1.35916		298.15	Density...
n0	1.35932		298.15	Densiti...
n0	1.35940		298.15	Density...
n0	1.35940		298.15	Activit...
n0	1.36068		298.15	Vapor L...
n0	1.35940		298.15	Isobari...
n0	1.35924		298.15	Densiti...
n0	1.35920		298.15	Effect ...
n0	1.35941		298.15	Liquid-...
n0	1.35950		298.15	Excess ...
n0	1.35960		298.15	Physica...
n0	1.35923		298.15	Volumet...
n0	1.36023		298.15	Physica...
n0	1.35960		298.15	Effect ...
n0	1.35941		298.15	Measure...
n0	1.35950		298.15	Excess ...
n0	1.35930		298.15	Liquid ...
n0	1.35936		298.15	Ethanol...
n0	1.35910		298.15	Excess ...
n0	1.35950		298.20	Liquid ...
n0	1.35960		298.20	Isobari...
n0	1.35720		303.15	Thermod...
n0	1.35740		303.15	Density...
n0	1.35890		303.15	Physico...
n0	1.35800		303.15	Experim...
n0	1.35702		303.15	Refract...
n0	1.35725		303.15	Study o...
n0	1.35720		303.15	Thermod...
n0	1.35725		303.15	Mixing ...
n0	1.35500		308.15	Excess ...
n0	1.35510		308.15	Liquid ...
n0	1.35630		308.15	Physico...
n0	1.35502		308.15	Densiti...
n0	1.35504		308.15	Densiti...
n0	1.35509		308.15	Densiti...
n0	1.35500		308.15	Thermod...
n0	1.35477		308.15	Refract...
n0	1.35502		308.15	Densiti...
n0	1.35500		308.15	Thermod...
n0	1.35315		313.15	Thermop...
n0	1.35270		313.15	Refract...
n0	1.35409		313.15	Thermop...
n0	1.35353		313.15	1-Alkyl...
n0	1.35320		313.15	Density...
n0	1.35100		318.15	Densiti...
n0	1.35068		318.15	Refract...
n0	1.35095		318.15	Densiti...
n0	1.35090		318.15	Liquid ...
n0	1.34837		323.15	Refract...
n0	1.34930		323.15	Density...
n0	1.34827		328.15	Thermop...
ρl	[732.40; 866.84]	kg/m3	[278.15; 348.14]
ρl	802.08	kg/m3	278.15	Volumet...
ρl	802.39	kg/m3	278.15	Density...
ρl	802.10	kg/m3	278.15	Thermop...
ρl	802.33	kg/m3	278.15	Thermod...
ρl	802.69	kg/m3	278.15	Densiti...
ρl	798.46	kg/m3	283.15	Densiti...
ρl	797.97	kg/m3	283.15	Densiti...
ρl	798.10	kg/m3	283.15	Thermod...
ρl	798.51	kg/m3	283.15	Effects...
ρl	797.96	kg/m3	283.15	Volumet...
ρl	797.88	kg/m3	283.15	Density...
ρl	797.88	kg/m3	283.15	Excess ...
ρl	793.60	kg/m3	288.15	Volumet...
ρl	793.85	kg/m3	288.15	Thermod...
ρl	793.72	kg/m3	288.15	Volumet...
ρl	795.17	kg/m3	288.15	Density...
ρl	793.91	kg/m3	288.15	Excess ...
ρl	793.71	kg/m3	288.15	Volumet...
ρl	794.31	kg/m3	288.15	The exc...
ρl	793.68	kg/m3	288.15	Mass de...
ρl	794.04	kg/m3	288.15	Excess ...
ρl	793.72	kg/m3	288.15	Effect ...
ρl	794.40	kg/m3	288.15	Density...
ρl	793.70	kg/m3	288.15	Thermop...
ρl	789.00	kg/m3	293.00	KDB
ρl	789.40	kg/m3	293.00	Fluid-P...
ρl	789.40	kg/m3	293.00	Fluid-P...
ρl	789.94	kg/m3	293.14	Densiti...
ρl	789.44	kg/m3	293.15	Volumet...
ρl	790.91	kg/m3	293.15	Volumet...
ρl	788.90	kg/m3	293.15	Isobari...
ρl	788.33	kg/m3	293.15	Densiti...
ρl	790.00	kg/m3	293.15	Measure...
ρl	789.50	kg/m3	293.15	Charact...
ρl	792.17	kg/m3	293.15	Excess ...
ρl	789.66	kg/m3	293.15	Excess ...
ρl	789.55	kg/m3	293.15	Thermod...
ρl	789.56	kg/m3	293.15	Densiti...
ρl	789.48	kg/m3	293.15	Electro...
ρl	789.92	kg/m3	293.15	Density...
ρl	789.40	kg/m3	293.15	Measure...
ρl	788.88	kg/m3	293.15	Volumet...
ρl	789.43	kg/m3	293.15	Densiti...
ρl	789.63	kg/m3	293.15	A Volum...
ρl	789.41	kg/m3	293.15	Investi...
ρl	789.38	kg/m3	293.15	Isother...
ρl	789.47	kg/m3	293.15	Volumet...
ρl	790.70	kg/m3	293.15	Viscosi...
ρl	790.00	kg/m3	293.15	Isobari...
ρl	789.48	kg/m3	293.15	Volumet...
ρl	789.66	kg/m3	293.15	Thermod...
ρl	788.70	kg/m3	293.15	The den...
ρl	789.45	kg/m3	293.15	Volumet...
ρl	789.38	kg/m3	293.15	(Liquid...
ρl	790.60	kg/m3	293.15	Investi...
ρl	789.60	kg/m3	293.15	Density...
ρl	788.88	kg/m3	293.15	Volumet...
ρl	789.58	kg/m3	293.15	Thermod...
ρl	789.99	kg/m3	293.15	Effects...
ρl	789.51	kg/m3	293.15	Propert...
ρl	789.99	kg/m3	293.15	(Vapor-...
ρl	789.86	kg/m3	293.15	Densiti...
ρl	789.48	kg/m3	293.15	Propert...
ρl	789.40	kg/m3	293.15	Volumet...
ρl	790.04	kg/m3	293.15	The exc...
ρl	789.45	kg/m3	293.15	Effect ...
ρl	790.10	kg/m3	293.15	Density...
ρl	789.29	kg/m3	293.15	Excess ...
ρl	789.62	kg/m3	293.15	Densiti...
ρl	789.92	kg/m3	293.15	Apparen...
ρl	789.20	kg/m3	293.15	Three B...
ρl	789.57	kg/m3	293.15	Density...
ρl	789.54	kg/m3	293.22	Thermod...
ρl	785.10	kg/m3	298.00	Fluid-P...
ρl	785.10	kg/m3	298.00	Fluid-P...
ρl	785.80	kg/m3	298.10	Density...
ρl	785.19	kg/m3	298.10	Excess ...
ρl	785.85	kg/m3	298.10	Surface...
ρl	785.80	kg/m3	298.15	Density...
ρl	785.32	kg/m3	298.15	Liquid-...
ρl	785.50	kg/m3	298.15	Excess ...
ρl	786.47	kg/m3	298.15	Liquid-...
ρl	784.97	kg/m3	298.15	Densiti...
ρl	785.24	kg/m3	298.15	Tempera...
ρl	785.28	kg/m3	298.15	Density...
ρl	785.30	kg/m3	298.15	Density...
ρl	785.03	kg/m3	298.15	Volumet...
ρl	785.00	kg/m3	298.15	Dynamic...
ρl	785.20	kg/m3	298.15	Dynamic...
ρl	784.80	kg/m3	298.15	Volumet...
ρl	785.13	kg/m3	298.15	Excess ...
ρl	785.41	kg/m3	298.15	Propert...
ρl	785.60	kg/m3	298.15	Volumet...
ρl	785.23	kg/m3	298.15	Ebullio...
ρl	785.25	kg/m3	298.15	Densiti...
ρl	785.24	kg/m3	298.15	Ternary...
ρl	785.00	kg/m3	298.15	Volumet...
ρl	784.90	kg/m3	298.15	Bubble ...
ρl	787.58	kg/m3	298.15	Modifie...
ρl	785.07	kg/m3	298.15	Viscosi...
ρl	785.30	kg/m3	298.15	Isobari...
ρl	785.00	kg/m3	298.15	Refract...
ρl	785.90	kg/m3	298.15	Density...
ρl	785.70	kg/m3	298.15	Liquid-...
ρl	785.32	kg/m3	298.15	Density...
ρl	785.15	kg/m3	298.15	Thermod...
ρl	784.89	kg/m3	298.15	Isother...
ρl	785.20	kg/m3	298.15	Applica...
ρl	784.70	kg/m3	298.15	Density...
ρl	785.04	kg/m3	298.15	Vapor P...
ρl	785.34	kg/m3	298.15	Density...
ρl	785.06	kg/m3	298.15	Isobari...
ρl	785.48	kg/m3	298.15	Physica...
ρl	785.75	kg/m3	298.15	The exc...
ρl	785.30	kg/m3	298.15	Thermod...
ρl	785.90	kg/m3	298.15	Cation ...
ρl	785.90	kg/m3	298.15	Isobari...
ρl	785.36	kg/m3	298.15	Thermod...
ρl	785.20	kg/m3	298.15	Measure...
ρl	785.09	kg/m3	298.15	Isother...
ρl	785.12	kg/m3	298.15	The phy...
ρl	784.90	kg/m3	298.15	A combi...
ρl	785.10	kg/m3	298.15	(Liquid...
ρl	784.20	kg/m3	298.15	Solubil...
ρl	785.02	kg/m3	298.15	Solid-l...
ρl	785.40	kg/m3	298.15	Propert...
ρl	785.46	kg/m3	298.15	Experim...
ρl	785.32	kg/m3	298.15	Binary ...
ρl	785.24	kg/m3	298.15	Influen...
ρl	785.39	kg/m3	298.15	Measure...
ρl	785.20	kg/m3	298.15	Propert...
ρl	784.94	kg/m3	298.15	Densiti...
ρl	785.48	kg/m3	298.15	Study o...
ρl	785.05	kg/m3	298.15	Density...
ρl	785.57	kg/m3	298.15	Densiti...
ρl	785.30	kg/m3	298.15	Solubil...
ρl	785.20	kg/m3	298.15	Molar h...
ρl	785.27	kg/m3	298.15	Isobari...
ρl	785.32	kg/m3	298.15	Liquid ...
ρl	785.11	kg/m3	298.15	Experim...
ρl	785.46	kg/m3	298.15	Vapor L...
ρl	785.37	kg/m3	298.15	Thermod...
ρl	785.70	kg/m3	298.15	Apparen...
ρl	785.20	kg/m3	298.15	Liquid-...
ρl	785.20	kg/m3	298.15	Density...
ρl	785.10	kg/m3	298.15	Fully a...
ρl	785.02	kg/m3	298.15	Determi...
ρl	785.16	kg/m3	298.15	Volumet...
ρl	789.50	kg/m3	298.15	Liquid-...
ρl	785.16	kg/m3	298.15	Densiti...
ρl	866.84	kg/m3	298.15	Tempera...
ρl	785.41	kg/m3	298.15	Investi...
ρl	785.35	kg/m3	298.15	Binary ...
ρl	785.06	kg/m3	298.15	Physica...
ρl	786.47	kg/m3	298.15	Density...
ρl	785.64	kg/m3	298.15	Apparen...
ρl	785.11	kg/m3	298.15	Isobari...
ρl	789.50	kg/m3	298.15	Liquid-...
ρl	785.11	kg/m3	298.15	Volumet...
ρl	785.49	kg/m3	298.15	Excess ...
ρl	786.40	kg/m3	298.15	Solubil...
ρl	785.20	kg/m3	298.15	Capacit...
ρl	785.73	kg/m3	298.15	Excess ...
ρl	786.71	kg/m3	298.15	Excess ...
ρl	785.22	kg/m3	298.15	Azeotro...
ρl	785.08	kg/m3	298.15	Topolog...
ρl	786.60	kg/m3	298.15	Volumet...
ρl	785.18	kg/m3	298.15	Phase e...
ρl	785.32	kg/m3	298.15	Liquid ...
ρl	785.10	kg/m3	298.15	Thermop...
ρl	784.83	kg/m3	298.15	Thermod...
ρl	785.04	kg/m3	298.15	Liquid-...
ρl	786.47	kg/m3	298.15	Experim...
ρl	785.29	kg/m3	298.15	Binary ...
ρl	785.26	kg/m3	298.15	Thermod...
ρl	785.15	kg/m3	298.15	Excess ...
ρl	786.40	kg/m3	298.15	Volumet...
ρl	785.26	kg/m3	298.15	Tempera...
ρl	785.45	kg/m3	298.15	Excess ...
ρl	785.46	kg/m3	298.15	ACSExce...
ρl	785.83	kg/m3	298.15	Surface...
ρl	785.20	kg/m3	298.15	Solubil...
ρl	785.12	kg/m3	298.15	Electro...
ρl	785.18	kg/m3	298.15	Ebullio...
ρl	785.63	kg/m3	298.15	Density...
ρl	785.31	kg/m3	298.15	Excess ...
ρl	785.20	kg/m3	298.15	Charact...
ρl	785.46	kg/m3	298.15	Experim...
ρl	785.15	kg/m3	298.15	Volumet...
ρl	788.36	kg/m3	298.15	Volumet...
ρl	785.16	kg/m3	298.15	Volumet...
ρl	785.10	kg/m3	298.15	Refract...
ρl	785.29	kg/m3	298.15	Thermod...
ρl	785.00	kg/m3	298.15	Isobari...
ρl	785.13	kg/m3	298.15	Volumet...
ρl	786.00	kg/m3	298.15	Isobari...
ρl	785.14	kg/m3	298.15	Mass de...
ρl	785.16	kg/m3	298.15	Effect ...
ρl	785.07	kg/m3	298.15	Excess ...
ρl	785.22	kg/m3	298.15	Effect ...
ρl	785.12	kg/m3	298.15	Density...
ρl	785.00	kg/m3	298.15	Refract...
ρl	785.46	kg/m3	298.16	Thermod...
ρl	784.93	kg/m3	298.20	Ternary...
ρl	785.18	kg/m3	298.20	Physica...
ρl	786.10	kg/m3	298.20	Deterpe...
ρl	780.80	kg/m3	303.00	Fluid-P...
ρl	780.80	kg/m3	303.00	Fluid-P...
ρl	781.33	kg/m3	303.14	Densiti...
ρl	780.75	kg/m3	303.15	Viscosi...
ρl	780.88	kg/m3	303.15	Densiti...
ρl	782.20	kg/m3	303.15	Viscosi...
ρl	781.69	kg/m3	303.15	Volumet...
ρl	780.86	kg/m3	303.15	Electro...
ρl	780.83	kg/m3	303.15	Volumet...
ρl	780.98	kg/m3	303.15	Tempera...
ρl	780.78	kg/m3	303.15	Vapor-l...
ρl	781.02	kg/m3	303.15	A Volum...
ρl	780.94	kg/m3	303.15	Thermod...
ρl	780.85	kg/m3	303.15	Volumet...
ρl	780.79	kg/m3	303.15	Excess ...
ρl	780.80	kg/m3	303.15	Charact...
ρl	782.28	kg/m3	303.15	Volumet...
ρl	781.31	kg/m3	303.15	Density...
ρl	781.05	kg/m3	303.15	Excess ...
ρl	772.40	kg/m3	303.15	Effect ...
ρl	780.78	kg/m3	303.15	Isobari...
ρl	781.33	kg/m3	303.15	Apparen...
ρl	780.98	kg/m3	303.15	Densiti...
ρl	780.97	kg/m3	303.15	Thermod...
ρl	784.40	kg/m3	303.15	Viscous...
ρl	782.01	kg/m3	303.15	Investi...
ρl	780.75	kg/m3	303.15	Volumet...
ρl	781.69	kg/m3	303.15	Volumet...
ρl	780.84	kg/m3	303.15	Volumet...
ρl	781.00	kg/m3	303.15	Density...
ρl	781.04	kg/m3	303.15	Thermod...
ρl	782.00	kg/m3	303.15	Apparen...
ρl	781.16	kg/m3	303.15	Physica...
ρl	782.16	kg/m3	303.15	Densiti...
ρl	781.08	kg/m3	303.15	Thermod...
ρl	780.96	kg/m3	303.15	Density...
ρl	781.00	kg/m3	303.15	Propert...
ρl	780.85	kg/m3	303.15	Effect ...
ρl	780.72	kg/m3	303.15	Densiti...
ρl	780.83	kg/m3	303.15	Propert...
ρl	781.38	kg/m3	303.15	Effects...
ρl	782.00	kg/m3	303.15	Excess ...
ρl	780.20	kg/m3	303.15	Isobari...
ρl	780.65	kg/m3	303.15	Propert...
ρl	781.30	kg/m3	303.15	Excess ...
ρl	781.43	kg/m3	303.15	The exc...
ρl	780.89	kg/m3	303.15	Densiti...
ρl	781.60	kg/m3	303.15	Density...
ρl	780.90	kg/m3	303.15	Volumet...
ρl	781.90	kg/m3	303.15	Investi...
ρl	781.05	kg/m3	303.17	Thermod...
ρl	775.90	kg/m3	308.15	Volumet...
ρl	776.20	kg/m3	308.15	Density...
ρl	777.08	kg/m3	308.15	The exc...
ρl	776.31	kg/m3	308.15	Propert...
ρl	776.81	kg/m3	308.15	Physica...
ρl	777.20	kg/m3	308.15	Density...
ρl	776.35	kg/m3	308.15	Volumet...
ρl	776.50	kg/m3	308.15	Isobari...
ρl	776.48	kg/m3	308.15	Propert...
ρl	777.82	kg/m3	308.15	Densiti...
ρl	776.82	kg/m3	308.15	Study o...
ρl	776.61	kg/m3	308.15	Density...
ρl	776.70	kg/m3	308.15	Propert...
ρl	776.70	kg/m3	308.15	Thermod...
ρl	776.70	kg/m3	308.15	Density...
ρl	776.41	kg/m3	308.15	Viscosi...
ρl	777.70	kg/m3	308.15	Investi...
ρl	776.48	kg/m3	308.15	Volumet...
ρl	777.83	kg/m3	308.15	Density...
ρl	776.60	kg/m3	308.15	Density...
ρl	776.99	kg/m3	308.15	Apparen...
ρl	776.40	kg/m3	308.15	Physica...
ρl	776.44	kg/m3	308.15	Isobari...
ρl	771.60	kg/m3	308.15	Effect ...
ρl	777.94	kg/m3	308.15	Volumet...
ρl	776.59	kg/m3	308.15	Thermod...
ρl	776.70	kg/m3	308.15	Excess ...
ρl	776.40	kg/m3	308.15	Thermop...
ρl	776.50	kg/m3	308.15	Charact...
ρl	776.41	kg/m3	308.15	Excess ...
ρl	776.59	kg/m3	308.15	Thermod...
ρl	776.66	kg/m3	308.15	Tempera...
ρl	776.48	kg/m3	308.15	Electro...
ρl	776.96	kg/m3	308.15	Density...
ρl	776.51	kg/m3	308.15	Volumet...
ρl	776.43	kg/m3	308.15	Volumet...
ρl	776.41	kg/m3	308.15	Volumet...
ρl	776.63	kg/m3	308.15	Thermod...
ρl	776.48	kg/m3	308.15	Mass de...
ρl	776.51	kg/m3	308.15	Effect ...
ρl	777.10	kg/m3	308.15	Density...
ρl	777.70	kg/m3	308.15	Apparen...
ρl	776.52	kg/m3	308.15	Densiti...
ρl	776.75	kg/m3	308.17	Thermod...
ρl	772.23	kg/m3	313.15	Thermod...
ρl	772.30	kg/m3	313.15	Volumet...
ρl	772.57	kg/m3	313.15	Density...
ρl	772.14	kg/m3	313.15	Volumet...
ρl	773.40	kg/m3	313.15	Viscosi...
ρl	772.09	kg/m3	313.15	Volumet...
ρl	771.20	kg/m3	313.15	Effect ...
ρl	772.60	kg/m3	313.15	Apparen...
ρl	772.27	kg/m3	313.15	A Volum...
ρl	773.30	kg/m3	313.15	Investi...
ρl	772.14	kg/m3	313.15	Effect ...
ρl	772.10	kg/m3	313.15	Charact...
ρl	772.30	kg/m3	313.15	Density...
ρl	772.50	kg/m3	313.15	Density...
ρl	772.05	kg/m3	313.15	Excess ...
ρl	772.61	kg/m3	313.15	Densiti...
ρl	773.70	kg/m3	313.15	Excess ...
ρl	772.23	kg/m3	313.15	Density...
ρl	772.90	kg/m3	313.15	Density...
ρl	772.08	kg/m3	313.15	Propert...
ρl	772.12	kg/m3	313.15	Densiti...
ρl	772.04	kg/m3	313.15	Volumet...
ρl	772.02	kg/m3	313.15	Viscosi...
ρl	772.69	kg/m3	313.15	The exc...
ρl	772.64	kg/m3	313.15	Effects...
ρl	773.42	kg/m3	313.15	Densiti...
ρl	773.60	kg/m3	313.15	Apparen...
ρl	772.15	kg/m3	313.15	Propert...
ρl	772.30	kg/m3	313.15	Propert...
ρl	772.31	kg/m3	313.15	Thermod...
ρl	772.22	kg/m3	313.15	Densiti...
ρl	773.20	kg/m3	313.15	Investi...
ρl	771.14	kg/m3	313.15	Excess ...
ρl	772.42	kg/m3	313.15	Excess ...
ρl	772.00	kg/m3	313.15	Experim...
ρl	773.56	kg/m3	313.15	Volumet...
ρl	772.31	kg/m3	313.15	Excess ...
ρl	772.30	kg/m3	313.15	Volumet...
ρl	772.28	kg/m3	313.15	Tempera...
ρl	772.34	kg/m3	313.15	Densiti...
ρl	772.17	kg/m3	313.15	Electro...
ρl	771.90	kg/m3	313.15	The den...
ρl	772.58	kg/m3	313.16	Densiti...
ρl	772.42	kg/m3	313.17	Thermod...
ρl	768.90	kg/m3	313.20	Density...
ρl	767.84	kg/m3	318.15	Density...
ρl	767.60	kg/m3	318.15	Electro...
ρl	767.61	kg/m3	318.15	Thermod...
ρl	767.52	kg/m3	318.15	Volumet...
ρl	767.65	kg/m3	318.15	Volumet...
ρl	767.70	kg/m3	318.15	Charact...
ρl	767.60	kg/m3	318.15	Thermop...
ρl	767.88	kg/m3	318.15	Excess ...
ρl	768.17	kg/m3	318.15	Apparen...
ρl	767.80	kg/m3	318.15	Density...
ρl	767.57	kg/m3	318.15	Thermod...
ρl	769.15	kg/m3	318.15	Volumet...
ρl	767.80	kg/m3	318.15	Density...
ρl	767.62	kg/m3	318.15	Isobari...
ρl	768.13	kg/m3	318.15	Density...
ρl	767.60	kg/m3	318.15	Physica...
ρl	768.98	kg/m3	318.15	Density...
ρl	767.86	kg/m3	318.15	Density...
ρl	768.40	kg/m3	318.15	Density...
ρl	766.30	kg/m3	318.15	Propert...
ρl	767.00	kg/m3	318.15	Density...
ρl	767.54	kg/m3	318.15	Volumet...
ρl	768.08	kg/m3	318.15	Study o...
ρl	768.99	kg/m3	318.15	Densiti...
ρl	767.71	kg/m3	318.15	Densiti...
ρl	767.68	kg/m3	318.15	Mass de...
ρl	768.26	kg/m3	318.15	The exc...
ρl	767.59	kg/m3	318.15	Viscosi...
ρl	768.30	kg/m3	318.15	Density...
ρl	768.00	kg/m3	318.18	Thermod...
ρl	763.68	kg/m3	323.14	Densiti...
ρl	764.40	kg/m3	323.15	Investi...
ρl	764.49	kg/m3	323.15	Densiti...
ρl	764.69	kg/m3	323.15	Volumet...
ρl	764.14	kg/m3	323.15	Densiti...
ρl	765.29	kg/m3	323.15	Volumet...
ρl	764.00	kg/m3	323.15	Density...
ρl	765.29	kg/m3	323.15	Volumet...
ρl	763.64	kg/m3	323.15	Density...
ρl	763.22	kg/m3	323.15	Electro...
ρl	763.30	kg/m3	323.15	Density...
ρl	763.29	kg/m3	323.15	Densiti...
ρl	763.20	kg/m3	323.15	Charact...
ρl	763.26	kg/m3	323.15	Densiti...
ρl	763.11	kg/m3	323.15	Viscosi...
ρl	763.35	kg/m3	323.15	A Volum...
ρl	763.04	kg/m3	323.15	Volumet...
ρl	763.61	kg/m3	323.15	Vapor-l...
ρl	760.10	kg/m3	323.15	Viscosi...
ρl	763.17	kg/m3	323.15	Volumet...
ρl	758.70	kg/m3	328.15	Charact...
ρl	758.65	kg/m3	328.15	Mass de...
ρl	758.70	kg/m3	328.15	Density...
ρl	758.60	kg/m3	328.15	Isobari...
ρl	759.40	kg/m3	328.15	Density...
ρl	758.60	kg/m3	328.15	Thermop...
ρl	758.58	kg/m3	328.15	Viscosi...
ρl	758.63	kg/m3	328.15	Volumet...
ρl	758.96	kg/m3	328.15	Excess ...
ρl	754.52	kg/m3	333.14	Densiti...
ρl	754.01	kg/m3	333.15	Volumet...
ρl	755.10	kg/m3	333.15	Investi...
ρl	754.20	kg/m3	333.15	A Volum...
ρl	754.10	kg/m3	333.15	Charact...
ρl	754.18	kg/m3	333.15	Densiti...
ρl	753.70	kg/m3	333.15	The den...
ρl	749.54	kg/m3	338.15	Density...
ρl	752.70	kg/m3	338.20	Density...
ρl	745.05	kg/m3	343.15	Densiti...
ρl	732.40	kg/m3	343.20	Density...
ρl	740.21	kg/m3	348.14	Densiti...
ΔfusS	[5.20; 31.68]	J/mol×K	[111.40; 159.00]
ΔfusS	28.16	J/mol×K	111.40	NIST
ΔfusS	5.20	J/mol×K	127.50	NIST
ΔfusS	31.68	J/mol×K	158.50	NIST
ΔfusS	21.22	J/mol×K	158.70	NIST
ΔfusS	29.25	J/mol×K	158.80	NIST
ΔfusS	31.30	J/mol×K	159.00	NIST
ΔfusS	31.00	J/mol×K	159.00	NIST
csound,fluid	[1042.79; 1212.52]	m/s	[278.15; 328.15]
csound,fluid	1212.52	m/s	278.15	Volumet...
csound,fluid	1195.20	m/s	283.15	Excess ...
csound,fluid	1177.84	m/s	288.15	Thermop...
csound,fluid	1178.19	m/s	288.15	Effect ...
csound,fluid	1177.30	m/s	288.15	Tempera...
csound,fluid	1177.69	m/s	288.15	Volumet...
csound,fluid	1169.12	m/s	290.65	Effect ...
csound,fluid	1169.17	m/s	290.65	Thermop...
csound,fluid	1160.63	m/s	293.15	Thermop...
csound,fluid	1160.34	m/s	293.15	Effect ...
csound,fluid	1151.65	m/s	295.65	Effect ...
csound,fluid	1152.03	m/s	295.65	Thermop...
csound,fluid	1141.80	m/s	298.15	Ultraso...
csound,fluid	1142.88	m/s	298.15	Volumet...
csound,fluid	1142.40	m/s	298.15	Tempera...
csound,fluid	1142.10	m/s	298.15	Compres...
csound,fluid	1143.30	m/s	298.15	Excess ...
csound,fluid	1143.50	m/s	298.15	Thermop...
csound,fluid	1142.02	m/s	298.15	Densiti...
csound,fluid	1143.12	m/s	298.15	Effect ...
csound,fluid	1134.98	m/s	300.65	Thermop...
csound,fluid	1134.62	m/s	300.65	Effect ...
csound,fluid	1126.23	m/s	303.15	Effect ...
csound,fluid	1126.50	m/s	303.15	Thermop...
csound,fluid	1118.06	m/s	305.65	Thermop...
csound,fluid	1117.77	m/s	305.65	Effect ...
csound,fluid	1109.16	m/s	308.15	Volumet...
csound,fluid	1109.40	m/s	308.15	Effect ...
csound,fluid	1109.66	m/s	308.15	Thermop...
csound,fluid	1101.00	m/s	310.65	Effect ...
csound,fluid	1101.24	m/s	310.65	Thermop...
csound,fluid	1092.70	m/s	313.15	Effect ...
csound,fluid	1093.80	m/s	313.15	Excess ...
csound,fluid	1092.85	m/s	313.15	Thermop...
csound,fluid	1084.34	m/s	315.65	Effect ...
csound,fluid	1084.53	m/s	315.65	Thermop...
csound,fluid	1075.80	m/s	318.15	Volumet...
csound,fluid	1076.22	m/s	318.15	Thermop...
csound,fluid	1075.90	m/s	318.15	Effect ...
csound,fluid	1067.46	m/s	320.65	Effect ...
csound,fluid	1067.90	m/s	320.65	Thermop...
csound,fluid	1059.32	m/s	323.15	Tempera...
csound,fluid	1059.58	m/s	323.15	Thermop...
csound,fluid	1058.83	m/s	323.15	Effect ...
csound,fluid	1042.79	m/s	328.15	Volumet...
γ	[0.02; 0.02]	N/m	[274.77; 333.20]
γ	0.02	N/m	274.77	PVT, vi...
γ	0.02	N/m	274.87	PVT, vi...
γ	0.02	N/m	280.56	PVT, vi...
γ	0.02	N/m	281.05	PVT, vi...
γ	0.02	N/m	281.17	PVT, vi...
γ	0.02	N/m	283.15	Study o...
γ	0.02	N/m	284.25	PVT, vi...
γ	0.02	N/m	288.15	Surface...
γ	0.02	N/m	288.15	Study o...
γ	0.02	N/m	288.15	The mol...
γ	0.02	N/m	288.15	Surface...
γ	0.02	N/m	288.21	PVT, vi...
γ	0.02	N/m	288.23	PVT, vi...
γ	0.02	N/m	288.65	PVT, vi...
γ	0.02	N/m	293.15	Surface...
γ	0.02	N/m	293.15	Study o...
γ	0.02	N/m	293.15	Surface...
γ	0.02	N/m	293.15	Investi...
γ	0.02	N/m	293.15	Thermod...
γ	0.02	N/m	293.15	Densiti...
γ	0.02	N/m	293.15	PVT, vi...
γ	0.02	N/m	293.15	Surface...
γ	0.02	N/m	293.15	Density...
γ	0.02	N/m	293.15	The mol...
γ	0.02	N/m	293.20	KDB
γ	0.02	N/m	293.20	Surface...
γ	0.02	N/m	294.19	PVT, vi...
γ	0.02	N/m	298.15	PVT, vi...
γ	0.02	N/m	298.15	Surface...
γ	0.02	N/m	298.15	Experim...
γ	0.02	N/m	298.15	Study o...
γ	0.02	N/m	298.15	Surface...
γ	0.02	N/m	298.15	Interfa...
γ	0.02	N/m	298.15	Surface...
γ	0.02	N/m	298.15	Effect ...
γ	0.02	N/m	298.15	The mol...
γ	0.02	N/m	298.15	Surface...
γ	0.02	N/m	298.15	Surface...
γ	0.02	N/m	298.41	PVT, vi...
γ	0.02	N/m	298.55	PVT, vi...
γ	0.02	N/m	303.15	Surface...
γ	0.02	N/m	303.15	The mol...
γ	0.02	N/m	303.15	Surface...
γ	0.02	N/m	303.15	Study o...
γ	0.02	N/m	303.15	Thermod...
γ	0.02	N/m	303.15	Interfa...
γ	0.02	N/m	303.15	PVT, vi...
γ	0.02	N/m	303.15	Surface...
γ	0.02	N/m	303.15	Densiti...
γ	0.02	N/m	303.20	Surface...
γ	0.02	N/m	303.20	PVT, vi...
γ	0.02	N/m	308.15	Surface...
γ	0.02	N/m	308.15	Effect ...
γ	0.02	N/m	308.15	Surface...
γ	0.02	N/m	308.15	Interfa...
γ	0.02	N/m	308.15	Surface...
γ	0.02	N/m	308.15	Study o...
γ	0.02	N/m	308.15	Surface...
γ	0.02	N/m	308.15	The mol...
γ	0.02	N/m	308.23	PVT, vi...
γ	0.02	N/m	311.79	PVT, vi...
γ	0.02	N/m	313.15	Surface...
γ	0.02	N/m	313.15	Thermod...
γ	0.02	N/m	313.15	Study o...
γ	0.02	N/m	313.15	Densiti...
γ	0.02	N/m	313.15	Surface...
γ	0.02	N/m	313.15	Surface...
γ	0.02	N/m	313.15	The mol...
γ	0.02	N/m	313.15	Interfa...
γ	0.02	N/m	313.20	Surface...
γ	0.02	N/m	318.15	Surface...
γ	0.02	N/m	318.15	Effect ...
γ	0.02	N/m	318.15	Surface...
γ	0.02	N/m	318.15	The mol...
γ	0.02	N/m	318.15	Surface...
γ	0.02	N/m	318.15	Interfa...
γ	0.02	N/m	318.15	Surface...
γ	0.02	N/m	318.99	PVT, vi...
γ	0.02	N/m	323.15	Densiti...
γ	0.02	N/m	323.15	Surface...
γ	0.02	N/m	323.15	Thermod...
γ	0.02	N/m	323.15	Surface...
γ	0.02	N/m	323.20	Surface...
γ	0.02	N/m	328.15	Effect ...
γ	0.02	N/m	333.20	Surface...
λ	[0.15; 0.17]	W/m×K	[276.51; 342.82]
λ	0.17	W/m×K	276.51	Experim...
λ	0.17	W/m×K	276.51	Measure...
λ	0.17	W/m×K	276.51	Measure...
λ	0.17	W/m×K	276.51	Measure...
λ	0.17	W/m×K	278.92	Thermal...
λ	0.17	W/m×K	280.80	Experim...
λ	0.17	W/m×K	280.80	Measure...
λ	0.17	W/m×K	283.48	Thermal...
λ	0.17	W/m×K	283.54	Measure...
λ	0.17	W/m×K	284.27	Experim...
λ	0.17	W/m×K	284.27	Measure...
λ	0.17	W/m×K	287.55	Measure...
λ	0.17	W/m×K	287.55	Measure...
λ	0.17	W/m×K	288.98	Thermal...
λ	0.17	W/m×K	290.37	Experim...
λ	0.17	W/m×K	290.37	Measure...
λ	0.17	W/m×K	293.31	Measure...
λ	0.17	W/m×K	293.43	Measure...
λ	0.17	W/m×K	293.43	Experim...
λ	0.17	W/m×K	293.47	Thermal...
λ	0.16	W/m×K	297.25	Measure...
λ	0.16	W/m×K	297.25	Measure...
λ	0.17	W/m×K	298.87	Thermal...
λ	0.16	W/m×K	303.20	Thermal...
λ	0.16	W/m×K	303.28	Measure...
λ	0.16	W/m×K	307.16	Measure...
λ	0.16	W/m×K	307.16	Measure...
λ	0.16	W/m×K	308.81	Thermal...
λ	0.16	W/m×K	313.15	Thermal...
λ	0.16	W/m×K	313.25	Measure...
λ	0.16	W/m×K	318.86	Thermal...
λ	0.16	W/m×K	323.07	Measure...
λ	0.16	W/m×K	323.42	Thermal...
λ	0.16	W/m×K	328.52	Thermal...
λ	0.15	W/m×K	332.97	Measure...
λ	0.15	W/m×K	333.01	Thermal...
λ	0.16	W/m×K	338.22	Thermal...
λ	0.15	W/m×K	342.82	Measure...
λ	0.15	W/m×K	342.82	Thermal...

Pressure Dependent Properties

Property	Value	Unit	Pressure (kPa)	Source
Tboil	[303.30; 369.75]	K	[9.60; 200.00]
Tboil	303.30	K	9.60	Vapor-l...
Tboil	308.80	K	13.33	Isobari...
Tboil	309.90	K	13.70	Vapor-l...
Tboil	316.20	K	20.00	Isobari...
Tboil	315.61	K	20.14	A novel...
Tboil	320.00	K	23.80	Vapor-l...
Tboil	321.60	K	26.66	Isobari...
Tboil	323.82	K	30.24	A novel...
Tboil	325.75	K	33.30	Vapor-L...
Tboil	326.00	K	33.33	Isobari...
Tboil	330.10	K	38.90	Vapor-l...
Tboil	330.00	K	40.00	Isobari...
Tboil	329.92	K	40.31	A novel...
Tboil	334.84	K	50.39	A novel...
Tboil	336.20	K	53.33	Isobari...
Tboil	337.50	K	54.50	Vapor-l...
Tboil	341.40	K	66.66	Isobari...
Tboil	342.80	K	69.50	Vapor-l...
Tboil	342.49	K	70.33	A novel...
Tboil	345.60	K	79.99	Isobari...
Tboil	345.77	K	80.63	A novel...
Tboil	347.26	K	85.67	A novel...
Tboil	349.70	K	91.70	Vapor-l...
Tboil	349.40	K	93.33	Isobari...
Tboil	350.80	K	98.12	Isobari...
Tboil	350.68	K	98.45	A novel...
Tboil	351.28	K	100.79	A novel...
Tboil	351.43	K	100.90	Vapor L...
Tboil	353.68	K	110.86	A novel...
Tboil	355.92	K	120.93	A novel...
Tboil	357.99	K	131.02	A novel...
Tboil	359.94	K	141.10	A novel...
Tboil	361.77	K	151.10	A novel...
Tboil	363.56	K	160.00	A novel...
Tboil	365.24	K	170.00	A novel...
Tboil	366.77	K	180.00	A novel...
Tboil	368.31	K	190.00	A novel...
Tboil	369.75	K	200.00	A novel...

Datasets

1. Molar heat capacity at constant pressure, J/K/mol (3)
2. Viscosity, Pa*s (3)
3. Refractive index (Na D-line) (2)
4. Mass density, kg/m3 (24)
5. Speed of sound, m/s (3)
6. Molar volume, m3/mol (1)

Molar heat capacity at constant pressure, J/K/mol

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Molar heat capacity at constant pressure, J/K/mol - Liquid
273.17	100.00	103.42
293.16	100.00	111.62
313.18	100.00	120.47
333.19	100.00	130.65
273.17	5000.00	103.10
293.16	5000.00	111.02
313.18	5000.00	119.09
333.19	5000.00	129.73
273.17	10000.00	102.18
293.16	10000.00	109.97
313.18	10000.00	117.70
333.19	10000.00	128.35
273.17	15000.00	101.77
293.16	15000.00	108.95
313.18	15000.00	116.78
333.19	15000.00	126.83
273.17	20000.00	100.80
293.16	20000.00	108.21
313.18	20000.00	115.68
333.19	20000.00	125.91
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Molar heat capacity at constant pressure, J/K/mol - Liquid
273.15	100.00	103.50
273.15	5000.00	103.10
273.15	10000.00	102.10
273.15	15000.00	101.70
273.15	20000.00	100.70
293.15	100.00	111.20
293.15	5000.00	110.20
293.15	10000.00	109.00
293.15	15000.00	108.10
293.15	20000.00	107.40
313.15	100.00	119.20
313.15	5000.00	118.00
313.15	10000.00	116.80
313.15	15000.00	115.50
313.15	20000.00	114.90
333.15	100.00	130.00
333.15	5000.00	129.10
333.15	10000.00	127.70
333.15	15000.00	126.00
333.15	20000.00	124.70
Reference

Fixed		Measured
Pressure, kPa - Liquid	Temperature, K - Liquid	Molar heat capacity at constant pressure, J/K/mol - Liquid
101.30	265.00	102.04
101.30	270.01	102.92
101.30	273.00	103.52
101.30	275.01	104.35
101.30	280.00	105.36
101.30	285.01	106.51
101.30	290.01	107.66
101.30	294.99	108.54
101.30	300.03	109.69
101.30	305.00	111.35
101.30	310.01	112.91
101.30	320.01	117.24
500.30	320.01	117.43
997.90	320.00	117.61
1494.10	320.01	116.92
Reference

Viscosity, Pa*s

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Viscosity, Pa*s - Liquid
293.15	100.00	0.0012
293.15	20000.00	0.0013
293.15	40000.00	0.0015
293.15	60000.00	0.0016
293.15	80000.00	0.0018
293.15	100000.00	0.0020
313.15	100.00	0.0008
313.15	20000.00	0.0009
313.15	40000.00	0.0011
313.15	60000.00	0.0012
313.15	80000.00	0.0013
313.15	100000.00	0.0014
333.15	100.00	0.0006
333.15	20000.00	0.0007
333.15	40000.00	0.0008
333.15	60000.00	0.0009
333.15	80000.00	0.0009
333.15	100000.00	0.0010
353.15	20000.00	0.0005
353.15	40000.00	0.0006
353.15	60000.00	0.0006
353.15	80000.00	0.0007
353.15	100000.00	0.0008
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Viscosity, Pa*s - Liquid
293.15	20000.00	0.0013
293.15	40000.00	0.0015
293.15	60000.00	0.0016
293.15	80000.00	0.0018
293.15	100000.00	0.0020
313.15	20000.00	0.0009
313.15	40000.00	0.0011
313.15	60000.00	0.0012
313.15	80000.00	0.0013
313.15	100000.00	0.0014
333.15	20000.00	0.0007
333.15	40000.00	0.0008
333.15	60000.00	0.0009
333.15	80000.00	0.0009
333.15	100000.00	0.0010
353.15	20000.00	0.0005
353.15	40000.00	0.0006
353.15	60000.00	0.0006
353.15	80000.00	0.0007
353.15	100000.00	0.0008
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Viscosity, Pa*s - Liquid
298.15	81.50	0.0011
Reference

Refractive index (Na D-line)

Fixed		Measured
Pressure, kPa - Liquid	Temperature, K - Liquid	Refractive index (Na D-line) - Liquid
100.00	298.15	1.3598
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Refractive index (Na D-line) - Liquid
298.15	100.00	1.3595
Reference

Mass density, kg/m3

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
298.15	100.00	785.7
298.15	10000.00	794.0
298.15	20000.00	801.9
298.15	30000.00	808.9
298.15	40000.00	815.7
323.15	100.00	763.7
323.15	10000.00	773.4
323.15	20000.00	782.3
323.15	30000.00	790.3
323.15	40000.00	797.7
348.15	100.00	739.4
348.15	10000.00	751.2
348.15	20000.00	761.2
348.15	30000.00	770.3
348.15	40000.00	778.6
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
283.15	100.00	798.0
283.15	5000.00	802.0
283.15	10000.00	805.9
283.15	15000.00	809.5
283.15	20000.00	813.0
283.15	25000.00	816.4
283.15	30000.00	819.7
283.15	35000.00	822.8
283.15	40000.00	825.9
283.15	45000.00	828.8
293.15	100.00	789.5
293.15	5000.00	793.7
293.15	10000.00	797.8
293.15	15000.00	801.6
293.15	20000.00	805.3
293.15	25000.00	808.9
293.15	30000.00	812.3
293.15	35000.00	815.6
293.15	40000.00	818.7
293.15	45000.00	821.8
303.15	100.00	780.9
303.15	5000.00	785.3
303.15	10000.00	789.6
303.15	15000.00	793.7
303.15	20000.00	797.5
303.15	25000.00	801.3
303.15	30000.00	804.8
303.15	35000.00	808.2
303.15	40000.00	811.5
303.15	45000.00	814.7
313.15	100.00	772.1
313.15	5000.00	776.8
313.15	10000.00	781.3
313.15	15000.00	785.6
313.15	20000.00	789.6
313.15	25000.00	793.5
313.15	30000.00	797.2
313.15	35000.00	800.8
313.15	40000.00	804.2
313.15	45000.00	807.6
323.15	100.00	763.3
323.15	5000.00	768.3
323.15	10000.00	773.0
323.15	15000.00	777.6
323.15	20000.00	781.8
323.15	25000.00	785.9
323.15	30000.00	789.7
323.15	35000.00	793.5
323.15	40000.00	797.1
323.15	45000.00	800.5
333.15	100.00	754.0
333.15	5000.00	759.3
333.15	10000.00	764.3
333.15	15000.00	769.1
333.15	20000.00	773.6
333.15	25000.00	777.8
333.15	30000.00	781.9
333.15	35000.00	785.8
333.15	40000.00	789.5
333.15	45000.00	793.1
343.15	100.00	744.5
343.15	5000.00	750.1
343.15	10000.00	755.5
343.15	15000.00	760.5
343.15	20000.00	765.3
343.15	25000.00	769.8
343.15	30000.00	774.0
343.15	35000.00	778.1
343.15	40000.00	782.0
343.15	45000.00	785.7
353.15	5000.00	740.6
353.15	10000.00	746.4
353.15	15000.00	751.7
353.15	20000.00	756.7
353.15	25000.00	761.5
353.15	30000.00	766.0
353.15	35000.00	770.2
353.15	40000.00	774.3
353.15	45000.00	778.2
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
298.15	101.33	785.9
313.15	101.00	772.84
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
283.15	100.00	798.0
283.15	5000.00	802.0
283.15	10000.00	805.9
283.15	15000.00	809.5
283.15	20000.00	813.0
283.15	25000.00	816.4
283.15	30000.00	819.7
283.15	35000.00	822.8
283.15	40000.00	825.9
283.15	45000.00	828.8
293.15	100.00	789.5
293.15	5000.00	793.7
293.15	10000.00	797.8
293.15	15000.00	801.6
293.15	20000.00	805.3
293.15	25000.00	808.9
293.15	30000.00	812.3
293.15	35000.00	815.6
293.15	40000.00	818.7
293.15	45000.00	821.8
303.15	100.00	780.9
303.15	5000.00	785.3
303.15	10000.00	789.6
303.15	15000.00	793.7
303.15	20000.00	797.5
303.15	25000.00	801.3
303.15	30000.00	804.8
303.15	35000.00	808.2
303.15	40000.00	811.5
303.15	45000.00	814.7
313.15	100.00	772.1
313.15	5000.00	776.8
313.15	10000.00	781.3
313.15	15000.00	785.6
313.15	20000.00	789.6
313.15	25000.00	793.5
313.15	30000.00	797.2
313.15	35000.00	800.8
313.15	40000.00	804.2
313.15	45000.00	807.6
323.15	100.00	763.3
323.15	5000.00	768.3
323.15	10000.00	773.0
323.15	15000.00	777.6
323.15	20000.00	781.8
323.15	25000.00	785.9
323.15	30000.00	789.7
323.15	35000.00	793.5
323.15	40000.00	797.1
323.15	45000.00	800.5
333.15	100.00	754.0
333.15	5000.00	759.3
333.15	10000.00	764.3
333.15	15000.00	769.1
333.15	20000.00	773.6
333.15	25000.00	777.8
333.15	30000.00	781.9
333.15	35000.00	785.8
333.15	40000.00	789.5
333.15	45000.00	793.1
343.15	100.00	744.5
343.15	5000.00	750.1
343.15	10000.00	755.5
343.15	15000.00	760.5
343.15	20000.00	765.3
343.15	25000.00	769.8
343.15	30000.00	774.0
343.15	35000.00	778.1
343.15	40000.00	782.0
343.15	45000.00	785.7
353.15	5000.00	740.6
353.15	10000.00	746.4
353.15	15000.00	751.7
353.15	20000.00	756.7
353.15	25000.00	761.5
353.15	30000.00	766.0
353.15	35000.00	770.2
353.15	40000.00	774.3
353.15	45000.00	778.2
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
233.15	103.29	840.318
233.15	1104.68	840.959
233.15	2004.58	841.531
233.15	4076.78	842.835
233.15	6134.09	844.107
233.15	8092.61	845.306
233.15	10007.20	846.455
233.15	12136.60	847.721
233.15	14138.70	848.897
233.15	16099.10	850.035
233.15	18082.00	851.168
233.15	20011.30	852.258
233.15	22095.70	853.419
233.15	24039.90	854.493
233.15	25991.00	855.559
233.15	27977.80	856.635
233.15	29956.30	857.691
253.15	102.67	823.303
253.15	1104.14	824.013
253.15	2003.89	824.651
253.15	4116.44	826.119
253.15	6065.68	827.455
253.15	8137.55	828.849
253.15	10136.50	830.174
253.15	12071.90	831.443
253.15	14126.20	832.763
253.15	16132.90	834.037
253.15	17950.00	835.17
253.15	19862.60	836.357
253.15	22054.80	837.687
253.15	23993.00	838.859
253.15	25929.00	840.004
253.15	27984.90	841.212
253.15	30008.70	842.379
273.15	102.91	806.406
273.15	1098.98	807.191
273.15	2003.89	807.905
273.15	4161.84	809.57
273.15	6026.59	810.981
273.15	8023.17	812.466
273.15	10006.40	813.916
273.15	12106.70	815.421
273.15	13929.10	816.718
273.15	15980.40	818.142
273.15	17875.10	819.435
273.15	20011.40	820.885
273.15	21848.10	822.104
273.15	24049.90	823.548
273.15	25880.00	824.728
273.15	27864.90	826.002
273.15	29956.20	827.312
293.15	103.01	789.433
293.15	1103.94	790.313
293.15	2004.04	791.096
293.15	4147.78	792.937
293.15	6147.47	794.616
293.15	8110.82	796.232
293.15	10007.70	797.758
293.15	11859.50	799.229
293.15	13879.80	800.802
293.15	15954.50	802.391
293.15	17852.00	803.817
293.15	19966.90	805.383
293.15	21842.50	806.743
293.15	23888.10	808.2
293.15	25962.80	809.658
293.15	27862.20	810.975
293.15	30030.80	812.452
313.15	102.50	772.101
313.15	1103.52	773.094
313.15	2103.51	774.069
313.15	4115.98	775.994
313.15	6079.66	777.835
313.15	8130.36	779.714
313.15	10007.30	781.394
313.15	12116.00	783.241
313.15	14081.20	784.928
313.15	16092.20	786.617
313.15	18055.60	788.235
313.15	19919.40	789.747
313.15	22045.50	791.432
313.15	24129.90	793.056
313.15	26106.70	794.571
313.15	27987.30	795.987
313.15	29995.30	797.476
333.15	1102.49	755.18
333.15	2002.73	756.173
333.15	4085.91	758.43
333.15	6133.01	760.589
333.15	8031.91	762.538
333.15	9967.10	764.48
333.15	12099.00	766.557
333.15	13992.40	768.358
333.15	16124.20	770.342
333.15	18019.00	772.071
333.15	20012.30	773.85
333.15	22049.80	775.625
333.15	24135.80	777.409
333.15	26129.80	779.08
333.15	28069.30	780.679
333.15	30017.80	782.258
353.15	1101.80	736.102
353.15	2002.93	737.255
353.15	4009.55	739.749
353.15	5946.09	742.072
353.15	8005.64	744.473
353.15	10091.50	746.834
353.15	12107.60	749.042
353.15	14010.10	751.074
353.15	16061.40	753.214
353.15	18135.50	755.321
353.15	20136.90	757.302
353.15	22100.30	759.195
353.15	24062.40	761.047
353.15	26068.70	762.906
353.15	28075.10	764.73
353.15	30016.50	766.442
373.15	1102.90	715.263
373.15	2003.39	716.613
373.15	4088.27	719.636
373.15	6108.70	722.45
373.15	8075.99	725.091
373.15	10096.50	727.71
373.15	12124.50	730.256
373.15	14043.60	732.583
373.15	16078.20	734.983
373.15	18121.90	737.319
373.15	20098.20	739.516
373.15	22115.70	741.702
373.15	24049.00	743.742
373.15	26068.30	745.822
373.15	28108.40	747.871
373.15	29941.70	749.678
393.15	1102.90	691.923
393.15	2003.62	693.559
393.15	3981.03	697.012
393.15	6085.61	700.514
393.15	8006.06	703.56
393.15	10040.30	706.659
393.15	12072.50	709.623
393.15	14119.40	712.504
393.15	16086.20	715.168
393.15	18080.80	717.782
393.15	19899.60	720.097
393.15	22039.20	722.726
393.15	24041.00	725.121
393.15	26092.40	727.505
393.15	28069.70	729.738
393.15	29851.20	731.71
413.15	1102.62	665.097
413.15	2002.82	667.194
413.15	4113.30	671.781
413.15	6094.15	675.838
413.15	8091.48	679.694
413.15	10043.90	683.283
413.15	11973.10	686.66
413.15	14084.80	690.174
413.15	16052.90	693.316
413.15	18080.20	696.427
413.15	20002.60	699.262
413.15	22068.80	702.204
413.15	24048.90	704.916
413.15	26035.10	707.559
413.15	27915.50	709.988
413.15	30020.80	712.618
433.15	2003.29	636.052
433.15	4004.87	641.895
433.15	6117.66	647.513
433.15	7970.25	652.088
433.15	10076.30	656.927
433.15	12092.50	661.27
433.15	14023.80	665.195
433.15	16095.10	669.184
433.15	17956.10	672.597
433.15	20024.80	676.22
433.15	22076.10	679.658
433.15	23970.50	682.703
433.15	26097.00	685.993
433.15	27970.80	688.786
433.15	29931.20	691.61
453.15	2000.69	597.505
453.15	4003.08	606.126
453.15	5998.33	613.615
453.15	7995.30	620.308
453.15	10006.80	626.429
453.15	12085.80	632.177
453.15	14048.30	637.222
453.15	15953.80	641.798
453.15	17939.00	646.288
453.15	20011.80	650.704
453.15	22018.00	654.751
453.15	24140.40	658.813
453.15	25981.50	662.178
453.15	28126.70	665.939
453.15	30017.40	669.115
473.15	4002.59	562.328
473.15	6007.14	573.872
473.15	8001.41	583.438
473.15	10005.60	591.752
473.15	12008.70	599.085
473.15	14092.60	605.96
473.15	15976.70	611.66
473.15	18013.10	617.325
473.15	20009.60	622.485
473.15	21972.70	627.259
473.15	24020.00	631.94
473.15	25868.10	635.925
473.15	28002.20	640.289
473.15	30014.50	644.229
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
278.15	100.00	801.9
278.15	1000.00	802.7
278.15	5000.00	805.9
278.15	10000.00	809.9
278.15	15000.00	813.6
278.15	20000.00	817.2
278.15	25000.00	820.6
278.15	30000.00	824.0
278.15	35000.00	827.2
278.15	40000.00	830.3
278.15	45000.00	833.3
278.15	50000.00	836.3
278.15	55000.00	839.1
278.15	60000.00	841.8
288.15	100.00	793.4
288.15	1000.00	794.2
288.15	5000.00	797.6
288.15	10000.00	801.8
288.15	15000.00	805.8
288.15	20000.00	809.5
288.15	25000.00	813.1
288.15	30000.00	816.6
288.15	35000.00	819.9
288.15	40000.00	823.1
288.15	45000.00	826.3
288.15	50000.00	829.3
288.15	55000.00	832.3
288.15	60000.00	835.0
298.15	100.00	784.8
298.15	1000.00	785.6
298.15	5000.00	789.3
298.15	10000.00	793.6
298.15	15000.00	797.7
298.15	20000.00	801.7
298.15	25000.00	805.3
298.15	30000.00	809.0
298.15	35000.00	812.5
298.15	40000.00	815.9
298.15	45000.00	819.2
298.15	50000.00	822.3
298.15	55000.00	825.4
298.15	60000.00	828.1
308.15	100.00	776.1
308.15	1000.00	777.0
308.15	5000.00	780.9
308.15	10000.00	785.4
308.15	15000.00	789.7
308.15	20000.00	793.9
308.15	25000.00	797.8
308.15	30000.00	801.5
308.15	35000.00	805.2
308.15	40000.00	808.7
308.15	45000.00	812.0
308.15	50000.00	815.3
308.15	55000.00	818.5
308.15	60000.00	821.4
318.15	100.00	767.4
318.15	1000.00	768.3
318.15	5000.00	772.4
318.15	10000.00	777.2
318.15	15000.00	781.7
318.15	20000.00	786.0
318.15	25000.00	790.1
318.15	30000.00	794.0
318.15	35000.00	797.8
318.15	40000.00	801.4
318.15	45000.00	804.9
318.15	50000.00	808.3
318.15	55000.00	811.6
318.15	60000.00	814.6
328.15	100.00	758.4
328.15	1000.00	759.4
328.15	5000.00	763.7
328.15	10000.00	768.8
328.15	15000.00	773.6
328.15	20000.00	778.1
328.15	25000.00	782.4
328.15	30000.00	786.5
328.15	35000.00	790.4
328.15	40000.00	794.2
328.15	45000.00	797.8
328.15	50000.00	801.3
328.15	55000.00	804.7
328.15	60000.00	807.8
338.15	100.00	749.1
338.15	1000.00	750.2
338.15	5000.00	754.8
338.15	10000.00	760.1
338.15	15000.00	765.2
338.15	20000.00	769.9
338.15	25000.00	774.4
338.15	30000.00	778.7
338.15	35000.00	782.8
338.15	40000.00	786.7
338.15	45000.00	790.5
338.15	50000.00	794.1
338.15	55000.00	797.7
338.15	60000.00	800.8
348.15	100.00	739.5
348.15	1000.00	740.7
348.15	5000.00	745.6
348.15	10000.00	751.3
348.15	15000.00	756.6
348.15	20000.00	761.6
348.15	25000.00	766.4
348.15	30000.00	770.8
348.15	35000.00	775.1
348.15	40000.00	779.2
348.15	45000.00	783.1
348.15	50000.00	786.9
348.15	55000.00	790.5
348.15	60000.00	793.8
358.15	100.00	729.5
358.15	1000.00	730.7
358.15	5000.00	736.0
358.15	10000.00	742.1
358.15	15000.00	747.7
358.15	20000.00	753.0
358.15	25000.00	758.0
358.15	30000.00	762.8
358.15	35000.00	767.2
358.15	40000.00	771.5
358.15	45000.00	775.6
358.15	50000.00	779.5
358.15	55000.00	783.3
358.15	60000.00	786.7
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
273.15	100.00	806.6
273.15	1000.00	807.3
273.15	2000.00	808.1
273.15	5000.00	810.4
273.15	10000.00	814.1
273.15	15000.00	817.6
273.15	20000.00	821.0
273.15	30000.00	827.4
273.15	40000.00	833.4
273.15	50000.00	839.1
273.15	60000.00	844.4
273.15	70000.00	849.6
293.15	100.00	789.5
293.15	1000.00	790.4
293.15	2000.00	791.3
293.15	5000.00	793.8
293.15	10000.00	797.9
293.15	15000.00	801.8
293.15	20000.00	805.5
293.15	30000.00	812.5
293.15	40000.00	818.9
293.15	50000.00	825.0
293.15	60000.00	830.9
293.15	70000.00	836.2
313.15	100.00	772.2
313.15	1000.00	773.0
313.15	2000.00	774.0
313.15	5000.00	776.9
313.15	10000.00	781.4
313.15	15000.00	785.7
313.15	20000.00	789.7
313.15	30000.00	797.4
313.15	40000.00	804.4
313.15	50000.00	810.9
313.15	60000.00	817.1
313.15	70000.00	822.8
333.15	100.00	754.3
333.15	1000.00	755.3
333.15	2000.00	756.4
333.15	5000.00	759.7
333.15	10000.00	764.7
333.15	15000.00	769.4
333.15	20000.00	773.9
333.15	30000.00	782.3
333.15	40000.00	789.9
333.15	50000.00	797.0
333.15	60000.00	803.6
333.15	70000.00	809.7
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
303.20	1000.00	782.2
303.20	2000.00	783.1
303.20	3000.00	784.0
303.20	4000.00	784.8
303.20	5000.00	785.7
303.20	6000.00	786.5
303.20	7000.00	787.5
303.20	8000.00	788.3
303.20	9000.00	789.2
303.20	10000.00	790.1
323.20	1000.00	763.2
323.20	2000.00	764.3
323.20	3000.00	765.3
323.20	4000.00	766.4
323.20	5000.00	767.4
323.20	6000.00	768.4
323.20	7000.00	769.3
323.20	8000.00	770.3
323.20	9000.00	771.3
323.20	10000.00	772.3
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
283.15	101.00	797.99
298.15	101.00	785.2
313.15	101.00	772.15
328.15	101.00	758.71
283.15	20000.00	813.3
283.15	25000.00	816.8
283.15	30000.00	820.2
283.15	35000.00	823.4
283.15	40000.00	826.6
298.15	20000.00	801.7
298.15	25000.00	805.4
298.15	30000.00	809.0
298.15	35000.00	812.5
298.15	40000.00	815.8
313.15	20000.00	790.1
313.15	25000.00	794.1
313.15	30000.00	797.8
313.15	35000.00	801.5
313.15	40000.00	805.0
328.15	20000.00	778.1
328.15	25000.00	782.4
328.15	30000.00	786.4
328.15	35000.00	790.3
328.15	40000.00	794.1
Reference

Fixed		Measured
Pressure, kPa - Liquid	Temperature, K - Liquid	Mass density, kg/m3 - Liquid
100.00	298.20	785.07
Reference

Fixed		Measured
Pressure, kPa - Liquid	Temperature, K - Liquid	Mass density, kg/m3 - Liquid
101.80	298.15	785.07
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
298.15	100.00	785.2
Reference

Fixed		Measured
Pressure, kPa - Liquid	Temperature, K - Liquid	Mass density, kg/m3 - Liquid
91.20	303.15	781.0
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
303.15	101.00	780.83
313.15	101.00	772.1
323.15	101.00	763.22
288.15	100.00	793.7
288.15	1000.00	794.4
288.15	5000.00	797.6
288.15	10000.00	801.5
288.15	15000.00	805.3
288.15	20000.00	808.9
288.15	25000.00	812.4
288.15	30000.00	815.7
288.15	35000.00	819.0
288.15	40000.00	822.1
288.15	45000.00	825.1
288.15	50000.00	828.0
288.15	55000.00	830.7
288.15	60000.00	833.3
293.15	100.00	789.4
293.15	1000.00	790.2
293.15	5000.00	793.5
293.15	10000.00	797.4
293.15	15000.00	801.3
293.15	20000.00	805.0
293.15	25000.00	808.6
293.15	30000.00	812.0
293.15	35000.00	815.3
293.15	40000.00	818.5
293.15	45000.00	821.5
293.15	50000.00	824.5
293.15	55000.00	827.2
293.15	60000.00	829.9
298.15	100.00	785.2
298.15	1000.00	785.9
298.15	5000.00	789.3
298.15	10000.00	793.4
298.15	15000.00	797.3
298.15	20000.00	801.1
298.15	25000.00	804.8
298.15	30000.00	808.3
298.15	35000.00	811.7
298.15	40000.00	814.9
298.15	45000.00	818.0
298.15	50000.00	821.0
298.15	55000.00	823.8
298.15	60000.00	826.5
303.15	100.00	780.9
303.15	1000.00	781.6
303.15	5000.00	785.1
303.15	10000.00	789.3
303.15	15000.00	793.3
303.15	20000.00	797.2
303.15	25000.00	801.0
303.15	30000.00	804.6
303.15	35000.00	808.0
303.15	40000.00	811.3
303.15	45000.00	814.5
303.15	50000.00	817.5
303.15	55000.00	820.3
303.15	60000.00	823.1
308.15	100.00	776.5
308.15	1000.00	777.3
308.15	5000.00	780.9
308.15	10000.00	785.2
308.15	15000.00	789.3
308.15	20000.00	793.3
308.15	25000.00	797.1
308.15	30000.00	800.8
308.15	35000.00	804.3
308.15	40000.00	807.7
308.15	45000.00	810.9
308.15	50000.00	814.0
308.15	55000.00	816.9
308.15	60000.00	819.6
313.15	100.00	772.1
313.15	1000.00	773.0
313.15	5000.00	776.6
313.15	10000.00	781.0
313.15	15000.00	785.3
313.15	20000.00	789.4
313.15	25000.00	793.3
313.15	30000.00	797.0
313.15	35000.00	800.6
313.15	40000.00	804.1
313.15	45000.00	807.4
313.15	50000.00	810.5
313.15	55000.00	813.4
313.15	60000.00	816.2
318.15	100.00	767.7
318.15	1000.00	768.5
318.15	5000.00	772.3
318.15	10000.00	776.8
318.15	15000.00	781.2
318.15	20000.00	785.4
318.15	25000.00	789.4
318.15	30000.00	793.2
318.15	35000.00	796.9
318.15	40000.00	800.4
318.15	45000.00	803.8
318.15	50000.00	806.9
318.15	55000.00	809.9
318.15	60000.00	812.8
323.15	100.00	763.2
323.15	1000.00	764.1
323.15	5000.00	768.0
323.15	10000.00	772.6
323.15	15000.00	777.1
323.15	20000.00	781.4
323.15	25000.00	785.5
323.15	30000.00	789.4
323.15	35000.00	793.2
323.15	40000.00	796.8
323.15	45000.00	800.2
323.15	50000.00	803.4
323.15	55000.00	806.5
323.15	60000.00	809.3
328.15	100.00	758.7
328.15	1000.00	759.6
328.15	5000.00	763.6
328.15	10000.00	768.3
328.15	15000.00	772.9
328.15	20000.00	777.3
328.15	25000.00	781.6
328.15	30000.00	785.6
328.15	35000.00	789.5
328.15	40000.00	793.1
328.15	45000.00	796.6
328.15	50000.00	799.9
328.15	55000.00	803.0
328.15	60000.00	805.9
333.15	100.00	754.1
333.15	1000.00	755.0
333.15	5000.00	759.1
333.15	10000.00	764.0
333.15	15000.00	768.8
333.15	20000.00	773.3
333.15	25000.00	777.6
333.15	30000.00	781.7
333.15	35000.00	785.7
333.15	40000.00	789.4
333.15	45000.00	792.9
333.15	50000.00	796.3
333.15	55000.00	799.4
333.15	60000.00	802.4
343.15	100.00	744.6
343.15	1000.00	745.6
343.15	5000.00	750.0
343.15	10000.00	755.2
343.15	15000.00	760.2
343.15	20000.00	765.0
343.15	25000.00	769.6
343.15	30000.00	773.9
343.15	35000.00	778.0
343.15	40000.00	781.9
343.15	45000.00	785.6
343.15	50000.00	789.1
343.15	55000.00	792.3
343.15	60000.00	795.3
353.15	1000.00	736.0
353.15	5000.00	740.6
353.15	10000.00	746.2
353.15	15000.00	751.5
353.15	20000.00	756.5
353.15	25000.00	761.3
353.15	30000.00	765.9
353.15	35000.00	770.2
353.15	40000.00	774.3
353.15	45000.00	778.1
353.15	50000.00	781.7
353.15	55000.00	785.1
353.15	60000.00	788.2
363.15	1000.00	725.9
363.15	5000.00	730.8
363.15	10000.00	736.7
363.15	15000.00	742.4
363.15	20000.00	747.7
363.15	25000.00	752.8
363.15	30000.00	757.7
363.15	35000.00	762.2
363.15	40000.00	766.5
363.15	45000.00	770.5
363.15	50000.00	774.3
363.15	55000.00	777.7
363.15	60000.00	780.9
373.15	1000.00	715.3
373.15	5000.00	720.6
373.15	10000.00	727.0
373.15	15000.00	733.0
373.15	20000.00	738.7
373.15	25000.00	744.2
373.15	30000.00	749.3
373.15	35000.00	754.1
373.15	40000.00	758.6
373.15	45000.00	762.8
373.15	50000.00	766.7
373.15	55000.00	770.2
373.15	60000.00	773.5
393.15	1000.00	692.2
393.15	5000.00	698.4
393.15	10000.00	705.8
393.15	15000.00	712.8
393.15	20000.00	719.4
393.15	25000.00	725.6
393.15	30000.00	731.4
393.15	35000.00	736.8
393.15	40000.00	741.8
393.15	45000.00	746.4
393.15	50000.00	750.7
393.15	55000.00	754.5
393.15	60000.00	757.9
413.15	1000.00	666.3
413.15	5000.00	673.6
413.15	10000.00	682.3
413.15	15000.00	690.5
413.15	20000.00	698.1
413.15	25000.00	705.3
413.15	30000.00	712.0
413.15	35000.00	718.2
413.15	40000.00	723.8
413.15	45000.00	729.0
413.15	50000.00	733.7
413.15	55000.00	737.9
413.15	60000.00	741.5
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
298.15	100.00	785.16
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
288.15	100.00	794.39
288.15	5000.00	798.18
288.15	10000.00	802.2
288.15	15000.00	806.02
288.15	20000.00	809.69
288.15	25000.00	812.95
288.15	30000.00	816.23
288.15	35000.00	819.12
288.15	40000.00	822.29
293.15	100.00	789.87
293.15	5000.00	793.83
293.15	10000.00	797.88
293.15	15000.00	801.84
293.15	20000.00	805.45
293.15	25000.00	809.12
293.15	30000.00	812.52
293.15	35000.00	815.8
293.15	40000.00	818.81
298.15	100.00	785.59
298.15	5000.00	789.72
298.15	10000.00	793.76
298.15	15000.00	797.75
298.15	20000.00	801.4
298.15	25000.00	805.07
298.15	30000.00	808.47
298.15	35000.00	811.58
298.15	40000.00	815.03
303.15	100.00	781.19
303.15	5000.00	785.47
303.15	10000.00	789.66
303.15	15000.00	793.71
303.15	20000.00	797.54
303.15	25000.00	801.26
303.15	30000.00	804.81
303.15	35000.00	808.29
303.15	40000.00	811.43
308.15	100.00	776.6
308.15	5000.00	780.98
308.15	10000.00	785.42
308.15	15000.00	789.62
308.15	20000.00	793.63
308.15	25000.00	797.42
308.15	30000.00	801.06
308.15	35000.00	804.6
308.15	40000.00	808.06
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
298.15	1022.00	785.87
298.15	3922.00	788.69
298.15	8793.00	792.53
298.15	12491.00	795.7
298.15	17711.00	799.91
298.15	21982.00	802.87
298.15	24097.00	804.5
298.15	26940.00	806.36
298.15	29139.00	807.89
323.16	626.00	763.659
323.15	3237.00	766.361
323.15	9248.00	772.358
323.15	12839.00	775.758
323.16	15104.00	777.664
323.15	18790.00	780.78
323.15	23256.00	784.532
323.15	25042.00	786.147
323.15	27936.00	788.458
333.28	909.00	754.25
333.28	1891.00	756.361
333.28	5093.00	758.805
333.28	9067.00	762.841
333.28	12887.00	766.568
333.27	16623.00	770.196
333.28	22108.00	775.145
333.28	25690.00	777.944
333.28	29272.00	780.933
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
298.15	81.50	785.12
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
298.15	100.00	785.1
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
293.15	100.00	788.94
293.15	5000.00	793.35
293.15	10000.00	797.51
293.15	15000.00	801.44
293.15	20000.00	805.18
293.15	25000.00	808.74
293.15	30000.00	812.17
293.15	35000.00	815.49
303.15	100.00	780.83
303.15	5000.00	785.54
303.15	10000.00	789.89
303.15	15000.00	793.92
303.15	20000.00	797.7
303.15	25000.00	801.28
303.15	30000.00	804.72
303.15	35000.00	808.06
313.15	100.00	772.04
313.15	5000.00	776.85
313.15	10000.00	781.35
313.15	15000.00	785.59
313.15	20000.00	789.62
313.15	25000.00	793.47
313.15	30000.00	797.2
313.15	35000.00	800.84
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
283.15	100.00	797.7
283.15	5000.00	801.8
283.15	10000.00	805.6
283.15	15000.00	809.6
283.15	20000.00	813.1
298.15	100.00	784.9
298.15	5000.00	789.3
298.15	10000.00	793.6
298.15	15000.00	797.7
298.15	20000.00	801.6
313.15	100.00	771.9
313.15	5000.00	776.8
313.15	10000.00	781.3
313.15	15000.00	785.7
313.15	20000.00	789.9
328.15	100.00	758.6
328.15	5000.00	763.8
328.15	10000.00	768.9
328.15	15000.00	773.6
328.15	20000.00	778.1
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
283.15	100.00	797.9
283.15	5000.00	802.0
283.15	10000.00	805.9
283.15	15000.00	809.7
283.15	20000.00	813.4
298.15	100.00	784.9
298.15	5000.00	789.3
298.15	10000.00	793.7
298.15	15000.00	797.8
298.15	20000.00	801.5
313.15	100.00	772.0
313.15	5000.00	777.0
313.15	10000.00	781.5
313.15	15000.00	786.0
313.15	20000.00	790.1
Reference

Fixed		Measured
Pressure, kPa - Liquid	Temperature, K - Liquid	Mass density, kg/m3 - Liquid
200.00	313.15	770.0
200.00	353.15	734.0
600.00	313.15	770.0
600.00	353.15	734.0
600.00	393.15	691.0
1000.00	313.15	770.0
1000.00	353.15	735.0
1000.00	393.15	692.0
1400.00	313.15	771.0
1400.00	353.15	735.0
1400.00	393.15	693.0
1400.00	433.15	638.0
1800.00	313.15	771.0
1800.00	353.15	736.0
1800.00	393.15	694.0
1800.00	433.15	639.0
2000.00	313.15	772.0
2000.00	353.15	738.0
2000.00	393.15	694.0
2000.00	433.15	639.0
Reference

Fixed		Measured
Pressure, kPa - Liquid	Temperature, K - Liquid	Mass density, kg/m3 - Liquid
100.00	283.15	797.76
100.00	288.15	793.65
100.00	293.15	789.19
100.00	298.15	784.92
100.00	303.15	780.63
100.00	308.15	776.26
100.00	313.15	771.91
100.00	318.15	767.58
100.00	323.15	763.09
100.00	328.15	758.54
100.00	333.15	753.96
100.00	338.15	749.42
100.00	343.15	744.74
2500.00	283.15	799.74
2500.00	288.15	795.66
2500.00	293.15	791.25
2500.00	298.15	787.03
2500.00	303.15	782.81
2500.00	308.15	778.54
2500.00	313.15	774.26
2500.00	318.15	769.99
2500.00	323.15	765.56
2500.00	328.15	761.09
2500.00	333.15	756.61
2500.00	338.15	752.16
2500.00	343.15	747.57
5000.00	283.15	801.73
5000.00	288.15	797.73
5000.00	293.15	793.37
5000.00	298.15	789.21
5000.00	303.15	785.04
5000.00	308.15	780.82
5000.00	313.15	776.62
5000.00	318.15	772.41
5000.00	323.15	768.08
5000.00	328.15	763.7
5000.00	333.15	759.27
5000.00	338.15	754.89
5000.00	343.15	750.39
10000.00	283.15	805.58
10000.00	288.15	801.67
10000.00	293.15	797.42
10000.00	298.15	793.38
10000.00	303.15	789.3
10000.00	308.15	785.22
10000.00	313.15	781.13
10000.00	318.15	777.04
10000.00	323.15	772.84
10000.00	328.15	768.58
10000.00	333.15	764.32
10000.00	338.15	760.09
10000.00	343.15	755.74
15000.00	283.15	809.28
15000.00	288.15	805.43
15000.00	293.15	801.3
15000.00	298.15	797.34
15000.00	303.15	793.37
15000.00	308.15	789.37
15000.00	313.15	785.4
15000.00	318.15	781.43
15000.00	323.15	777.34
15000.00	328.15	773.22
15000.00	333.15	769.08
15000.00	338.15	764.99
15000.00	343.15	760.75
20000.00	283.15	812.8
20000.00	288.15	809.06
20000.00	293.15	804.99
20000.00	298.15	801.11
20000.00	303.15	797.25
20000.00	308.15	793.34
20000.00	313.15	789.45
20000.00	318.15	785.59
20000.00	323.15	781.59
20000.00	328.15	777.57
20000.00	333.15	773.56
20000.00	338.15	769.59
20000.00	343.15	765.47
25000.00	283.15	816.2
25000.00	288.15	812.52
25000.00	293.15	808.53
25000.00	298.15	804.75
25000.00	303.15	800.93
25000.00	308.15	797.14
25000.00	313.15	793.33
25000.00	318.15	789.55
25000.00	323.15	785.65
25000.00	328.15	781.73
25000.00	333.15	777.81
25000.00	338.15	773.96
25000.00	343.15	769.94
30000.00	283.15	819.47
30000.00	288.15	815.87
30000.00	293.15	811.94
30000.00	298.15	808.21
30000.00	303.15	804.49
30000.00	308.15	800.76
30000.00	313.15	797.04
30000.00	318.15	793.36
30000.00	323.15	789.53
30000.00	328.15	785.7
30000.00	333.15	781.87
30000.00	338.15	778.09
30000.00	343.15	774.17
35000.00	283.15	822.63
35000.00	288.15	819.04
35000.00	293.15	815.23
35000.00	298.15	811.58
35000.00	303.15	807.95
35000.00	308.15	804.27
35000.00	313.15	800.61
35000.00	318.15	796.98
35000.00	323.15	793.24
35000.00	328.15	789.5
35000.00	333.15	785.76
35000.00	338.15	782.06
35000.00	343.15	778.23
Reference

Speed of sound, m/s

Operational condition: Frequency, MHz = 8 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Speed of sound, m/s - Liquid
253.15	101.00	1304.806
253.15	4988.00	1329.862
253.15	10126.00	1355.145
253.15	15056.00	1378.442
253.15	19988.00	1400.85
253.15	25051.00	1423.022
253.15	30366.00	1445.462
273.15	101.00	1230.416
273.15	5095.00	1258.487
273.15	10288.00	1286.113
273.15	15102.00	1310.574
273.15	19986.00	1334.356
273.15	25007.00	1357.867
273.15	30061.00	1380.605
293.15	101.00	1159.797
293.15	5052.00	1190.031
293.15	9984.00	1218.487
293.15	15097.00	1246.444
293.15	20038.00	1272.2
293.15	25073.00	1297.301
293.15	30034.00	1321.027
313.15	101.00	1091.63
313.15	5015.00	1124.396
313.15	10081.00	1155.978
313.15	15057.00	1185.269
313.15	20137.00	1213.592
313.15	25255.00	1240.699
313.15	30161.00	1265.527
333.15	101.00	1024.883
333.15	5287.00	1062.52
333.15	10309.00	1096.396
333.15	15132.00	1126.884
333.15	20140.00	1156.744
333.15	25071.00	1184.629
333.15	30117.00	1211.744
353.15	110.00	957.67
353.15	5428.00	1000.125
353.15	10327.00	1036.103
353.15	15492.00	1071.331
353.15	20337.00	1102.27
353.15	25296.00	1132.12
353.15	29944.00	1158.638
Reference

Operational condition: Frequency, MHz = 2 (Liquid)

Fixed		Measured
Pressure, kPa - Liquid	Temperature, K - Liquid	Speed of sound, m/s - Liquid
1410.00	323.31	1070.65
5245.00	323.31	1096.75
11101.00	323.31	1135.02
17687.00	323.31	1174.47
23114.00	323.31	1204.23
30237.00	323.31	1241.91
36831.00	323.31	1274.55
43809.00	323.31	1306.05
50864.00	323.31	1337.26
58500.00	323.31	1369.4
62862.00	323.31	1386.24
1446.00	347.10	991.29
4092.00	347.10	1011.79
7163.00	347.10	1035.01
14616.00	347.10	1085.64
21177.00	347.10	1126.37
28408.00	347.10	1168.14
35022.00	347.10	1203.39
42067.00	347.10	1238.63
48843.00	347.10	1270.33
54137.00	347.10	1294.14
58348.00	347.10	1312.64
62859.00	347.10	1331.57
1432.00	369.38	914.53
3923.00	369.38	936.5
7109.00	369.38	963.26
11382.00	369.38	996.24
19601.00	369.38	1053.82
27704.00	369.38	1104.72
33060.00	369.38	1135.35
41165.00	369.38	1179.11
49420.00	369.38	1220.33
54796.00	369.38	1246.14
58367.00	369.38	1261.46
65148.00	369.38	1291.23
1546.00	397.28	811.26
4302.00	397.28	840.39
7333.00	397.28	870.18
12482.00	397.28	915.79
18105.00	397.28	960.62
24432.00	397.28	1006.22
29996.00	397.28	1043.31
36074.00	397.28	1080.66
44752.00	397.28	1129.46
49805.00	397.28	1156.02
58415.00	397.28	1198.58
63790.00	397.28	1223.51
1514.00	422.90	701.53
5675.00	422.90	755.36
9530.00	422.90	798.44
15206.00	422.90	853.77
23492.00	422.90	923.37
31793.00	422.90	984.06
38446.00	422.90	1027.65
47571.00	422.90	1081.97
53132.00	422.90	1112.23
58734.00	422.90	1141.24
63754.00	422.90	1166.21
Reference

Fixed		Measured
Pressure, kPa - Liquid	Temperature, K - Liquid	Speed of sound, m/s - Liquid
30113.50	253.22	1444.78
24920.60	253.22	1422.9
20403.40	253.22	1402.94
15229.30	253.22	1379.41
10245.90	253.22	1355.82
5283.40	253.22	1331.49
104.20	253.22	1304.82
30202.90	273.20	1381.57
25221.00	273.20	1359.31
20253.00	273.20	1336.04
15284.40	273.20	1311.72
10100.10	273.20	1285.41
5193.30	273.20	1259.26
99.90	273.20	1230.84
30068.80	293.20	1321.4
25256.40	293.20	1298.55
20222.10	293.20	1273.42
15196.90	293.20	1247.21
10367.90	293.20	1220.84
5339.40	293.20	1191.95
103.70	293.20	1160.02
30383.60	313.21	1266.85
25383.20	313.21	1241.6
20316.70	313.21	1214.8
15237.90	313.21	1186.56
10351.10	313.21	1157.83
5318.60	313.21	1126.47
103.80	313.21	1091.91
30214.10	333.21	1212.32
25377.10	333.21	1186.4
20181.30	333.21	1157.08
15294.30	333.21	1127.88
10228.40	333.21	1095.91
5212.70	333.21	1062.1
104.10	333.21	1024.91
30289.00	353.21	1160.47
25249.80	353.21	1131.76
20272.60	353.21	1101.73
15210.90	353.21	1069.36
10319.20	353.21	1035.89
5006.00	353.21	996.7611
103.50	353.20	957.7319
30052.00	253.23	1444.46
25022.30	253.22	1423.58
19990.70	253.22	1401.38
15106.20	253.22	1379.06
10111.90	253.22	1355.38
5018.80	253.22	1330.44
130.20	253.22	1305.11
30338.50	273.21	1382.25
25058.50	273.20	1358.75
20069.80	273.21	1335.23
15029.40	273.21	1310.76
10148.20	273.21	1285.83
5026.60	273.21	1258.54
128.60	273.21	1231.07
30268.10	293.21	1322.46
25034.40	293.21	1297.52
20101.40	293.21	1272.93
15051.60	293.21	1246.58
9977.30	293.21	1218.73
5169.00	293.21	1191.02
140.00	293.21	1160.43
30116.20	313.21	1265.63
25162.60	313.21	1240.51
20051.60	313.21	1213.46
14993.30	313.21	1185.13
10011.10	313.21	1155.8
5023.30	313.21	1124.67
121.80	313.21	1092.27
30028.40	333.21	1211.35
24959.30	333.21	1184.2
19953.80	333.21	1155.86
15024.90	333.21	1126.4
10089.60	333.21	1095.04
5087.60	333.21	1061.23
137.30	333.21	1025.23
30102.10	353.21	1159.45
25007.10	353.21	1130.47
20108.20	353.21	1100.89
15035.00	353.21	1068.32
10088.80	353.21	1034.43
5137.50	353.21	997.7471
132.10	353.21	957.5929
Reference

Molar volume, m3/mol

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Molar volume, m3/mol - Liquid
298.15	100.00	0.0001
298.15	10000.00	0.0001
313.15	100.00	0.0001
313.15	10000.00	0.0001
328.15	100.00	0.0001
328.15	10000.00	0.0001
Reference

Correlations

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 6101.25]	kPa	[268.00; 513.90]	The Yaw...
Equation			ln(Pvp) = A + B/(T + C)
Coefficient A			1.67022e+01
Coefficient B			-3.82430e+03
Coefficient C			-3.50190e+01
Temperature range, min.			268.00
Temperature range, max.			513.90
Pvap	1.33	kPa	268.00	Calculated Property
Pvap	7.47	kPa	295.32	Calculated Property
Pvap	30.15	kPa	322.64	Calculated Property
Pvap	95.54	kPa	349.97	Calculated Property
Pvap	251.85	kPa	377.29	Calculated Property
Pvap	575.25	kPa	404.61	Calculated Property
Pvap	1172.72	kPa	431.93	Calculated Property
Pvap	2181.16	kPa	459.26	Calculated Property
Pvap	3763.30	kPa	486.58	Calculated Property
Pvap	6101.25	kPa	513.90	Calculated Property
Pvap	[7.15e-07; 6251.05]	kPa	[159.05; 516.25]	KDB Vap...
Equation			ln(Pvp) = A + B/T + C*ln(T) + D*T^2
Coefficient A			5.31703e+01
Coefficient B			-6.60645e+03
Coefficient C			-5.08941e+00
Coefficient D			5.95405e-07
Temperature range, min.			159.05
Temperature range, max.			516.25
Pvap	7.15e-07	kPa	159.05	Calculated Property
Pvap	9.29e-04	kPa	198.74	Calculated Property
Pvap	0.09	kPa	238.43	Calculated Property
Pvap	2.27	kPa	278.12	Calculated Property
Pvap	22.65	kPa	317.81	Calculated Property
Pvap	127.14	kPa	357.49	Calculated Property
Pvap	480.06	kPa	397.18	Calculated Property
Pvap	1366.46	kPa	436.87	Calculated Property
Pvap	3160.27	kPa	476.56	Calculated Property
Pvap	6251.05	kPa	516.25	Calculated Property

Similar Compounds

Find more compounds similar to Ethanol.

Mixtures

• Toluene + Ethanol
• Ethanol + 2-Butanone, 4-(4-hydroxyphenyl)- + Water
• Ethanol + 2-Butanone, 4-(4-hydroxyphenyl)-
• Ethanol + Water
• Ethanol + Acetone
• Ethanol + Pentane, 2,2,4-trimethyl-
• Ethanol + Acetone + Pentane, 2,2,4-trimethyl-
• Ethanol + Propanoic acid, 2-hydroxy-, ethyl ester
• Ethanol + Isobutane
• Ethanol + Butane, 2-ethoxy-2-methyl-
• Ethanol + Butane, 2-ethoxy-2-methyl- + Water
• Ethanol + Oxygen
• Nitrogen + Ethanol
• Methane + Ethanol
• Carbon dioxide + Ethanol
• Ethanol + Piperazine, 1-methyl-
• Ethanol + Ethyl Acetate
• n-Hexane + Ethanol
• Ethanol + Triethylamine
• n-Hexane + Ethanol + Triethylamine

Find more mixtures with Ethanol.

Sources

• KDB Pure (Korean Thermophysical Properties Databank)
• KDB Vapor Pressure Data
• Crippen Method
• Dortmund Data Bank Vapor-Liquid Equilibrium Data
• High-Pressure Viscosity Measurements for the Ethanol + Toluene Binary System
• Densities and Excess, Apparent, and Partial Molar Volumes of Binary Mixtures of BMIMBF4 + Ethanol as a Function of Temperature, Pressure, and Concentration
• Solubility of Baicalein in Different Solvents from (287 to 323) K
• The Precise Measurement of Vapor Liquid Equilibrium Properties of the CO2/Isopentane Binary Mixture, and Fitted Parameters for a Helmholtz Energy Mixture Model
• Solubility Determination and Modeling and Dissolution Thermodynamic Properties of Raspberry Ketone in Binary Solvent Mixtures of Ethanol andWater
• CO2 Solubility in Physicochemical Absorbent: Dibutyl Ether/N-Methylethanolamine/Ethanol
• Vapor liquid equilibrium in systems (water + organic solvent + salt) at low water concentrations but high ratios of salt to water: experimental results and modeling
• Solubility of thiopene in carbon dioxide and carbon dioxide + 1-propanol mixtures at temperatures from 313 to 363K
• Volumetric properties of ethanol-water mixtures under high temperatures and pressures
• Vapor pressures and apparent molal volumes of the solutions of ZnCl2 in ethanol at 298.15 K
• Measurement and correlation of vapor liquid equilibria of binary systems containing the ionic liquids [EMIM][(CF3SO2)2N], [BMIM][(CF3SO2)2N], [MMIM][(CH3)2PO4] and oxygenated organic compounds respectively water
• Apparent molal volumes of the solutions of CaCl2 and Ca(NO3)2 in ethanol at 298.15: experimental data and correlation by local composition models
• Isobaric vapor liquid equilibria for mixtures of acetone, ethanol, and 2,2,4-trimethylpentane at 101.3 kPa
• Vapor liquid equilibria and excess volumes of the binary systems ethanol + ethyl lactate, isopropanol + isopropyl lactate and n-butanol + n-butyl lactate at 101.325 kPa
• Vapour liquid equilibrium for the 2-methylpropane + methanol, +ethanol, +2-propanol, +2-butanol and +2-methyl-2-propanol systems at 313.15K
• Isobaric vapor liquid equilibria for systems composed by 2-ethoxy-2-methylbutane, methanol or ethanol and water at 101.32 kPa
• Establishing benchmarks for the Second Industrial Fluids Simulation Challenge
• Determination of activity coefficients at infinite dilution of organic solutes in the ionic liquid, trihexyl(tetradecyl)-phosphonium tris(pentafluoroethyl) trifluorophosphate, by gas liquid chromatography
• Viscosities and densities for binary mixtures of N-methylpiperazine with methanol, ethanol, n-propanol, iso-propanol, n-butanol and iso-butanol at 293.15, 298.15 and 303.15K
• Vapor liquid equilibria of carbon dioxide with isopropyl acetate, diethyl carbonate and ethyl butyrate at elevated pressures
• Prediction and experimental verification of the effect of salt on the vapour liquid equilibrium of ethanol/1-propanol/water mixture
• Density, viscosity, refractive index and electrical conductivity of saturated solutions of the lithium hydroxide + ethanol +water system at 298.15 K, and thermodynamic description of the solid liquid equilibrium
• Volumetric properties under pressure for the binary system ethanol + toluene
• The influence of temperature on the liquid liquid solid equilibria of the ternary system water + ethanol + 1-dodecanol
• Thermodynamic properties of mixtures containing ionic liquids Vapor pressures and activity coefficients of n-alcohols and benzene in binary mixtures with 1-methyl-3-butyl-imidazolium bis(trifluoromethyl-sulfonyl) imide
• Vapor liquid equilibria for the quaternary reactive system ethyl acetate + ethanol +water + acetic acid and some of the constituent binary systems at 101.3 kPa
• Isobaric vapor liquid and vapor liquid liquid equilibrium data for the system water + ethanol + cyclohexane
• Excess molar volumes and excess molar enthalpies of binary and ternary mixtures of (ethanol or 1-butanol), triethylamine and n-hexane
• Solubility of aspirin in supercritical carbon dioxide/alcohol mixtures
• Vapour liquid equilibrium of carboxylic acid systems: Propionic acid + valeric acid and isobutyric acid + valeric acid
• Enhancement of liquid phase splitting of water + ethanol + ethyl acetate mixtures in the presence of a hydrophilic agent or an electrolyte substance
• Measurement of infinite dilution activity coefficients of 1-alkanols (C1 C5) in water as a function of temperature (273 373 K)
• Enhancement of the anthracene aqueous solubility by a synergistic effect of alcohols and beta-cyclodextrin
• Measurement and modelling of urea solubility in supercritical CO2 and CO2 + ethanol mixtures
• Liquid liquid equlibria of the mixture linalool + ethanol +water at different temperatures
• Effect of temperature on the excess molar volumes of some alcohol + aromatic mixtures and modelling by cubic EOS mixing rules
• Effect of anion fluorination in 1-ethyl-3-methylimidazolium as solvent for the liquid extraction of ethanol from ethyl tert-butyl ether
• Vapor liquid equilibria for the ternary system of carbon dioxide + ethanol + ethyl acetate at elevated pressures
• Isobaric vapor liquid equilibria for ethanol water system containing different ionic liquids at atmospheric pressure
• Liquid liquid equilibrium data for water + ethanol + trans-decalin: Measurement and predication
• Comparative experimental and modeling studies of the viscosity behavior of ethanol +C7 hydrocarbon mixtures versus pressure and temperature
• Solubility of disperse dyes in supercritical carbon dioxide and ethanol
• Vapor pressures of lithium bromide or lithium chloride and ethanol solutions
• Viscous synergy and antagonism and isentropic compressibility of ternary mixtures containing 1,3-dioxolane, water and monoalkanols at 303.15K
• Activity coefficients of the binary mixtures of a-cresol or p-cresol with C l-C4 aliphatic alcohols near ambient pressure
• Excess enthalpies of binary mixtures of 2-ethoxyethanol with four hydrocarbons at 298.15, 308.15, and 318.15K An experimental and theoretical study
• Solubility of carbon dioxide in binary and ternary mixtures with ethanol and water
• Vapor pressure measurement for binary and ternary systems containing a phosphoric ionic liquid
• Vapor liquid equilibria for binary and ternary mixtures of diisopropyl ether, ethanol, and 2,2,4-trimethylpentane at 101.3 kPa
• Vapour liquid liquid and vapour liquid equilibrium of the system water + ethanol + heptane at 101.3 kPa
• Excess Gibbs energies of selected binary mixtures formed by N,N-dimethyl formamide at 95.5 kPa
• (Liquid + liquid) equilibria for the quaternary system water + methyl tert-butyl ether + ethanol + benzene at 303.15K
• Volumetric properties of the ternary system ethanol + chloroform + benzene at temperature range (288.15 313.15) K: Experimental data, correlation and prediction by cubic EOS
• Experimental isobaric vapour liquid liquid equilibrium data for the quaternary systems water (1) ethanol (2) acetone (3) n-butyl acetate (4) and water (1) ethanol (2) acetone (3) methyl ethyl ketone (4) and their partially miscible-constituent ternaries
• Measurement and modelling of the ternary phase equilibria for high pressure carbon dioxide ethanol water mixtures
• Isobaric vapor liquid equilibria of 1,1-dimethylethoxy-butane + methanol or ethanol +water at 101.32 kPa
• Liquid liquid equilibria of 1,3-dimethylimidazolium methyl sulfate with ketones, dialkyl carbonates and acetates
• Study of the behaviour of the azeotropic mixture ethanol water with imidazolium-based ionic liquids
• Vapor pressure measurement for water, methanol, ethanol, and their binary mixtures in the presence of an ionic liquid 1-ethyl-3-methylimidazolium dimethylphosphate
• Isobaric vapor liquid and vapor liquid liquid equilibrium data for the water ethanol hexane system
• Liquid liquid equilibria for binary systems of tert-amyl ethyl ether (TAEE), isopropyl tert-butyl ether (IPTBE) and di-sec-butyl ether (DSBE) with water and for ternary systems with methanol or ethanol
• Volumetric properties of the boldine + alcohol mixtures at atmospheric pressure from 283.15 to 333.15K A new method for the determination of the density of pure boldine
• Measurement of vapor.liquid equilibria (VLE) and excess enthalpies (HE) of binary systems with 1-alkyl-3-methylimidazolium bis(trifluoromethylsulfonyl)imide and prediction of these properties and A using modified UNIFAC (Dortmund)
• Vapor liquid equilibria for binary and ternary mixtures of ethanol, 2-butanone, and 2,2,4-trimethylpentane at 101.3 kPa
• Determination of partial molar excess enthalpies at infinite dilution for the systems four alcohols + [bmim]PF6 at different temperatures by isothermal titration calorimeter
• Isobaric vapor liquid equilibrium for ternary mixtures of ethanol and methylcyclohexane with 3-methylpentane and tert-butyl alcohol at 101.3 kPa
• Solubilities of rutin in eight solvents at T = 283.15, 298.15, 313.15, 323.15, and 333.15K
• Solubility of disperse yellow 54 in supercritical carbon dioxide with or without cosolvent
• Thermodynamic study of the solubility of ibuprofen and naproxen in some ethanol + propylene glycol mixtures
• Effect of temperature on ultrasonic velocity and thermodynamic parameters of bisphenol-C-formaldehyde-acrylate resin solutions
• Isothermal vapor liquid equilibrium at 333.15K and excess volumes and molar refractivity deviation at 298.15K for the ternary system di-butyl ether (1) + ethanol (2) + toluene (3) and its binary subsystems
• Limiting activity coefficients in binary mixtures of 1-alkanols and ethylbenzene
• Measurement and correlation of vapor liquid equilibria for ethanol + ethyl laurate and ethanol + ethyl myristate systems near critical temperature of ethanol
• Measurements of the solubilties of m-phthalic acid in acetone, ethanol and acetic ether
• Homogeneity of the water + ethanol + toluene azeotrope at 101.3 kPa
• Vapour liquid equilibria, azeotropic data, excess enthalpies, activity coefficients at infinite dilution and solid liquid equilibria for binary alcohol ketone systems
• Isothermal vapor liquid equilibria for different binary mixtures involved in the alcoholic distillation
• Experimental and predicted phase equilibria and excess properties for systems with ionic liquids
• Excess molar enthalpies of ethyl acetoacetate + (methanol, +ethanol, +1-propanol, and +2-propanol) at T = (298.15, 313.15 and 328.15)K and p = (0.1 and 10.0)MPa
• Liquid liquid equilibria for the binary system of di-isopropyl ether (DIPE) +water in between 288.15 and 323.15K and the ternary systems of DIPE +water + C1 C4 alcohols at 298.15K
• Solubility of l-serine, l-threonine and l-isoleucine in aqueous aliphatic alcohol solutions
• A study on the liquid liquid equilibria of 1-alkyl-3-methylimidazolium hexafluorophosphate with ethanol and alkanes
• Isobaric vapour liquid equilibria for binary systems of 2-butanone with ethanol, 1-propanol, and 2-propanol at 20 and 101.3 kPa
• Isobaric vapour liquid equilibria of binary 1-propoxy-2-propanol mixtures with water and alcohols at reduced pressure
• Excess properties for binary systems ionic liquid + ethanol: Experimental results and theoretical description using the ERAS model
• Activity coefficients at infinite dilution measurements for organic solutes in the ionic liquid N-butyl-4-methylpyridinium tosylate using GLC at T = (328.15, 333.15, 338.15, and 343.15)K
• Isothermal vapor liquid equilibrium at 333.15K and excess molar volumes and refractive indices at 298.15K for the mixtures of di-methyl carbonate, ethanol and 2,2,4-trimethylpentane
• Solubility of antioxidant 1010 in pure alkanols
• Activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid 1-butyl-1-methylpyrrolidinium trifluoromethanesulfonate using GLC
• Solubility and limiting activity coefficient of simvastatin in different organic solvents
• Phase equilibria of glycerol containing systems and their description with the Cubic-Plus-Association (CPA) Equation of State
• Isobaric vapor liquid liquid equilibrium and vapor liquid equilibrium for the system water ethanol-1,4-dimethylbenzene at 101.3 kPa
• Isothermal vapor liquid equilibrium at 333.15K, excess molar volumes and refractive indices at 298.15K for mixtures of tert-amyl methyl ether + ethanol + 2,2,4-trimethylpentane
• Measurement and calculation of vapor liquid equilibria for methanol + glycerol and ethanol + glycerol systems at 493 573K
• Density and surface tension in binary mixtures of CnMIM-BF4 ionic liquids with water and ethanol
• Vapor liquid equilibrium measurements and modeling of the n-butane + ethanol system from 323 to 423K
• Solubilities of cholesterol and desmosterol in binary solvent mixtures of n-hexane + ethanol
• Activity coefficients at infinite dilution measurements for organic solutes and water in the 1-hexyloxymethyl-3-methyl-imidazolium and 1,3-dihexyloxymethyl-imidazolium bis(trifluoromethylsulfonyl)-imide ionic liquids The cation influence
• Experimental measurements of vapor liquid equilibria at low pressure: Systems containing alcohols, esters and organic acids
• Measurement and correlation of the solubility of 1-(4-methyl-1-naphthyl) ethanone in an aqueous ethanol solution
• Solubilities of N-[(4-bromo- 3,5 - difluorine) phenyl]-acrylamide in methanol-ethanol solution
• Solubility and density measurements of palmitic acid in supercritical carbon dioxide + alcohol mixtures
• Phase equilibria for reactive distillation of diethyl succinate. Part II: Systems diethyl succinate + ethyl acetate + water and diethyl succinate + acetic acid + water
• Phase equilibria for reactive distillation of diethyl succinate Part I. System diethyl succinate + ethanol + water
• Buffer interactions: Solubilities and transfer free energies of TRIS, TAPS, TAPSO, and TABS from water to aqueous ethanol solutions
• Alkylsulfate-based ionic liquids to separate azeotropic mixtures
• Solubility of CF4 in lower alcohols
• Study on the effect of increasing the chain length of the alkanol in excess molar enthalpies of mixtures containing 2-methoxy-2-methylpropane, 1-alkanol, decane
• Densities and derived thermodynamic properties of ternary mixtures 1-butyl-3-methyl-imidazolium tetrafluoroborate + ethanol + water at seven pressures and two temperatures
• Alkylsulfate-based ionic liquids to separate azeotropic mixtures
• Measurements of binary diffusion coefficients for metal complexes in organic solvents by the Taylor dispersion method
• Thermodynamic properties of new heat pump working pairs: 1,3-Dimethylimidazolium dimethylphosphate and water, ethanol and methanol
• Solubilities of cefodizime disodium in aqueous alcohol mixtures at atmospheric pressure and different temperatures
• Gas-liquid chromatography measurements of activity coefficients at infinite dilution of hydrocarbons and alkanols in 1-alkyl-3-methylimidazolium bis(oxalato)borate
• Determination and correlation of solubilities of famotidine in water + co-solvent mixed solvents
• Activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-ethyl-3-methylimidazolium methanesulfonate
• Solubility of alpha-form and beta-form of L-glutamic acid in different aqueous solvent mixtures
• Phase equilibria on binary systems containing diethyl sulfide
• Solubility of HFCs in lower alcohols
• The Solubility of ammonia in ethanol between 277.35 K and 328.15 K
• Isothermal vapor-liquid equilibrium at T = 333.15 K and excess volumes and molar refractivity deviation at T = 298.15 K for the ternary mixtures {di-methyl carbonate (DMC) + ethanol + benzene} and {DMC+ ethanol + toluene}
• Effect of mono-, di- and tri-ethanolammonium tetrafluoroborate protonic ionic liquids on the volatility of water, ethanol, and methanol
• VLE of CO2 + glycerol + (ethanol or 1-propanol or 1-butanol)
• Solubility of decanedioic acid in binary solvent mixtures
• Thermophysical properties of pure 1-ethyl-3-methylimidazolium methylsulfate and its binary mixtures with alcohols
• Solubility and preferential solvation of meloxicam in ethanol + water mixtures
• Experimental measurement and modeling of solubility of LiBr and LiNO3 in methanol, ethanol, 1-propanol, 2-propanol and 1-butanol
• Measurement and correlation of solubility of benzamide in supercritical carbon dioxide with and without cosolvent
• Experimental determination and calculation of the critical curves for the binary systems of CO2 containing ketone, alkane, ester and alcohol, respectively
• Solubility of CsNO3 in binary solvents formed by ethanol and water in the temperature range between 278.15 and 313.15 K
• Measurements and thermodynamic modeling of the ethanol-water system with emphasis to the azeotropic region
• Thermophysical behaviour of the mixture (+-)-3,7-dimethyl-1,6-octadien-3-ol with ethanol
• Thermodynamic analysis and enthalpy-entropy compensation for the solubility of indomethacin in aqueous and non-aqueous mixtures
• Phase equilibria in binary mixtures with monoethyl succinate
• Total vapour pressure and excess Gibbs energy of ethanol with 1,8-cineole at temperatures between 278.15 K and 323.15 K
• Vapor-liquid equilibria at 333.15 K and excess molar volumes and deviations in molar refractivity at 298.15 K for mixtures of diisopropyl ether, ethanol and ionic liquids
• Solubility of L-phenylalanine in water and different binary mixtures from 288.15 to 318.15 K
• Liquid-liquid equilibria for ternary mixtures of methyl tert-amyl ether + methanol (or ethanol) + imidazolium-based ionic liquids at 298.15 K
• Solubility of itaconic acid in different organic solvents: Experimental measurement and thermodynamic modeling
• Determination of the crystallization thermodynamics and kinetics of L-tryptophan in alcohols - water system
• Solubility of citric, malonic, and malic acids in different solvents from 303.2 to 333.2 K
• Vapor-liquid equilibrium for the ternary carbon dioxide + ethanol + n-hexane and quaternary carbon dioxide + ethanol + n-hexane + thiophene systems
• Solubility of o-tolidine in pure and modified supercritical carbon dioxide
• Effect of temperature on the solubility of 3-aminopyridine in binary ethanol + toluene solvent mixtures
• Measurements and correlation of liquid-liquid equilibria of 4-methyl-2-pentanone + ethanol + water and 4-methyl-2-pentanone + n-butanol + water ternary systems between 283.2 and 323.2 K
• Determination of the solubility, dissolution enthalpy and entropy of pyrene in different solvents
• Solubility of naproxen in ethyl acetate + ethanol mixtures at several temperatures and correlation with the Jouyban-Acree model
• Thermodynamics of the solubility of lomefloxacin in methanol, ethanol, 1-propanol, 2-propanol, acetone, and chloroform from 293.15 to 323.15 K
• Thermodynamic study of aqueous two phase systems for some aliphatic alcohols + sodium thiosulfate + water
• Isopiestic study of mixed electrolyte solution {yCuCl2 + (1-y)CaCl2} in ethanol at T = 298.15 K
• Determination of the solubility, dissolution enthalpy and entropy of 3-pentadecylphenyl acrylate in methanol-ethanol solutions
• Determination of the solubility, dissolution enthalpy and entropy of icariin in water, ethanol, and methanol
• Solubility of osthole in a binary system of ethanol and water
• Activity coefficients at infinite dilution of organic solutes in the ionic liquid ethyl(2-hydroxyethyl)dimethyl-ammonium diethylphosphate using gas liquid chromatography
• Solid-liquid phase equilibrium of glyphosate in selected solvents
• Activity coefficients at infinite dilution of organic solutes in 1-octyl-3-methylimidazolium nitrate using gas-liquid chromatography
• Vapour-liquid and chemical equilibria in the ethyl ethanoate + ethanol + propyl ethanoate + propanol system accompanied with transesterification reaction
• Solubility of triclosan and iodopropynyl butylcarbamate in pure alkanols at several temperatures
• Measurement and correlation for solubility of levofloxacin in six solvents at temperatures from 288.15 to 328.15 K
• Solubility of chlocyphos in different solvents
• Determination of the solubility, dissolution enthalpy and entropy of suberic acid in different solvents
• Isobaric VLE at 0.6 MPa for binary systems isobutyl acetate + ethanol, + 1-propanol or + 2-propanol
• Thermodynamic analysis and correlation of solubility of candesartan cilexetil in aqueous solvent mixtures
• Ionic liquids as solvents to separate the azeotropic mixture hexane/ethanol
• Vapor liquid equilibrium for the ternary carbon dioxide ethanol nonane and decane systems
• Solid liquid equilibrium of 1-hydroxyethane-1,1-diphosphonic acid in different solvents
• Prediction of different thermodynamic properties for systems of alcohols and sulfate-based anion Ionic Liquids using modified UNIFAC
• Vapor liquid equilibrium of the ethanol + 3-methyl-1-butanol system at 50.66, 101.33 and 151.99 kPa
• A novel static analytical apparatus for phase equilibrium measurements
• Isothermal vapor liquid and vapor liquid liquid equilibrium for the ternary system ethanol + water + diethyl carbonate and constituent binary systems at different temperatures
• Measurement and correlation of liquid liquid equilibrium data for 2-methyl-1-propanol + 2-propanol + water at several temperatures
• Liquid liquid equilibria at 298.15 K for ternary mixtures of methyl tert-butyl ether + methanol (or ethanol) + imidazolium-based ionic liquids at atmospheric pressure
• High-temperature vapour liquid equilibrium for the water alcohol systems and modeling with SAFT-VR: 1. Water ethanol
• Solubility of succinic acid in different aqueous solvent mixtures: Experimental measurement and thermodynamic modeling
• Phase equilibria for the ternary systems ethanol, water + ethylene glycol or + glycerol at 101.3 kPa
• Solubility of dimethyl fumarate in water + (methanol, ethanol, 1-propanol) from (278.15 to 333.15) K
• Azeotrope breaking for the system ethyl tert-butyl ether (ETBE) + ethanol at 313.15 K and excess properties at 298.15 K for mixtures of ETBE and ethanol with phosphonium-based ionic liquids
• Isobaric vapor-liquid equilibrium data for the binary system methyl acetate + isopropyl acetate and the quaternary system methyl acetate + methanol + isopropanol + isopropyl acetate at 101.3 kPa
• Solubility of propanoic acid 3-(hydroxyphenylphosphinyl)-sodium salts in different solvent
• Measurement and correlation of solubility of N-chlorobenzenesulfonamide sodium and N-chloro-4-toluenesulfonamide sodium in binary ethanol + propan-2-ol mixtures from 278.00 K to 323.00 K
• Liquid-liquid equilibrium data for ternary aqueous mixtures containing 1-pentanol and 2-methyl-1-propanol at (298.15, 323.15, and 348.15) K
• Thermodynamics of solubility of thiomalic acid in different organicsolvents from 278.15 K to 333.15 K
• Correlation of solubility of pioglitazone hydrochloride in different binary solvents
• Solubility of citric acid in water, ethanol, n-propanol and in mixtures of ethanol + water
• Using binary mixtures of dicationic ionic liquids for determination ofactivity coefficients at infinite dilution by gas-liquid chromatography
• A new microebulliometer for the measurement of the vapor liquidequilibrium of ionic liquid systems
• Capacity of two 1-butyl-1-methylpyrrolidinium-based ionic liquidsfor the extraction of ethanol from its mixtures with heptane and hexane
• LLE for the systems ethyl palmitate (palmiticacid)(1) + ethanol(2) + glycerol (water)(3)
• Measurement and correlation solubility and mixing properties of dimethyl succinylsuccinate in pure and mixture organic solvents from (278.15 to 333.15) K
• Solubilities of crotonic acid in different organic solvents at severaltemperatures from (278.15 to 333.15) K
• Vapor-liquid equilibrium measurements of dimethylsulfide, +ethanol, +dimethylether, +methylacetate with a static total pressure method
• A novel continuous flow apparatus with a video camera system for high pressure phase equilibrium measurements
• Measurement and correlation of the solubility of 4,4'-oxydianiline in different organic solvents
• Excess Gibbs energies and volumes of the ternary system ethanol + dimethylformamide + tetrahydrofuran at 298.15K
• A novel dynamic recirculating apparatus for vapour-liquid equilibrium measurements at moderate pressures and temperatures
• Catechin sublimation pressure and solubility in supercritical carbon dioxide
• Solubility of glycine in binary system of ethanol + water solvent mixtures: Experimental data and thermodynamic modeling
• Solubility and solution thermodynamics of sulfamerazine and sulfamethazine in some ethanol + water mixtures
• Solubility of 1, 3, 2-dioxaphosphorinane-5,5-dimethyl -2- (2,4,6-tribromophenoxy)-2-oxide in selected solvents
• Solubility of erythritol in methanol, ethanol and methanol + ethanol: Experimental measurement and thermodynamic modeling
• Liquid-liquid equilibrium data for the system limonene + carvone + ethanol + water at 298.2 K
• Measurement and correlation solubility and mixing properties of L-malic acid in pure and mixture organic solvents
• Measurements of activity coefficients at infinite dilution in vegetable oils and capric acid using the dilutor technique
• Towards automated characterisation of liquid-liquid equilibria
• Vapor-liquid equilibrium and interfacial tensions of the system ethanol + hexane + tetrahydro-2H-Pyran
• The solubility of mercaptosuccinic acid in water + (methanol, ethanol, acetone) mixtures from (278.15 to 333.15 K)
• Determination and correlation of cefoperazone solubility in different pure solvents and binary mixture
• Solubility of androstenedione in lower alcohols
• Solubility and solution thermodynamics of 2,3,4,5-tetrabromothiophene in (ethanol + trichloromethane) binary solvent mixtures
• Solid-liquid equilibrium of dicyandiamide in different solvents
• Thermodynamics of fenofibrate and solubility in pure organic solvents
• Measurement and correlation of the solubilities of tetra(5,5-dimethyl-1,3-dioxaphosphorinanyl-2-oxy) neopentane in different pure solvents
• Volumetric investigation of the ternary system ethanol + dimethylformamide + cyclohexane at 298.15 K
• Prediction of solubility of CO2 in ethanol-[EMIM] [Tf2N] ionic liquid mixtures using artificial neural networks based on genetic algorithm
• Thermodynamic analysis and correlation of solubility of disodium 5'-guanylate heptahydrate in aqueous ethanol mixtures
• Present status of the modified UNIFAC Model for the prediction of phase equilibria and excess enthalpies for systems with ionic liquids
• Determination and correlation of solubility and solution thermodynamics of valnemulin hydrogen tartrate in different pure solvents
• Vapor-liquid equilibria for tetrahydrofuran + ethanol system containing three different ionic liquids at 101.3 kPa
• Probing effect of lipophilic butylated hydroxytoluene on anionic surfactant properties for potential food and pharmaceutical applications: Thermo-acoustic and spectroscopic study
• Solution thermodynamics of S-ibuprofen n-octyl-d-glucamine salt in ethanol + water cosolvent mixtures
• Solubility and polymorphic forms of antibiotic lasalocid sodium in different organic solvents
• Solubility, liquid-liquid equilibrium and critical states for the quaternary system acetic acid-ethanol-ethyl acetate-water at 303.15 K and 313.15 K
• Thermodynamics of risperidone and solubility in pure organic solvents
• Solid-liquid equilibrium and thermodynamic of 2,5-thiophenedicarboxylic acid in different organic solvents
• High pressure vapor-liquid equilibria measurements and modeling of butane/ethanol system and isobutane/ethanol system
• Phase equilibria and excess properties for binary systems in reactive distillation processes Part II. Ethyl acetate synthesis
• Experimental study of the density and derived (excess, apparent, and partial molar volumes) properties of binary water+ethanol and ternary water+ethanol+lithium nitrate mixtures at temperatures from 298 K to 448 K and pressures up to 40 MPa
• Ternary phase diagrams of ethyl paraben and propyl paraben in ethanol aqueous solvents
• Solubility of DL-malic acid in water, ethanol and in mixtures of ethanol + water
• Experimental and theoretical study of interaction between organic compounds and 1- (4-sulfobutyl)-3-methylimidazolium based ionic liquids
• Solubility of N-Ethylcarbazole in different organic solvent at 279.15 - 319.15 K
• Ionic liquids as entrainers for the separation of the ethanol/water system
• Liquid-liquid equilibria for multicomponent mixtures of 2,2-dimethyl-1,3-dioxolane with n-heptane, toluene, ethanol and water
• Liquid-liquid equilibrium for the ternary system water + 2-methyl-1-propanol + butyl acetate and water + 2-methyl-2-propanol + butyl acetate at (298.15 and 323.15) K
• Measurement and correlation of the solubility of N-(phosphonomethyl)iminodiacetic acid in different organic solvents
• Solid-liquid equilibrium of sulbactam in pure solvents and binary solvent mixtures
• Solubility of (+)-Catechin in Water and Water-Ethanol Mixtures within the Temperature Range 277.6 to 331.2 K: Fundamental Data to Design Polyphenol Extraction Processes
• Sodium sulfate solubility in (water + ethanol) mixed solvents in the presence of hydrochloric acid: Experimental measurements and modeling
• Measurement, correlation, and prediction of vapor pressure for binary and ternary systems containing an ionic liquid 1,3-dimethylimidazolium methylsulfate
• Determination of the solubility and dissolution thermodynamic properties of wedelolactone in a binary solvent of ethanol and water
• Correlation of solubility of hexamethylene-1,6-bisthiosulphate disodium salt dihydrate versus dielectric constants of water + ethanol mixtures
• Low transition temperature mixtures (LTTMs) as novel entrainers in extractive distillation
• Apparent molar properties of benzyldimethylammonium based protic ionic liquids in water and ethanol at different temperatures
• Phase equilibrium and mechanisms of crystallization in liquid-liquid phase separating system
• Study of interaction between organic compounds and mono or dicationic oxygenated ionic liquids using gas chromatography
• Liquid liquid equilibria for ternary systems ethanol + heptane + phosphoric-based ionic liquids
• Solubilities of phosphoric acid, P,P0-1,4-phenylene P,P,P0,P0-tetraphenyl ester in the organic solvents
• Correlation of solubility and calculation of thermodynamic properties of guanidine nitrate in different solvents
• Thermodynamic analysis and correlation of solubility of Cefaclor in different solvents from 278.15 to 313.15 K
• Solubilities of 5,10,15,20-tetrakis(4-chlorophenyl) porphyrin and 5,10,15,20-tetrakis(4- chlorophenyl) porphyrin manganese(III) chloride in binary ethanol + water solvent mixtures
• Solubility of methylphosphonic acid in selected organic solvents
• Separation of azeotropic mixtures using high ionicity ionic liquid based on 1-ethyl-3- methylimidazolium thiocyanate
• Solubility of pharmaceuticals in water and alcohols
• Measurement, correlation and prediction of isothermal vapor liquid equilibria of different systems containing vegetable oils
• Determination and correlation of solubility and solution thermodynamics of coumarin in different pure solvents
• Solid-liquid equilibrium of diphenyl anilinophosphonate in the different organic solvents
• High-temperature vapor-liquid equilibrium for ethanol-1-propanol mixtures and modeling with SAFT-VR
• Fractionation of orange essential oil using liquid-liquid extraction: Equilibrium data for model and real systems at 298.2 K.
• Determination and correlation of solubility of thiamine nitrate in water + ethanol mixtures and aqueous solution with different pH values from 278.15 K to 303.15 K
• Thermodynamic models for determination of the solid-liquid equilibrium of 2,5-thiophenedicarboxylic acid in (acetic acid + ethanol) binary solvent mixtures
• Measurement and correlation of solubility and dissolution properties of flunixin meglumine in pure and binary solvents
• Measurements and correlations of density and viscosity for short chain (C1-C3) n-alcohol - water mixtures in the temperature range from 350.7 K to 476.2 K at pressures up to 40 MPa
• Liquid-liquid equilibria for ternary mixtures of 2,2-dimethyl-1,3-dioxolane-4-methanol with n-heptane, toluene, ethanol and water
• Measurements of vapor-liquid equilibrium in both binary carbon dioxide-ethanol and ternary carbon dioxide-ethanol-water systemswith a newly developed flow-type apparatus
• Determination and prediction of solubilities of active pharmaceutical ingredients in selected organic solvents
• Study of phase equilibria and the physicochemical properties of selected pharmaceuticals
• Thermodynamic models for determination of the solubility of omeprazole sulfide in (ethanol + ethyl acetate) binary solvent mixtures
• Separation of the ethanol/water azeotropic mixture using ionic liquids and deep eutectic solvents
• Density of ethanolic alkali halide salt solutions by experiment andmolecular simulation
• Isobaric vapor-liquid equilibrium of trifluoroacetic acid + water, trifluoroacetic acid + ethyl trifluoroacetate and ethyl trifluoroacetate + ethanol binary mixtures
• Activity coefficients at infinite dilution for different alcohols and ketones in [EMpy][ESO4]: Experimental data and modeling with PC-SAFT
• Solubility correlation and thermodynamic analysis of two forms of Metaxalone in different pure solvents
• Phase equilibria of three binary systems containing 2,5-dimethylthiophene and 2-ethylthiophene in hydrocarbons
• Determination and correlation of solid-liquid phase equilibrium and phase diagram for multicomponent system of mixed dibasic acids. (I) Ternary system of adipic acid + glutaric acid + ethanol system
• An improved static-analytic apparatus for vapor-liquid equilibrium (PTxy) measurement using modified in-situ samplers
• Measurement and correlation of solid-liquid equilibria for three binaries, ethanol-antipyrine, chloroform-antipyrine, and dimethyl ether-antipyrine
• Limiting activity coefficient measurements in binary mixtures of dichloromethane and 1-alkanols (C1 - C4)
• Water-ethanol-sodium chloride system: The main sources of uncertainties in thermodynamic properties determined by potentiometry
• Measurement of binary diffusion coefficient and solubility estimation for dyes in supercritical carbon dioxide by CIR method
• Determination and correlation of infinite dilution binary diffusion coefficients for aluminum acetylacetonate in supercritical and liquid fluids
• Study of liquid-liquid equilibria at different temperatures of water + ethanol + 1-butyl-1-methylpyrrolidinium bis(trifluoromethylsulfonyl) imide ternary system
• Activity coefficients at infinite dilution of organic solvents and water in 1-butyl-3-methylimidazolium dicyanamide. A literature review of hexane/hex-1-ene separation
• Solubility of D-phenylglycine methyl ester hydrochloride in water and in organic individual or mixed solvents: Experimental data and results of thermodynamic modeling
• Effect of polymorphism on thermodynamic properties of cefamandole nafate
• Solid-liquid phase equilibrium and ternary phase diagrams of ethenzamide-saccharin cocrystals in different solvents
• High pressure vapor-liquid equilibria for binary methane and protic ionic liquid based on propionate anions
• Solubility of flavone, 6-methoxyflavone and anthracene in supercritical CO2 with/without a co-solvent of ethanol correlated by using a newly proposed entropy-based solubility parameter
• Measurements of isobaric heat capacities for HFE-7000 and HFE-7100 at different temperatures and pressures
• Measurement and correlation of phase equilibria for ternary systems of water + (ethanol / 1-propanol) + 1-decyl-3-methylimidazolium bis(trifluoromethylsulfonyl) imide at 298.15 K
• Interfacial tension and adsorption in the binary system ethanol and carbon dioxide: Experiments, molecular simulation and density gradient theory
• Determination and correlation of solubility and solution thermodynamics of ethenzamide in different pure solvents
• The density, viscosity, vapor pressure, melting point and flash point of a liquid propellant: 1-(2-azidoethyl) pyrrolidine
• Use of HS-SPME for analysis of the influence of salt concentration and temperature on the activity coefficient at infinite dilution of ethanol-water-salt systems.
• Phase equilibria of ternary systems of carbon dioxide + ethanol, dimethyl sulfoxide, or N,N-dimethyl formamide + water at elevated pressures including near critical regions
• Equilibrium data and GC-PC SAFT predictions for furanic extraction
• Determination and correlation of solubility of linezolid form II in different pure and binary solvents
• Equilibrium study and diversified models of drug Norfloxacin in eight pure organic and binary solvents at T = (278.15 to 328.15) K
• In situ measurement of liquid-liquid equilibria by medium field nuclear magnetic resonance
• Separation of azeotropic mixtures (ethanol and water) enhanced by deep eutectic solvents
• Application of 1-hexyl-3-methylimidazolium trifluoromethanesulfonate to the removal of alcohol from mixtures with heptane
• Determination and correlation of solubility of N-methyl-3,4,5- trinitropyrazole (MTNP) in ten pure solvents from 283.15 K to 323.15 K
• A milliliter-scale setup for the efficient characterization of isothermal vapor-liquid equilibria using Raman spectroscopy
• Thermodynamic analysis of the solubility of polymorphic cytarabine in a variety of pure solvents
• High selective water/butan-1-ol separation on investigation of limiting activity coefficients with [P8,8,8,8][[NTf2] ionic liquid
• Measurement and correlation of density and viscosity of n-alcohol-water mixtures at temperatures up to 618 K and at pressures up to 40 MPa
• Thermodynamic equilibrium of hydrocortisone form I in different solvent systems
• Phase equilibria of phenolic compounds in water or ethanol
• Separation of ethyl acetate and ethanol azeotrope mixture using dialkylphosphates-based ionic liquids as entrainers
• Isobaric vapor-liquid equilibrium for 2-butanone + ethanol + phosphate-based ionic liquids at 101.3 kPa
• Effect of different variables in the solubility of ampicillin and corresponding solid phase
• Solubility and dissolution characteristics of capecitabine in pure lower alcohols and water with methanol mixture solvents at atmospheric pressure and different temperatures
• Separation of binary mixtures based on limiting activity coefficients data using specific ammonium-based ionic liquid and modelling of thermodynamic functions
• Solubilities of six lithium salts in five non-aqueous solvents and in a few of their binary mixtures
• Solubility and mixing thermodynamic properties of (2,4,6-trimethylbenzoyl) diphenylphosphine oxide in pure and binary solvents
• Measurements of activity coefficient at infinite dilution for organic solutes in tetramethylammonium chloride + ethylene glycol deep eutectic solvent using gas-liquid chromatography
• Isobaric vapor-liquid equilibrium for chloroform + ethanol + 1,3- dimethylimidazolium dimethylphosphate at 101.3 kPa
• Guaiacol and its mixtures: new data and predictive models Part 2: Gibbs energy of solvation
• Measurement of critical properties for binary and ternary mixtures containing potential gasoline additive diethyl carbonate (DEC)
• Solubility evaluation and thermodynamic modeling of beta-lapachone in water and ten organic solvents at different temperatures
• Investigation of solutions of ethyl alcohol and the deep eutectic solvent of Reline for their volumetric properties
• Solubility of 1-methyl-4-nitropyrazole in seventeen pure solvents at temperatures from 283.15 K to 323.15 K
• Effect of bis(trifluoromethylsulfonyl)imide-based ionic liquids on the isobaric vapor - liquid equilibrium behavior of ethanol + dimethyl carbonate at 101.3 kPa
• Tetramethylammonium chloride + glycerol deep eutectic solvent as separation agent for organic liquid mixtures: Assessment from experimental limiting activity coefficients
• Measurement on the thermal conductivity of five saturated fatty acid ethyl esters components of biodiesel
• Thermodynamics and activity coefficients at infinite dilution for organic solutes in the ionic liquid 1-butyl-1-methylpyrrolidinium dicyanamide
• Separation of acetonitrile + ethanol mixture using imidazolium - Based ionic liquids as entrainers
• Vapor-liquid equilibrium in the binary and ternary systems containing ethyl propionate, ethanol and alkane at 101.3 kPa
• Vapor-liquid and liquid-liquid equilibrium modeling of systems involving ethanol, water, and ethyl valerate (valeric acid) using the PC-SAFT equation of state
• Solubility determination and correlation of cyromazine in sixteen pure solvents and mixing properties of solutions
• New ionic liquid [P4,4,4,4][NTf2] in bio-butanol extraction on investigation of limiting activity coefficients
• Study of the physicochemical properties of protein kinase CK2 inhibitors -TBBt, TBBi and 2-Me-TBBi
• Solubility of citalopram hydrobromide in(ethanol + toluene) and (ethanol + ethyl acetate) at 283.15-318.15 K and its correlation with the Jouyban-Acree and CNIBS/R-K models
• Solid-liquid equilibria for selected binary systems containing diphenyl carbonate
• Ammonium ionic liquids in extraction of bio-butan-1-ol from water phase using activity coefficients at infinite dilution
• Solubility of cinnamic acid in supercritical carbon dioxide and subcritical 1,1,1,2-tetrafluoroethane: Experimental data and modelling
• Measurements of activity coefficients at infinite dilution for organic solutes in two quaternary ammonium-based ionic liquids [DDA][ClO4] and [DDA][BF4]
• Thermodynamic equilibrium of hexamethylenediammonium glutarate in mono-solvents and binary solvent systems
• Solubility, liquid-liquid equilibrium and critical states for the quaternary system formic acid - ethanol - ethyl formate - water at 298.15 K and 308.15 K
• Liquid-liquid measurement and correlation for separation of azeotrope (dimethyl carbonate and ethanol) with different imidazolium-based ionic liquids
• Development of a rolling ball viscometer for simultaneous measurement of viscosity, density, bubble-point pressure of CO2-expanded liquids
• Measurement and modeling of infinite dilution activity coefficients of organic compounds in an equimolar ionic liquid mixture of [Bmim]Cl and [Bmim][Tf2N]
• Measurement and correlation of vapor-liquid distribution coefficients of flavonoids in high pressure carbon dioxide - ethanol - water systems
• Isothermal vapor-liquid equilibria at 383.15-413.15 K for the binary system methanol + dimethyl carbonate and the pressure dependency of the azeotropic point
• Application of trihexyltetradecylphosphonium dicyanamide ionic liquid for various types of separations problems: Activity coefficients at infinite dilution measurements utilizing GLC method
• Measurement of the thermal conductivity of biofuel mixtures: Methyl caprate components of biodiesel and alcohols
• Phase equilibrium measurements and thermodynamic modeling of {CO2 + diethyl succinate + cosolvent} systems
• Excess molar enthalpies of ternary mixtures of (methanol, ethanol + 2-propanol + 1,4-dioxane) at T ? 298:15 K
• Thermodynamic and acoustic properties of binary mixtures of alcohols and alkanes. I. Speed of sound in (ethanol + n-heptane) under elevated pressures
• Thermodynamic and acoustic properties of binary mixtures of alcohols and alkanes. II. Density and heat capacity of (ethanol + n-heptane) under elevated pressures
• Excess isobaric molar heat capacities and excess molar volumes for ethanol + n-decane and n-undecane systems
• Apparent molar volume and isentropic compressibility of ionic liquid 1-butyl-3-methylimidazolium bromide in water, ethanol, and ethanol at T = (298.15 to 318.15) K
• Density measurements under pressure for the binary system (ethanol + methylcyclohexane)
• (Liquid + liquid) equilibria for ternary mixtures of (methanol or ethanol + toluene or m-xylene + n-dodecane)
• (Vapor + liquid) equilibria of binary mixtures formed by iso-octane with a variety of compounds at 95.8 kPa
• Systems with ionic liquids: Measurement of VLE and c1 data and prediction of their thermodynamic behavior using original UNIFAC, mod. UNIFAC(Do) and COSMO-RS(Ol)
• Tailor-made ionic liquids
• Speeds of sound, isentropic compressibilities, viscosities and excess molar volumes of binary mixtures of methylcyclohexane + 2-alkanols or ethanol at T = 298.15 K
• Experimental and predicted volumetric and refractive index properties of ternary mixtures of iodoethane with toluene and alcohols at temperature 298.15 K and pressure 101 kPa
• Excess molar volumes and partial molar volumes for (propionitrile + an alkanol) at T = 298.15 K and p = 0.1 MPa
• Physico-chemical and excess properties of the binary mixtures of methylcyclohexane + ethanol, + propan-1-ol, + propan-2-ol, + butan-1-ol, + 2-methyl-1-propanol, or 3-methyl-1-butanol at T = (298.15, 303.15, and 308.15) K
• Measurement and correlation of excess molar enthalpy for(1,2-propanediol, or 1,3-propanediol, or 1,4-butanediol + water) at the temperatures (298.15, 323.15, and 343.15) K
• Dynamic viscosities of the ternary liquid mixtures (dimethyl carbonate + methanol + ethanol) and (dimethyl carbonate + methanol + hexane) at several temperatures
• Study of vapour pressure of lithium nitrate solutions in ethanol
• (Vapour + liquid) equilibrium in (N,N-dimethylacetamide + ethanol + water) at the temperature 313.15 K
• Bubble point temperatures of the binary mixtures of nitrobenzene with C1 C4 aliphatic alcohols at 94.95 kPa
• Ternary and quaternary (liquid + liquid) equilibria for (water + ethanol + a-pinene, +b-pinene, or +limonene) and (water + ethanol + a-pinene + limonene) at the temperature 298.15 K
• Thermodynamic properties of (tetradecane + benzene, + toluene, + chlorobenzene, + bromobenzene, + anisole) binary mixtures at T = (298.15, 303.15, and 308.15) K
• Viscosity, density, and speed of sound of methylcyclopentane with primary and secondary alcohols at T = (293.15, 298.15, and 303.15) K
• (Vapor + liquid) equilibria of the binary mixtures of m-cresol with C1 C4 aliphatic alcohols at 95.5 kPa
• Densities, viscosities, and ultrasonic velocity studies of binary mixtures of trichloromethane with methanol, ethanol, propan-1-ol, and butan-1-ol at T=(298.15 and 308.15) K
• Thermodynamic interactions in binary mixtures of anisole with ethanol, propan-1-ol, propan-2-ol, butan-1-ol, pentan-1-ol, and 3-methylbutan-1-ol at T = (298.15, 303.15, and 308.15) K
• Dynamic viscosities of binary mixtures of cycloalkanes with primary alcohols at T = (293.15, 298.15, and 303.15) K: New UNIFAC-VISCO interaction parameters
• Densities and volumetric properties of (formamide + ethanol, or 1-propanol, or 1,2-ethanediol, or 1,2-propanediol) mixtures at temperatures between 293.15 K and 318.15 K
• Molar excess enthalpies of binary mixtures of [tributyl phosphate + {CH3(CH2)nOH (n = 0 to 3)}] at 298.15 K
• (p, v,T,x) Measurements of {(1 - x)H2O + xC2H5OH} mixtures in the near-critical and supercritical regions
• Solubilities and liquid liquid equilibria of (water + ethanol + a,a,a-trifluorotoluene) at temperatures T = (288.15, 298.15, and 308.15) K and pressure p = 101.2 kPa
• Volumetric properties of binary and ternary mixtures of diisopropyl ether, a,a,a-trifluorotoluene, 2,2,2-trifluoroethanol, and ethanol at a temperature 298.15 K and pressure 101 kPa
• Excess molar volumes of binary mixtures of 1,3-dimethylimidazolidin-2-one with an alkan-1-ol at the temperatures 283.15 K, 298.15 K, and 313.15 K
• Densities and viscosities of binary mixtures of {dimethylsulfoxide + aliphatic lower alkanols (C1 C3)} at temperatures from T = 303.15 K to T = 323.15 K
• Study on the phase behaviour and thermodynamic properties of ionic liquids containing imidazolium cation with ethanol at several temperatures
• Vapour pressure measurement for binary and ternary systems containing water methanol ethanol and an ionic liquid 1-ethyl-3-ethylimidazolium diethylphosphate
• Measurement of activity coefficients at infinite dilution in 1-hexadecyl-3-methylimidazolium tetrafluoroborate ionic liquid
• Mixing properties of binary mixtures presenting azeotropes at several temperatures
• Density and speed of sound of lithium bromide with organic solvents: Measurement and correlation
• Density, dynamic viscosity, and derived properties of binary mixtures of methanol or ethanol with water, ethyl acetate, and methyl acetate at T = (293.15, 298.15, and 303.15) K
• Temperature influence on mixing properties of {ethyl tert-butyl ether (ETBE) + gasoline additives}
• Effect of temperature on mixing thermodynamics of a new ionic liquid: {2-Hydroxy ethylammonium formate (2-HEAF) + short hydroxylic solvents}
• Phase diagrams of (vapour + liquid) equilibrium for binary mixtures of a,a,a-trifluorotoluene with ethanol, or benzene, or chloroform at pressure 101.4 kPa
• Excess volumes of mixing in (N,N-dimethylacetamide + methanol + water) and (N,N-dimethylacetamide + ethanol + water) at the temperature 313.15 K
• Measurement and correlation of solubility of trans-resveratrol in 11 solvents at T = (278.2, 288.2, 298.2, 308.2, and 318.2) K
• Densities and volumetric properties of (N-(2-hydroxyethyl)morpholine + ethanol, + 1-propanol, + 2-propanol, + 1-butanol, and + 2-butanol) at (293.15, 298.15, 303.15, 313.15, and 323.15) K
• Measurements of activity coefficients at infinite dilution of aromatic and aliphatic hydrocarbons, alcohols, and water in the new ionic liquid [EMIM][SCN] using GLC
• Density and refractive index in mixtures of ionic liquids and organic solvents: Correlations and predictions
• Mixing thermodynamic properties of 1-butyl-4-methylpyridinium tetrafluoroborate [b4mpy][BF4] with water and with an alkan-1ol (methanol to pentanol)
• Excess molar volumes and isentropic compressibility of binary systems {trioctylmethylammonium bis(trifluoromethysulfonyl)imide + methanol or ethanol or 1-propanol} at different temperatures
• Physical properties of the ternary system (ethanol + water + 1-butyl-3-methylimidazolium methylsulphate) and its binary mixtures at several temperatures
• Selection of ionic liquids as entrainers for separation of (water + ethanol)
• Excess molar properties of ternary system (ethanol + water + 1,3-dimethylimidazolium methyl sulfate) and its binary mixtures at several temperatures
• Osmotic coefficients of binary mixtures of four ionic liquids with ethanol or water at T = (313.15 and 333.15) K
• Activity coefficients at infinite dilution of hydrocarbons, alkylbenzenes, and alcohols in the paramagnetic ionic liquid 1-butyl-3-methyl-imidazolium tetrachloridoferrate(III) using gas liquid chromatography
• Boiling temperature measurement for water, methanol, ethanol, and their binary mixtures in the presence of a hydrochloric or acetic salt of mono-, di-, or tri-ethanolamine at 101.3 kPa
• Temperature dependence on mutual solubility of binary (methanol + limonene) mixture and (liquid + liquid) equilibria of ternary (methanol + ethanol + limonene) mixture
• Activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid triethylsulphonium bis(trifluoromethylsulfonyl)imide
• Measurements of activity coefficients at infinite dilution of aliphatic and aromatic hydrocarbons, alcohols, thiophene, tetrahydrofuran, MTBE, and water in ionic liquid [BMIM][SCN] using GLC
• Osmotic coefficients of binary mixtures of 1-butyl-3-methylimidazolium methylsulfate and 1,3-dimethylimidazolium methylsulfate with alcohols at T = 323.15 K
• Phase equilibria study of the binary systems (N-butyl-4-methylpyridinium tosylate ionic liquid + an alcohol)
• The (p, q, T) properties and apparent molar volumes V/ of (ZnBr2 + C2H5OH)
• Thermodynamic properties of ethanol solution of chiral camphors and its derivatives
• Phase equilibrium measurements of ternary systems formed by linoleic and linolenic acids in carbon dioxide/ethanol mixtures
• Activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid 4-methyl-N-butyl-pyridinium bis(trifluoromethylsulfonyl)-imide
• Density and viscosity of 1-butyl-3-methylimidazolium nitrate with ethanol, 1-propanol, or 1-butanol at several temperatures
• Vapour pressures and osmotic coefficients of binary mixtures of 1-ethyl-3-methylimidazolium ethylsulfate and 1-ethyl-3-methylpyridinium ethylsulfate with alcohols at T = 323.15 K
• (Vapor + liquid) equilibria of binary mixtures containing light alcohols and ionic liquids
• Activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-ethyl-3-methylimidazolium trifluoromethanesulfonate using gas liquid chromatography at T = (313.15, 323.15, and 333.15) K
• Activity coefficients at infinite dilution for solutes in the trioctylmethylammonium bis(trifluoromethylsulfonyl)imide ionic liquid using gas liquid chromatography
• Thermophysical properties of the binary mixtures (1,8-cineole + 1-alkanol) at T = (298.15 and 313.15) K and at atmospheric pressure
• Activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-octyl-3-methylimidazolium hexafluorophosphate using gas liquid chromatography at T = (313.15, 323.15, and 333.15) K
• Gas liquid chromatography measurements of activity coefficients at infinite dilution of various organic solutes and water in tri-iso-butylmethylphosphonium tosylate ionic liquid
• Ternary excess molar volumes of {methyltrioctylammonium bis(trifluoromethylsulfonyl)imide + ethanol + methyl acetate, or ethyl acetate} systems at T = (298.15, 303.15, and 313.15) K
• Volumetric properties, viscosity and refractive index of the protic ionic liquid, pyrrolidinium octanoate, in molecular solvents
• Activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-ethyl-3-methylimidazolium tetracyanoborate [EMIM][TCB] using gas liquid chromatography
• PVT, viscosity, and surface tension of ethanol: New measurements and literature data evaluation
• (Vapour + liquid) equilibria of ternary systems with ionic liquids using headspace gas chromatography
• Ultrasonic speeds and isentropic compressibilities of {difurylmethane + (C1 C6) n-alkanol} binary mixtures at T = 298.15 K
• Measurements of activity coefficients at infinite dilution of organic solutes and water in 1-propyl-1-methylpiperidinium bis{(trifluoromethyl)sulfonyl}imide ionic liquid using g.l.c.
• Activity coefficients at infinite dilution of organic solutes in N-alkylpyridinium bis(trifluoromethylsulfonyl)imide ([CnPY][NTf2], n = 2, 4, 5) using gas liquid chromatography
• Solubility and pKa of select pharmaceuticals in water, ethanol, and 1-octanol
• Thermodynamic study of binary mixtures containing 1-butylpyridinium tetrafluoroborate and methanol, or ethanol
• Measurement and correlation of the (p, rho, T) relation of liquid cyclohexane, toluene, and ethanol in the temperature range from 233.15 K to 473.15 K at pressures up to 30 MPa for use as density reference liquids
• Measurement and correlation of solubilities of apigenin and apigenin 7-O-rhamnosylglucoside in seven solvents at different temperatures
• Effect of mono-, di- and tri-ethanolammonium tetrafluoroborate protonic ionic liquids on vapour liquid equilibria of ethanol aqueous solution
• Measurements of activity coefficients at infinite dilution of organic compounds and water in isoquinolinium-based ionic liquid [C8iQuin][NTf2] using GLC
• Vapor pressures, excess enthalpies, and specific heat capacities of the binary working pairs containing the ionic liquid 1-ethyl-3-methylimidazolium dimethylphosphate
• Thermodynamic properties of chiral fenchones in some solutions at T = 298.15 K
• Activity coefficients at infinite dilution of organic solutes in the ionic liquid trihexyl(tetradecyl)phosphonium tetrafluoroborate using gas liquid chromatography at T = (313.15, 333.15, 353.15, and 373.15) K
• Application of the ERAS model to volumetric properties of binary mixtures of banana oil with primary and secondary alcohols (C1- C4) at different temperatures
• Activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-butyl-3-methylimidazolium hexafluoroantimonate using gas liquid chromatography at T = (313.15, 323.15, and 333.15) K
• Thermophysical properties of binary mixtures of {ionic liquid 2-hydroxy ethylammonium acetate + (water, methanol, or ethanol)}
• Activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid 1-ethyl-3-methylimidazolium tetracyanoborate
• Volumetric and viscometric properties of binary mixtures of {methyl tert-butyl ether (MTBE) + alcohol} at several temperatures and p = 0.1 MPa: Experimental results and application of the ERAS model
• Investigation of sodium 4-nitrotoluene-2-sulfonate solubility in aqueous organic solutions
• Interfacial tensions of binary mixtures of ethanol with octane, decane, dodecane, and tetradecane
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(3-hydroxypropyl)pyridinium bis(trifluoromethylsulfonyl)-amide
• Application of the extended real associated solution (ERAS) theory to excess molar enthalpies of benzaldehyde + 1-alkanols (C1 to C5) at T = 298.15 K
• Volumetric properties and enthalpies of solution of alcohols CkH2k+1OH (k = 1, 2, 6) in 1-methyl-3-alkylimidazolium bis(trifluoromethylsulfonyl)imide {[C1CnIm][NTf2] n = 2, 4, 6, 8, 10} ionic liquids
• Experimental and predicted refractive index properties in ternary mixtures of associated liquids
• Solubility and phase separation of 4-morpholinepropanesulfonic acid (MOPS), and 3-morpholino-2-hydroxypropanesulfonic acid (MOPSO) in aqueous 1,4-dioxane and ethanol solutions
• (Vapor + liquid) equilibrium properties of (ethane + ethanol) system at (295, 303, and 313) K
• Effect of ionic liquid 1-methylimidazolium chloride on the vapour liquid equilibrium of water, methanol, ethanol, and {water + ethanol} mixture
• Thermodynamics and activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid 1-butyl-1-methylpyrrolidinium tetracyanoborate
• (Vapor + liquid) equilibrium for the binary systems {water + glycerol} and {ethanol + glycerol, ethyl stearate, and ethyl palmitate} at low pressures
• Osmotic and activity coefficients in the binary solutions of 1-butyl-3-methylimidazolium chloride and bromide in methanol or ethanol at T = 298.15 K from isopiestic measurements
• Thermodynamic properties of biofuels: Heat capacities of binary mixtures containing ethanol and hydrocarbons up to 20 MPa and the pure compounds using a new flow calorimeter
• Volumetric behaviour of binary and ternary liquid systems composed of ethanol, isooctane, and toluene at temperatures from (298.15 to 328.15) K. Experimental data and correlation
• Solubility of b-carotene in ethanol- and triolein-modified CO2
• Effect of the temperature on the physical properties of pure 1-propyl-3-methylimidazolium bis(trifluoromethylsulfonyl)imide and characterization of its binary mixtures with alcohols
• Interactions of volatile organic compounds with the ionic liquid 1-ethyl-3-methylimidazolium tetracyanoborate
• Volumetric properties of dilute solutions of water in ethanol and water-d2 in ethanol-d1 between T = (278.15 and 318.15) K
• Volumetric and surface properties of pure ionic liquid n-octyl-pyridinium nitrate and its binary mixture with alcohol
• (Liquid + liquid) equilibrium for the system {ethyl stearate(1) + ethanol(2) + glycerol(3)}
• PrhoT measurements and derived properties of liquid 1-alkanols
• Excess properties of binary mixtures containing 1-hexyl-3-methylimidazolium bis(trifluoromethylsulfonyl)imide ionic liquid and polar organic compounds
• Solubility of diosgenin in different solvents
• Solubilities of oleanolic acid and ursolic acid in (ethanol + water) mixed solvents from T = (292.2 to 328.2) K
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 4-(2-methoxyethyl)-4-methylmorpholinium bis(trifluoromethylsulfonyl)-amide
• Measurements of activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-hexyl-3-methylimidazolium tetracyanoborate
• Activity coefficients at infinite dilution of organic solutes in the ionic liquid trihexyltetradecylphosphonium hexafluorophosphate using gas liquid chromatography at T = (313.15, 333.15, 353.15, and 363.15) K
• Isopiestic determination of the osmotic coefficient and vapour pressure of N-R-4-(N,N-dimethylamino)pyridinium tetrafluoroborate (R = C4H9, C5H11, C6H13) in the ethanol solution at T = 298.15 K
• Properties of pure 1-methylimidazolium acetate ionic liquid and its binary mixtures with alcohols
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-methoxyethyl)-1-methylpiperidinium bis(trifluoromethylsulfonyl)-amide
• Surface tension of four binary systems containing (1-ethyl-3-methyl imidazolium alkyl sulphate ionic liquid + water or + ethanol)
• Determination and correlation of the solubility for diosgenin in alcohols solvents
• Surface thermodynamics of binary mixtures of aliphatic alcohols in heavy water
• Thermodynamic properties of binary mixtures combining two pyridinium-based ionic liquids and two alkanols
• Experimental densities, dynamic viscosities and surface tensions of the ionic liquids series 1-ethyl-3-methylimizazolium acetate and dicyanamide and their binary and ternary mixtures with water and ethanol at T = (298.15 K to 343.15 K)
• Experimental study on the calorimetric data of cyclohexanol with alkanols (C1-C4) and correlation with Wilson, NRTL and UNIQUAC models at 300 K
• Densities and derived thermodynamic properties of binary alkanol + boldine mixtures in the compressed liquid region
• Measurements of activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-ethyl-3-methylimidazolium methanesulfonate
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-methoxyethyl)-1-methylpyrrolidinium bis(trifluoromethylsulfonyl)-amide
• Volumetric and steric properties of hydroxamic acids in ethanol at different temperatures
• Phase equilibrium measurements and thermodynamic modeling of methane alcohol systems at ambient temperature
• Ternary (liquid + liquid) equilibria for b-citronellol in aqueous alcohol at different temperatures
• 1-Alkyl-3-methylimidazolium bis(trifluoromethylsulfonyl)imide ionic liquids as solvents in the separation of azeotropic mixtures
• Effect of alkanolammonium formates ionic liquids on vapour liquid equilibria of binary systems containing water, methanol, and ethanol
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 4-(2-methoxyethyl)-4-methylmorpholinium trifluorotris(perfluoroethyl)phosphate
• Measurement and correlation of the solubility of 2,3,4,5-tetrabromothiophene in different solvents
• Activity coefficient at infinite dilution measurements for organic solutes (polar and non-polar) in fatty compounds: Saturated fatty acids
• Derived thermodynamic properties for the (ethanol + decane) and (carbon dioxide + ethanol + decane) systems at high pressures
• Solubility of gallic acid in liquid mixtures of (ethanol + water) from (293.15 to 318.15) K
• Ethanol extraction from its azeotropic mixture with hexane employing different ionic liquids as solvents
• Heat capacities and densities of the binary mixtures containing ethanol, cyclohexane or 1-hexene at high pressures
• Thermodynamic investigation of the ATPSs composed of some (aliphatic alcohol + sodium carbonate + water) ternary systems
• Measurement and correlation of solubility of Tetracycline hydrochloride in six organic solvents
• Phase equilibrium measurements and thermodynamic modelling for the system (CO2 + ethyl palmitate + ethanol) at high pressures
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-methoxyethyl)- 1-methylpiperidinium trifluorotris(perfluoroethyl)phosphate
• Henry s constants and activity coefficients of some organic solutes in 1-butyl,3-methylimidazolium hydrogen sulfate and in 1-methyl,3-trimethylsilylmethylimidazolium chloride
• Viscosity and density data for the ternary system water(1) ethanol(2) ethylene glycol(3) between 298.15 K and 328.15 K
• Solubility of salicylic acid in pure alcohols at different temperatures
• Interactions of volatile organic compounds with the ionic liquids 1-butyl-1-methylpyrrolidinium tetracyanoborate and 1-butyl-1-methylpyrrolidinium bis(oxalato)borate
• Thermophysical properties of biodiesel and related systems. Part I. Vapour liquid equilibrium at low pressures of binary and ternary systems involving methanol, ethanol, glycerol, water and NaCl
• Physicochemical properties and activity coefficients at infinite dilution for organic solutes and water in a novel bicyclic guanidinium superbase-derived protic ionic liquid
• Experimental measurements and predictions of density, viscosity, and carbon dioxide solubility in methanol, ethanol, and 1-propanol
• Properties of pure n-butylammonium nitrate ionic liquid and its binary mixtures of with alcohols at T = (293.15 to 313.15) K
• Isothermal (vapour + liquid) equilibria for binary mixtures of diisopropyl ether with (methanol, or ethanol, or 1-butanol): Experimental data, correlations, and predictions
• Measurements and predictions of density and carbon dioxide solubility in binary mixtures of ethanol and n-decane
• Solubilities of evodiamine in twelve organic solvents from T = (283.2 to 323.2) K
• Activity coefficient at infinite dilution measurements for organic solutes (polar and non-polar) in fatty compounds Part II: C18 fatty acids
• Application of 1-alkyl-3-methylpyridinium bis(trifluoromethylsulfonyl)imide ionic liquids for the ethanol removal from its mixtures with alkanes
• Experimental and theoretical study on infinite dilution activity coefficients of various solutes in piperidinium ionic liquids
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-methoxyethyl)- 1-methylpyrrolidinium trifluorotris(perfluoroethyl)phosphate
• Measurements of activity coefficients at infinite dilution for organic solutes and water in N-hexylisoquinolinium thiocyanate, [HiQuin][SCN] using GLC
• Activity coefficients at infinite dilution of organic solutes in N-formylmorpholine and N-methylpyrrolidone from gas-liquid chromatography
• Measurement of critical temperatures and critical pressures for binary mixtures of methyl tert-butyl ether (MTBE) + alcohol and MTBE + alkane
• Solubility and phase behavior of binary systems containing salts based on transitional metals
• Quantitative NMR spectroscopy of binary liquid mixtures (aldehyde + alcohol) Part I: Acetaldehyde + (methanol or ethanol or 1-propanol)
• Density and surface tension of pure ionic liquid 1-butyl-3-methylimidazolium L-lactate and its binary mixture with alcohol and water
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-hydroxyethyl)- 3-methylimidazolium trifluorotris(perfluoroethyl)phosphate
• Activity coefficients at infinite dilution of organic solutes in diethylene glycol and triethylene glycol from gas-liquid chromatography
• Effect of water content on the equilibrium pressure of (carbon dioxide + decane and + decalin) from T = (313.15 to 333.15) K
• Assessment, measurement and correlation of (vapour + liquid) equilibrium of (carbon dioxide + butyl, isobutyl, and amyl formate) systems
• Isobaric VLE of the mixture {(+-)-linalool + ethanol}: A case study for the distillation of absolute and volatile oils
• Solubility and solution thermodynamics of 2,3,4,5-tetrabromothiophene in (ethanol + tetrahydrofuran) binary solvent mixtures
• Excess molar enthalpies of {diethyl oxalate + (methanol, + ethanol, + 1-propanol, and + 2-propanol)} at T = (288.2, 298.2, 313.2, and 328.2) K and p = 101.3 kPa
• Infinite dilution activity coefficients of volatile organic compounds in two ionic liquids composed of the tris(pentafluoroethyl) trifluorophosphate ([FAP]) anion and a functionalized cation
• Quantitative NMR spectroscopy of binary liquid mixtures (aldehyde + alcohol). Part II: (Propanal or butanal or heptanal) + (methanol or ethanol or 1-propanol)
• Thermodynamics of fenoxycarb in solution
• Measurements of activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-butyl-1-methylpyrrolidinium tricyanomethanide
• Vapor-liquid equilibrium of the (water + ethanol + glycerol) system: Experimental and modelling data at normal pressure
• Measurement and correlation of solubility of abietic acid in ethanol + water mixtures
• Biocompatible choline based ionic salts: Solubility in short-chain alcohols
• Isobaric (vapor + liquid) equilibria for the ternary system of (ethanol + water + 1,3-propanediol) and three constituent binary systems at P = 101.3 kPa
• Physical properties of the pure 1-methyl-1-propylpyrrolidinium bis(trifluoromethylsulfonyl)imide ionic liquid and its binary mixtures with alcohols
• Cation effect of ammonium imide based ionic liquids in alcohols extraction from alcohol-alkane azeotropic mixtures
• Thermodynamics and activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-butyl-1-methylmorpholinium tricyanomethanide
• Isobaric, isothermal theoretical investigation and examination of different prediction equations on some physicochemical properties in PEG liquid polymer system
• The study of activity coefficients at infinite dilution for organic solutes and water in 1-butyl-4-methylpyridinium dicyanamide, [B4MPy][DCA] using GLC
• Measurement and correlation of solubility of dodecanedioic acid in different pure solvents from T = (288.15 to 323.15) K
• Thermophysical properties of {R-fenchone + ethanol} at several temperatures and pressures
• Deterpenation of eucalyptus essential oil by liquid + liquid extraction: Phase equilibrium and physical properties for model systems at T = 298.2 K
• (Vapor-liquid) equilibria and excess Gibbs free energy functions of (ethanol + glycerol), or (water + glycerol) binary mixtures at several temperatures
• Measurement of activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-ethyl-3-methylimidazolium 2-(2-methoxyethoxy) ethylsulfate at T = (308.15, 313.15, 323.15 and 333.15) K using gas + liquid chromatography
• Measurement of activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-hexyl-1,4-diaza[2.2.2]bicyclooctanium bis(trifluoromethylsulfonyl)imide using gas-liquid chromatography
• Activity coefficients at infinite dilution of organic solutes in 1-hexyl-3- methylimidazolium trifluoroacetate and influence of interfacial adsorption using gas liquid chromatography
• Viscosities and densities of systems involved in the deterpenation of essential oils by liquid-liquid extraction: New UNIFAC-VISCO parameters
• Determination and correlation of the solubility of four Bronsted-acidic ionic liquids based on benzothiazolium cations in six alcohols
• Measurement and correlation of critical properties for binary mixtures and ternary mixtures containing gasoline additives
• Quantitative NMR spectroscopy of binary liquid mixtures (aldehyde + alcohol). Part III: (1-decanal or 3-phenylpropanal or 2-chlorobenzaldehyde) + (methanol or ethanol or 1-propanol)
• Effect of the temperature on the physical properties of the pure ionic liquid 1-ethyl-3-methylimidazolium methylsulfate and characterization of its binary mixtures with alcohols
• Measurement, correlation and dissolution thermodynamics of biological active chalcone in organic solvents at different temperatures
• Solubility of climbazole in various alcohols at different temperatures
• Experimental measurement and modelling of solubility of inosine-5'-monophosphate disodium in pure and mixed solvents
• Thermodynamics and activity coefficients at infinite dilution for organic solutes, water and diols in the ionic liquid choline bis(trifluoromethylsulfonyl)imide
• The physicochemical properties and solubility of pharmaceuticals - Methyl xanthines
• An odd-even effect on solubility of dicarboxylic acids in organic solvents
• Excess enthalpy for the (benzene + cyclohexane) mixture over a wide range of temperature and pressure
• Effect of temperature on density, sound velocity, refractive index and their derived properties for the binary systems (heptanoic acid + propanoic or butanoic acids)
• Phase behaviour of pseudo-binary systems of pressurized ((propane + L,L-lactide)) at different ethanol to L,L-lactide mole ratios
• Thermodynamic study of the surface of liquid mixtures containing pyridinium-based ionic liquids and alkanols
• Equilibrium solubility of sodium 3-sulfobenzoate in binary (sodium chloride + water), (sodium sulfate + water), and (ethanol + water) solvent mixtures at temperatures from (278.15 to 323.15) K
• Determination and correlation of solubility of spironolactone form II in pure solvents and binary solvent mixtures
• Determination and correlation of solubility of tylosin tartrate in alcohol mixtures
• A combined experimental and computational investigation of excess molar enthalpies of (nitrobenzene + alkanol) mixtures
• Measurement and correlation of solubility of 4-chloro-2,5-dimethoxynitrobenzene and 4-chloro-2,5- dimethoxyaniline in methanol, ethanol, xylene and toluene
• (Liquid + liquid) equilibria for mixtures of dodecane and ethanol with alkylsulfate-based ionic liquids
• Phosphoric-based ionic liquids as solvents to separate the azeotropic mixture of ethanol and hexane
• Equilibrium solubility of sodium 2-naphthalenesulfonate in binary (sodium chloride + water), (sodium sulfate + water), and (ethanol + water) solvent mixtures at temperatures from (278.15 to 323.15) K
• Thermodynamics of 4'-bromomethyl-2-cyanobiphenyl in different solvents
• Solubility of rutaecarpine and evodiamine in (ethanol + water) mixed solvents at temperatures from (288.2 to 328.2) K
• Solvation parameter model and thermodynamic parameters in a dicationic ionic liquid based on pyrrolidinium
• Experimental and theoretically study of interaction between organic compounds and tricyanomethanide based ionic liquids
• Solubility and solution thermodynamics of sorbic acid in eight pure organic solvents
• High-pressure phase equilibrium data for the (carbon dioxide + L-lactide + ethanol) system
• Isothermal (vapor + liquid) equilibria for the binary mixtures of (propylene oxide + ethanol) and (propylene oxide + 1-propanol) at several temperatures
• Activity coefficients at infinite dilution of organic solutes in methylphosphonate based ionic liquids using gas-liquid chromatography
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 4-(3-hydroxypropyl)-4-methylmorpholinium bis(trifluoromethylsulfonyl)-amide
• Thermodynamic models for determination of the solubility of (-)-shikimic acid in different pure solvents and in (H2O + ethanol) binary solvent mixtures
• Phase equilibrium data for systems composed of oregano essential oil compounds and hydroalcoholic solvents at T = 298.2 K
• Solubility of daidzin in different organic solvents and (ethyl alcohol + water) mixed solvents
• Properties of pure 1,1,3,3-tetramethylguanidine imidazole ionic liquid and its binary mixtures with alcohols at T = (293.15 to 313.15) K
• Determination and correlation of the solubility of tricin in water and ethanol mixtures
• High-pressure (vapour + liquid) equilibria for ternary systems composed by {(E)-2-hexenal or hexanal + carbon dioxide + water}: Partition coefficient measurement
• Activity coefficients at infinite dilution for organic solutes and water in 1-ethyl-1-methylpyrrolidinium lactate
• Measurement and correlation of the solubility of genistin in eleven organic solvents from T = (283.2 to 323.2) K
• Activity coefficients at infinite dilution, physicochemical and thermodynamic properties for organic solutes and water in the ionic liquid ethyl-dimethyl-(2-methoxyethyl)ammonium trifluorotris-(perfluoroethyl)phosphate
• Solubility of tridecanedioic acid in pure solvent systems: An experimental and computational study
• Measurement and correlation of the solubility of 3,4-bis(3-nitrofurazan-4-yl)furoxan (DNTF) in different solvents
• Measurements and equation-of-state modelling of thermodynamic properties of binary mixtures of 1-butyl-1-methylpyrrolidinium tetracyanoborate ionic liquid with molecular compounds
• (Vapour + liquid) equilibria, (VLE) excess molar enthalpies and infinite dilution activity coefficients of selected binary systems involving n-hexyl pyridinium bis(trifluoromethylsulphonyl)imide ionic liquid: Experimental and predictions using modified UNIFAC (Dortmund)
• Volumetric and compressibility behaviour of poly(propylene glycol) - Amino acid aqueous solutions at different temperatures
• Solubility measurement and modelling of 1,8-dinitronaphthalene in nine organic solvents from T = (273.15 to 308.15) K and mixing properties of solutions
• Solution thermodynamics of valnemulin hydrogen fumarate in different pure solvents
• Screening of environmental friendly ionic liquid as a solvent for the different types of separations problem: Insight from activity coefficients at infinite dilution measurement using (gas + liquid) chromatography technique
• Experimental determination and correlation of the solubility of 4-hydroxy-2,5-dimethyl-3(2H)-furanone (DMHF) in six different solvents
• Thermodynamic equilibrium of 4-hydroxy-2,5-dimethyl-3(2H)-furanone in different solvent systems
• Properties for binary mixtures of (acetamide + KSCN) eutectic ionic liquid with ethanol at several temperatures
• Solubility and solution thermodynamics of thymol in six pure organic solvents
• Solution thermodynamics of creatine monohydrate in binary (water + ethanol) solvent systems at T = (278.15 to 328.15) K
• Molar heat capacities of the mixture {1,8-cineole + ethanol} at several temperatures and atmospheric pressure
• Determination and correlation of pyridoxine hydrochloride solubility in different binary mixtures at temperatures from (278.15 to 313.15) K
• Correlation and thermodynamic analysis of solubility of diphenhydramine hydrochloride in pure and binary solvents
• Speed of sound measurements of liquid C1-C4 alkanols
• (Liquid + liquid) equilibrium for systems composed of clove and allspice essential oil compounds and hydrous ethanol at T = 298.2 K
• Solubility modelling and thermodynamic dissolution functions of phthalimide in ten organic solvents
• Measurement and correlation of solubility of thiourea in two solvent mixtures from T = (283.15 to 313.15) K
• Thermodynamic models for determination of the solubility of omeprazole in pure and mixture organic solvents from T = (278.15 to 333.15) K
• Ternary (liquid + liquid) equilibria for the extraction of ethanol, or 2-propanol from aqueous solutions with 1,1'-oxybis(butane) at different temperatures
• Determination and correlation of solubility and solution thermodynamics of oxiracetam in three (alcohol + water) binary solvents
• Solubility of rosuvastatin calcium in different neat solvents at different temperatures
• Measurement and correlation of solubility of cefmenoxime hydrochloride in pure solvents and binary solvent mixtures
• Solubility and solution thermodynamics of ethyl 5-amino-4-cyano-3-(2-ethoxy-2-oxoethyl)-2-thiophenecarboxylate in nine organic solvents at evaluated temperatures
• Determination and correlation of solubility and thermodynamic properties of L-methionine in binary solvents of water + (methanol, ethanol, acetone)
• Isobaric VLE of the mixture {1,8-cineole + ethanol}. EOS analysis and COSMO-RS modeling
• Physicochemical properties of binary mixtures of 1,1,3,3-tetramethylguanidine imidazolide ionic liquid with water and alcohols
• A 1-alkylcyanopyridinium-based ionic liquid in the separation processes
• Thermodynamic models for determination of the solubility of 4-(4-aminophenyl)-3-morpholinone in different pure solvents and (1,4-dioxane + ethyl acetate) binary mixtures with temperatures from (278.15 to 333.15) K
• Solubility measurement and thermodynamic functions of dehydroepiandrosterone acetate in different solvents at evaluated temperatures
• Experimental measurement and correlation of the solubility of aloe-emodin in seven pure solvents
• NaCl and KCl effect on (vapour + liquid) equilibrium of binary, ternary and quaternary systems involving water, ethanol and glycerol at low pressures
• Solubility determination and thermodynamic dissolution functions of 1,3-diphenylguanidine in nine organic solvents at evaluated temperatures
• Measurement and calculation of solid liquid equilibrium for ternary systems of 3,4-dichloronitrobenzene + 2,3-dichloronitrobenzene + ethanol/n-propanol
• Measurement and correlation of solubility of pronamide in five organic solvents at (278.15-323.15) K
• Measurement and thermodynamic functions of solid-liquid phase equilibrium of D-(-)-quinic acid in H2O, methanol, ethanol and (H2O + methanol), (H2O + ethanol) binary solvent mixtures
• Densities and derived thermodynamic properties for the (n-heptane + n-octane), (n-heptane + ethanol) and (n-octane + ethanol) systems at high pressures
• Solubility determination and thermodynamic modeling of 5-nitro-8- hydroxyquinoline in ten organic solvents from T = (278.15 to 313.15) K and mixing properties of solutions
• Solubility and thermodynamic function of a bioactive compound bergenin in various pharmaceutically acceptable neat solvents at different temperatures
• Determination and correlation of solubility and thermodynamic properties of pyraclostrobin in pure and binary solvents
• Solubility and solution thermodynamics of 2-methyl-6-nitroaniline in ten organic solvents at elevated temperatures
• Effect of temperature and composition on the surface tension and surface properties of binary mixtures containing DMSO and short chain alcohols
• (Liquid + liquid) equilibria of four alcohol-water systems containing 1,8-cineole at T = 298.15 K
• Solubility determination and thermodynamic models for dehydroepiandrosterone acetate in mixed solvents of (ethyl acetate + methanol), (ethyl acetate + ethanol) and (ethyl acetate + isopropanol)
• Thermodynamics and selectivity of separation based on activity coefficients at infinite dilution of various solutes in 1-allyl-3-methylimidazolium bis{(trifluoromethyl)sulfonyl}imide ionic liquid
• Determination and correlation of solubility of 4'-bromomethyl-2-cyanobiphenyl in acetone + (ethanol, n-propanol, n-butanol) mixtures
• Thermodynamic study of the solubility of 2,4'-dihydroxydiphenyl sulfone in nine organic solvents from T = (278.15 to 313.15) K and thermodynamic properties of dissolution
• Solubility determination and thermodynamic modeling of 2,4-dinitroaniline in nine organic solvents from T = (278.15 to 318.15) K and mixing properties of solutions
• Solubility determination and thermodynamic modelling of terephthaldialdehyde in ten organic solvents from T = (273.15 to 318.15) K and mixing properties of solutions
• Separation of aliphatic from aromatic hydrocarbons and sulphur compounds from fuel based on measurements of activity coefficients at infinite dilution for organic solutes and water in the ionic liquid N,N-diethyl-N-methyl-N-(2-methoxy-ethyl)ammonium bis(trifluoromethylsulfonyl)imide
• Solubility determination and thermodynamic modeling of 3-methyl-4- nitrobenzoic acid in twelve organic solvents from T = (283.15-318.15) K and mixing properties of solutions
• Determination and correlation thermodynamic models for solid liquid equilibrium of the Nifedipine in pure and mixture organic solvents
• Measurement and modelling of econazole nitrate in twelve pure organic solvents at temperatures from 278.15 K to 318.15 K
• Measurement and prediction of dabigatran etexilate mesylate Form II solubility in mono-solvents and mixed solvents
• Solubility of cefoxitin acid in different solvent systems
• Experimental study on the calorimetric data of 2-butoxyethanol with aliphatic alcohols (C1-C4) and correlation with the Wilson, NRTL and UNIQUAC models at T = 298 K
• Solubility determination and thermodynamic modelling of 2,4-dihydro-5-methyl-2-(4-methylphenyl)-3H-pyrazol-3-one in twelve organic solvents from T = (278.15 to 313.15) K and mixing properties of solutions
• Thermodynamics and limiting activity coefficients measurements for organic solutes and water in the ionic liquid 1-dodecyl-3-methylimidzolium bis(trifluoromethylsulfonyl) imide
• Solubility measurement and correlation of 4-nitrophthalimide in (methanol, ethanol, or acetone) + N,N-dimethylformamide mixed solvents at temperatures from 273.15 K to 323.15 K
• Solubility of N-phenylanthranilic acid in nine organic solvents from T = (283.15 to 318.15) K: Determination and modelling
• Thermodynamic functions of 1-methyl-4-(methylsulfonyl)benzene solubility in nine organic solvents from T = (278.15 to 318.15) K
• Determination and thermodynamic modelling for 4-nitropyrazole solubility in (methanol + water), (ethanol + water) and (acetonitrile + water) binary solvent mixtures from T = (278.15 to 318.15) K
• Correlation and thermodynamic analysis of solubility of cefmetazole acid in three (alcohol + water) binary solvents at temperatures from 278.15 K to 303.15 K
• Ferulic acid solubility in supercritical carbon dioxide, ethanol and water mixtures
• Solubility measurement and modelling of ethyl 5-amino-4-cyano-3-(2-ethoxy-2-oxoethyl)-2-thiophenecarboxylate in four groups mixed solvents
• Thermodynamic and spectroscopic properties of binary mixtures of n-butylammonium butanoate ionic liquid with alcohols at T = (293.15-313.15) K
• Solubility of oxcarbazepine in eight solvents within the temperature range T = (288.15 308.15) K
• Thermodynamic modelling for solubility of 4-nitrobenzaldehyde in different solvents at temperature range from (273.15 to 313.15) K and mixing properties of solutions
• Determination and modelling of troxerutin solubility in eleven mono-solvents and (1,4-dioxane + 2-propanol) binary solvents at temperatures from 288.15 K to 323.15 K
• Fully automatized apparatus for determining speed of sound for liquids in the temperature and pressure interval (283.15-343.15) K and (0.1-95) MPa
• Volumetric and sound speed study of ammonium-based ionic liquid mixtures with ethanol
• Solubility determination and thermodynamic modelling of 3-amino-1,2,4-triazole in ten organic solvents from T = 283.15 K to T = 318.15 K and mixing properties of solutions
• Investigation on molecular interactions of antibiotics in alcohols using volumetric and acoustic studies at different temperatures
• Solubility determination and thermodynamic modeling of paclobutrazol in nine organic solvents from T = (278.15 to 318.15) K and mixing properties of solutions
• Solubility of L-histidine in different aqueous binary solvent mixtures from 283.15 K to 318.15 K with experimental measurement and thermodynamic modelling
• Thermodynamic modelling for solubility of 5-chloro-1-methyl-4-nitroimidazole in eleven organic solvents from T = (283.15 to 318.15) K
• Measurement and correlation of the diffusion coefficients of chromium (III) acetylacetonate at infinite dilution in supercritical carbon dioxide and in liquid ethanol
• Measurement and correlation of solubility of ciclesonide in seven pure organic solvents
• Thermodynamic properties of L-Theanine in different solvents
• Solubility determination and correlation for o-phenylenediamine in (methanol, ethanol, acetonitrile and water) and their binary solvents from T = (283.15-318.15) K
• Thermodynamic study of solubility for 2-amino-4-chloro-6-methoxypyrimidine in twelve organic solvents at temperatures from 273.15 K to 323.15 K
• Solid-liquid phase equilibrium and dissolution properties of ethyl vanillin in pure solvents
• Solubility and solution thermodynamics of 2-methyl-4-nitroaniline in eleven organic solvents at elevated temperatures
• Solubility measurement and thermodynamic functions of 3-nitrobenzaldehyde in different solvents at elevated temperatures
• Determination and thermodynamic modelling for 2-methyl-6-nitroaniline solubility in binary solvent mixtures of ethyl acetate + (methanol, ethanol, n-propanol and isopropanol)
• Determination and correlation of terephthaldialdehyde solubility in (ethanol, isopropanol, ethyl acetate, isopentanol) + N,Ndimethylformamide mixed solvents at temperatures from 273.15 K to 318.15 K
• High pressure densities and derived thermodynamic properties for the (n-heptane + n-octane + ethanol) ternary system
• Solubility determination and modelling of 4-nitro-1,2-phenylenediamine in eleven organic solvents from T = (283.15 to 318.15) K and thermodynamic properties of solutions
• Solubility determination and thermodynamic modelling for 2-amino-4-chlorobenzoic acid in eleven organic solvents from T = (278.15 to 313.15) K and mixing properties of solutions
• Liquid-liquid equilibrium measurements and correlation for phase behaviors of alcohols + heptane + ILs ternary systems
• Solubility determination and thermodynamic functions of 2-chlorophenothiazine in nine organic solvents from T = 283.15 K to T = 318.15 K and mixing properties of solutions
• Solubility and thermodynamic properties of vanillyl alcohol in some pure solvents
• Solubility and thermodynamic functions of tebuconazole in nine organic solvents from T = (278.15 to 313.15) K and mixing properties of solutions
• Thermodynamic models for determination of solid liquid equilibrium of the 6-benzyladenine in pure and binary organic solvents
• Determination and correlation of solid-liquid phase equilibrium and phase diagram for multicomponent system of mixed dibasic acids. (III) Ternary system of succinic acid + glutaric acid + ethanol system
• Solubility of 2-isopropylimidazole in nine pure organic solvents and liquid mixture of (methanol + ethyl acetate) from T = (278.15 to 313.15) K: Experimental measurement and thermodynamic modelling
• Excess molar enthalpies of ethane-1,2-diamine plus primary and secondary alkanols (C1-C4) and correlation with Redlich-Kister, Wilson, NRTL and UNIQUAC models at T = 298 K
• Thermodynamic equilibrium of hydroxyacetic acid in pure and binary solvent systems
• Solubility of 2-nitro-p-phenylenediamine in nine pure solvents and mixture of (methanol + N-methyl-2-pyrrolidone) from T = (283.15 to 318.15) K: Determination and modelling
• Effect of temperature on density, sound velocity, and their derived properties for the binary systems glycerol with water or alcohols
• Solubility of 4-methyl-2-nitroaniline in fourteen organic solvents from T = (278.15 to 313.15) K and mixing properties of solutions
• Solubility determination and thermodynamic modelling of 3,5-dimethylpyrazole in nine organic solvents from T = (283.15 to 313.15) K and mixing properties of solutions
• Thermodynamic functions for solubility of 3-nitro-o-toluic acid in nine organic solvents from T = (283.15 to 318.15) K and apparent thermodynamic properties of solutions
• Separation of binary mixtures hexane/hex-1-ene, cyclohexane/cyclohexene and ethylbenzene/styrene based on limiting activity coefficients
• Measurement and correlation of (vapour-liquid) equilibrium for binary mixtures composed of 1-(ethoxymethoxy)-propane with ethanol and 1-propanol at 101.33 kPa
• Thermodynamic properties of enantiotropic polymorphs of glycolide
• Measurement and thermodynamic modeling of ternary (liquid + liquid) equilibrium for extraction of ethanol from diethoxymethane solution with different solvents
• Isobaric molar heat capacities of the mixture (p-cymene + ethanol) at several temperatures and atmospheric pressure
• Liquid-liquid equilibrium of ternary systems comprising ethyl valerate(1), water(2), ethanol(3) and valeric acid(4)
• Solubility and preferential solvation of econazole nitrate in binary solvent mixtures of methanol, ethanol and 1,4-dioxane in water
• Thermodynamic study of solubility for pyrazinamide in ten solvents from T = (283.15 to 323.15) K
• Measurement and correlation of solubility of boscalid with thermodynamic analysis in pure and binary solvents from 288.15 K to 313.15 K
• Solubility modelling and dissolution properties of 5-phenyltetrazole in thirteen mono-solvents and liquid mixtures of (methanol + ethyl acetate) at elevated temperatures
• Solubility modelling and preferential solvation of paclobutrazol in cosolvent mixtures of (ethanol, n-propanol and 1,4-dioxane) + water
• Solubility, solution thermodynamics and preferential solvation for 4- bromopyrazole in mixed solvents of (methanol/ethanol + water) from T = (283.15 to 318.15) K
• Phase equilibrium measurements and thermodynamic modelling for the systems involving valeric acid, ethanol, ethyl valerate and water plus CO2
• Solubility modelling, solution thermodynamics and preferential solvation for nitroxoline in solvent mixtures of ethyl acetate + (methanol, ethanol, n-propanol and isopropanol)
• Thermodynamic and molecular investigation into the solubility, stability and self-assembly of gabapentin anhydrate and hydrate
• Solubility and preferential solvation of 2-methyl-4-nitroaniline in mixed solvents of ethyl acetate + (methanol, ethanol, n-propanol and isopropanol)
• Physical properties of systems of interest to the edible oil industry: Viscosities and densities of model systems formed by (triacylglycerol + fatty acid + solvent)
• Thermodynamics and activity coefficients at infinite dilution for organic compounds and water in the ionic liquid 1-butyl-3-methylimidazolium perchlorate
• Vapour-liquid equilibria for (water + ethanol + fructose): Experimental data and thermodynamic modelling
• Excess molar volume and excess Gibbs energy of activation for viscous flow for the binary mixtures of N-ethylpyridinium dicyanamide [C2py][DCA] with alcohols
• Phase behaviour of the pseudo-ternary system carbon dioxide + ethanol + fish oil at high pressures
• Experiment and correlation of the equilibrium interfacial tension for paraffin + CO2 modified with ethanol
• Separation of water/butan-1-ol based on activity coefficients at infinite dilution in 1,3-didecyl-2-methylimidazolium dicyanamide ionic liquid
• Estimation and confirmation of the thermodynamic stability relationships of the enantiotropic polymorphs of glycolide
• Study of liquid-liquid extraction of ethanol + water azeotropic mixtures using two imidazolium-based ionic liquids
• Separation of binary mixtures hexane/hex-1-ene, cyclohexane/cyclohexene and ethylbenzene/styrene based on gamma infinity data measurements
• Thermophysical properties of binary mixtures of 1-butyl-1-methylpyrrolidinium trifluoromethanesulfonate ionic liquid with alcohols at several temperatures
• Separation of binary mixtures based on gamma infinity data using [OMMIM][NTf2] ionic liquid and modelling of thermodynamic functions
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid trihexyl-tetradecyl-phosphonium tricyanomethanide
• Solubility and thermodynamics of vitamin C in binary liquid mixtures involving water, methanol, ethanol and isopropanol at different temperatures
• Thermodynamic study of molecular interaction-selectivity in separation processes based on limiting activity coefficients
• Thermodynamics properties of binary mixtures of aqueous solutions of glycols at several temperatures and atmospheric pressure
• Temperature and composition dependence of the volumetric and acoustic properties of ionic liquid [emim][HSO4] with polar protic and aprotic co-solvents
• Experimental and modeling vapor-liquid equilibrium for the binary systems {ethanol(1) + glycerol(2)} and {tert-butanol(1) + glycerol(2)} at high pressures
• Abraham model correlations for describing the thermodynamic properties of solute transfer into pentyl acetate based on headspace chromatographic and solubility measurements
• Solubility of l-tyrosine in aqueous solutions of methanol, ethanol, n-propanol and dimethyl sulfoxide: Experimental determination and preferential solvation analysis
• Thermodynamics and selectivity of separation based on activity coefficients at infinite dilution of various solutes in ionic liquid [HMMIM][BF4]
• Electrostriction of water and lower alcohols around ammonium nitrate - Volumetric approach
• Experimental investigations on the liquid thermal conductivity of five saturated fatty acid methyl esters components of biodiesel
• Thermodynamic evidence for nano-heterogeneity in solutions of the macrocycle C-butylresorcin[4]arene in non-aqueous solvents
• Thermodynamic behaviour of alkyl lactate-alkanol systems
• The use of ionic liquids for separation of binary hydrocarbons mixtures based on gamma infinity data measurements
• Construction and evaluation of ternary solid-liquid phase diagram of pyraclostrobin (form IV) and its intermediate in ethanol and N,N-dimethylformamide
• Solubility modelling, solvent effect and preferential solvation of 6-chloropurine in several aqueous co-solvent mixtures between 283.15 K and 328.15 K
• Solubility modelling, solvent effect and preferential solvation of carbendazim in aqueous co-solvent mixtures of N,N-dimethylformamide, methanol, ethanol and n-propanol
• The molar surface Gibbs energy and its application to the binary mixtures of N-butylpyridinium dicyanamide [C4py][DCA] with alcohols
• Experimental solubility evaluation and thermodynamic analysis of biologically active D-tryptophan in aqueous mixtures of N,N-dimethylformamide and several alcohols
• Thermodynamics and activity coefficients at infinite dilution for organic compounds in the ionic liquid 1-hexyl-3-methylimidazolium chloride
• Separation of binary mixtures based on gamma infinity data using [OMMIM][BF4] ionic liquid and modelling of thermodynamic functions
• Equilibrium solubility, solvent effect and preferential solvation of chlorhexidine in aqueous co-solvent solutions of (methanol, ethanol, N,N-dimethylformamide and 1,4-dioxane)
• Solubility of dibenzothiophene in nine organic solvents: Experimental measurement and thermodynamic modelling
• Determination of the thermodynamic parameters of ionic liquid 1-propyl-3-methylimidazolium bromide by gas-liquid chromatography
• Experimental solubility evaluation and thermodynamic analysis of quinocetone in aqueous co-solvent solutions of ethanol, isopropanol, dimethyl sulfoxide and N,N-dimethylformamide
• Thermodynamic solubility modeling, solvent effect and preferential solvation of curcumin in aqueous co-solvent mixtures of ethanol, n-propanol, isopropanol and propylene glycol
• The dissolution behavior and apparent thermodynamic analysis of temozolomide in pure and mixed solvents
• Separation of ethanol from n-decane-ethanol mixtures using imidazolium based ionic liquids
• Solubility modelling, solvent effect and preferential solvation of allopurinol in aqueous co-solvent mixtures of ethanol, isopropanol, N,N-dimethylformamide and 1-methyl-2-pyrrolidone
• Mass density, sound velocity, mixing enthalpy, 1H NMR, Ab initio calculations and intermolecular interactions in binary mixtures of N-methylimidazole + water, +methanol, +ethanol, +1-propanol, +2-propanol
• Isobaric vapour-liquid equilibrium for binary systems of ethyl iodide with ethanol, propionic acid and ethyl propionate at 101.3 kPa
• Solubility and critical surface in the system propionic acid-ethanol-ethyl propionate-water at 293.15, 303.15 and 313.15 K
• Solubility parameter of lenalidomide for predicting the type of solubility profile and application of thermodynamic model
• Solubility modelling and thermodynamic aspect of 2,3-dihydro-6-propyl-2-thioxo-4(1H)-pyrimidinone in binary aqueous solutions of several alcohols
• Thermodynamic and spectroscopic study of molecular interactions between ethanol and isomeric cresols
• Solubility and thermodynamic properties of dirithromycin form A and form B in pure solvents and binary solvent mixture
• Equilibrium solubility determination, modelling and preferential solvation of bioactive iminodibenzyl in aqueous co-solvent mixtures at various temperatures
• Equilibrium solubility of dinitolmide in several neat solvents and binary aqueous co-solvent mixtures: Experimental determination and thermodynamic analysis
• Measurement and correlation of solubility of methyleneaminoacetonitrile in pure and binary solvents and thermodynamic properties of solution
• Volumetric properties of monoethanolamine and alcohol binary mixtures at different temperatures and 0.1 MPa
• Vapour-liquid equilibrium measurements and extractive distillation process design for separation of azeotropic mixture (dimethyl carbonate + ethanol)
• Research on the application of 7-chloro-quinaldine adducts in 7-chloro-quinaldine separation process
• Thermodynamic properties of paracetamol impurities 4-nitrophenol and 4'-chloroacetanilide and the impact of such impurities on the crystallisation of paracetamol from solution
• Determination and correlation of solubility and solution thermodynamics of saccharin in different pure solvents
• Thermodynamic and spectroscopic study of binary mixtures containing {dimethyl carbonate (DMC) + alcohols} at T = (288.15-308.15) K and p = (0.1-40) MPa: Experimental study and modelling
• Thermodynamic solubility modelling, solvent effect and preferential solvation of naftopidil in aqueous co-solvent solutions of (n-propanol, ethanol, isopropanol and dimethyl sulfoxide)
• Volumetric and viscometric properties of ternary solution of (N-methyldiethanolamine + monoethanolamine + ethanol)
• Excess volumes and partial molar volumes of binary liquid mixtures of furfural or 2-methylfuran with alcohols at 298.15 K
• Surface tension and interfacial compositions of binary glycerol/alcohol mixtures
• Solubility and vapor pressure data of bioactive 6-(acetylamino)-N-(5-ethyl-1,3,4-thiadiazol-2-yl) hexanamide
• Determination and correlation of solubility and solution thermodynamics of musk xylene in different pure solvents
• Densities and viscosities of binary mixtures of 2,2-diethyl-1,1,3,3-tetramethylguanidinium bis(trifluoromethylsulfonyl)imide with methanol and ethanol
• Solubility of CO2 in methanol, ethanol, 1,2-propanediol and glycerol from 283.15 K to 373.15 K and up to 6.0 MPa
• Thermodynamic solubility modelling, solvent effect and preferential solvation of p-nitrobenzamide in aqueous co-solvent mixtures of dimethyl sulfoxide, ethanol, isopropanol and ethylene glycol
• Separation of (water/butan-1-ol) binary systems based on activity coefficients at infinite dilution with phosphonium ionic liquid
• The molar surface quasi-Gibbs energy and its application to the binary mixtures of 1-(2-methoxyethyl)-3-methylimidazolium bis[(trifluoromethyl)sulfonyl]imide [MOEMIM][NTf2] with methanol and ethanol
• The dissolution behaviour and apparent thermodynamic analysis of diprophylline in pure and mixed solvents
• Solubility behaviour and thermodynamic analysis of methyleneaminoacetonitrile in binary (ethanol + water, ethanol + 2-propanol, ethanol + n-butanol) solvents
• Measurement of the thermal conductivity of five aliphatic esters in the liquid phase
• Co-solvence phenomenon and thermodynamic properties of edaravone in pure and mixed solvents
• Solvent effect on solubility and preferential solvation analysis of buprofezin dissolved in aqueous co-solvent mixtures of N,N-dimethylformamide, ethanol, acetonitrile and isopropanol
• Improving the solubility of temozolomide by cosolvent and its correlation with the Jouyban-Acree and CNIBS/R-K models
• Solubility and mixing thermodynamic properties of levamisole hydrochloride in twelve pure solvents at various temperatures
• Vapor-liquid equilibrium and excess properties of the binary mixtures formed by ethyl isobutyrate and n-alkanols
• Excess molar enthalpies of methyl isobutyl ketone (MIBK) with alkan-1-ols (C1-C6) and their correlations at 298.15 K
• Excess molar enthalpies of binary mixtures containing ethylene glycols or poly(ethylene glycols) + ethyl alcohol at 308.15K and atmospheric pressure
• Molar excess enthalpies of ethyl acetate + alkanols at T=298.15K, p=10MPa
• PHYSICAL AND EXCESS PROPERTIES OF BINARY AND TERNARY MIXTURES OF 1,1-DIMETHYLETHOXY-BUTANE, METHANOL, ETHANOL AND WATER AT 298.15K.
• Construction of solid liquid phase diagrams in ternary systems by titration calorimetry
• Thermophysical properties and thermodynamic phase behavior of ionic liquids
• Excess molar enthalpies and heat capacities of dimethyl sulfoxide + seven normal alkanols at 303.15K and atmospheric pressure
• Thermodynamic properties of binary mixtures of 2.2.2-Trifluoroethanol with Water or Alkanols at T=298.15 K
• Excess molar enthalpies for binary mixtures of trimethyl phosphate with alkanols {CH3(CH2)nOH, n = 0 3} at 298.15K
• High-pressure densities and derived volumetric properties (excess and partial molar volumes, vapor-pressures) of binary methanol + ethanol mixtures
• Measurement and correlation of saturated vapor pressure of 2,4,6,8,10-pentamethylcyclopentasiloxane by means of an inclined ebulliometer
• Measurement and correlation of the solubility of urea l-tartaric acid in aqueous ethanol solution
• Topological investigations of the molecular species and molecular interactions that characterize pyrrolidin-2-one + lower alkanol mixtures
• Experimental and predicted excess molar enthalpies of some working pairs for absorption cycles
• Excess molar volumes of Diisopropylamine + (C1-C5) Alkan-1-ols: application of the ERAS model and cubic EOS
• Solubilities of benzene sulfonamide in supercritical CO2 in the absence and presence of cosolvent
• Densities and Excess Molar Volumes for Binary Mixtures of Diethanolamine with Water, Methanol, Ethanol and Ternary Solutions of Diethanolamine + Water with Methanol, Ethanol at Atmospheric Pressure from 278.15 to 353.15 K
• Solubilities of succinimide in different pure solvents and binary methanol+ethyl acetate solvent mixtures
• Solubilities of 1,3-dimethyl-1,1,3,3-tetraphenyldisiloxane in different solvents from (288.15 to 313.15) K
• Measurement of solubility of mitomycin C in ethanol-water solutions at different temperatures
• Liquid-Liquid Equilibrium of Aqueous Two-Phase Systems Composed of Hydrophilic Alcohols (Ethanol/2-Propanol/1-Propanol) and MgSO4 /ZnSO4 at (303.15 and 313.15) K and Correlation
• Solubility in binary solvent mixtures: pyrene dissolved in alcohol + toluene mixtures
• Solubility, dissolution enthalpy and entropy of L-Glutamine in mixed solvents of ethanol+water and acetone+water
• Solubility of disodium cytidine 5'-monophosphate in different binarymixtures from 288.15 K to 313.15 K
• Apparent molar volume and apparent molar isentropic compressibility for thebinary systems {methyltrioctylammoniumbis(trifluoromethylsulfonyl)imide + ethyl acetate or ethanol} at different temperatures underatmospheric pressure
• Liquid liquid equilibria of hydrophilic alcohol + sodiumhydroxide + water systems: Experimental and correlation
• Refractive properties of binary mixtures containing pyridinium-basedionic liquids and alkanols
• Effects of temperature and concentration on interactions in (methanol + ethyl acetate) and (ethanol + methyl acetate or ethyl acetate) systems: insights from apparent molar volume and apparent molar isentropic compressibility study
• Study of intermolecular interactions in binary mixtures of 2-(dimethylamino)ethanol with methanol and ethanol at various temperatures
• Influence of alkyl group and temperature on thermophysical properties of carboxylic acid and their binary mixtures
• Solubility and solution thermodynamics of 2,5-thiophenedicarboxylic acid in (water + ethanol) binary solvent mixtures
• Thermogravimetric measurement of evaporation: Data analysis based on the Stefan tube
• Effects of alkyl group and temperature on the interactions between furfural and alcohol: Insight from density and sound velocity studies
• Volumetric and acoustic properties of binary systems (furfural or furfuryl alcohol + toluene) and (furfuryl alcohol + ethanol) at different temperatures
• Mutual diffusion behavior of short chain alcohols + n-octane mixtures
• Measurement and correlation of the solubility of (1-benzyl-1H-1,2,3-triazole-4-yl)methanol in water and alcohols at temperatures from 292.15 K to 310.15 K
• Determination and correlation of solubility and mixing properties of isonicotinamide (form II) in some pure solvents
• Experimental measurement and phase equilibria calculation for ternary systems of carbon dioxide+ toluene + naphthalene and carbon dioxide+ ethanol + acridine, applicable for fine particle production in GAS process
• Vapor-liquid equilibria, density and sound velocity measurements of (water or methanol or ethanol + 1,3-propanediol) binary systems at different temperatures
• Microscale calorimetric device for determining reaction parameters
• Physico-chemical study of bioactive N-(5-ethyl-1,3,4-thiadiazole-2-yl)-4-nitrobenzamide: Sublimation, solubility and distribution
• Renewable platform chemicals: Thermochemical study of levulinic acid esters
• Measurement and correlation of solubility of carbendazim in lower alcohols
• Experimental solubility and thermodynamic aspects of methylene blue in different solvents
• Apparent thermodynamic analysis and the dissolution behavior of levamisole hydrochloride in three binary solvent mixtures
• The excess molar volume and the molar surface Gibbs energy of the binary of the ether-functionalized ionic liquids [C22O1IM][TfO] with ethanol and isomeric propanols at T = (288.15-318.15) K
• Isobaric Vapor Liquid Equilibria for Binary Systems of Diethyl Carbonate + Propylene Carbonate, Diethyl Carbonate + Propylene Glycol, and Ethanol + Propylene Carbonate at 101.3 kPa
• Vapor Liquid Equilibrium of Water + Ethanol + Glycerol: Experimental Measurement and Modeling for Ethanol Dehydration by Extractive Distillation
• Modified Method for Measuring the Solubility of Pharmaceutical Compounds in Organic Solvents by Visual Camera
• Determination and Correlation of Solubility of N-tertbutylacrylamide in Seven Different Solvents at Temperatures between (279.15 and 353.15) K
• Capillary Viscometer and Vibrating Tube Densimeter for Simultaneous Measurements up to 70 MPa and 423 K
• Experimental and Computational Thermodynamic Properties of (Benzyl alcohol + Alkanols) Mixtures
• Solubility and Solution Thermodynamics of Gibberellin A4 in Different Organic Solvents from 278.15 K to 333.15 K
• Solubility of Etoricoxib in Aqueous Solutions of 1,4-Butanediol, 1,4-Dioxane, N,N-Dimethylacetamide, N,N-Dimethylformamide, Dimethyl Sulfoxide, and Ethanol at 298.2 K
• Influence of the Temperature on the Liquid Liquid Solid Equilibria of the Water + Ethanol + 1-Undecanol Ternary System
• Determination of the Solubility of Ammonium Dihydrogen Phosphate in Water Ethanol System at Different Temperatures from 283.2 to 343.2 K
• Densities and Viscosities of Binary Mixtures of 2-Ethyl-1,1,3,3- tetramethylguanidinium Ionic Liquids with Ethanol and 1-Propanol
• Liquid-liquid equilibria of water + ethanol + 1-butyl-3- methylimidazolium bis(trifluoromethanesulfonyl)imide ternary system: measurements and correlation at different temperatures
• Lamotrigine Solubility in Some Nonaqueous Solvent Mixtures at 298.2 K
• Density and Viscosity for Binary Mixtures of the Ionic Liquid 2,2-Diethyl-1,1,3,3-Tetramethylguanidinium Ethyl Sulfate with Water, Methanol, or Ethanol
• Solubility Measurement and Correlation for 2- Naphthaldehyde in Pure Organic Solvents and Methanol + Ethanol Mixtures
• Solubility and Thermodynamic Analysis of Tenoxicam in Different Pure Solvents at Different Temperatures
• Investigation of Surface and Solubility Properties of N-Vinylimidazolium Tetrahalogenidoferrate(III) Magnetic Ionic Liquids Using Density Functional Theory
• Liquid-Liquid Equilibrium for the Ternary System 2,2,3,3,4,4,5,5-Octafluoro-1-Pentanol + Ethanol + Water at (298.15, 308.15, and 318.15) K
• Equilibrium Solubilities of Diisooctyl Sebacate in Supercritical Carbon Dioxide
• Application of Conductance Study to Analyze Micellization Behavior of Cationic Gemini Surfactants in Water and Water Ethanol Solvent Mixed Media
• Solubility, Density, and Metastable Zone Width of Pyridoxine Hydrochloride in Water and Ethanol Solvent Mixtures
• Thermodynamic Analysis of the Experimental Equilibria for the Liquid-Phase Etherification of Isobutene with C1 to C4 Linear Primary Alcohols
• Measurement and Correlation of the Solubility of Maltitol in Different Pure Solvents, Methanol Water Mixtures, and Ethanol Water Mixtures
• Isobaric Vapor Liquid Equilibrium for the Binary Systems of sec-Butyl Acetate + Methyl Ethyl Ketone, 2-Methoxyethanol, or 1,2-Dimethoxyethane at 101.3 kPa
• Solubility and Solution Thermodynamics of the d Form of l-Citrulline in Water + Ethanol Binary Solvent Mixtures
• Solubility of Trimethoprim in Selected Pure Solvents and (Water + Ethanol/2-Propanol) Mixed-Solvent Systems
• Measurement and Correlation of Solubility of Cefathiamidine in Water + (Acetone, Ethanol, or 2-Propanol) from (278.15 to 308.15) K
• Measurement and Correlation of the Solubility of Vanillic Acid in Eight Pure and Water + Ethanol Mixed Solvents at Temperatures from (293.15 to 323.15) K
• Determination and Modeling of MgCl2 Solubility in Methanol, Ethanol, 2-Propanol and Their Mixtures from 283 to 343 K
• Measurement and Correlation of the Solubility of Sodium 2- Chlorotoluene-4-sulfonate in Selected Pure Solvents and Aqueous Organic Solutions
• Solubility Measurement and Simulation of Rivaroxaban (Form I) in Solvent Mixtures from 273.15 to 323.15 K
• Solubility Measurement and Modeling of 4,4'-Dihydroxydiphenyl Sulfone in Nine Organic Solvents from T = (278.15 to 313.15) K and Thermodynamic Property of Dissolution
• Thermodynamic Models for Determination of the Solubility of Boc-(R)-3-Amino-4-(2, 4, 5-trifluorophenyl)butanoic acid in Different Pure Solvents and (Tetrahydrofuran + n-Butanol) Binary Mixtures with Temperatures from 280.15 to 330.15 K
• Solubility Determination and Modeling of Sodium Mononitrobenzenesulphonate in Different Solvents at Temperatures Ranging from (283.15 to 323.15) K
• Experimental Measurement and Modeling of the Solubility of Methane in Methanol and Ethanol
• Liquid-Liquid Equilibria for Ternary Systems of Water + Methoxycyclopentane (CPME) + Alcohol; Methanol, Ethanol, 1-Propanol, or 2-Propanol
• Solid Liquid Phase Equilibrium of trans-Cinnamic Acid in Several Alcohols: Measurements and Thermodynamic Modeling
• Measurement and Correlation of the Solubility of Antioxidant 626 in Alcohols
• Measurement and Correlation of Solubility of -Aminobutyric Acid in Different Binary Solvents
• Solubility of 1,3,5-Benzenetricarboxylic Acid in Different Solvents
• Thermodynamics of 1,3-dimethylurea in eight alcohols
• Surface Tension of Binary Mixtures of 2,2,4-Trimethylpentane +1-Alkanols from 298.15 to 323.15 K
• Measurements of Infinite Dilution Activity Coefficients of Alkanols in the Ionic Liquid Tributylmethylammonium Methyl Sulfate Using HS-SPME/GC/FID
• Activity Coefficients at Infinite Dilution of Organic Solutes and Water in Tributylethylphosphonium Diethylphosphate Using Gas Liquid Chromatography: Thermodynamic Properties of Mixtures Containing Ionic Liquids
• Measurement and Correlation of the Solubility for Camptothecine in Different Organic Solvents
• Density, Speed of Sound, Refractive Index, and Viscosity of the Binary Mixtures of N,N-dimethylacetamide with Methanol and Ethanol
• Isobaric Vapor Liquid Equilibrium for Binary Systems of Allyl Alcohol with Water, Methanol, and Ethanol at 101.3 kPa
• Solubility Modeling of 4-(Methylsulfonyl)benzaldehyde in Nine Organic Solvents at Elevated Temperatures
• Sucrose Solubility in Binary Liquid Mixtures Formed by Water Methanol, Water Ethanol, and Methanol Ethanol at 303 and 313 K
• Liquid Liquid Equilibrium for the Ternary System of Methyl Laurate/Methyl Myristate + Ethanol + Glycerol at 318.15 and 333.15 K
• Solubilities of Dihydroxylammonium 5,5'-Bistetrazole-1,1'-diolate in Various Pure Solvents at Temperatures Between 293.15 and 323.15 K
• Determination and Correlation of Solid Liquid Phase Equilibrium and Phase Diagram for a Multicomponent System of Mixed Dibasic Acids. Ternary System of Succinic Acid + Adipic Acid + Ethanol
• Solubility of Ethyl p-Aminobenzoate in Six Alcohols within (283.15 to 327.15) K
• Isobaric Vapor Liquid Equilibrium for Nine Binary Systems of Cracking C5 Fraction at 250 kPa
• Effect of Pressure on the Azeotrope of the Mixture Isoamyl Acetate Isoamyl Alcohol at 50.00, 101.32, 250.00, and 350.00 kPa
• Solubility Measurement and Thermodynamic Modeling of 4-Nitrophthalimide in Twelve Pure Solvents at Elevated Temperatures Ranging from (273.15 to 323.15) K
• Experimental Measurement and Modeling of Vapor Liquid Equilibrium for the Ternary Systems Water + Ethanol + Ethylene Glycol, Water + 2-Propanol + Ethylene Glycol, and Water + 1-Propanol + Ethylene Glycol
• Solubility of Fenofibrate in Different Binary Solvents: Experimental Data and Results of Thermodynamic Modeling
• Solubility Measurement and Modeling of Methane in Methanol and Ethanol Aqueous Solutions
• Solubility of 2-Ethylanthraquinone in Binary Mixtures of Oligooxymethylene Dimethyl Ethers with Different Number of CH2O Groups of n = 2, 3, and 4 from 293.15 to 343.15 K
• Solubility of 3,7,9,11-Tetraoxo-2,4,6,8,10-pentaaza[3.3.3] Propellane (TOPAP) in Different Pure Solvents at Temperatures between 273.15 and 318.15 K
• Measurement and Correlation of the Solubility of p-Coumaric Acid in Nine Pure and Water + Ethanol Mixed Solvents at Temperatures from 293.15 to 333.15 K
• Isobaric Vapor Liquid Equilibria for Binary Mixtures of .gamma.-Valerolactone + Methanol, Ethanol, and 2-Propanol
• Measurement and Correlation of Solubility on Reactive Crystallization of Methyl D-(-)-4-Hydroxy-phenylglycinate
• Solubility Determination and Modeling for 4,4'-Dihydroxydiphenyl Sulfone in Mixed Solvents of (Acetone, Ethyl Acetate, or Acetonitrile) + Methanol and Acetone + Ethanol from (278.15 to 313.15) K
• Liquid Liquid Equilibrium for the Ternary System Isopropyl Acetate + Ethanol + Water at (293.15, 313.15, and 333.15) K
• Measurement and Modeling of Solid Liquid Equilibrium of para-tert-Butylbenzoic Acid in Acetic Acid/Methanol + Water and Acetic Acid + para-tert-Butyltoluene Binary Systems at Various Temperatures
• Liquid Liquid Equilibria of Quaternary Systems Composed of 1,3-Propanediol, Short-Chain Alcohol, Water, and Salt
• Solubilities of Naringin Dihydrochalcone in Pure Solvents and Mixed Solvents at Different Temperatures
• Physical Properties of the Pure Deep Eutectic Solvent, [ChCl]:[Lev] (1:2) DES, and Its Binary Mixtures with Alcohols
• Measurement of Solubility of Thiamine Hydrochloride Hemihydrate in Three Binary Solvents and Mixing Properties of Solutions
• Solubility of 4-Methylsulfonylacetophenone in Nine Pure Solvents and (Ethyl Acetate + n-Hexane) Binary Solvent Mixtures from 278.15 K to 328.15 K
• Solubility and Thermodynamic Behavior of Veramoss in Different Pure Solvents and {Ethanol + Water} Mixtures from T = 283.15 to 333.15 K
• Measurement and Correlation of Solubility of Loratadine in Different Pure Solvents and Binary Mixtures
• Isobaric Vapor Liquid Liquid Phase Equilibria Measurements of Three Ternary Water + 2-Butanone + Aliphatic Alcohol (Ethanol, 1-Propanol, 2-Propanol) Systems at 101.3 kPa
• Measurement and Correlation of Solubility of Amorphous Cefmetazole Sodium in Pure Solvents and Binary Solvent Mixtures
• Measurement and Correlation of the Solubility of e-CL-20 in 12 Organic Solvents at Temperatures Ranging from 278.15 to 318.15 K
• Measurement and Modeling of Liquid Liquid Equilibrium for the Systems Vinyl Acetate + Acetic Acid/Ethanol + Water at 298.15 and 308.15 K
• Solubility Measurement and Correlation of Two Erlotinib Hydrochloride Polymorphs in Alcohols and Ketones from 273.15 to 323.15 K
• Measurement and Correlation of Curcumin Solubility in Supercritical Carbon Dioxide
• Solubility Measurement and the Correlation of 1-Naphthaleneacetic Acid in Pure and Methanol + Water Binary Solvents from T = (278.25 to 323.55) K
• Experimental determination and correlation of liquid-liquid equilibria data for a system of water + ethanol +1-butyl-3- methylimidazolium hexafluorophosphate at different temperatures
• Determination and Correlation of Solubility of Phenylbutazone in Monosolvents and Binary Solvent Mixtures
• Solubilities of 4',5,7-Triacetoxyflavanone in Fourteen Organic Solvents at Different Temperatures
• Measurement and Correlation of Phase Equilibria for Isobutyl Acetate + {Ethanol or Methanol} + Water at 303.15 and 323.15 K
• Measurement and Correlation of the Solubility of 2,6-Dihydroxybenzoic Acid in Alcohols and Binary Solvents
• Measurement and Modeling of Solubility of para-tert-Butylbenzoic Acid in Pure and Mixed Organic Solvents at Different Temperatures
• Determination and Correlation of Ethyl Vanillin Solubility in Different Binary Solvents at Temperatures from 273.15 to 313.15 K
• Vapor Liquid Equilibrium Measurements for Carbon Dioxide + Cyclohexene + Squalane at High Pressures Using a Synthetic Method
• Measurement and Correlation of Liquid Liquid Equilibrium for Quaternary Systems of Water + Methanol or Ethanol + Ethyl Methyl Carbonate + Heptane at 25 deg C
• Determination and Thermodynamic Modeling of Solid Liquid Phase Equilibrium for Esomeprazole Sodium in Monosolvents and in the (Ethanol + Ethyl Acetate) Binary Solvent Mixtures
• Volumetric Properties of Sodium Lauroylsarcosinate in Aqueous Alcohol Solutions of Methanol, Ethanol, and 1-Propanol
• Measurement and Correlation of Solubility of Theobromine, Theophylline, and Caffeine in Water and Organic Solvents at Various Temperatures
• Isobaric Vapor Liquid Equilibrium for the Binary Systems Dimethyl Disulfide + C1 C4 n-Alkanol at 40.000 and 101.325 kPa
• Proposal of Isobutyl Alcohol as Entrainer To Separate Mixtures Formed by Ethanol and Water and 1-Propanol and Water
• Influence of Temperature on the Liquid Liquid Phase Equilibria of Ternary (Water + Alcohol + Entrainer) Systems
• Pressurized-Synthetic Methodology for Solubility Determination at Elevated Temperatures with Application to Paracetamol in Pure Solvents
• Vapor Liquid Equilibrium and Excess Enthalpy Data for Systems Containing N,N-Dimethylacetamide
• Isobaric Vapor Liquid Equilibrium for Three Binary Systems of Acetaldehyde + Ethanol, Ethyl Acetate, 1-Butanol at 101.3 kPa
• Solubility of Benzoin in Six Monosolvents and in Some Binary Solvent Mixtures at Various Temperatures
• Determination of Infinite Dilution Activity Coefficients of Several Organic Solutes in N-Butylpyridinium Nitrate/N-Octylpyridinium Nitrate by Blend Inverse Gas Chromatography
• Solubility Determination and Thermodynamic Modeling of Sodium Thioglycolate in Pure and Binary Solvent Mixtures from T = (293.15 to 333.15) K
• Characteristics of Potassium Prolinate + Water + Ethanol Solution as a Phase Changing Absorbent for CO2 Capture
• Volumetric Properties, Viscosity, and Refractive Indices of Different Naringenin Solutions at Several Temperatures
• Measurement and Correlation of Solubility of Two Isomers of Cyanopyridine in Eight Pure Solvents from 268.15 K to 318.15 K
• Thermodynamic Functions for Solubility of 1-Hydroxybenzotriazole in Sixteen Solvents at Temperatures from (278.15 to 313.15) K and Mixing Property of Mixtures
• Volumetric and Viscometric Properties of Alcohol Amines + Ethanol Binary Mixtures
• Solubility and Thermodynamic Behavior of Syringic Acid in Eight Pure and Water + Methanol Mixed Solvents
• Study on the Solubilities of Mononitro-Substituted Products of Nitration of m-Toluic Acid in Several Solvents at Temperatures between 297.65 and 351.75 K
• Isobaric Vapor-Liquid Equilibrium for the Binary Systems of Sec-butyl Acetate and Ethanol, 1-Propanol, or 2-Propanol at 101.3 kPa
• Solubility of the Proteinogenic a-Amino Acids in Water, Ethanol, and Ethanol-Water Mixtures
• Determination and Correlation of Solubility of Quetiapine Fumarate in Nine Pure Solvents and Two Aqueous Binary Solvents
• Solubility in Different Solvents, Crystal Polymorph and Morphology, and Optimization of Crystallization Process of AIBN
• Density Measurements of CO2-Expanded Liquids
• Solubility Modeling and Mixing Thermodynamics of Thiamphenicol in Water and Twelve Neat Organic Solvents from T = (278.15 to 318.15) K
• Solid-Liquid Equilibria for the Glycine-Alcohol-NaCl-H2O System
• Thermodynamic Functions for the Solubility of 3-Nitrobenzonitrile in 12 Organic Solvents from T/K = (278.15 to 318.15)
• Solubility Measurement and Correlation of Fosfomycin Sodium in Six Organic Solvents and Different Binary Solvents at Temperatures between 283.15 and 323.15 K
• Separation of Azeotropes Hexane + Ethanol/1-Propanol by Ionic Liquid Extraction: Liquid-Liquid Phase Equilibrium Measurements and Thermodynamic Modeling
• Determination and Correlation of Solubility and Thermodynamic Properties of trans-Cinnamyl Alcohol in Pure and Binary Solvents from 253.15 K to 293.15 K
• Measurement and Correlation of the Solubility of Azoxystrobin in Seven Monosolvents and Two Different Binary Mixed Solvents
• Measurement and Correlation of Solubility of Resorcinol Bis(cyclic 2,2-dimethyl-1,3-propanediol phosphate) in Selected Solvents from T = 293.15 to 333.15 K
• Solubility and Mixing Thermodynamics Properties of p-Toluenesulfonamide and o-Toluenesulfonamide in Seven Monosolvents at Different Temperatures
• Three Binary Azeotropic Systems for 1-(Methoxymethoxy)-propane, 1-(Ethoxymethoxy)-propane, and Methoxy(methoxymethoxy)methane with Three Alcohols at 101.33 kPa: Experimental Data, Correlation, and Purification
• Solubility Modeling and Mixing Properties for Benzoin in Different Monosolvents and Solvent Mixtures at the Temperature Range from 273.15 to 313.15 K
• The Solid-Liquid Equilibrium and Crystal Habit of l-Carnitine Fumarate
• Vapor-Liquid Equilibrium of Ethyl Lactate Highly Diluted in Ethanol-Water Mixtures at 101.3 kPa. Experimental Measurements and Thermodynamic Modeling Using Semiempirical Models
• Isobaric Vapor-Liquid Equilibrium for 2-Butanone + Ethanol System Containing Different Ionic Liquids at 101.3 kPa
• Determination and Correlation of Dipyridamole p-Toluene Sulfonate Solubility in Seven Alcohol Solvents and Three Binary Solvents
• Measurement and Correlation of the Dissolution Equilibria of o-Iodoaniline and p-Iodoaniline in Pure Solvents
• Determination, Correlation, and Application of Sodium l-Ascorbate Solubility in Nine Pure Solvents and Two Binary Solvents at Temperatures from 278.15 to 323.15 K
• Determination and Thermodynamic Analysis of the Solubility of Limonin in Eight Organic Solvents and Ethyl Acetate + 2-Propanol Binary Solvents from 283.2 to 323.2 K
• Vapor-Liquid Equilibrium Measurements of Ethanol and n-Nonane or n-Decane Binary Mixtures with Large Relative Volatility
• Experimental Phase Equilibrium for the Binary System of n-Pentane +2-Propanol Using a New Equilibrium Cell and the Static Total Pressure Method
• Deterpenation of Citrus Essential Oils Using Glycerol-Based Deep Eutectic Solvents
• Solubility and Modeling of Hesperidin in Cosolvent Mixtures of Ethanol, Isopropanol, Propylene Glycol, and n-Propanol + Water
• Solubility of p-Aminobenzoic Acid Potassium in Organic Solvents and Binary (Water + Isopropyl Alcohol) Mixture at Temperatures from (283.15 to 318.15) K
• Solubility and Preferential Solvation of Carbazochrome in Solvent Mixtures of N,N-Dimethylformamide Plus Methanol/Ethanol/n-Propanol and Dimethyl Sulfoxide Plus Water
• Density, Speed of Sound, and Other Derived Properties of Ethanol at Pressures up to 65 MPa
• Mutual Influence of Furfural and Furancarboxylic Acids on Their Solubility in Aqueous Solutions: Experiments and Perturbed-Chain Statistical Associating Fluid Theory (PC-SAFT) Predictions
• Synthesis and Characterization of Diethyl Citrate and Phase Equilibria in Mixtures with Ethanol and Water
• Solution Thermodynamics of Benzotriazole in Different Pure Solvents
• Measurement and Correlation for the Solubility of Sodium p-Toluenesulfonate, Sodium Sulfite, and Sodium p-Methylphenoxide in Aqueous Sodium Hydroxide Solutions and Sodium Sulfite in Aqueous Ethanol Solutions
• Solubility of Ionic Liquid [Bmim]Ac in Supercritical CO2 Containing Different Cosolvents
• Solubilities of 2,5-Furandicarboxylic Acid in Binary Acetic Acid + Water, Methanol + Water, and Ethanol + Water Solvent Mixtures
• Solubility of Sulfachloropyridazine in Pure and Binary Solvent Mixtures and Investigation of Intermolecular Interactions
• Investigation on Isobaric Vapor-Liquid Equilibria of the Isopropyl Acetate + Water + Ethanol System
• Aniracetam Solubility in Pure and Binary Solvents: Effect of Molecular Interaction and Analysis of Crystallized Products
• Solubility Measurement and Thermodynamic Modeling of Benzoic Acid in Monosolvents and Binary Mixtures
• Isobaric Vapor-Liquid Phase Equilibrium Measurements, Correlation, and Prediction for Separation of the Mixtures of Cyclohexanone and Alcohols
• Measurement and Correlation of the Solubility of Florfenicol Form A in Several Pure and Binary Solvents
• Determination of Activity Coefficients at Infinite Dilution of Organic Solutes in the Ionic Liquid 1-(2-Hydroxyethyl)-3-methylimidazolium Nonafluoro-1-butanesulfonate Using Gas-Liquid Chromatography
• Solid-Liquid Phase Equilibria of the KH2PO4-KCl-H3PO4-H2O and KH2PO4-KCl-C2H5OH-H2O Systems at T = (298.15 and 313.15) K
• Physical Behavior of the Phases from the Liquid-Liquid Equilibrium of Citrus Essential Oils Systems at 298.2 K
• Measurement and Correlation of the Solubility of Pyrimethanil in Seven Monosolvents and Two Different Binary Mixed Solvents
• Solubility of 2-Chlorophenylacetic Acid in 12 Pure Solvents from T = (273.15/283.15 to 318.15) K: Determination and Modeling
• Experimental Determination and Thermodynamic Models for Solid-Liquid Equilibrium of 4-(4-Aminophenoxy)-N-methylpyridine-2-carboxamide in Pure and Binary Solvent Mixtures for T = (278.15-328.15) K
• Solubility Modeling, Solvent Effect, and Preferential Solvation of Thiamphenicol in Cosolvent Mixtures of Methanol, Ethanol, N,N-Dimethylformamide, and 1,4-Dioxane with Water
• Determination of Physicochemical Parameters of Sodium Dodecyl Sulfate in Aqueous Micellar Solutions Containing Short-Chain Alcohols
• Measurement and Modelization of VLE for Butyl Acetate with Methanol, Ethanol, 1-Propanol, and 1-Butanol. Experimental Data at 0.15 MPa
• Solubility Measurement and Modeling of 1-(3-nitrophenyl)Ethanone and 1-(4-nitrophenyl)Ethenone in Nine Pure Organic Solvents from T = (278.15 to 318.15) K and Mixing Properties of Solutions
• Determination of Solubility and Thermodynamic Properties of Benzophenone in Different Pure Solvents
• Solubility and Molecular Interactions of Trimetazidine Hydrochloride in 12 Monosolvents and Solvent Mixtures of Methanol + (Ethanol, N,N-Dimethylformamide or Ethyl Acetate)
• Cosolvency and Mathematical Modeling Analysis of Chloroxine in Some Binary Solvent System
• Research on Dissolution Capability of Several Antofloxacin Salts
• Solubility Measurement and Modeling of 2-Amino-4,6-dichoropyrimidine in Ten Pure Solvents and (Ethyl Acetate + Ethanol) Solvent Mixtures
• Solubility Determination and Correlation for Pyridoxal 5-Phosphate Monohydrate in Different Binary Solvents from 278.15 K to 318.15 K
• Experiment and Computation of Solubility and Dissolution Properties for Enalapril Maleate and Its Intermediate in Pure Solvents
• Determination and Correlation of the Solubility of l-Fucose in Four Binary Solvent Systems at the Temperature Range from 288.15 to 308.15 K
• Liquid-Liquid Extraction of Alcohols from Their Azeotropic Mixtures with Hexane Using Ionic Liquid
• Influence of Different Solvent Properties and Composition for the Solubility of Iopromide
• Measurement and Correlation of the Solubility of 5-Fluorouracil in Pure and Binary Solvents
• Solubility Modeling and Solvent Effects of Allopurinol in 15 Neat Solvents
• Solubilities of Organic Semiconductors and Nonsteroidal Anti-inflammatory Drugs in Pure and Mixed Organic Solvents: Measurement and Modeling with Hansen Solubility Parameter
• Liquid-Liquid Equilibria for Ternary Systems of (Ethyl Methyl Carbonate + Methanol or Ethanol + Water) at 293.15, 303.15, and 308.15 K
• Thermodynamic Study of Solubility for Imatinib Mesylate in Nine Monosolvents and Two Binary Solvent Mixtures from 278.15 to 318.15 K
• Solubility Determination and Modeling for 4-Nitrobenzonitrile in Binary Solvent Mixtures of Ethyl Acetate Plus (Methanol, Ethanol, n-Propanol, and Isopropanol)
• Solubility Determination of Nicotinamide and Its Application for the Cocrystallization with Benzoic Acid
• Solubility Measurements at 296 and 310 K and Physicochemical Characterization of Abiraterone and Abiraterone Acetate
• Measurement and Correlation of Solubility of 3-Hydroxy-2-naphthoic Acid in Ten Pure and Binary Mixed Organic Solvents from T = (293.15 to 333.15 K)
• Solubility of Toltrazuril and the Effect of a Cosolvent
• Activity Coefficients at Infinite Dilution of Various Solutes in Tetrapropylammonium Bromide + 1,6-Hexanediol Deep Eutectic Solvent
• Thermodynamic Parameters of a New Synthesized Tricationic Ionic Liquid Stationary Phase by Inverse Gas Chromatography
• Solubility of Diflufenican in Pure and Binary Solvent Systems
• Measurement and Correlation of Solubility and Thermodynamic Properties of Vinpocetine in Nine Pure Solvents and (Ethanol + Water) Binary Solvent
• Low-Pressure VLE Measurements and Thermodynamic Modeling, with PSRK and NRTL, of Binary 1-Alcohol + n-Alkane Systems
• Solubility Determination and Correlation of Glibenclamide in 11 Monosolvents and (Acetone + Acetonitrile) Binary Solvents from 283.15 K to 323.15 K
• Solubility Modeling and Solution Thermodynamics of 4-Amino-2,6-Dimethoxypyrimidine in Cosolvent Mixtures of Methanol, Ethanol, Isopropanol, and N,N-Dimethylformamide + Water
• Solubility Measurement and Thermodynamic Properties of Levetiracetam in Pure and Mixed Solvents
• Effects of Aliphatic Alcohols on Solubility, Physicochemical Properties, and Morphology of Calcium Sulfate Dihydrate (Gypsum) in Aqueous Sodium Chloride Solution at 35 deg.C
• The Dependence of Temperature and Composition on the Equilibrium Solubility and Thermodynamic Studies of Bioactive N-(9-Fluorenylmethoxycarbonyloxy)succinimide in Various Water-Cosolvent Mixtures
• Solubility of Vitamin E Acetate in Supercritical Carbon Dioxide with Ethanol as Cosolvent
• Solution Thermodynamic Analysis of p-(Aminomethyl)benzoic Acid in Four Binary Solvents from 288.15 to 328.15 K
• Solid-Liquid Equilibrium of Rebaudioside A in Pure and Binary Mixed Solvents at T = (288.15 to 328.15) K
• Solubility and Data Correlation of Isoniazid in Different Pure and Binary Mixed Solvent Systems from 283.15 K to 323.15 K
• Viscosity and Density of Binary Mixtures of Ethanol + Igepal (CO-520, CO-630, CO-720, and CA-720)
• Solid-Liquid Equilibrium of Isomaltulose in Five Pure Solvents and Four Binary Solvents from (283.15 to 323.15) K
• Solubility Measurement and Correlation of Probenecid in 12 Pure Organic Solvents and Thermodynamic Properties of Mixing of Solutions
• Measurement and Correlation of the Solubility of Tetramethylpyrazine in Nine Monosolvents and Two Binary Solvent Systems
• Measurement and Correlation of Solubility of Gatifloxacin in 12 Pure Solvents from 273.15 K to 318.15 K
• Solubility Measurement and Thermodynamic Model Correlation and Evaluation of 2-Chloro-5-nitroaniline in 12 Pure Solvents
• Physical Properties of Model and Real Systems Composed of Essential Oils and Hydroalcoholic Solvents at 298.2 K and Atmospheric Pressure
• Solubility of N-tert-Butylbenzothiazole-2-sulfenamide in Several Pure and Binary Solvents
• A Volumetric and Viscosity Study for the Binary Mixtures of Ammonium-Based Asymmetrical Gemini Ionic Liquids with Alcohols at T = 293.15-333.15 K
• Density and Derived Properties of Binary Mixtures Containing {2-(Dimethylamino)ethyl Methacrylate + Alcohols} at Temperatures from T = (293.15 to 313.15) K and Pressures of up to 35 MPa
• Solubility Determination and Correlation of Warfarin Sodium 2-Propanol Solvate in Pure, Binary, and Ternary Solvent Mixtures
• Solubility Determination and Modeling for Artesunate in Binary Solvent Mixtures of Methanol, Ethanol, Isopropanol, and Propylene Glycol + Water
• Solubility Behavior of 2-Chloro-3- (trifluoromethyl)pyridine in (Ethyl Acetate + n-Butanol, DMF + n-Butanol, DMF + Ethanol) Solvent Mixtures
• Experimental Determination of Isobaric Vapor-Liquid Equilibrium and Isothermal Interfacial Tensions for the Binary Ethanol + Cyclopentyl Methyl Ether Mixture
• Experimental Solubility and Density Functional Theory Studies of Deferasirox in Binary Solvent Mixtures: Performance of Polarizable Continuum Model and Jouyban-Acree Model
• Density, Speed of Sound, and Viscosity of Diethylene Glycol Monoethyl Ether + N,N-Dimethylformamide (Ethanol, Water) at T = 288.15-318.15 K
• Solubility Modeling and Solvent Effect of 2-Amino-6-chloropurine in Twelve Neat Solvents
• Phase Equilibrium Measurements and Thermodynamic Modeling of the Systems (CO2 + Ethyl Levulinate) and (CO2 + Levulinic Acid)
• Salt Effect on Ethanol-Based Aqueous Biphasic Systems Applied to Alkaloids Partition: An Experimental and Theoretical Approach
• Solubility Measurement of Lauric, Palmitic, and Stearic Acids in Ethanol, n-Propanol, and 2-Propanol Using Differential Scanning Calorimetry
• Equilibrium Solubility of Biapenem in Different Neat and Binary Solvents: Experimental Determination and Model Correlation
• Measurement and Correlation of the Solubility of Palmatine Chloride in Four Different Binary Solvent Systems at (283.15-328.15) K
• Measurement and Correlation of the Solubility of Mifepristone in Eight Pure and Water + Methanol Mixed Solvents at Temperatures from 273.15 to 318.15 K
• Phase Behavior for the System Carbon Dioxide + p-Nitrobenzaldehyde: Experimental and Modeling
• Effect of Solvent Properties and Composition on the Solubility of Ganciclovir Form I
• Solubility Determination and Thermodynamic Modeling of Buprofezin in Different Solvents and Mixing Properties of Solutions
• Solubility in Different Solvents, Correlation, and Solvent Effect in the Solvent Crystallization Process of Iohexol
• Solubility Modeling and Solvent Effect for Flubendazole in 12 Neat Solvents
• Liquid Viscosity and Interfacial Tension of Binary and Ternary Mixtures Containing n-Octacosane by Surface Light Scattering
• Determination and Modeling of Solubility of 4-Aminobenzamide in Different Pure Solvents
• Measurement of the Thermal Conductivity of 1-Butyl-3-methylimidazolium l-Tryptophan + Water + Ethanol Mixtures at T = (283.15 to 333.15) K
• Binary Solid-Liquid Solubility Determination and Model Correlation of Quizalofop-p-ethyl in Different Pure Solvents
• Measurement and Correlation of the Solubility of Baicalin in Several Mixed Solvents
• Solid-Liquid Equilibrium of Azacyclotridecan-2-one in 15 Pure Solvents from T = 273.15 to 323.15 K: Experimental Determination and Thermodynamic Modeling
• Measurement and Correlation of the Solubility of 2-Cyanoacetamide in 14 Pure Solvents and the Mixing Properties of Solutions
• Solubility, Model Correlation, and Solvent Effect of 2-Amino-3-methylbenzoic Acid in 12 Pure Solvents
• Solubility and Solution Thermodynamics of 3-Nitrophthalonitrile in 12 Neat Solvents at Temperatures from 278.15 to 323.15 K
• Solubility Determination, Modeling, and Preferential Solvation of Terephthalaldehydic Acid Dissolvend in Aqueous Solvent Mixtures of Methanol, Ethanol, Isopropanol, and N-Methyl-2-pyrrolidone
• Equilibrium Solubility, Model Correlation, and Solvent Effect of Indole-3-acetic Acid in Twelve Pure Solvents
• Solubility of l-Phosphinothricin and Its Hydrochloride in Water + (Methanol and Ethanol) Binary Solvent Mixtures from 278.15 to 318.15 K
• 4-Nitrophenzylcyanide Solubility in Several Nonaqueous Solvent Mixtures: Determination and Modeling
• Measurement and Correlation of Solubility of Calcium Formate (Form alpha) in Different Binary Solvent Mixtures at Temperatures from 283.15 to 323.15 K
• Solubility of 4-Chloro-2,5-dimethoxynitrobenzene, 4-Chloro-2,5-dimethoxyaniline, and 2,5-Dimethoxyaniline in Binary and Pure Solvents: Determination and Modeling
• Surface Tension of Aqueous Solutions of Small-Chain Amino and Organic Acids
• Determination and Correlation of Solubility of Borneol, Camphor, and Isoborneol in Different Solvents
• Solubility Determination and Modeling of p-Nitrobenzamide Dissolved in Twelve Neat Solvents from 283.15 to 328.15 K
• Thermodynamic Models for Determination of Solid-Liquid Equilibrium of the Buprofezin in Pure and Binary Organic Solvents
• Solid-Liquid Equilibrium Measurements for Posaconazole and Voriconazole in Several Solvents between T = 278.2 and 323.2 K Using Differential Thermal Analysis/Thermal Gravimetric Analysis
• Solubility Determination and Thermodynamic Modeling of 2-Mercaptobenzimidazole in 12 Solvents from T = 278.15 K to T = 318.15 K
• Domperidone Solubility in Aqueous Cosolvent Mixtures of N,N-Dimethylformamide, Isopropanol, Dimethyl Sulfoxide, and Ethanol: Thermodynamic Modeling and Preferential Solvation Analysis
• Measurement and Correlation of Solubility of Hydrochlorothiazide in Monosolvents and Binary Solvent Mixtures from 283.15 to 323.15 K
• Solubility Measurement and Thermodynamic Model Correlation of 5-Nitrosalicylaldehyde in Different Solvents
• o-Nitrophenylacetonitrile Solubility in Several Pure Solvents: Measurement, Correlation, and Solvent Effect Analysis
• Isobaric Vapor-Liquid Equilibria for the Quaternary System Water + Ethanol + Ethylene Glycol + Choline Chloride and the Ternary System Water + Ethanol + Choline Chloride at 101.3 kPa
• Measurement and Correlation of Solubilities of 5,5'-Dinitramino-3,3'-bi[1,2,4-triazolate] Carbohydrazide Salt (CBNT) in Various Pure Solvents and a Binary Mixture (Dimethyl Sulfoxide + Water) from 298.15 to 343.15 K
• Solubility of Gastrodin in Pure and Mixed Solvents at 273.15-313.15 K and Its Correlation with Different Thermodynamic Models
• Solubility and Solvent Effect of Acetamiprid in Thirteen Pure Solvents and Aqueous Solutions of Ethanol
• Solubility Measurement and Correlation of 2-Oxindole in 12 Pure Organic Solvents
• Determination and Correlation of the Solubility of Musk Ketone in Pure and Binary Solvents at 273.15-313.15 K
• Solubility of d-Aspartic Acid in Several Neat Solvents: Determination, Modeling, and Solvent Effect Analysis
• Assessment of Pyrrolidinium-Based Ionic Liquid for the Separation of Binary Mixtures Based on Activity Coefficients at Infinite Dilution
• Solubility Measurement and Phase Equilibrium Modeling of 2-Aminobenzamide in 15 Pure Solvents
• Measurement of the Solubility of Diclazuril and Discussion of the Effect of the Cosolvent
• Solubility Determination, Modeling, and Thermodynamic Dissolution Properties of Benzenesulfonamide in 16 Neat Solvents from 273.15 to 324.45 K
• Solid-Liquid Equilibrium Solubility, Thermodynamic Properties, and Molecular Simulation of Phenylphosphonic Acid in 15 Pure Solvents at Different Temperatures
• Liquid-Liquid Equilibrium Data for Ternary Systems Containing Alkanes (n-Pentane, n-Hexane, n-Heptane, and n-Octane) + Alcohol (Methanol and Ethanol) + Protic Ionic Liquid (2-HEAF)
• Determination and Correlation of Solubilities of 1,3,5-Trifluoro-2,4,6-triiodobenzene in Different Solvents from 289.25 to 332.15 K
• Solubility Determination, Correlation, and Solute-Solvent Molecular Interactions of 5-Aminotetrazole in Various Pure Solvents
• Solubility Determination and Thermodynamic Mixing Properties of 5-Methyl-2-pyrazinecarboxylic Acid in Different Solvents
• Solubility and Thermodynamic Modeling of Sulfanilamide in 12 Mono Solvents and 4 Binary Solvent Mixtures from 278.15 to 318.15 K
• Measurement and Correlation of Vapor-Liquid Equilibrium for Binary Systems of Dimethyl Carbonate with Butyl Butyrate, o-Xylene, and Cyclohexanone at 101.3 kPa
• Solubility Determination and Modeling of EGCG Peracetate in 12 Pure Solvents at Temperatures from 278.15 to 318.15 K
• Solubility, Solubility Modeling, and Antisolvent Precipitation of 1,3-Bis(9-carbazolyl)benzene in Organic Solvents
• Solubility Measurement and Thermodynamic Modeling for o-Toluenesulfonamide in 16 Solvents from T = 273.15 to 323.85 K
• Binary Equilibrium Solubility of Amidinothiourea in Monosolvents: Experimental Determination, Model Correlation, and Solvent Effect Analysis
• The Research and Measurement about the Solubility of l-Serine in Eight Common Pure Solvents and Four Binary Mixed Solvents for T = (278.15-333.15) K
• Equilibrium Solubility Determination and Modeling of Fenbendazole in Cosolvent Mixtures at (283.15-328.15) K
• Measurement and Correlation of Solubility of Marbofloxacin in 12 Pure Solvents from 283.15 to 328.15 K
• Solubility Study and Mixing Property of 3,5-Dinitro-2-methylbenzoic Acid in 13 Pure Solvents from 288.15 to 333.15 K
• Measurement and Correlation of the Solubility of Aminocaproic Acid in Some Pure and Binary Solvents
• Solubility and Solvent Effect of 1-(2-Bromo-phenyl)-pyrrole-2,5-dione in 14 Pure Solvents from 278.15 to 323.15 K
• Saturated Solubility and Thermodynamic Evaluation of l-Tryptophan in Eight Pure Solvents and Three Groups of Binary Mixed Solvents by the Gravimetric Method at T = 278.15-333.15 K
• Solubility Measurement and Modeling of 3-Hydroxy-2-nitropyridine in Ten Pure Solvents and Two Binary Mixed Solvents for T = (278.15-318.15) K
• Solubility of Acetoguanamine in Twelve Neat Solvents from 283.15 to 323.15 K
• Thermodynamic Modeling and Solubility Measurement of Cetirizine Hydrochloride and Deferiprone in Pure Solvents of Acetonitrile, Ethanol, Acetic Acid, Sulfolane, and Ethyl Acetate and Their Mixtures
• Solubility and Thermodynamic Modeling of Dimethyl Terephthalate in Pure Solvents and the Evaluation of the Mixing Properties of the Solutions
• Determination and Modeling of d-Histidine Solubility in Several Pure Solvents from 293.15 to 333.15 K
• Solubility Determination of 2-Chloronicotinic Acid and Analysis of Solvent Effect
• Solubility measurement and thermodynamic model correlation of sancycline in twelve pure solvents
• Measurement and Correlation of the Solubility of Dienogest in Twelve Pure and Water + Methanol Binary Solvents at Temperatures from 273.15 to 318.15 K
• Solubility and Data Correlation of b-Arbutin in Different Monosolvents from 283.15 to 323.15 K
• Solubility Data for Roflumilast and Maraviroc in Various Solvents between T = (278.2-323.2) K
• Solubility Increment and Thermodynamic Analysis of Bioactive Antofloxacin Hydrochloride in Aqueous ChCl/PTS Deep Eutectic Solvent and Cosolvent Mixtures
• Solubility and Solution Thermodynamics of 2,6-Dichloro-4-nitroaniline in 12 Pure Solvents at Temperatures from 278.15 to 323.15 K
• Solubility Behavior and Data Modeling of l-Proline in Different Neat and Binary Solvent Systems
• Thermodynamic Solubility and Mixing Properties of Phenformin in 14 Pure Solvents at Temperatures Ranging from 278.15 to 323.15 K
• Solid-Liquid Phase Equilibrium and Thermodynamic Analysis of N,N'-Diethylthiourea in Different Solvent Systems
• Thermodynamic Solubility of Gatifloxacin in Nonaqueous Solvent Mixtures of N,N-Dimethylformamide Plus Isopropanol/Methanol/n-Propanol/Ethanol
• Infinite Dilution Activity Coefficients in Ethylene Glycol and Ethylene Carbonate
• Vapor-Liquid Equilibrium of the Ethanol + 2-Methyl-1-butanol System
• Thermodynamic Properties of Mixtures Containing Precursors of Vitamin B5
• Isobaric Phase Equilibria of Diethyl Carbonate with Five Alcohols at 101.3 kPa
• Vapor Liquid Equilibria for Ethanol + 2,4,4-Trimethyl-1-pentene and 2-Propanol + 2,4,4-Trimethyl-1-pentene at 101 kPa
• Liquid-Liquid Equilibria for Ternary Mixtures of Water + Ethanol with 1-Hexanol, Butyl Propionate, or Ethyl Caproate
• Excess Molar Enthalpies for Binary Mixtures of Ethanol + Acetone, + Octane, + Cyclohexane and 1-Propanol + Acetone, + Octane, + Heptane at 323.15
• Compositions, Densities, and Refractive Indices of Potassium Chloride + Ethanol + Water and Sodium Chloride + Ethanol + Water Solutions at (298.15 and 313.15) K
• Solubility of Rofecoxib in the Presence of Methanol, Ethanol, and Sodium Lauryl Sulfate at (298.15, 303.15, and 308.15) K
• Solubility in Binary Solvent Mixtures: Anthracene Dissolved in Alcohol + Acetonitrile Mixtures at 298.2 K
• Vapor-Liquid Equilibrium Data at 343 K and Excess Molar Enthalpy Data at 298 K for the Binary Systems of Ethanol + 2,4,4-Trimethyl-1-pentene and 2-Propanol + 2,4,4-Trimethyl-1-pentene
• Measurement of the Effect of Salt on Vapor-Liquid Equilibria by Using Headspace Gas Chromatography
• VLE and VLLE Measurements of Dimethyl Ether Containing Systems. 2
• Vapor-Liquid Equilibrium in a Ternary System Cyclohexane + Ethanol + Water
• Ternary Liquid-Liquid Equilibria for Mixtures of 1-Methyl-3-octylimidazolium Chloride + an Alkanol + an Alkane at 298.2 K and 1 bar
• Surface Tension of Binary Mixtures of Ethanol + Ethylene glycol from 20 to 50 oC
• Bubble Temperatures of the Binary Mixtures of Dimethylcarbonate with Some Alcohols at 95.8 kPa
• Vapor-Liquid Equilibria in Alcohol + Cyclohexane + Water Systems
• Measurement and Correlation of Excess Molar Enthalpies for Ethylene Glycol + Alkanol Systems at the Temperatures (298.15, 308.15, and 323.15) K
• Experimental Determination of Liquid-Liquid Equilibrium Using Ionic Liquids: tert-Amyl Ethyl Ether + Ethanol + 1-Octyl-3-Methylimidazolium Chloride System at 298.15 K
• Density, Refractive Index, and Speed of Sound at 298.15 K and Vapor-Liquid Equilibria at 101.3 kPa for Binary Mixtures of Ethyl Acetate + 1-Pentanol and Ethanol + 2-Methyl-1-propanol
• Vapor-Liquid Equilibrium Measurements for Tetraethyl Orthosilicate + Ethanol at 24.00 kPa and 53.32 kPa
• Excess Molar Volumes, Viscosities, and Refractive Indexes for Binary Mixtures of 1-Chlorobutane with Four Alcohols at T = (288.15, 298.15 and 308.15) K
• Liquid Densities and Refractive Indices of Binary Mixtures for the Dimethyl Ether of a Glycol + Ethanol from T=288.15 K to 318.15 K
• Thermodynamic Functions for Transfer of Anthracene from Water to (Water + Alcohol) Mixtures at 298.15K
• High-Pressure Vapor-Liquid Equilibrium Data and Modeling of Propane + Methanol and Propane + Ethanol Systems
• Density, Surface Tension, and Refractive Index of Octane + 1-Alkanol Mixtures at T ) 298.15 K.
• Conductivities and Viscosities of the Ionic Liquid [bmim][PF6] + Water + Ethanol and [bmim][PF6] + Water + Acetone Ternary Mixtures
• Solubility of Flurbiprofen in Supercritical Carbon Dioxide
• Isobaric Vapor Liquid Equilibrium for 2,3-Dimethyl-2-butene + Methanol, + Ethanol, + 2-Propanol, or + 2-Butanol at Atmospheric Pressure
• Vapor Liquid Equilibrium for the Trans-2-Butene + Methanol, + Ethanol, + 2-Propanol, + 2-Butanol and + 2-Methyl-2-Propanol Systems at 332 K
• Isothermal Vapor Liquid Equilibrium for Binary 2-Methylpropene - C1-C4 Alcohol-Systems
• Determination and Study on the Solubility of Methane in Heptane + Cyclohexane and Heptane + Ethanol at High Pressures
• Dynamic Viscosities of Diethyl Carbonate with Linear and Secondary Alcohols at Several Temperatures
• Thermochemistry of Branched Ethers: Experimental Study of Chemical Equilibrium in the Reacting System of tert-Amyl Alkyl Ether Synthesis
• Influence of Ionic Liquids on the Phase Behavior of Aqueous Azeotropic Systems
• Vapor-Pressure Measurements of Liquid Solutions at Different Temperatures: Apparatus for Use over an Extended Temperature Range and Some New Data
• Densities and Viscosities of Binary Liquid Mixtures of Trichloroethylene and Tetrachloroethylene with Some Polar and Nonpolar Solvents
• Vapor-Liquid Equilibrium of Durene in Methanol or Ethanol
• Isobaric Vapor-Liquid Equilibria for Binary and Ternary Mixtures of Ethanol, Methylcyclohexane and p-Xylene
• High-Pressure Phase Equilibrium for Carbon Dioxide + Ethanol at 291.15 K
• Dynamic Viscosities, Densities, and Speed of Sound and Derived Properties of the Binary Systems Acetic Acid with Water, Methanol, Ethanol, Ethyl Acetate and Methyl Acetate at T = (293.15, 298.15, and 303.15) K at Atmospheric Pressure
• Effect of Organic Cosolvents on the Solubility of Ionic Liquids in Supercritical CO2
• Solubility of 11r-Hydroxy-16r,17r-Epoxyprogesterone in Different Solvents between 283 K and 323 K
• Excess Molar Volumes and Viscosity Deviations of Binary Mixtures of 2,4,6-Trimethyl-1,3,5-trioxane + Ethanol, 1-Propanol, and 1-Butanol at (298.15, 303.15, and 308.15) K
• Determination of Henry s Law Constants and Activity Coefficients at Infinite Dilution of Flavor Compounds in Water at 298 K with a Gas-Chromatographic Method
• Solid-Liquid Phase Equilibria of Binary and Ternary Mixtures for 2,6-Dimethylnaphthalene and 2,7-Dimethylnaphthalene with Ethanol or Methanol
• Phase Behavior, Densities, and Isothermal Compressibility of the CO2 + Ethanol + Dichloromethane Ternary System in Different Phase Regions
• Densities and Viscosities for Binary and Ternary Mixtures of Ethanol, 2-Butanone, and 2,2,4-Trimethylpentane at T = (298.15, 308.15, and 318.15) K
• Solubility of Valdecoxib in the Presence of Ethanol and Sodium Lauryl Sulfate at (298.15, 303.15, and 308.15) K
• Solubility of Acetazolamide in Supercritical Carbon Dioxide in the Presence of Ethanol as a Cosolvent
• Measurement of Diffusion Coefficients in Thermodynamically Nonideal Systems
• Solubility, Density, Viscosity, Electrical Conductivity, and Refractive Index of Saturated Solutions of Lithium Hydroxide in Water + Ethanol
• Critical Properties of the Reacting Mixture in the Esterification of Acetic Acid with Ethanol
• Vapor-Liquid Equilibrium Behavior of Tolan in Alcohol
• Solubilities of Sodium Chloride and Potassium Chloride in Water + Ethanol Mixtures from (298 to 323) K
• Conductivity and Viscosity of 1-Allyl-3-methyl-imidazolium Chloride + Water and + Ethanol from 293.15 K to 333.15 K
• High-Pressure Phase Equilibrium for Ethylene + Ethanol at 283.65 K
• Liquid-Liquid Equilibrium of MTBE + Ethanol + Water and MTBE + 1-Hexanol + Water over the Temperature Range of 288.15 to 308.15 K
• Dynamic Viscosities of KI or NH4I in Methanol and NH4I in Ethanol at Several Temperatures and 0.1 MPa
• Solubility of Dexamethasone Sodium Phosphate in Different Solvents
• Excess Molar Enthalpies of Ternary Mixtures of Ethanol + 1-Propanol + Tetrahydropyran or 1,4-Dioxane at 298.15 K
• Measurement of Activity Coefficients at Infinite Dilution of Benzene, Toluene, Ethanol, Esters, Ketones, and Ethers at Various Temperatures in Water Using the Dilutor Technique
• Solubilities of Proxetine Hydrochloride Hemihydrate between 286 K and 363 K
• Viscosities, Densities, and Ultrasonic Velocities of Binary Mixtures of Ethylbenzene with Ethanol, 1-Propanol, and 1-Butanol at (298.15 and 308.15)K
• Solid - Liquid Phase Equilibrium of Some Aliphatic Alcohols + Cesium Sulfate + Water
• Solubility of NaCl, NaBr, and KCl in Water, Methanol, Ethanol, and Their Mixed Solvents
• Solubility and Density of 2,6-Dimethylnaphthalene in C1-C7 1-Alkanols
• Solubility of 1,3,5-Trioxane in Methanol, Ethanol, and 2-Propanol
• Density and Viscosity for a Binary Mixture of cis-3-Hexenyl Formate, Butyl Acetate, trans-2-Hexenyl Acetate, and cis-3-Hexenyl Acetate with Ethanol at Several Temperatures
• Excess Enthalpy, Excess Volume, and Speed of Sound Deviation for the Mixtures ss-Pinene + Ethanol and ss-Pinene + 1-propanol at (283.15, 298.15 and, 313.15) K
• Densities, Refractive indices and Viscosities for Binary and Ternary Mixtures of Acetone, Ethanol and 2,2,4-Trimethylpentane at T = (288.15, 298.15, and 308.15) K
• Densities and Viscosities for Binary and Ternary Mixtures of Diisopropyl Ether, Ethanol, and Methylcyclohexane
• Density, Refractive Index, Speed of Sound at 298.15 K, and Vapor-Liquid Equilibria at 101.3 kPa for Binary Mixtures of Methanol + 2-Methyl-1-butanol and Ethanol + 2-Methyl-1-butanol
• Excess Molar Enthalpies of Dimethyl Carbonate and (Methanol, Ethanol, 1-Propanol, and 2-Propanol) at T = (298.15, 313.15, and 328.15) K and p = (0.1, 1.0, and 10.0) MPa
• Density and Viscosity of Binary Mixtures of Ethyl-2-methylbutyrate and Ethyl Hexanoate with Methanol, Ethanol, and 1-Propanol at (293.15, 303.15, and 313.15) K
• Solubility of Cesium Nitrate in Alcohol Aqueous Solutions at (25, 35 and 45 ) C
• Solubility of Puerarin in Water, Ethanol, and Acetone from (288.2 to 328.2) K
• Solubility of Lovastatin in Acetone, Methanol, Ethanol, Ethyl Acetate, and Butyl Acetate between 283 K and 323 K
• Entrainer Effect of Ethanol on High-Pressure Vapor-Liquid Equilibria for Supercritical Carbon Dioxide + Limonene + Linalool System
• Phase Diagrams of Some Aliphatic Alcohols + Potassium or Sodium Citrate + Water at 25 deg C
• Experimental Determination of the Solubility of Thiophene in Carbon Dioxide and in Carbon Dioxide + Ethanol
• Solubility of Erythritol in Different Solvents
• Thermodynamic Properties of Mixtures Containing Ionic Liquids. 5. Activity Coefficients at Infinite Dilution of Hydrocarbons, Alcohols, Esters, and Aldehydes in 1-Methyl-3-butyl-imidazolium Bis(trifluoromethyl-sulfonyl) Imide Using Gas-Liquid Chromatography
• Thermodynamic Properties of Mixtures Containing Ionic Liquids. 6. Activity Coefficients at Infinite Dilution of Hydrocarbons, Alcohols, Esters, and Aldehydes in 1-Methyl-3-octyl-imidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
• Solubility of Potassium Clavulanate in Ethanol, 1-Propanol, 1-Butanol, 2-Propanol, and 2-Methyl-1-propanol between 273 K and 305 K
• Densities, Viscosities, and Refractive Indices for Binary and Ternary Mixtures of Ethanol, 2-Methylpropan-2-ol, and 2,2,4-Trimethylpentane
• Solubility of Puerarin in Ethanol + Supercritical Carbon Dioxide
• Experimental and Predicted Results of Anomeric Equilibrium of Glucose in Alcohols
• Solubility of 16.alpha.,17.alpha.-Epoxyprogesterone in Six Different Solvents
• Solubility of Ceftriaxone Disodium in Acetone, Methanol, Ethanol, N,N-Dimethylformamide, and Formamide between 278 and 318 K
• Vapor Pressure Measurements of Binary Solutions of CaCl2 with Methanol and Ethanol at T = (298.15 to 323.15) K Using a Static Method
• Density and Viscosity of Several Aldehydes Fragrance Compounds in Their Binary Mixtures with Ethanol at (298.15 K, 308.15 K, and 318.15 K)
• Solubility of Cefazolin Sodium Pentahydrate in Different Solvents between 275 K and 310 K
• High-Pressure Density Measurements for the Binary System Ethanol + Heptane
• Solubility of Hydroquinone in Different Solvents from 276.65 K to 345.10 K
• Solubility of Rofecoxib in the Presence of Aqueous Solutions of Glycerol, Propylene Glycol, Ethanol, Span 20, Tween 80, and Sodium Lauryl Sulfate at (298.15, 303.15, and 308.15) K
• Experimental Measurement and Correlation of Solubility of Pentachloropyridine and Tetrachloropyridine in Methanol, Ethanol, and 2-Propanol
• Solubility of p-Nitrobenzoic Acid in Supercritical Carbon Dioxide with and without Cosolvents
• Thermodynamic Properties of Mixtures Containing Ionic Liquids. 8. Activity Coefficients at Infinite Dilution of Hydrocarbons, Alcohols, Esters, and Aldehydes in 1-Hexyl-3-methylimidazolium Bis(trifluoromethylsulfonyl) Imide Using Gas-Liquid Chromatography
• Densities, Viscosities, and Refractive Indices for Binary and Ternary Mixtures of Diisopropyl Ether, Ethanol, and 2,2,4-Trimethylpentane
• Solubilities of Phenylphosphinic Acid, Hydroxymethylphenylphosphinic Acid, p-Methoxyphenylphosphinic Acid, p-Methoxyphenylhydroxymethylphosphinic Acid, Triphenylphosphine, Tri(p-methoxyphenyl)phosphine, and Tri(p-methoxyphenyl)phosphine Oxide in Selected Solvents
• Densities and Viscosities of Binary Mixtures of Isoamyl Acetate, Ethyl Caproate, Ethyl Benzoate, Isoamyl Butyrate, Ethyl Phenylacetate, and Ethyl Caprylate with Ethanol at T = (288.15, 298.15, 308.15, and 318.15) K
• Vapor Pressures and Activity Coefficients of n-Alcohols and Benzene in Binary Mixtures with 1-Methyl-3-Butyl-Imidazolium Octylsulfate and 1-Methyl-3-Octyl-Imidazolium Tetrafluoroborate
• Densities and Viscosities of Binary Mixtures of Ethyl Acetoacetate, Ethyl Isovalerate, Methyl Benzoate, Benzyl Acetate, Ethyl Salicylate, and Benzyl Propionate with Ethanol at T ) (288.15, 298.15, 308.15, and 318.15) K
• Solubility of Organic Systems Containing 1,4-Dioxan-2-one
• Liquid-Liquid Phase Equilibria of (Ethanol or Methanol + Water) Containing either Dipotassium Hydrogen Phosphate or Sodium Dihydrogen Phosphate
• Density, Viscosity, Excess Molar Volume, and Viscosity Deviation of Three Amyl Alcohols + Ethanol Binary Mixtures from 293.15 to 323.15 K
• Solubility of Berberine Chloride in Various Solvents
• Thermodynamic Properties of Mixtures Containing Ionic Liquids. 9. Activity Coefficients at Infinite Dilution of Hydrocarbons, Alcohols, Esters, and Aldehydes in Trimethyl-butylammonium Bis(trifluoromethylsulfonyl) Imide Using Gas-Liquid Chromatography and Static Method
• Densities and Viscosities of Aqueous Ternary Mixtures of 2-(Methylamino)ethanol and 2-(Ethylamino)ethanol with Diethanolamine, Triethanolamine, N-Methyldiethanolamine, or 2-Amino-1-methyl-1-propanol from 298.15 to 323.15 K
• Liquid-Liquid Equilibrium in Mixtures of the Ionic Liquid 1-n-Butyl-3-methylimidazolium Hexafluorophosphate and an Alkanol
• Temperature Effect on the Liquid-Liquid Equilibria for Some Aliphatic Alcohols + Water + K2CO3 Systems
• Vapor-Liquid Equilibrium Behaviors of Coumarin and Vanillin in Ethanol, 1-Propanol, and 2-Propanol
• Density and Surface Tension of Binary Mixtures of Acetonitrile + 1-Alkanol at 293.15 K
• Solubility of Erythromycin A Dihydrate in Different Pure Solvents and Acetone + Water Binary Mixtures between 293 K and 323 K
• Vapor-Liquid Equilibria in the Systems Ethyl Lactate + Ethanol and Ethyl Lactate + Water
• Activity Coefficients at Infinite Dilution in 1-Alkyl-3-methylimidazolium Tetrafluoroborate Ionic Liquids
• Vapor-Liquid Equilibrium of Ferrocene in Some Organic Solvents Using Spectroscopic Methods
• Vapor-Liquid Equilibrium of Binary Mixtures. 1. Ethanol + 1-Butanol, Ethanol + Octane, 1-Butanol + Octane
• Vapor-Liquid Equilibrium of Binary Mixtures. 2. Ethanol + 2,2,4-Trimethylpentane, 1-Butanol + 2,2,4-Trimethylpentane, and Ethanol + o-Xylene
• Thermodynamic Properties of Mixtures Containing Ionic Liquids: Activity Coefficients at Infinite Dilution of Organic Compounds in 1-Propyl Boronic Acid-3-Alkylimidazolium Bromide and 1-Propenyl-3-alkylimidazolium Bromide Using Inverse Gas Chromatography
• Solubility of Chiral Threonine Species in Water/Ethanol Mixtures
• Liquid-Liquid Equilibrium Diagrams of Ethanol + Water + (Ethyl Acetate or 1-Pentanol) at Several Temperatures
• Solubilities of Glycine and Its Oligopeptides in Aqueous Solutions
• Excess Molar Enthalpies of 1,2-Propanediol + Alkan-1-ols (C1-C6) and Their Correlations at 298.15 K and Ambient Pressure (81.5 kPa)
• Henry s Constants of 1-Alkanols and 2-Ketones in Salt Solutions
• Phase Boundaries of CO2 + Toluene, CO2 + Acetone, and CO2 + Ethanol at High Temperatures and High Pressures
• Solubility of Cefazolin Sodium Pentahydrate in Binary System of Ethanol + Water Mixtures
• Compressibility Studies of Binary Solutions Involving Water as a Solute in Nonaqueous Solvents at T ) 298.15 K
• Refractive Indices and Surface Tensions of Binary Mixtures of Isoamyl Acetate, Ethyl Caproate, Ethyl Benzoate, Isoamyl Butyrate, Ethyl Phenylacetate, and Ethyl Caprylate with Ethanol at (288.15, 298.15, 308.15, and 318.15) K
• Physical Properties of Binary Mixtures of the Ionic Liquid 1-Methyl-3-octylimidazolium Chloride with Methanol, Ethanol, and 1-Propanol at T = (298.15, 313.15, and 328.15) K and at P ) 0.1 MPa
• Volumetric and Viscosity Study for the Mixtures of 2-Ethoxy-2-methylpropane, Ethanol, and 1-Ethyl-3-methylimidazolium Ethyl Sulfate Ionic Liquid
• Ebulliometric Determination of Vapor-Liquid Equilibria for Methanol + Ethanol + Dimethyl Carbonate
• Measurement and Correlation of Solubilities of Luteolin in Organic Solvents at Different Temperatures
• Refractive Indices and Surface Tensions of Binary Mixtures of Ethyl Acetoacetate, Ethyl Isovalerate, Methyl Benzoate, Benzyl Acetate, Ethyl Salicylate, and Benzyl Propionate with Ethanol at (288.15, 298.15, 308.15, and 318.15) K
• Vapor Pressure Measurement and Prediction for Ethanol + Methanol and Ethanol + Water Systems Containing Ionic Liquids
• Measurement and Correlation of Vapor-Liquid Equilibria at T ) 333.15 K and Excess Molar Volumes at T ) 298.15 K for Ethanol + Dimethyl Carbonate (DMC), DMC + 1-Propanol, and DMC + 1-Butanol
• Effect of NiCl2a6H2O and CoCl2a6H2O on the Viscosity of Aqueous Ethanol Mixtures
• Physical Properties of Pure 1-Ethyl-3-methylimidazolium Ethylsulfate and Its Binary Mixtures with Ethanol and Water at Several Temperatures
• Effect of Pressure on the Static Relative Permittivities of Alkan-1-ols at 298.15 K
• Measurement and Modeling of Phase Equilibria for Ethanol + Water + Methanol at Isobaric Condition
• Experimental Study of Thermodynamic Properties of Mixtures Containing Ionic Liquid 1-Ethyl-3-methylimidazolium Ethyl Sulfate Using Gas-Liquid Chromatography and Transpiration Method
• Solubility of the Natural Antioxidant Gallic Acid in Supercritical CO2 + Ethanol as a Cosolvent
• Diffusion Coefficients of Aromatic Compounds at Infinite Dilution in Binary Mixtures at 298.15 K
• Infinite Dilution Activity Coefficients for Trihexyltetradecyl Phosphonium Ionic Liquids: Measurements and COSMO-RS Prediction
• Vapor-Liquid Equilibria for the Ternary System Ethanol + Water + 1-Butyl-3-methylimidazolium Chloride and the Corresponding Binary Systems at 101.3 kPa
• Solubility of D-(-)-p-Hydroxyphenylglycine Dane Salt in Mixtures of Methanol and Ethanol
• Solubility of D-p-Hydroxyphenylglycine in Water, Methanol, Ethanol, Carbon Tetrachloride, Toluene, and N,N-Dimethylformamide between 278 K and 323 K
• Activity Coefficients at Infinite Dilution of Polar Solutes in 1-Butyl-3-methylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
• Fluid-Phase Behavior of {1-Hexyl-3-methylimidazolium Bis(trifluoromethylsulfonyl) Imide, [C6mim][NTf2], + C2-C8 n-Alcohol} Mixtures: Liquid-Liquid Equilibrium and Excess Volumes
• Solubility of 4-(3,4-Dichlorophenyl)-1-tetralone in Some Organic Solvents
• Densities of Univalent Cation Sulfates in Ethanol + Water Solutions
• Solubility of Artemisinin in Ethanol + Water from (278.2 to 343.2) K
• Solubility of Phenazine-1-carboxylic Acid in Water, Methanol, and Ethanol from (278.2 to 328.2) K
• Solubility of Xylitol in Ethanol, Acetone, N,N-Dimethylformamide, 1-Butanol, 1-Pentanol, Toluene, 2-Propanol, and Water
• Solubilities of Triphenylphosphine in Ethanol, 2-Propanol, Acetone, Benzene, and Toluene
• Vapor-Liquid Equilibria and HE for Binary Systems of Dimethyl Ether (DME) with C1-C4 Alkan-1-ols at 323.15 K and Liquid-Liquid Equilibria for Ternary System of DME + Methanol + Water at 313.15 K
• Ethanol + 2-Methyl-1-butanol + Calcium Chloride System: Vapor-Liquid Equilibrium Data and Correlation Using the NRTL Electrolyte Model
• Solubility of Benzoic Acid in Mixed Solvents
• Viscosities and Interfacial Properties of I-Methyl-3-butylimidazolium Hexafluorophosphate and 1-Isobutenyl-3-methylimidazolium Tetrafluoroborate Ionic Liquids
• Solubility of 1H-1,2,4-Triazole in Ethanol, 1-Propanol, 2-Propanol, 1,2-Propanediol, Ethyl Formate, Methyl Acetate, Ethyl Acetate, and Butyl Acetate at (283 to 363) K
• Densities of (Lithium, Magnesium, or Copper(II)) Sulfates in Ethanol-Water Solutions
• Solubility of Clopidogrel Hydrogen Sulfate (Form II) in Different Solvents
• Activity Coefficients at Infinite Dilution Measurements for Organic Solutes and Water in the Ionic Liquid 1-Butyl-3-methyl-pyridinium Trifluoromethanesulfonate
• Density and Viscosity of Clopidogrel Hydrogen Sulfate + Methanol and Clopidogrel Hydrogen Sulfate + Ethanol from (278.15 to 313.15) K
• Solubilities of Nizatidine in Water, Methanol, Ethanol, Acetone, and Ethyl Acetate from (273.15 to 343.15) K
• Excess Molar Enthalpies of Benzyl Alcohol + Alkanols (C1-C6) and Their Correlations at 298.15 K and Ambient Pressure
• Excess Molar Volumes of 1,3-Diethyl Propanedioate with Methanol, Ethanol, Propan-1-ol, Propan-2-ol, Butan-2-ol, 2-Methyl-propan-1-ol, and Pentan-1-ol at T = (288.15, 298.15, 313.15, and 328.15) K
• Solubilities of Apigenin in Ethanol + Water at Different Temperatures
• Solubility of Artemisinin in Different Single and Binary Solvent Mixtures Between (284.15 and 323.15) K and NRTL Interaction Parameters
• Measurement and Correlation of the Densities and Viscosities of 2-Bromopropane + Ethanol Binary Mixtures at Temperatures from (298.15 to 318.15) K
• Effect of 2,2',2''-Nitrilotrisethanol on the Vapor-Liquid Equilibria of the Ethanol + Water System at Atmospheric Pressure
• Solubility of Anthracene in C1-C3 Alcohols from (298.2 to 333.2) K and Their Mixtures with 2-Propanone at 298.2 K
• Solubility of Sulpiride in Pure Organic Solvents between (278 and 333) K
• Effect of Dissolved Inorganic Salts on the Enthalpy of Mixing of the Ethanol + Pyridine System at 303.15 K
• Densities and Excess Molar Volumes for Binary Mixtures of Ionic Liquid 1-Ethyl-3-methylimidazolium Ethylsulfate with Solvents
• Solubility of Physalin D in Ethanol, Methanol, Propanone, Trichloromethane, Ethyl Ethanoate, and Water at Temperatures from (283.2 to 313.2) K
• Solubility of Scutellarin in Methanol, Water, Ethanol, and Ethanol + Water Binary Mixtures from (293.2 to 333.2) K
• Solubilities of Ibuprofen in Different Pure Solvents
• Solubility of Genistein in Water, Methanol, Ethanol, Propan-2-ol, 1-Butanol, and Ethyl Acetate from (280 to 333) K
• Ion Association and Solvation of Sulfathiazole Sodium in Aqueous and Partial Aqueous Media
• Solubilities of Cefepime Hydrochloride in Water + (Ethanol, 1-Propanol, or 2-Propanol) from (278.15 to 308.15) K
• The (p, n, T) Properties and Apparent Molar Volumes V of LiBr + C2H5OH
• Solubility of 3,5-Dinitrobenzoic Acid in Supercritical Carbon Dioxide with Cosolvent at Temperatures from (308 to 328) K and Pressures from (10.0 to 21.0) MPa
• Solubilities of Phosphorus-Containing Compounds in Selected Solvents
• Solubility of Andrographolide in Various Solvents from (288.2 to 323.2) K
• Solubilities of 2,4-Dinitro-l-phenylalanine in Monosolvents at (273.15 to 368.15) K
• Electrical Conductivity of Caprolactam Tetrabutylammonium Bromide Ionic Liquids in Aqueous and Alcohol Binary Systems
• Solubility of Form III Piracetam in a Range of Solvents
• Measurement and Correlation of Solubility of Cefuroxime Acid in Pure and Binary Solvents at Various Temperatures
• Determination of Activity Coefficients at Infinite Dilution of 35 Solutes in the Ionic Liquid, 1-Butyl-3-methylimidazolium Tosylate, Using Gas-Liquid Chromatography
• Experimental Isobaric Vapor-Liquid Equilibrium for Binary Systems of Ethyl Methyl Carbonate + Methanol, + Ethanol, + Dimethyl Carbonate, or + Diethyl Carbonate at 101.3 kPa
• Liquid-Liquid Equilibrium of Potassium Phosphate/Potassium Citrate/Sodium Citrate + Ethanol Aqueous Two-Phase Systems at (298.15 and 313.15) K and Correlation
• Solid-Liquid Phase Diagram of the Ternary System of p-Nitroaniline + o-Nitroaniline + Ethanol
• Activity Coefficients at Infinite Dilution for Hydrocarbons in Fatty Alcohols Determined by Gas-Liquid Chromatography
• Excess Gibbs Energies of the Ternary System 2-Methoxyethanol + Tetrahydrofuran + Cyclohexane and Other Relevant Binaries at 298.15 K
• PpT Measurements of the (Ethanol + Linalool), (Propan-1-ol + Linalool), and (Propan-2-ol + Linalool) Mixtures: Cubic and Statistical Associating Fluid Theory-Based Equation of State Analyses
• Solubility of Carbonyl Sulfide in Aqueous Solutions of Ethylene Glycol at Temperatures from (308.15 K to 323.15) K
• Solubility and Crystal Size of Sirolimus in Different Organic Solvents
• Solubility of Butyl Paraben in Methanol, Ethanol, Propanol, Ethyl Acetate, Acetone, and Acetonitrile
• Excess Molar Enthalpies of Methyl Acetoacetate + (Methanol, + Ethanol, + 1-Propanol, and + 2-Propanol) at T = (288.2, 298.2, 313.2, and 328.2) K and p = 101.3 kPa
• Volumetric Properties, Viscosities, and Isobaric Heat Capacities of Imidazolium Octanoate Protic Ionic Liquid in Molecular Solvents
• Solubility of Benzoic Acid in Pure Solvents and Binary Mixtures
• Viscosity and Electrical Conductivity of Binary Mixtures of CnMIM-BF4 with Ethanol at 288 K, 298 K, 308 K, and 318 K
• Influence of the Temperature on the Liquid-Liquid-Solid Equilibria of the Ternary System Water + Ethanol + 1-Decanol
• Solubilities of N-[(4-Bromo-3,5-difluorine)-phenyl]maleimide in Pyridine, Acetone, Tetrahydrofuran, Ethanol, Trichloromethane, and Acetonitrile at Temperature between (285.00 and 350.15) K
• Solubility of Florfenicol in Different Solvents at Temperatures from (278 to 318) K
• Volumetric Properties for (Ionic Liquid + Methanol or Ethanol or 1-Propanol + Nitromethane) at 298.15 K and Atmospheric Pressure
• Densities and Viscosities of Binary Mixture of the Ionic Liquid Bis(2-hydroxyethyl)ammonium Propionate with Methanol, Ethanol, and 1-Propanol at T = (293.15, 303.15, 313.15, and 323.15) K and at P = 0.1 MPa
• Measurement and Correlation of Solubilities of Cefpirome Sulfate in Aqueous Alcohol Solution between (278.15 and 308.15) K
• Solid Liquid Phase Equilibrium and Phase Diagram for the Ternary Carbamazepine Succinic Acid Ethanol or Acetone System at (298.15 and 308.15) K
• Effect of the Ionic Liquid Triethylmethylammonium Dimethylphosphate on the Vapor Pressure of Water, Methanol, Ethanol, and Their Binary Mixtures
• Influence of Typical Impurities on the Surface Tension Measurements of Binary Mixtures of Water and the Ionic Liquids 1-Butyl-3-Methylimidazolium Tetrafluoroborate and Chloride
• Solubility of Dimethyl Fumarate in Methanol, Ethanol, 1-Propanol, 2-Propanol, 1,2-Propanediol, and Water from (289.95 to 347.15) K
• Density, Speed of Sound, Viscosity, Refractive Index, and Excess Volume of N-Methyl-2-pyrrolidone + Ethanol (or Water or Ethanolamine) from T = (293.15 to 323.15) K
• Solubilities of Sodium, Potassium, and Copper(II) Sulfates in Ethanol-Water Solutions
• Solubilities of Phenylphosphinic Acid, Methylphenylphosphinic Acid, Hexachlorocyclotriphosphazene, and Hexaphenoxycyclotriphosphazene in Selected Solvents
• Solubility of 5-Hydroxymethylfurfural in Supercritical Carbon Dioxide with and without Ethanol as Cosolvent at (314.1 to 343.2) K
• Activity Coefficients at Infinite Dilution in Methylimidazolium Nitrate Ionic Liquids
• Measurements of Activity Coefficients at Infinite Dilution for Organic Solutes and Water in the Ionic Liquid 1-Butyl-1-methylpiperydinium Thiocyanate
• Solubility of Candesartan Cilexetil in Different Solvents at Various Temperatures
• Excess Molar Enthalpies of 2-Methyl-2-butanol (1) + 1-Alkanols (C1-C5) (2) at 298.15 K
• Liquid-Liquid Equilibria of the (Water + Ethanol + Linalyl Acetate) Ternary System at Different Temperatures
• Solubility of 1,6-Naphthalene Disulfonic Acid Disodium in Binary Sodium Chloride + Water, Sodium Sulfate + Water, and Ethanol + Water Solvent Mixtures at Elevated Temperatures
• Measurement and Correlation for the Solubilities of Dihydrocapsaicin in n-Heptane, n-Hexane, n-Pentane, Ethyl Acetate, Acetone, Ethanol, and Water
• Solubility of 2-Chloro-4,6-dinitroresorcinol in Ethanol, Methanol, Acetic Acid, Ethyl Acetate, and Water
• Solubility of Dexibuprofen in Different Solvents from (263.15 to 293.15) K
• Solubilities of 3-Carboxy-3-hydroxypentanedioic Acid in Ethanol, Butan-1-ol, Water, Acetone, and Methylbenzene
• Solubilities of Phloretin in 12 Solvents at Different Temperatures
• Densities and Viscosities of Binary Solutions of Benzene-1,3-diol + Water, Ethanol, Propan-1-ol, and Butan-1-ol at T = (293.15 to 333.15) K
• Measurement and Correlation of the Solubility of Prednisone Acetate in Different Solvents
• Measurement and Correlation of Solubilities of Asiaticoside in Water, Methanol, Ethanol, n-Propanol, n-Butanol, and a Methanol + Water Mixture from (278.15 to 343.15) K
• Solubilities of Pioglitazone Hydrochloride in Different Solvents
• Densities and Viscosities of [Bmim][PF6] and Binary Systems [Bmim][PF6] + Ethanol, [Bmim][PF6] + Benzene at Several Temperatures and Pressures: Determined by the Falling-Ball Method
• Solubility of Anthracene and Phenanthrene in Ethanol + 2,2,4-Trimethylpentane Mixtures at Different Temperatures
• Solubility of Minoxidil in Methanol, Ethanol, 1-Propanol, 2-Propanol, 1-Butanol, and Water from (278.15 to 333.15) K
• Solubility of Imperatorin in Ethyl Acetate, Ethanol, Methanol, n-Hexane, and Petroleum Ether from (278.2 to 318.2) K
• Solubilities of Ursolic Acid and Oleanolic Acid in Four Solvents from (283.2 to 329.7) K
• Measurement and Correlation for Solubilities of 16-Dehydropregnenolone Acetate in Different Solvents
• Solubility of CO2 in Alcohols, Glycols, Ethers, and Ketones at High Pressures from (288.15 to 318.15) K
• Densities and Viscosities of Four Binary Diethyl Carbonate + 1-Alcohol Systems from (288.15 to 313.15) K
• Measurement and Correlation of Solubilities of (Z)-2-(2-Aminothiazol-4-yl)-2-methoxyiminoacetic Acid in Different Pure Solvents and Binary Mixtures of Water + (Ethanol, Methanol, or Glycol)
• Phase Diagram Data for Ethanol/Propan-1-ol/Propan-2-ol-2,3-Dihydroxybutanedioate Aqueous Two-Phase Systems at 298.15 K and Data Correlation
• Vapor-Liquid Equilibrium for Dimethyl Disulfide + Butane, + trans-But-2-ene, + 2-Methylpropane, + 2-Methylpropene, + Ethanol, and 2-Ethoxy-2-methylpropane
• Activity Coefficients at Infinite Dilution of Organic Solutes in 1-Butyl-3-methylimidazolium Nitrate Using Gas-Liquid Chromatography
• Measurement and Correlation of Solubility of Clopidogrel Hydrogen Sulfate (Metastable Form) in Lower Alcohols
• Solubility of 2-(2,4,6-Trichlorophenoxy)ethyl Bromide in Methanol, Ethanol, Propanol, Isopropanol, Acetonitrile, n-Heptane, and Acetone
• Solubility of Phenothiazine in Water, Ethanol, and Propylene Glycol at (298.2 to 338.2) K and Their Binary and Ternary Mixtures at 298.2 K
• Activity Coefficients at Infinite Dilution of Organic Compounds in Four New Imidazolium-Based Ionic Liquids
• Vapor Liquid Equilibria and Interfacial Tensions of the System Ethanol + 2-Methoxy-2-methylbutane
• Solubility and Phase Separation of 2-(N-Morpholino)ethanesulfonic Acid (MES) and 4-(N-Morpholino)butanesulfonic Acid (MOBS) in Aqueous 1,4-Dioxane and Ethanol Solutions
• Solubilities of Tris(o-phenylenedioxy)cyclotriphosphazene in Selected Solvents
• ACSExcess Molar Enthalpies of Mixtures of (+-)-Linalool with Several Alkanols
• Isobaric Vapor Liquid Equilibrium for the Ethanol + Water + 1,3-Dimethylimidazolium Dimethylphosphate System at 101.3 kPa
• Solubility of 2,7-Dihydroxynaphthalene in Binary Sodium Chloride + Water, Sodium Sulfate + Water, and Ethanol + Water Solvent Mixtures at Elevated Temperatures
• Solubilities of Betulinic Acid in Thirteen Organic Solvents at Different Temperatures
• Vapor Liquid Equilibrium Measurements of Difluoromethane + [Emim]OTf, Difluoromethane + [Bmim]OTf, Difluoroethane + [Emim]OTf, and Difluoroethane + [Bmim]OTf Systems
• Evaluation of Excess Molar Enthalpies for a Quaternary Mixture System of Acetic Anhydride, Ethanol, Acetic Acid, and Ethyl Acetate
• Viscosity and density measurement for six binary mixtures of water (methanol or ethanol) with an ionic liquid [BMIM][DMP] or [EMIM][DMP] at atmospheric pressure in the temperature range of (293.15 to 333.15) K
• Electrical Conductivity of Solutions of Ionic Liquids with Methanol, Ethanol, Acetonitrile, and Propylene Carbonate
• Activity Coefficients at Infinite Dilution by GLC in Alkanediamines as Stationary Phases
• Partition Coefficients of Organic Compounds in Four New Tetraalkylammonium Bis(trifluoromethylsulfonyl)imide Ionic Liquids Using Inverse Gas Chromatography
• Liquid Liquid Equilibria of Methanol, Ethanol, and Propan-2-ol with Water and Dodecane
• Isobaric Vapor Liquid Equilibrium for Binary Systems of Toluene + Acrylic Acid, Toluene + Acetic Acid, and Cyclohexane + Acrylic Acid at 20 kPa
• Density, Viscosity, and Refractive Index Properties for the Binary Mixtures of n-Butylammonium Acetate Ionic Liquid + Alkanols at Several Temperatures
• Surface Tensions of Three Amyl Alcohol + Ethanol Binary Mixtures from (293.15 to 323.15) K
• Isobaric Vapor Liquid Equilibria for the Extractive Distillation of Ethanol + Water Mixtures Using 1-Ethyl-3-methylimidazolium Dicyanamide
• New High Pressure Vapor Liquid Equilibrium and Density Predictions for the Carbon Dioxide + Ethanol System
• Interactions of Volatile Organic Compounds with the Ionic Liquid 1-Butyl-1-methylpyrrolidinium Dicyanamide
• Excess Molar Enthalpies of Ternary and Binary Mixtures Containing 2-Methoxy-2-Methylpropane, Ethanol, and Nonane
• Antisolvent Precipitation of Vitamin B6: A Thermodynamic Study
• Ebulliometric Determination and Prediction of Vapor Liquid Equilibria for Binary Mixtures of Ethanol and Ethyl Hexanoate
• Isobaric Vapor-Liquid Equilibria for Ethanol + Water + Ethylene Glycol and Its Constituent Three Binary Systems
• Isobaric Vapor-Liquid Equilibrium for Binary Systems of Toluene + Ethanol, Toluene + Isopropanol at (101.3, 121.3, 161.3 and 201.3) kPa
• Densities and Viscosities of the Binary Mixtures of 1-Ethyl-3-methylimidazolium Bis(trifluoromethylsulfonyl)imide with N-Methyl-2-pyrrolidone or Ethanol at T = (293.15 to 323.15) K
• Liquid-Liquid Phase Behaviors of Geraniol in Aqueous Alcohol Mixtures
• Densities, Viscosities, Refractive Indexes, and Surface Tensions for Mixtures of Ethanol, Benzyl Acetate, and Benzyl Alcohol
• Solubility of Sodium 4-Nitrobenzenesulfonate in Binary Sodium Chloride + Water, Sodium Sulfate + Water, and Ethanol + Water Solvent Mixtures at Elevated Temperatures
• Experimental Measurement and Modeling of Aniline Hydrochloride Solubility in Water, Methanol, Ethanol, 1- Propanol and Their Mixed Systems
• Densities and Viscosities for Binary Mixtures of the Ionic Liquid N-Ethyl Piperazinium Propionate with n-Alcohols at Several Temperatures
• Evaluation of the Performance of Trigeminal Tricationic Ionic Liquids for Separation Problems
• Excess Volumes of Ternary Mixtures 2,2,4-Trimethylpentane + Diisopropyl Ether or Methyl tert-Butyl Ether + Methanol, Ethanol, or 1-Propanol at 298.15 K
• Vapor Liquid Equilibrium, Densities, and Interfacial Tensions of the System Ethanol + Tetrahydro-2H-pyran
• Solubility of Thiotriazinone in Binary Solvent Mixtures of Water + Methanol and Water + Ethanol from (283 to 330) K
• Density, Speed of Sound, Viscosity, Refractive Index, and Excess Volume of N-Methyl-2-pyrrolidone (NMP) + Water + Ethanol from T = (293.15 to 323.15) K
• Solubility and Solution Thermodynamics of Betaine in Different Pure Solvents and Binary Mixtures
• Densities and Viscosities of Naphthalen-1-ol, Naphthalen-2-ol, and 1-Aminonaphthalene in the Solvents of Ethanol, Propan-1-ol, and Butan-1-ol
• Density and Derived Thermodynamic Properties of 1-Ethyl-3-methylimidazolium Alkyl Sulfate Ionic Liquid Binary Mixtures with Water and with Ethanol from 288 K to 318 K
• Solubility of 2-Butyl-3-benzofuranyl 4-(2-(Diethylamino)ethoxy)-3,5-diiodophenyl Ketone Hydrochloride (Amiodarone HCl) in Ethanol + Water and N-Methyl-2-pyrrolidone + Water Mixtures at Various Temperatures
• Solid Liquid Phase Equilibrium and Solubility of Dibenzo[b,d]furan and 9H-Fluoren-9-one in Organic Solvents
• Specific Heat Capacity at Constant Pressure of Ethanol by Flow Calorimetry
• Effects of NaOH and Ethanol on the Solubility of Disodium Decanedioate in Water
• Solubility of L-Phenylalanine Anhydrous and Monohydrate Forms: Experimental Measurements and Predictions
• Determination of Gas Concentrations in Liquids by Nuclear Magnetic Resonance: Hydrogen in Organic Solvents
• Solubility of o-Nitrobenzoic Acid in Modified Supercritical Carbon Dioxide at (308 to 328) K
• Liquid Liquid Equilibrium for the Water + Diethyl Carbonate + Ethanol System at Different Temperatures
• Solubility of 6-Chloropyridazin-3-amine in Different Solvents
• Measurement and Correlation of the Solubility of 2,6-Diaminohexanoic Acid Hydrochloride in Aqueous Methanol and Aqueous Ethanol Mixtures
• Solubilities of Protocatechuic Aldehyde, Caffeic Acid, d-Galactose, and d-Raffinose Pentahydrate in Ethanol Water Solutions
• Solubilities of Bis(2,4,6-trimethylbenzoyl)phenylphosphine Oxide in Different Organic Solvents at Several Temperatures
• Vapor Liquid Equilibrium Data for Binary Systems of 1-Methyl-4-(1-methylethenyl)-cyclohexene + {Ethanol, Propan-1-ol, Propan-2-ol, Butan-1-ol, Pentan-1-ol, or Hexan-1-ol} at 40 kPa
• Solubility of Vitamin D3 in Six Organic Solvents at Temperatures from (248.2 to 273.2) K
• Vapor Liquid Equilibria Measurements of Bitter Orange Aroma Compounds Highly Diluted in Boiling Hydro-Alcoholic Solutions at 101.3 kPa
• Determination and Correlation of Pyridazin-3-amine Solubility in Eight Organic Solvents at Temperatures Ranging from (288.05 to 333.35) K
• Determination and Prediction of Vapor Liquid Equilibria for a System Containing Water + Butyl Acetate + Cyclohexane + Ethanol
• Viscosimetric Study of Binary Mixtures Containing Pyridinium-Based Ionic Liquids and Alkanols
• Solubility of 3-Ethyl-5-methyl-(4RS)-2-((2-aminoethoxy)methyl)-4-(2-chlorophenyl)-1,4-dihydro-6-methyl-3,5-pyridinedicarboxylate Monobenzenesulfonate (Amlodipine Besylate) in Ethanol + Water and Propane-1,2-diol + Water Mixtures at Various Temperatures
• Densities and Viscosities for Binary Liquid Mixtures of Ethanol + 1-Propanol, 1-Butanol, and 1-Pentanol from (293.15 to 328.15) K at 0.1 MPa
• Measurement and Correlation of the Solubility of Febuxostat in Four Organic Solvents at Various Temperatures
• Liquid Liquid Equilibrium for the Ternary System 2-Methyl-1-propanol + 3-Methyl-1-butanol + Water at (298.15, 323.15, and 348.15) K
• Activity Coefficients at Infinite Dilution for Organic Compounds Dissolved in 1-Alkyl-1-methylpyrrolidinium Bis(trifluoromethylsulfonyl)imide Ionic Liquids Having Six-, Eight-, and Ten-Carbon Alkyl Chains
• Isobaric Vapor Liquid Equilibrium Data of 2-Methyl-propan-2-ol (1) + Heptan-1-ol (2), Methanol (1) + Heptan-1-ol (2), Ethanol (1) + Heptan-1-ol (2), and Propan-1-ol (1) + Heptan-1-ol (2) at 96.5 kPa
• Solubility of the Metastable Polymorph of Piracetam (Form II) in a Range of Solvents
• Isobaric Vapor Liquid Equilibrium for the Ethanol + Water + 2-Aminoethanol Tetrafluoroborate System at 101.3 kPa
• Solubility of N-Chloro-4-toluenesulfonamide Sodium and N-Chlorobenzenesulfonamide Sodium in Ethanol, Water, 1-Propanol, and Butan-2-ol
• Solubility, Density and Solution Thermodynamics of NaI in Different Pure Solvents and Binary Mixtures
• Geometric Structures of Associating Component Optimized toward Correlation and Prediction of Isobaric Vapor Liquid Equilibria for Binary and Ternary Mixtures of Ethanal, Ethanol, and Ethanoic Acid
• Electrical Conductivity of Aqueous Ethanol Solutions Containing Ammonium Salts under High Pressure at 298 K
• Vapor Liquid Liquid Equilibria Measurements for the Dehydration of Ethanol, Isopropanol, and n-Propanol via Azeotropic Distillation Using DIPE and Isooctane as Entrainers
• Solubility of Xylose, Mannose, Maltose Monohydrate, and Trehalose Dihydrate in Ethanol Water Solutions
• Effect of Inorganic Salts on the Isobaric Vapor Liquid Equilibrium of the Ethyl Acetate Ethanol System
• Solubility of Clonazepam and Diazepam in Polyethylene Glycol 200, Propylene Glycol, N-Methyl Pyrrolidone, Ethanol, and Water at (298.2 to 318.2) K and in Binary and Ternary Mixtures of Polyethylene Glycol 200, Propylene Glycol, and Water at 298.2 K
• Solubility of p-Nitroaniline in Supercritical Carbon Dioxide with and without Mixed Cosolvents
• Equilibrium Solubility of Sodium 3-Nitrobenzenesulfonate in Binary NaCl + H2O, Na2SO4 + H2O, and C2H5OH + H2O Solvent Mixtures at Elevated Temperatures from (273.15 to 323.15) K
• Determination and Correlation of Solubility Data and Dissolution Thermodynamic Data of l-Lactide in Different Pure Solvents
• Determination and Correlation of Solubility of Tris(3-hydroxypropyl)phosphine Oxide in Selected Solvents
• Densities and Viscosities of Three Binary Monoglyme + 1-Alcohol Systems from (283.15 to 313.15) K
• Thermal Conductivity of DMSO + C2H5OH, DMSO + H2O, and DMSO + C2H5OH + H2O Mixtures at T = (278.15 to 338.15) K
• Solubilities of 4,4'-Dichlorodiphenyl Disulfide in Six Organic Solvents between (303.15 and 333.15) K
• Ionic Conductivities of Binary Mixtures Containing Pyridinium-Based Ionic Liquids and Alkanols
• Isothermal Vapor Liquid Equilibrium Measurements of 1,1-Difluoroethane + N,N-Dimethylformamide and N,N-Dimethylacetamide
• Surface Tension Measurements for Seven Imidazolium-Based Dialkylphosphate Ionic Liquids and Their Binary Mixtures with Water (Methanol or Ethanol) at 298.15 K and 1 atm
• Solubility of Veratric Acid in Eight Monosolvents and Ethanol + 1-Butanol at Various Temperatures
• Measurement and Correlation of the Solubility of Disodium 4,4?-Dinitrostilbene-2,2?-disulfonate in Aqueous Organic Solutions
• Isothermal Vapor Liquid Equilibrium Data for the Butan-2-one + Methanol or Ethanol Systems Using a Static-Analytic Microcell
• Solubility of Naringenin in Ethanol and Water Mixtures
• Solubility of 3-Aminobenzoic Acid in Supercritical Carbon Dioxide Modified by Ethanol
• Solubilities of Rutaecarpine in Twelve Organic Solvents from (283.2 to 323.2) K
• Measurement and Prediction of Excess Enthalpies for Ternary Solutions 1-Ethyl-3-methylimidazolium Dimethylphosphate + Methanol or Ethanol + Water at 298.15 K and at Normal Atmospheric Pressure
• Determination and Correlation of Solubilities of (S)-Indoline-2-carboxylic Acid in Six Different Solvents from (283.15 to 358.15) K
• Activity Coefficients at Infinite Dilution for Organic Solutes Dissolved in Three 1-Alkyl-1-methylpyrrolidinium Bis(trifluoromethylsulfonyl)imide Ionic Liquids Bearing Short Linear Alkyl Side Chains of Three to Five Carbons
• Isobaric Vapor Liquid Equilibrium Data of Acrylonitrile (1) + Heptan-1-ol (2), Acrylonitrile (1) + Ethanol (2), and Nitrobenzene (1) + Heptan-1-ol (2) at 96.5 kPa
• Determination and Correlation of Solubility of Cefradine Form I in Five Pure Solvents from (283.15 to 308.15) K
• Measurement and Modeling of Vapor Liquid Equilibria for the Octane + Sulfuric Acid + Water + Ethanol System
• Solubilities of 4-Bromo-1,8-naphthalic Anhydride in Different Pure Solvents and Binary Solvent Mixtures with the Temperature Range from (278.15 to 333.15) K
• Thermal Conductivities of [EMIM][EtSO4], [EMIM][EtSO4] + C2H5OH, [EMIM][EtSO4] + H2O, and [EMIM][EtSO4] + C2H5OH + H2O at T = (283.15 to 343.15) K
• Experimental Study of Chemical Equilibria in the Liquid-Phase Reaction between 1-Octanol and Ethanol to 1-Ethoxyoctane
• Solubilities of 1,3,2-Dioxaphosphorinane-2-methanol-a,a-5,5-tetramethyl 2-oxide in Selected Solvents at 273.15 K to 343.15 K
• Binary Diffusion Coefficients of Platinum(II) Acetylacetonate in Supercritical Carbon Dioxide
• Solubility of Benzyl Disulfide in Five Organic Solvents between (283.45 and 333.15) K
• Volumetric, Viscometric, and Refractive Index Behavior of 7-Hydroxy-4-methylcoumarin in Aqueous Ethanol or 1-Propanol Solutions in the Temperature Range of (293.15 to 313.15) K
• Liquid Liquid Solid Triple-Phase Data for Aqueous Two-Phase Systems comprising Ethanol 1-Propanol 2-Propanol Acetone and Salts
• Solubilities of Phosphonic Acid, P,P'-(1,4-Piperazinediyl)bis-,P,P,P',P'-tetraphenyl Ester in Selected Solvents
• Liquid Liquid Equilibrium of Various Aqueous Two-Phase Systems: Experiment and Correlation
• Fructose solubility in mixed (ethanol + water) solvent: experimental data and comparison among different thermodynamic models.
• Volumetric and Transport Properties of Binary Mixtures of n-Octane + Ethanol, + 1-Propanol, + 1-Butanol, and + 1-Pentanol from (293.15 to 323.15) K at Atmospheric Pressure
• Solubility and Partition Coefficients of 5-Fluorouracil in ScCO2 and ScCO2/Poly(l-lactic acid)
• Solubility of 3,4-Dichloronitrobenzene in Methanol, Ethanol, and Liquid Mixtures (Methanol + Water, Ethanol + Water): Experimental Measurement and Thermodynamic Modeling
• Solubility of Hesperetin in Mixed Solvents
• Vapor Liquid Equilibrium for the 1,1,1-Trifluorotrichloroethane + Sulfuryl Chloride System at 101.3 kPa
• Solubility of 3,4-Bis(3-nitrofurazan-4-yl)furoxan in Common Solvents at Temperatures between 293.15 K and 313.15 K
• Equilibrium Solubility of Sodium 2,4-Diaminobenzenesulfonate in Binary NaCl + H2O, Na2SO4 + H2O, and C2H5OH + H2O Solvent Mixtures at Elevated Temperatures from 273.15 K to 323.15 K
• Density and Viscosity of the Binary Systems Ethanol + Butan-1-ol, + Pentan-1-ol, + Heptan-1-ol, + Octan-1-ol, Nonan-1-ol, + Decan-1-ol at 0.1 MPa and Temperatures from 283.15 K to 313.15 K
• Measurement and Correlation of Solubility of 2-Chloro-4-ethylamino-6-isopropylamino-1,3,5-triazine in Different Organic Solvents
• Isobaric Vapor Liquid Equilibrium and Isothermal Interfacial Tensions for the System Ethanol + 2,5-Dimethylfuran
• Excess Molar Enthalpies of Binary Mixtures Containing 1-Methyl-3-octyl-imidazolium Tetrafluoroborate and Alcohols at T = 298.15 K
• Solubility and Dissolution Thermodynamic Data of Mefenamic Acid Crystals in Different Classes of Organic Solvents
• Solubility of Cefpiramide Sodium in Binary Ethanol + Water and 2-Propanol + Water Solvent Mixtures
• Evaluation of the 2-Methoxyethanol as Entrainer in Ethanol Water and 1-Propanol Water Mixtures
• Measurement and Correlation of Solubilities of Indole-2-carboxylic Acid in Ten Different Pure Solvents from (278.15 to 360.15) K
• Phase Equilibria in Systems with Levulinic Acid and Ethyl Levulinate
• Effect of Solvent Composition and Temperature on the Solubility of Ibuprofen in Aqueous Ethanol
• Solubility of 2-Hydroxypropane-1,2,3-tricarboxylic Acid Monohydrate in Different Binary Solvents from (278.15 to 303.15) K
• Isobaric Vapor Liquid Equilibrium for the Binary Systems (Diethylamine + Ethanol), (Ethanol + N,N-Diethylethanolamine), and (Diethylamine + N,N-Diethylethanolamine) at p = (80.0 and 40.0) kPa
• Measurement and Correlation of Solubility of Azithromycin Monohydrate in Five Pure Solvents
• Solubility Measurement and Stability Study of Sodium Cefuroxime
• Solubility of 1-Fluoro-4-(methylsulfonyl)benzene in Five Pure Organic Solvents at Temperatures from (288.40 to 331.50) K
• Densities and Viscosities of Diaminotoluene with Water, Ethanol, Propan-1-ol, and Butan-1-ol from (293.15 to 333.15) K
• Solubilities of 4-(Hydroxymethyl)-1-oxido-2,6,7-trioxa-1-phosphabicyclo[2.2.2]octane in Organic Solvents
• Measurement and Correlation of Tadalafil Solubility in Five Pure Solvents at (298.15 to 333.15) K
• Thermodynamics of Fluconazole Solubility in Various Solvents at Different Temperatures
• Measurement and Correlation of Solubilities of 4-Amino-3,6-dichloropyridazine in Ethanol + Water Mixtures from (303.15 to 323.15) K
• Solubility of 4-Hydroxybenzaldehyde in Supercritical Carbon Dioxide with and without Cosolvents
• Solid Liquid Phase Equilibria of N,N'-[1,3-Phenylenebis(methylene)]bis(phosphoramidic acid) P,P,P',P'-Tetraphenyl Ester in 10 Pure Solvents
• Densities and Viscosities of Binary Mixtures Containing 1,3-Dimethylimidazolium Dimethylphosphate and Alcohols
• Measurement and Correlation of Solubility and Dissolution Thermodynamic Properties of Furan-2-carboxylic Acid in Pure and Binary Solvents
• Solubility of Cefotaxime Sodium in Ethanol + Water Mixtures under Acetic Acid Conditions
• Measurement and Correlation for Solubility of L-valine in Water, Ethanol, N,N-Dimethylformamide, Acetone, and Isopropyl alcohol between 293.15 and 343.15 K
• Experimental Measurements and Modeling of the Solubility of Aceclofenac in Six Pure Solvents from (293.35 to 338.25) K
• Solubility of Trehalose in Water + Ethanol Solvent System from (288.15 to 318.15) K
• Infinite Dilution Activity Coefficients of Solutes Dissolved in Two Trihexyl(tetradecyl)phosphonium Ionic Liquids
• Determination and Correlation of Solubility Data and Dissolution Thermodynamic Data of Cefixime Trihydrate in Seven Pure Solvents
• Measurement and Correlation of the Solubility of L-Carnitine in Different Pure Solvents and Ethanol Acetone Solvent Mixture
• Solubility of Metoclopramide Hydrochloride in Six Green Solvents at (298.15 to 338.15) K
• Solubility of chrysin in ethanol and water mixtures
• Isobaric Vapor Liquid Liquid Equilibria for the Ternary Systems Ethanol + Water + Propyl Acetate and 1-Propanol + Water + Propyl acetate
• Investigation of Surface Properties and Solubility of 1-Vinyl-3-alkyl/Esterimidazolium Halide Ionic Liquids by Density Functional Methods
• Solubility of Bioactive Compound Hesperidin in Six Pure Solvents at (298.15 to 333.15) K
• Measurement and Correlation of the Solubility of Enrofloxacin in Different Solvents from (303.15 to 321.05) K
• Determination and Correlation of Solubilities of Lauric Acid in Eight Alcohols
• Measurement and Correlation of Solubility of l-Valine in Water + (Ethanol, N,N-Dimethylformamide, Acetone, Isopropyl Alcohol) from 293.15 K to 343.15 K
• Solubility of Aspartame in Water, Methanol, Ethanol and Different Binary Mixtures in the Temperature Range of (278.15 to 333.15) K
• 4-Amino-3,6-dichloropyridazine Solubility Measurement and Correlation in Seven Pure Organic Solvents from (278.15 to 333.15) K
• Bubble Point Determination for CO2 + Ethanol + Alkanolamines (Monoethanolamine, Diethanolamine, or Triethanolamine) at High Pressures
• Solubility of Dexamethasone in Supercritical Carbon Dioxide with and without a Cosolvent
• Solubility of (2Z)-N-Cyclohexyl-2-(3-hydroxybenzylidine) Hydrazine Carbothioamide in Different Pure Solvents at (298.15 to 338.15) K
• Density, Viscosity, and Conductivity of Binary Mixtures of the Ionic Liquid N-(2-Hydroxyethyl)piperazinium Propionate with Water, Methanol, or Ethanol
• Measurement and Correlation of Solubility of Calcium-l-lactate Pentahydrate in Ethanol + Water and Acetone + Water Systems
• Thermodynamic Models for Determination of the Solubility of Dibenzothiophene in Different Solvents at Temperatures from (278.15 to 328.15) K
• Solubilities of 1,1'-[1,2-Ethanediylbis(oxy-1,2-ethanediyl)]bis-[3-methyl-1H-imidazolium-1-yl] Dihexafluorophosphate in Water, Methanol, Ethanol, Dimethylformamide, Dimethyl Sulfoxide, and (Acetone + Water) Binary Solvent Mixtures
• Solubility of N-(4-Chlorophenyl)-2-(pyridin-4-ylcarbonyl)hydrazinecarbothioamide (Isoniazid Analogue) in Five Pure Solvents at (298.15 to 338.15) K
• Experimental Measurement and Modeling of Solubility Data for 2,3-Dichloronitrobenzene in Methanol, Ethanol, and Liquid Mixtures (Methanol + Water, Ethanol + Water)
• Equilibrium Solubility of Sodium 1-Naphthalenesulfonate in Binary NaCl + Water, Na2SO4 + Water, and C2H5OH + Water Solvent Mixtures from (278.15 to 323.15) K
• Experimental Measurement and Correlation of Solubility Data and Thermodynamic Properties of Protocatechuic Acid in Four Organic Solvents
• Liquid Liquid Equilibria for Quaternary Systems of Water + Ethanol + Diethyl Carbonate + Methylbenzene or Heptane
• Liquid Liquid Equilibrium in Mixtures Containing Propane-1,2,3-triol and Mixtures Containing Vegetable Oils at Atmospheric Pressure
• Density, Speed of Sound, Viscosity, and Excess Properties of Binary Mixtures Formed by Ethanol and Bis(trifluorosulfonyl)imide-Based Ionic Liquids
• Solubility of Clopidogrel Hydrogen Sulfate (Form II) in Ethanol + Cyclohexane Mixtures at (283.35 to 333.75) K
• Measurement and Correlation of Solubility of Tetraphenyl Piperazine-1,4-diyldiphosphonate in Mixed Solvents
• Phase Equilibrium, Excess Enthalpies and Densities of Binary Mixtures of Trimethylbutylammonium Bis(trifluoromethylsulfonyl)imide with Ethanol, 1-Propanol and Dimethylformamide
• Vapor Liquid Equilibria Measurements for the Nine n-Alkane/Ketone Pairs Comprising 2-, 3-, and 4-Heptanone with n-Octane, n-Nonane, and n-Decane
• Solubility Measurement and Correlation for 3,5-Dichloroaniline in (Methanol + Water) and (Ethanol + Water) Mixed Solvents
• Equilibrium Solubilities of Iso-eicosane in Supercritical Carbon Dioxide
• Experimental Measurement and Modeling of the Solubility of Biotin in Six Pure Solvents at Temperatures from 298.15 K to 333.85 K
• Solubility and Thermodynamic Properties of (2S)-Pyrrolidine-2-carboxylic Acid in Water, Alcohols, and Water Alcohol Mixtures
• Solubilities of 1,3,2-Dioxaphosphorinane-2-methanol-a,5,5-trimethyl-a-phenyl-2-oxide in Selected Solvents between 278.15 K and 343.15 K
• Measurement and Correlation of the Solubility of Penicillin V potassium in Ethanol + Water and 1-Butyl alcohol + Water Systems
• Thermodynamic Models for Determination of the Solubility of Sulfanilic Acid in Different Solvents at Temperatures from (278.15 to 328.15) K
• Thermodynamic Properties of Polymorphs of 2,2'-Thiodiethylene Bis[3-(3,5-di-tert-butyl-4-hydroxyphenyl)propionate]
• Correlation of Solubility of Bioactive Compound Reserpine in Eight Green Solvents at (298.15 to 338.15) K
• Liquid Liquid Equilibria of Three Ternary Systems: {Glycerol + Benzene + Methanol}, {Glycerol + Benzene + Ethanol}, and {Glycerol + Benzene + 1-Propanol}
• Experimental and Modeling Studies on the Solubility of d-Pantolactone in Four Pure Solvents and Ethanol Water Mixtures
• Solubilities of 5,10,15,20-Tetraphenylporphyrin and 5,10,15,20-Tetraphenylporphyrin Manganese(III) Chloride in Binary Ethanol + Water Solvent Mixtures
• Solubility and Solution Thermodynamics of Diphenoxylate in Different Pure Solvents
• Determination and Correlation of Solubilities of 2-Isopropylthioxanthone (ITX) in Seven Different Solvents from (299.15 to 329.85) K
• Isothermal Vapor Liquid Equilibrium of Ethanol + Glycerol and 2-Propanol + Glycerol at Different Temperatures
• Solubility of 3,3'-(Oxidi-2,1-ethanediyl)bis[1-methyl-imidazolium] Dihexafluorophosphate in Water, Methanol, Ethanol, Acetone, and Acetonitrile and Binary Mixtures (Water + DMF) from (283.00 to 323.00) K
• Measurement, Correlation, and Thermodynamics of Solubility of Isatin in Nine Different Green Solvents at (298.15 to 338.15) K
• Vapor Liquid Equilibrium Measurements and Thermodynamic Modeling of the System (Methane + Cyclohexane + Ethanol)
• Determination and Modeling of the Solubility of 2,4-Dimethoxybenzoic Acid in Six Pure and Isopropanol + Ethyl Acetate Mixed Organic Solvents at Temperatures From (288.15 to 323.15) K
• Solubility of 2,5-Di-tert-butylhydroquinone and Process Design for Its Purification Using Crystallization
• Solid Liquid Phase Equilibrium of Phosphoramidic acid, N,N'-1,2-Ethanediylbis-P,P,P',P'-tetraphenyl Ester in Selected Solvents
• Solubility Determination and Thermodynamic Models for 2-Methylnaphthalene in Different Solvents from T = (278.15 to 303.15) K
• Speed of Sound Measurements in Ethanol and Benzene over the Temperature Range from (253.2 to 353.2) K at Pressures up to 30 MPa
• Measurement and Correlation of the Solubility for 4,4'-Diaminodiphenylmethane in Different Solvents
• Solubility of Glycyrrhizin in supercritical carbon dioxide with and without cosolvent
• Density and Viscosity of Binary Liquid Mixtures of Ethanol + 1-Hexanol and Ethanol + 1-Heptanol from (293.15 to 328.15) K at 0.1 MPa
• Solid-Liquid Phase Equilibrium and Ternary Phase Diagrams of Ibuprofen-Nicotinamide Cocrystals in Ethanol and Ethanol/Water Mixtures at (298.15 and 313.15) K
• Liquid Liquid Equilibrium for Ternary Systems Containing Water, Oleic Acid, and Alcohols at 313.15 K. Effect of Alcohol Chain Length
• Solubility of Atractylenolide III in Hexane, Ethyl Acetate, Diethyl Ether, and Ethanol from (283.2 to 323.2) K
• Viscosity and Density of Water + Ethyl Acetate + Ethanol Mixtures at 298.15 and 318.15 K and Atmospheric Pressure
• Isothermal Vapor-Liquid Equilibrium at 333.15 K, Density, and Refractive Index at 298.15 K for the Ternary Mixture of Dibutyl Ether + Ethanol + Benzene and Binary Subsystems
• Measurement and Prediction of Vapor Pressure of Binary and Ternary Systems Containing 1-Ethyl-3-methylimidazolium Ethyl Sulfate
• Solubilities of 2,4,8,10-Tetraoxa-3,9-diphosphaspiro[5.5]undecane-3,9-dimethanol, r,r,rcents,rcents-tetramethyl-3,9-dioxide in Selected Solvents
• Solubilities of Betulin in Fourteen Organic Solvents at Different Temperatures
• Isothermal Binary and Ternary VLE for the Mixtures of Propyl Vinyl Ether + Ethanol + Isooctane at 323.15 K and VE at 293.15 K
• Ternary Liquid-Liquid Equilibria Ethanol + 2-Butanone + 1-Butyl-3-methylimidazolium Hexafluorophosphate, 2-Propanol + 2-Butanone + 1-Butyl-3-methylimidazolium Hexafluorophosphate, and 2-Butanone + 2-Propanol + 1,3-Dimethylimidazolium Methyl Sulfate at 298.15 K
• High-Pressure Vapor-Liquid Equilibrium Data for Systems Involving Carbon Dioxide + Organic Solvent + a-Carotene
• Measurement and Correlation of Solubility of Xylitol in Binary Ethanol + Acetone Solvent Mixtures with the Combined Nearly Ideal Binary Solvent/ Redlich-Kister Equation
• Solubility of Chlorpheniramine Maleate in Ethanol, 1-Propanol, 1-Butanol, Benzene, Ethyl Acetate, Ethyl Formate, and Butyl Acetate between 283 K and 333 K
• Solubility of D-Glucose in Water and Ethanol/Water Mixtures
• Solubility of Fluorene in Different Solvents from 278.98 K to 338.35 K
• Volumetric and Ultrasonic Studies of 1-Ethyl-3-methylimidazolium Trifluoromethanesulfonate Ionic Liquid with Methanol, Ethanol, 1-Propanol, and Water at Several Temperatures
• Solubility of Triethylenediamine in Methanol, Ethanol, Isopropanol, I-Butanol, and Ethyl Acetate between 276.15 K and 363.15 K
• Properties of Sugar, Polyol, and Polysaccharide Water-Ethanol Solutions
• Solubility of 1-H-Tetrazole-1-acetic Acid in Different Solvents between 283 K and 323 K
• Solubility of Phenacetinum in Methanol, Ethanol, 1-Propanol, 1-Butanol, 1-Pentanol, Tetrahydrofuran, Ethyl Acetate, and Benzene between 282.65 K and 333.70 K
• Study of the Temperature Dependence of Surface Tensions of Some Alkanol + Hexane Mixtures
• Solubility of Clindamycin Phosphate in Binary Water-Ethanol Solvent
• Solubility of 2,6-Diaminopyridine in Toluene, o-Xylene, Ethylbenzene, Methanol, Ethanol, 2-Propanol, and Sodium Hydroxide Solutions
• Liquid-Liquid Equilibria for Binary System of Ethanol + Hexadecane at Elevated Temperature and the Ternary Systems of Ethanol + Heterocyclic Nitrogen Compounds + Hexadecane at 298.15 K
• Density and Speed of Sound of Binary Mixtures of N-Methyldiethanolamine and Triethanolamine with Ethanol
• Density and Heat Capacity as a Function of Temperature for Binary Mixtures of 1-Butyl-3-methylpyridinium Tetrafluoroborate + Water, + Ethanol, and + Nitromethane
• Thermodynamic Properties of 1-Butyl-3-methylpyridinium Tetrafluoroborate and Its Mixtures with Water and Alkanols
• Solubility of Irbesartan (Form A) in Different Solvents between 278 K and 323 K
• Solubilities of the Gaseous and Liquid Solutes and Their Thermodynamics of Solubilization in the Novel Room-Temperature Ionic Liquids at Infinite Dilution by Gas Chromatography
• Solubilities of 2-Methyl-1,4-naphthoquinone in Water + (Methanol, Ethanol, 1-Propanol, 2-Propanol, 1,2-Propanediol, and Glycerin, Respectively) from (293.15 to 337.92) K
• Temperature Dependence of the Volumetric Properties of Binary and Ternary Mixtures of Water (1) + Methanol (2) + Ethanol (3) at Ambient Pressure (81.5 kPa)
• Solubility of Oleanolic Acid in Various Solvents from (288.3 to 328.3) K
• Ionic Conductivity of Selected 2:1 Electrolytes in Dilute Solutions of Mixed Aqueous Organic Solvents at 298.15 K
• Vapor-Liquid Equilibrium Behaviors of 3-Ethoxy-4-hydroxybenzaldehyde in Alcohol
• Experimental Determination, Correlation, and Prediction of Physical Properties of the Ternary Mixtures Ethanol + Water with 1-Octyl-3-methylimidazolium Chloride and 1-Ethyl-3-methylimidazolium Ethylsulfate
• Isobaric Vapor-Liquid Equilibria for Ethyl Acetate + Ethanol + 1-Ethyl-3-methylimidazolium Trifluoromethanesulfonate at 100 kPa
• Ternary Liquid-Liquid Equilibria for Six Systems Containing Ethylacetate + Ethanol or Acetic Acid + an Imidazolium-Based Ionic Liquid with a Hydrogen Sulfate Anion at 313.2 K
• Solubility of Acenaphthylene in Different Solvents between (278 and 323) K
• Binary LLE for Propyl Vinyl Ether (PVE) + Water, Ternary LLE for PVE + Methanol or Ethanol + Water at 298.15 K, and VE and centsR at 293.15 K for the Mixture of PVE + Ethanol + 2,2,4-Trimethylpentane
• Vapor Liquid Equilibrium for Butane + Methanol, + Ethanol, + 2-Propanol, + 2-Butanol, and + 2-Methyl-2-Propanol (TBA) at 323 K
• Solubility of Imidacloprid in Different Solvents
• Solubilities of 2-(6-Oxido-6H-dibenz[c,e][1,2]oxaphosphorin-6-yl)-1,4-dihydroxy Phenylene in the Selected Solvents
• Experimental Determination of Solubilities of Betulin in Acetone + Water and Ethanol + Water Mixed Solvents at T ) (278.2, 288.2, 298.2, 308.2, and 318.2) K
• Solubility of 2-(4-Ethylbenzoyl)benzoic Acid in Eleven Organic Solvents between 279.55 K and 343.15 K
• Volumetric Properties and Viscosities of Binary Mixtures of N,N-Dimethylformamide with Methanol and Ethanol in the Temperature Range (293.15 to 333.15) K
• Investigations of the (p, G, T) Properties and Apparent Molar Volumes VO of the LiCl + C2H5OH Solutions
• Solubility of Dioxopromethazine Hydrochloride in Different Solvents
• Excess Enthalpies of 2,4-Pentanedione + (Methanol, + Ethanol, + 1-Propanol, and + 2-Propanol) at T = (298.15, 313.15, and 328.15) K and p = (0.1 and 10.0) MPa
• Solubility of Salicylic Acid in Water, Ethanol, Carbon Tetrachloride, Ethyl Acetate, and Xylene
• Solubility of Trimethoprim (TMP) in Different Organic Solvents from (278 to 333) K
• Naphthalene Solubility in Binary Solvent Mixtures of 2,2,4-Trimethylpentane + Alcohols at 298.15 K
• Densities and Excess Molar Volumes of N-Methylmorpholine + 1-Alkanol Systems at 298.15 K
• Separation of Ethyl Acetate and Ethanol by Room Temperature Ionic Liquids with the Tetrafluoroborate Anion
• Densities, Refractive Indices, and Viscosities of the Ionic Liquids 1-Methyl-3-octylimidazolium Tetrafluoroborate and 1-Methyl-3-butylimidazolium Perchlorate and Their Binary Mixtures with Ethanol at Several Temperatures
• Solubility of Sebacic Acid in Binary Water + Ethanol Solvent Mixtures
• Diffusion Coefficients of Organic Compounds at Infinite Dilution in Mixtures Involving Associating Compounds. Experimental Determination and Modeling by Group Contribution Methods
• Liquid Liquid Equilibria of the Ternary Systems 3-Methyl-1-butanol + Ethanol + Water and 2-Methyl-1-propanol + Ethanol + Water at 293.15 K
• Activity Coefficients at Infinite Dilution of Polar Solutes in 1-Butyl-3-methylimidazolium Trifluoromethanesulfonate Using Gas Liquid Chromatography
• Solubility of Acetylsalicylic Acid in Ethanol, Acetone, Propylene Glycol, and 2-Propanol
• Liquid Liquid Equilibrium for Ternary Systems of Propyl Vinyl Ether + C3 or C4 Alcohols + Water at 298.15 K and Excess Molar Enthalpies for Ternary and Constituent Binary Systems of Propyl Vinyl Ether + Ethanol + Isooctane at 303.15 K
• Viscosities and Volumetric Properties of Binary and Ternary Mixtures of Tris(2-hydroxyethyl) Methylammonium Methylsulfate + Water + Ethanol at 298.15 K
• Solubility of Irbesartan Form B in an Aqueous Ethanol Mixture
• Solubility of Gallic Acid in Methanol, Ethanol, Water, and Ethyl Acetate
• Solubility of p-Methylbenzene Sulfonic Acid in Pure and Modified Supercritical Carbon Dioxide
• Activity Coefficients at Infinite Dilution of Polar Solutes in 1-Propyl-2,3-dimethylimidazolium Tetrafluoroborate Using Gas Liquid Chromatography
• Surface Tension of Binary Mixtures of N-Methyldiethanolamine and Triethanolamine with Ethanol
• Solubilities of Stearic Acid in Organic Solvents and in Azeotropic Solvent Mixtures
• Excess Molar Enthalpies of Acetophenone + (Methanol, + Ethanol, + 1-Propanol, and + 2-Propanol) at Different Temperatures and Pressures
• Solubilities of Adefovir Dipivoxil in Different Binary Solvents at 298.15 K
• Vapor Liquid Equilibria for the Ternary System Ethanol + Water + 1-Ethyl-3-methylimidazolium Ethylsulfate and the Corresponding Binary Systems Containing the Ionic Liquid at 101.3 kPa
• Solubility of Acesulfame Potassium in Ethanol + Water and Methanol + Water Systems from (275.84 to 322.90) K
• Solubility of Losartan Potassium in Different Pure Solvents from (293.15 to 343.15) K
• Liquid-Liquid Equilibrium for 2,2,2-Trifluoroethanol + Ethanol + Cyclohexane from (288.15 to 308.15) K
• Solubility of Rifapentine in Different Organic Solvents
• Densities and Excess Enthalpies for Ionic Liquids + Ethanol or + Nitromethane
• Vapor Liquid Equilibrium Behaviors of 5-Methyl-2-(1-methylethyl)phenol in Alcohol
• Measurements and Correlation of Liquid Liquid Equilibria of (Water + Ethanol + Dimethyl Carbonate + 2,2,4-Trimethylpentane or n-Heptane) and (Water + Dimethyl Carbonate + n-Heptane + Toluene)
• Solubilities of Menadione Sodium Bisulfite in Water + (Methanol, Ethanol, 1-Propanol, 2-Propanol, 1,2-Propanediol, and Glycerin, Respectively) from (297.67 to 337.76) K
• Setup and Validation of a PGT Measuring Device. Volumetric Behavior of the Mixture 1,8-Cineole + Ethanol
• Solubilities of Diphenylphosphinic Acid in Selected Solvents
• solubility of L-(+)-ascorbic acid in water, ethanol, methanol, propan-2-ol, acetone, acetonitrile, ethyl acetate, and tetrahydrofuran from (293 to 323) K
• Solubility of Hesperetin in Various Solvents from (288.2 to 323.2) K
• Solid-Liquid Phase Equilibrium and Phase Diagram for the Ternary o-Nitrobenzoic Acid + m-Nitrobenzoic Acid + Ethanol System
• Liquid-Liquid Phase Equilibria of the System Ethanol (1) + Water (2) + Tripotassium Citrate (3)
• Determination of Activity Coefficients at Infinite Dilution of Solutes in the Ionic Liquid, Trihexyltetradecylphosphonium Bis(trifluoromethylsulfonyl) Imide, Using Gas-Liquid Chromatography at T ) (303.15, 308.15, 313.15, and 318.15) K
• Isobaric Vapor-Liquid Equilibria for Tetrahydropyran and Alcohol Systems
• Density, Viscosity, and Electrical Conductivity Measurements on the Ternary System H2O + C2H5OH + LiCl over the Entire Ranges of Solvent Composition and LiCl Solubility from (-5 to +50) deg C
• Solubility of Isoniazid in Various Organic Solvents from (301 to 313) K
• Synthesis and Physical Properties of 1-Ethyl 3-methylpyridinium Ethylsulfate and Its Binary Mixtures with Ethanol and Water at Several Temperatures
• Solubility of 11 -Hydroxypregna-1,4,16-triene-3,20-dione in Different Solvents
• Isobaric Vapor-Liquid Equilibrium for Ethyl Acetate + Ethanol + 1-Ethyl-3-methylimidazolium Tetrafluoroborate
• Solubility of Pravastatin Sodium in Water, Methanol, Ethanol, 2-Propanol, 1-Propanol, and 1-Butanol from (278 to 333) K
• Diffusion of Benzonitrile in CO2-Expanded Ethanol
• Solubility of Carbamazepine (Form III) in Different Solvents from (275 to 343) K
• High Temperature and High Pressure Volumetric (Density and Apparent Molar Volumes) Properties of (CaCl2 + C2H5OH) Solutions
• Solubility of 1,6,6-Trimethyl-6,7,8,9-tetrahydrophenanthro[1,2-b]furan-10,11-dione in Four Organic Solvents from (283.2 to 323.3) K
• Measurement of Infinite Dilution Activity Coefficients of Alcohols, Ketones, and Aromatic Hydrocarbons in 4-Methyl-N-butylpyridinium Tetrafluoroborate and 1-Butyl-3-methylimidazolium Hexafluorophosphate by Gas-Liquid Chromatography
• Solubility of Clindamycin Phosphate in Methanol, Ethanol, and Dimethyl Sulfoxide
• Solubility of Tobramycin in Binary Water-Ethanol Solvent
• Viscosities and Densities of Binary Mixtures of (N-Acetylmorpholine + Alkanols) from (293.15 to 323.15) K
• Solubility of 1-(2-Dimethylaminoethyl)-5-mercapto-1H-tetrazole in Water, DMF, Methanol, Ethanol, 1-Propanol, 2-Propanol, 1-Butanol, and 2-Butanol between (293 and 343) K
• Excess Molar Enthalpies of N,N-Dimethylethanolamine with (Methanol, Ethanol, 1-Propanol, and 2-Propanol) at T ) (298.2, 313.2, and 328.2) K and p ) (0.1 and 10.0) MPa
• Solubility of Methane in Tetrahydrofuran + Ethanol at High Pressures
• Activity Coefficients at Infinite Dilution of Alkanols in the Ionic Liquids 1-Butyl-3-methylimidazolium Hexafluorophosphate, 1-Butyl-3-methylimidazolium Methyl Sulfate, and 1-Hexyl-3-methylimidazolium Bis(trifluoromethylsulfonyl) Amide Using the Dilutor Technique
• Solubility of C.I. Disperse Violet 1 in Supercritical Carbon Dioxide with or without Cosolvent
• Vapor-Liquid Phase Boundaries of Binary Mixtures of Carbon Dioxide with Ethanol and Acetone
• Solubilities of Polyhydroxybenzophenones in an Ethanol + Water Mixture from (293.15 to 343.15) K
• Solubilities of 1,4-Naphthoquinone in Acetone, Toluene, Xylene, Ethanol, and n-Butyl Alcohol
• Temperature Dependence on Mutual Solubility Data of the Binary (Methanol + r-Pinene or -Pinene) Systems and Ternary Liquid-Liquid Equilibria for the (Methanol + Ethanol + r-Pinene or -Pinene) Systems
• Measurement and Correlation of Solubilities of trans-Resveratrol in Ethanol + Water and Acetone + Water Mixed Solvents at Different Temperatures
• Solubility of the Antimicrobial Agent Triclosan in Organic Solvents of Different Hydrogen Bonding Capabilities at Several Temperatures
• Binary Liquid-Liquid Equilibrium (LLE) for Dibutyl Ether (DBE) + Water from (288.15 to 318.15) K and Ternary LLE for Systems of DBE + C1 !less thanless than C4 Alcohols + Water at 298.15 K
• Physical Properties (Density, Excess Molar Volume, Viscosity, Surface Tension, and Refractive Index) of Ethanol + Glycerol
• Solubilities of Salicylic Acid in Pure Solvents and Binary Mixtures Containing Cosolvent
• Liquid-Liquid Equilibrium of Ternary Mixtures Formed by Some Oligooxaethylenes with Ethanol and Hexadecane
• Solubility of D(-)-p-Hydroxyphenylglycine Dane Salt in Eight Alcohols between (293 and 343) K
• Solubility of Benzoic Acid in Aqueous Solutions Containing Ethanol or N-Propanol
• Isothermal Vapor-Liquid Equilibrium of Binary Mixtures Containing 1-Chlorobutane, Ethanol, or Acetonitrile
• Solubility of Bis(benzoxazolyl-2-methyl) Sulfide in Different Pure Solvents and Ethanol + Water Binary Mixtures between (273.25 and 325.25) K
• Solubilities of Dodecanoic and Tetradecanoic Acids in Supercritical CO2 with and without Entrainers
• Isobaric Vapor-Liquid and Liquid-Liquid Equilibria for Chloroform + Ethanol + 1-Ethyl-3-methylimidazolium Trifluoromethanesulfonate at 100 kPa
• Solubility of Sebacic Acid in Binary Mixtures Containing Alcohols
• Solubility of Diphenyl Carbonate in Pure Alcohols from (283 to 333) K
• Solubilities of Palmitic Acid in Pure Solvents and Its Mixtures
• Solubility of Ethyl Maltol in Aqueous Ethanol Mixtures
• Solubility of Desmosterol in Five Organic Solvents
• Solubilities of 1-Ethylpyridinium Hexafluorophosphate in Ethanol + Water from (278.15 to 345.15) K
• Solubility of Ammonium Thiocyanate in Different Solvents
• Densities, Excess Molar Volumes, Viscosity, and Refractive Indices of Binary and Ternary Liquid Mixtures of Methanol (1) + Ethanol (2) + 1,2-Propanediol (3) at P = 81.5 kPa
• Solubility of 1,5-Diaminobromo-4,8-dihydroxyanthraquinone in Supercritical Carbon Dioxide with or without Cosolvent
• Activity Coefficients at Infinite Dilution of Organic Compounds in 1-Butyl-3-methylimidazolium Tetrafluoroborate Using Inverse Gas Chromatography
• Solubility of Hexamethylenetetramine in a Pure Water, Methanol, Acetic Acid, and Ethanol + Water Mixture from (299.38 to 340.35) K
• Solubility of Salol in Pure Alcohols from (283.15 to 308.15) K
• Binary Liquid-Liquid Equilibrium (LLE) for Methyl tert-Amyl Ether (TAME) + Water from (288.15 to 313.15) K and Ternary LLE for Systems of TAME + C1-C4 Alcohols + Water at 298.15 K
• Solubility and Density of Potassium Iodide in Binary Ethanol-Water Solvent Mixture at (298.15, 303.15, 308.15, and 313.15) K
• Solubility of Indinavir Sulfate in Different Solvents from (278.35 to 314.15) K
• Solubility of Podophyllotoxin in Six Organic Solvents from (283.2 to 323.2) K
• Solubility of Chloroquine Diphosphate and 4,7-Dichloroquinoline in Water, Ethanol, Tetrahydrofuran, Acetonitrile, and Acetone from (298.2 to 333.2) K
• Solubilities of Hexadecanoic and Octadecanoic Acids in Supercritical CO2 With and Without Cosolvents
• Solubility of Difloxacin in Acetone, Methanol, and Ethanol from (293.15 to 313.15) K
• Activity Coefficients at Infinite Dilution of Organic Compounds in Trihexyl(tetradecyl)phosphonium Bis(trifluoromethylsulfonyl)imide Using Inverse Gas Chromatography
• Separation of Hexane/Ethanol Mixtures. LLE of Ternary Systems (Ionic Liquid or Hyperbranched Polymer + Ethanol + Hexane) at T ) 298.15 K
• Solubility of Valsartan in Different Organic Solvents and Ethanol + Water Binary Mixtures from (278.15 to 313.15) K
• Solubility of Lamotrigine, Diazepam, and Clonazepam in Ethanol + Water Mixtures at 298.15 K
• Solubility of Deflazacort in Binary Solvent Mixtures
• Solubility of Canthaxanthin in Pure Solvents from (293.15 to 343.15) K
• Solubility of (+)-(S)-2-(6-Methoxynaphthalen-2-yl) Propanoic Acid in Acetone, Methanol, Ethanol, Propan-2-ol, and Ethyl Ethanoate at Temperatures between (278 and 320) K
• Solubility of Rutin in Ethanol + Water at (273.15 to 323.15) K
• Solubilities of Isonicotinic Acid in (Methanol, Ethanol, 1-Propanol, 2-Propanol, and 1,2-Propanediol, Respectively) from (289.65 to 358.75) K
• Temperature and Composition Dependence of the Density and Viscosity of Binary Mixtures of {1-Butyl-3-methylimidazolium Thiocyanate + 1-Alcohols}
• Vapor-Liquid Equilibria for the Ternary System Ethanol + Water + 1-Butyl-3-methylimidazolium Methylsulfate and the Corresponding Binary Systems at 101.3 kPa
• Solubility of 2-Aminopyridine in Ethanol + n-Butyl Acetate from (288.15 to 318.15) K
• Paramagnetic Ionic Liquid 1-Butyl-3-methylimidazolium Tetrabromidocobaltate(II): Activity Coefficients at Infinite Dilution of Organic Solutes and Crystal Structure
• Solubility of p-Toluenesulfonamide in Pure and Modified Supercritical Carbon Dioxide
• Physical Properties of Binary and Ternary Mixtures of Ethyl Acetate, Ethanol, and 1-Octyl-3-methyl-imidazolium Bis(trifluoromethylsulfonyl)imide at 298.15 K
• Solid-Liquid Equilibria of Nonanedioic Acid in Binary Ethanol + Water Solvent Mixtures from (292.35 to 345.52) K
• Viscosity and Density of Binary Mixtures of Ethyl Alcohol with n-Alkanes (C6, C8, and C10)
• Densities and Viscosities of Binary Mixtures of Cyclopropanecarboxylic Acid with Methanol, Ethanol, Propan-1-ol, and Butan-1-ol at Different Temperatures
• Densities and Viscosities of (1,6-Hexanediamine + Ethanol) and (1,6-Hexanediamine + Ethanol + Water) Mixtures at T ) (303.15 to 328.15) K
• Solubility of -Artemether in Methanol + Water and Ethanol + Water from (288.85 to 331.95) K
• Experimental Determination, Correlation, and Prediction of Physical Properties of the Ternary Mixtures Ethanol and 1-Propanol + Water + 1-Ethyl-3-methylpyridinium Ethylsulfate at 298.15 K
• Synthesis and Physical Properties of 1-Ethylpyridinium Ethylsulfate and its Binary Mixtures with Ethanol and 1-Propanol at Several Temperatures
• Solubility of Tobramycin in Methanol, Ethanol, Dimethyl Sulfoxide, and N,N-Dimethylformamide
• Experimental Measurement and Modeling of Vapor-Liquid Equilibrium for Ternary Systems Containing Ionic Liquids: A Case Study for the System Water + Ethanol + 1-Hexyl-3-methylimidazolium Chloride
• Solubility of Butanedioic Acid in Different Solvents at Temperatures between 283 K and 333 K
• Solubility of l-Lysine Hydrochloride in Dimethyl Sulfoxide, Methanol, Ethanol, Water, and Glycol between (283 and 323) K
• Solubility of Phenanthrene in Binary Mixtures of C1-C4 Alcohols + 2-Propanol and Ethanol + Methanol at 298.15 K
• Densities of Ionic Liquid [BMIM][BF4] + Ethanol, + Benzene, and + Acetonitrile at Different Temperature and Pressure
• Solubility and Liquid-Liquid Equilibrium of Aqueous Systems of Iodoethane with Methanol, Ethanol, or 1-Propanol at Temperature 298.15 K and Pressure 101.2 kPa
• Density, Speed of Sound, and Isentropic Compressibility of Triethanolamine (or N-Methyldiethanolamine) + Water + Ethanol Solutions from t = (15 to 50) deg C
• Volumetric Properties of Carbon Dioxide + Ethanol at 313.15 K
• Isothermal Vapor-Liquid Equilibrium at 333.15 K and Excess Molar Volumes, Refractive Indices, and Excess Molar Enthalpies at 303.15 K for the Binary and Ternary Mixtures of Di-isopropyl Ether, Ethanol, and 2,2,4-Trimethylpentane
• Trans-Cinnamic Acid Solubility Enhancement in the Presence of Ethanol As a Supercritical CO2 Cosolvent
• Solubility of Fumaric Acid in Propan-2-ol, Ethanol, Acetone, Propan-1-ol, and Water
• Solubility of Baicalin in Methanol, Ethanol, and Ethyl Acetate from (298.2 to 328.2) K
• Solubility of Thiotriazinone in Ethanol, 1-Propanol, 2-Propanol, 1-Butanol, Acetonitrile, Acetone, Ethyl Acetate, and Water from 293 K to 343 K
• Solubility of 3,5-Dimethoxybenzoic Acid, 4-Cyanobenzoic Acid, 4-Acetoxybenzoic Acid, 3,5-Diaminobenzoic Acid, and 2,4-Dichlorobenzoic Acid in Ethanol
• Solubility of Chlordiazepoxide, Diazepam, and Lorazepam in Ethanol + Water Mixtures at 303.2 K
• Measurement and Correlation of Vapor-Liquid Equilibrium for the Carbon Dioxide + 1-Butoxy Butane System
• Refractive Indices of Lithium, Magnesium, and Copper(II) Sulfates in Ethanol-Water Solutions
• Solution Thermodynamics of Ketoprofen in Ethanol + Water Cosolvent Mixtures
• Partition Coefficients of Organic Compounds in New Imidazolium and Tetralkylammonium Based Ionic Liquids Using Inverse Gas Chromatography
• Solubilities of 3-Pentadecylphenol in Ethanol, 1-Butanol, Toluene, Acetone, Tetrachloromethane, and Ethyl Acetate
• Solid-Liquid Equilibrium and Phase Diagram for the Ternary p-Nitrobenzoic Acid + m-Nitrobenzoic Acid + Ethanol System
• Solubility of 2,6-Diamino-3,5-dinitropyridine and 2,5-Dihydroxyterephthalic Acid in N,N-Dimethylformamide, Dimethylsulfoxide, Ethanol, and Methanol, N,N-Dimethylacetamide, and Acetic Acid
• Solubility of Budesonide, Hydrocortisone, and Prednisolone in Ethanol + Water Mixtures at 298.2 K
• Excess Molar Enthalpies of Diethyl Malonate + (Methanol, + Ethanol, + 1-Propanol, and + 2-Propanol) at T = (288.2, 298.2, 313.2, and 328.2) K and p = 101.3 kPa
• Solubility of Luteolin in Ethanol + Water Mixed Solvents at Different Temperatures
• Vapor-Liquid Equilibria and Interfacial Tensions of the System Ethanol + 2-Methoxy-2-methylpropane
• Densities, Excess Volumes, Isobaric Expansivities, and Isothermal Compressibilities of the 1-Ethyl-3-methylimidazolium Ethylsulfate + Ethanol System at Temperatures (283.15 to 343.15) K and Pressures from (0.1 to 35) MPa
• Solubilities of 3,9-Dimethyl-3,9-dioxide-2,4,8,10-tetraoxa-3,9-diphosphaspiro[5.5]undecane in Selected Solvents
• Solubility of Irganox 1010 in (Alcohol + Water) Mixtures from (293.15 to 333.15) K
• Solubility of Adenosine 5'-Monophosphate in Different Solvents from (288.15 to 330.15) K
• Solubility of Cytidine 5'-Diphosphocholine Sodium in Water and Different Binary Mixtures from (278.15 to 298.15) K
• Isobaric Vapor-Liquid Equilibria for Binary and Ternary Mixtures of Ethanol and 2-Propanol with 2-Butanone and Butyl Propionate at 101.3 kPa
• Isothermal Vapor-Liquid Equilibrium at 333.15 K and Excess Volumes and Molar Refractivity Deviation at 298.15 K for Binary System Dibutyl Ether (DBE) + 2,2,4-Trimethylpentane and for Ternary System DBE + Ethanol + 2,2,4-Trimethylpentane
• Phase Diagrams of Ammonium Sulfate + Ethanol/1-Propanol/2-Propanol + Water Aqueous Two-Phase Systems at 298.15 K and Correlation
• Density and Viscosity of (2,2-Dichloro-N,N-di-2-propenylacetamide + Acetone) and (2,2-Dichloro-N,N-di-2-propenylacetamide + Ethanol) at T = (278.15 to 313.15) K
• Density and Excess Molar Volume for Binary Mixtures of Naphthenic Acid Ionic Liquids and Ethanol
• Experimental Measurement and Correlation of the Solubilities of 2,4-Dichloro-5-methoxypyrimidine in Ethyl Ethanoate, Methanol, Ethanol, Acetone, Tetrachloromethane, and Heptane at Temperatures between (295 and 320) K
• Solubility of Phenanthrene in Binary Mixtures of C1-C4 Alcohols at 298.2 K
• Refractive Indices and Deviations in Refractive Indices for Binary Mixtures of 1-Ethyl-3-methylimidazolium Trifluoromethanesulfonate with Methanol, Ethanol, 1-Propanol, and 2-Propanol at Several Temperatures
• Solubilities of N-[(4-Bromo-3,5-difluorine)phenyl]acrylamide in Benzene, Methanol, Pyridine, Ethanol, Acetonitrile, and Toluene at Temperatures between (284.65 and 348.95) K
• Measurement and Correlation of Solubility of Pimelic Acid in Ether, Tetrahydrofuran, Ethanol, and Methanol
• Solubility of 5-Amino Salicylic Acid in Different Solvents at Various Temperatures
• Solubility of Vitamin C in Water, Ethanol, Propan-1-ol, Water + Ethanol, and Water + Propan-1-ol at (298.15 and 308.15) K
• Activity Coefficients at Infinite Dilution of Polar Solutes in 1-(2-Hydroxyethyl)-3-methylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
• Henry s Law Constants of Organic Compounds in Water and n-Octane at T = 293.2 K
• Using 1-Ethyl-3-methylimidazolium Trifluoromethanesulfonate as an Entrainer for the Extractive Distillation of Ethanol + Water Mixtures
• Experimental Measurement and Modeling of Vapor-Liquid Equilibrium for the Ternary System Water + Ethanol + 1-Butyl-3-methylimidazolium Chloride
• Levulinic Acid Solubility in Supercritical Carbon Dioxide with and without Ethanol as Cosolvent at Different Temperatures
• Solubilities of (2,5-Dihydroxyphenyl)diphenyl Phosphine Oxide in Selected Solvents
• Measurement and Correlation of Phase Diagram Data for Several Hydrophilic Alcohol + Citrate Aqueous Two-Phase Systems at 298.15 K
• Solubilities of Sulfadiazine in Methanol, Ethanol, 1-Propanol, 2-Propanol, Acetone, and Chloroform from (294.15 to 318.15) K
• Densities and Viscosities of 1,1'-(Pentane-1,5-diyl)-bis(pyridinium) Dibromide in Ethanol + Water from (293.15 to 344.15) K
• Dissociation Constant of Quinic Acid and Association Constants of Some Quinates in Aqueous and in Alcoholic-Aqueous Mixed Solvents
• Solubility of N-(Phosphonomethyl)iminodiacetic Acid in Different Binary Mixtures
• Solubility of Avermectin B1a in Some Pure and Mixed Solvents from (278.2 to 318.2) K
• Effect of Diaminomethanal on the Vapor-Liquid Equilibria of the Ethanol + Water System at Atmospheric Pressure
• Solubilities of (?,Z)-2-Amino-?-(methoxyimino)-4-thiazole-ethanethioic Acid S-2-Benzothiazolyl Ester in Pure Solvents and a Mixture of Acetonitrile and Dichloromethane
• Solubility of 5-Amino-N,N?-bis(2,3-dihydroxypropyl)-2,4,6-triiodobenzene-1,3-dicarboxamide in Ethanol + Water Mixtures
• Density of Carbon Dioxide Expanded Ethanol at (313.2, 328.2, and 343.2) K
• Study of Ether-, Alcohol-, or Cyano-Functionalized Ionic Liquids Using Inverse Gas Chromatography
• Solubility of Sucralose in Different Solvents from (283.15 to 333.15) K
• Activity Coefficients at Infinite Dilution of Organic Solutes in 1-Ethyl-3-methylimidazolium Tris(pentafluoroethyl)trifluorophosphate [EMIM][FAP] Using Gas-Liquid Chromatography
• Solubility of Delphinidin in Water and Various Organic Solvents between (298.15 and 343.15) K
• Apparent Molar Volume and Compressibility of Tetrabutylphosphonium Bromide in Various Solvents
• Activity Coefficients at Infinite Dilution Measurements for Organic Solutes and Water in the Ionic Liquid 1-Hexyl-3-methylimidazolium Thiocyanate
• Thermodynamic Study of the Solubility of Procaine HCl in Some Ethanol + Water Cosolvent Mixtures
• Determination and Correlation of the Solubility for Taurine in Water and Organic Solvent Systems
• ss-Sitosterol Solubility in Selected Organic Solvents
• Experimental Vapor-Liquid Equilibria for the Ternary System Ethanol + Water + 1-Ethyl-3-methylpyridinium Ethylsulfate and the Corresponding Binary Systems at 101.3 kPa: Study of the Effect of the Cation
• Solubility of Glyphosate in Ethanol + Water, 1-Propanol + Water, and 2-Propanol + Water from (293 to 333) K
• Refractive Indices of Sodium, Potassium, and Ammonium Sulfates in Ethanol-Water Solutions
• Measurement and Modeling of Epigallocatechin Gallate Solubility in Supercritical Carbon Dioxide Fluid with Ethanol Cosolvent
• Densities and Viscosities of Pure 1-Methyl-3-octylimidazolium Nitrate and Its Binary Mixtures with Alcohols at Several Temperatures
• Solubility of Quercetin in Water + Methanol and Water + Ethanol from (292.8 to 333.8) K
• Densities, Speeds of Sound, and Isentropic Compressibilities for Binary Mixtures of 1,2-Ethanediol with 2-Ethyl-1-hexanol, 1-Heptanol, or Ethanol at the Temperature 298.15 K and Densities for Mixtures of 1,2-Ethanediol with 1-Nonanol at the Temperatures (293.15 and 298.15) K
• Joback Method
• KDB
• Aqueous Solubility Prediction Method
• Estimated Solubility Method
• McGowan Method
• NIST Webbook
• The Yaws Handbook of Vapor Pressure

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