Chemical Properties of Methyl Alcohol (CAS 67-56-1)

InChI

InChI=1S/CH4O/c1-2/h2H,1H3

InChI Key

OKKJLVBELUTLKV-UHFFFAOYSA-N

Formula

CH4O

SMILES

CO

Molecular Weight¹

32.04

CAS

67-56-1

Other Names

• Alcool methylique
• Alcool metilico
• Bieleski's solution
• CARBINOL
• CH3OH
• Colonial spirit
• Columbian spirit
• Columbian spirits
• Hydroxymethane
• METHANOL
• METHYLHYDROXIDE
• Metanolo
• Methyl hydroxide
• Methylalkohol
• Methylol
• Metylowy alkohol
• Monohydroxymethane
• NSC 85232
• Pyro alcohol
• Pyroxylic spirit
• Rcra waste number U154
• Spirit of wood
• UN 1230
• Wood alcohol
• Wood naphtha
• Wood spirit

• 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).
• C_p,solid : Solid phase heat capacity (J/mol×K).
• μ : Dipole Moment (debye).
• η : Dynamic viscosity (Pa×s).
• 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).
• 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.
• NFPA Health : NFPA Health 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).
• S°_{solid,1 bar} : Solid phase molar entropy at standard conditions (J/mol×K).
• 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).
• α_diff : Thermal diffusivity (m²/s).
• T_fus : Normal melting (fusion) point (K).
• T_triple : Triple Point Temperature (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	0.5560		KDB
PAff	754.30	kJ/mol	NIST
Tig	737.04	K	KDB
BasG	724.50	kJ/mol	NIST
ΔcH°gas	-763.68 ± 0.20	kJ/mol	NIST
ΔcH°liquid	[-726.50; -713.83]	kJ/mol
ΔcH°liquid	-725.70 ± 0.10	kJ/mol	NIST
ΔcH°liquid	-726.50 ± 0.20	kJ/mol	NIST
ΔcH°liquid	-726.34 ± 0.20	kJ/mol	NIST
ΔcH°liquid	-715.05	kJ/mol	NIST
ΔcH°liquid	-713.83	kJ/mol	NIST
Cp,liquid	[80.81; 81.38]	J/mol×K
Cp,liquid	81.38	J/mol×K	Molar h...
Cp,liquid	80.81	J/mol×K	THERMOD...
μ	1.70	debye	KDB
η	[0.0005482; 0.0005500]	Pa×s
η	0.0005482	Pa×s	Densiti...
η	0.0005500	Pa×s	Densiti...
LFL	6.00	% in Air	KDB
UFL	36.50	% in Air	KDB
Tflash,cc	289.26	K	KDB
Tflash,oc	285.37	K	KDB
ΔfG°	-162.60	kJ/mol	KDB
Rg	1.5360		KDB
ΔfH°gas	-201.30	kJ/mol	KDB
ΔfH°liquid	[-251.30; -238.40]	kJ/mol
ΔfH°liquid	-238.40	kJ/mol	NIST
ΔfH°liquid	-239.50 ± 0.20	kJ/mol	NIST
ΔfH°liquid	-238.90 ± 3.60	kJ/mol	NIST
ΔfH°liquid	-250.60	kJ/mol	NIST
ΔfH°liquid	-251.30 ± 5.00	kJ/mol	NIST
ΔfusH°	2.43	kJ/mol	Joback Calculated Property
ΔvapH°	[35.30; 38.00]	kJ/mol
ΔvapH°	37.83	kJ/mol	NIST
ΔvapH°	37.80	kJ/mol	NIST
ΔvapH°	38.00	kJ/mol	NIST
ΔvapH°	37.40 ± 0.10	kJ/mol	NIST
ΔvapH°	37.43 ± 0.02	kJ/mol	NIST
ΔvapH°	37.43 ± 0.02	kJ/mol	NIST
ΔvapH°	37.30 ± 0.10	kJ/mol	NIST
ΔvapH°	37.30 ± 0.08	kJ/mol	NIST
ΔvapH°	37.70 ± 0.10	kJ/mol	NIST
ΔvapH°	37.40 ± 0.04	kJ/mol	NIST
ΔvapH°	37.80	kJ/mol	NIST
ΔvapH°	Outlier 35.30 ± 0.04	kJ/mol	NIST
IE	[10.82; 11.00]	eV
IE	10.84 ± 0.01	eV	NIST
IE	10.85 ± 0.03	eV	NIST
IE	10.82 ± 0.05	eV	NIST
IE	10.84 ± 0.07	eV	NIST
IE	10.90	eV	NIST
IE	10.84 ± 0.08	eV	NIST
IE	10.90 ± 0.03	eV	NIST
IE	10.85 ± 0.01	eV	NIST
IE	10.85 ± 0.00	eV	NIST
IE	10.90 ± 0.12	eV	NIST
IE	10.83 ± 0.03	eV	NIST
IE	10.85 ± 0.02	eV	NIST
IE	10.85	eV	NIST
IE	10.85	eV	NIST
IE	10.83 ± 0.01	eV	NIST
IE	10.85	eV	NIST
IE	10.83	eV	NIST
IE	10.84 ± 0.02	eV	NIST
IE	10.85	eV	NIST
IE	10.83	eV	NIST
IE	10.85 ± 0.02	eV	NIST
IE	10.96	eV	NIST
IE	Outlier 11.00	eV	NIST
IE	10.95	eV	NIST
IE	10.95	eV	NIST
IE	10.86	eV	NIST
IE	10.97 ± 0.03	eV	NIST
IE	10.96	eV	NIST
IE	10.95	eV	NIST
IE	10.94	eV	NIST
IE	10.95	eV	NIST
IE	10.96	eV	NIST
log10WS	[1.57; 1.57]
log10WS	1.57		Aq. Sol...
log10WS	1.57		Estimat...
logPoct/wat	-0.391		Crippen Calculated Property
McVol	30.820	ml/mol	McGowan Calculated Property
NFPA Fire	3		KDB
NFPA Health	1		KDB
Pc	[8084.00; 8120.00]	kPa
Pc	8084.00	kPa	KDB
Pc	8120.00	kPa	Critica...
Inp	[330.00; 408.00]
Inp	340.00		NIST
Inp	384.00		NIST
Inp	356.00		NIST
Inp	336.00		NIST
Inp	373.00		NIST
Inp	355.00		NIST
Inp	Outlier 330.00		NIST
Inp	380.00		NIST
Inp	372.70		NIST
Inp	378.20		NIST
Inp	400.00		NIST
Inp	400.00		NIST
Inp	361.00		NIST
Inp	368.00		NIST
Inp	382.00		NIST
Inp	338.00		NIST
Inp	370.00		NIST
Inp	348.00		NIST
Inp	395.00		NIST
Inp	379.00		NIST
Inp	367.50		NIST
Inp	381.00		NIST
Inp	370.00		NIST
Inp	353.50		NIST
Inp	381.00		NIST
Inp	373.00		NIST
Inp	373.00		NIST
Inp	408.00		NIST
Inp	373.00		NIST
Inp	362.00		NIST
Inp	381.00		NIST
Inp	381.00		NIST
Inp	381.00		NIST
Inp	353.00		NIST
Inp	381.00		NIST
Inp	381.00		NIST
Inp	348.00		NIST
Inp	353.00		NIST
Inp	391.00		NIST
Inp	404.00		NIST
Inp	384.00		NIST
Inp	382.00		NIST
Inp	380.00		NIST
Inp	381.00		NIST
Inp	362.00		NIST
Inp	404.00		NIST
I	[860.00; 921.00]
I	917.00		NIST
I	891.00		NIST
I	Outlier 860.00		NIST
I	881.00		NIST
I	892.00		NIST
I	904.00		NIST
I	897.00		NIST
I	886.00		NIST
I	914.00		NIST
I	899.00		NIST
I	888.00		NIST
I	Outlier 869.00		NIST
I	910.40		NIST
I	916.00		NIST
I	Outlier 866.00		NIST
I	892.00		NIST
I	899.00		NIST
I	895.00		NIST
I	921.00		NIST
I	911.00		NIST
I	907.00		NIST
I	911.00		NIST
I	903.00		NIST
I	905.00		NIST
I	898.00		NIST
I	905.00		NIST
I	920.00		NIST
I	897.00		NIST
I	909.00		NIST
I	907.00		NIST
I	920.00		NIST
I	883.00		NIST
I	910.40		NIST
I	899.00		NIST
S°liquid	[126.80; 136.40]	J/mol×K
S°liquid	127.19	J/mol×K	NIST
S°liquid	126.80	J/mol×K	NIST
S°liquid	129.70	J/mol×K	NIST
S°liquid	136.40	J/mol×K	NIST
S°solid,1 bar	1.12	J/mol×K	NIST
Tboil	[337.45; 363.41]	K
Tboil	337.70	K	KDB
Tboil	337.50	K	Isobari...
Tboil	337.50	K	Isobari...
Tboil	337.75	K	Isobari...
Tboil	337.70	K	Isobari...
Tboil	337.86	K	Isobari...
Tboil	337.83	K	Experim...
Tboil	337.85	K	Measure...
Tboil	337.65	K	Isobari...
Tboil	337.65	K	Isobari...
Tboil	Outlier 363.41	K	Measure...
Tboil	337.65	K	Isobari...
Tboil	337.45	K	Measure...
Tboil	337.68	K	Experim...
Tboil	337.78	K	A new a...
Tboil	337.68	K	Isobari...
Tboil	337.85	K	Vapor L...
Tboil	337.85	K	Measure...
Tboil	337.45	K	Effect ...
Tboil	337.83	K	Isobari...
Tboil	337.68	K	Determi...
Tboil	337.83	K	Isobari...
Tboil	337.69	K	Isobari...
Tboil	337.83	K	Isobari...
Tboil	337.69	K	Vapor-L...
Tboil	337.62	K	Measure...
Tboil	337.67	K	Vapor-L...
Tboil	337.90	K	Vapor-L...
Tboil	337.75	K	Isobari...
Tboil	337.67	K	Vapor-L...
Tboil	337.57	K	Vapor-L...
Tboil	337.65	K	Isother...
Tboil	337.84	K	Organic...
Tboil	337.85	K	Isobari...
Tboil	337.84	K	Organic...
Tboil	337.85	K	Vapor L...
Tboil	337.75	K	Vapor L...
Tboil	337.82	K	Isobari...
Tboil	337.65	K	Experim...
Tboil	337.64	K	Vapor L...
Tboil	337.80	K	Effect ...
Tc	[505.20; 536.00]	K
Tc	512.50	K	KDB
Tc	512.30	K	Measure...
Tc	512.30	K	Measure...
Tc	512.50 ± 0.20	K	NIST
Tc	512.50	K	NIST
Tc	512.64	K	NIST
Tc	512.47 ± 0.10	K	NIST
Tc	512.50	K	NIST
Tc	512.64	K	NIST
Tc	512.60	K	NIST
Tc	512.50 ± 1.00	K	NIST
Tc	512.36 ± 0.15	K	NIST
Tc	512.36 ± 0.20	K	NIST
Tc	512.36 ± 0.20	K	NIST
Tc	514.70	K	NIST
Tc	512.65 ± 0.30	K	NIST
Tc	513.00	K	NIST
Tc	512.68	K	NIST
Tc	513.15 ± 2.77	K	NIST
Tc	513.90	K	NIST
Tc	513.20	K	NIST
Tc	505.20	K	NIST
Tc	512.60	K	NIST
Tc	513.80	K	NIST
Tc	513.20	K	NIST
Tc	513.20	K	NIST
Tc	513.40 ± 0.50	K	NIST
Tc	514.35 ± 1.00	K	NIST
Tc	515.20	K	NIST
Tc	513.40	K	NIST
Tc	Outlier 536.00	K	NIST
Tc	513.20	K	NIST
Tc	506.20	K	NIST
Tc	505.90	K	NIST
Tfus	[175.15; 175.47]	K
Tfus	175.47	K	KDB
Tfus	175.25	K	Aq. Sol...
Tfus	175.15	K	Solid-l...
Ttriple	[175.22; 176.00]	K
Ttriple	175.59	K	KDB
Ttriple	175.61 ± 0.05	K	NIST
Ttriple	175.59 ± 0.02	K	NIST
Ttriple	175.60 ± 0.10	K	NIST
Ttriple	175.37 ± 0.08	K	NIST
Ttriple	175.67 ± 0.20	K	NIST
Ttriple	175.22 ± 0.10	K	NIST
Ttriple	Outlier 176.00 ± 1.00	K	NIST
Ttriple	175.30 ± 0.10	K	NIST
Vc	[0.113; 0.118]	m3/kmol
Vc	0.117	m3/kmol	KDB
Vc	0.117	m3/kmol	NIST
Vc	0.113	m3/kmol	NIST
Vc	0.118 ± 0.004	m3/kmol	NIST
Vc	0.117 ± 0.004	m3/kmol	NIST
Zc	0.2219640		KDB
Zra	0.24		KDB

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[42.40; 66.80]	J/mol×K	[279.00; 585.35]
Cp,gas	42.40 ± 1.30	J/mol×K	279.00	NIST
Cp,gas	48.00 ± 1.30	J/mol×K	345.60	NIST
Cp,gas	46.80 ± 1.20	J/mol×K	347.35	NIST
Cp,gas	46.10 ± 1.30	J/mol×K	349.65	NIST
Cp,gas	47.60 ± 1.20	J/mol×K	356.55	NIST
Cp,gas	46.70 ± 1.30	J/mol×K	358.15	NIST
Cp,gas	48.20 ± 1.30	J/mol×K	358.85	NIST
Cp,gas	48.80 ± 1.30	J/mol×K	359.85	NIST
Cp,gas	50.30 ± 1.30	J/mol×K	368.15	NIST
Cp,gas	49.00 ± 1.20	J/mol×K	373.35	NIST
Cp,gas	51.30 ± 1.30	J/mol×K	382.15	NIST
Cp,gas	51.10 ± 1.20	J/mol×K	398.95	NIST
Cp,gas	52.30 ± 1.30	J/mol×K	401.15	NIST
Cp,gas	51.30 ± 1.20	J/mol×K	401.35	NIST
Cp,gas	52.01 ± 0.42	J/mol×K	403.20	NIST
Cp,gas	53.20 ± 1.30	J/mol×K	420.15	NIST
Cp,gas	53.90 ± 1.20	J/mol×K	431.45	NIST
Cp,gas	54.80 ± 1.20	J/mol×K	442.15	NIST
Cp,gas	55.90 ± 1.30	J/mol×K	442.65	NIST
Cp,gas	56.00 ± 1.20	J/mol×K	457.35	NIST
Cp,gas	57.20 ± 0.42	J/mol×K	464.00	NIST
Cp,gas	57.80 ± 1.20	J/mol×K	477.75	NIST
Cp,gas	58.40 ± 1.20	J/mol×K	485.05	NIST
Cp,gas	59.50 ± 1.20	J/mol×K	498.95	NIST
Cp,gas	60.40 ± 1.30	J/mol×K	521.20	NIST
Cp,gas	61.40 ± 1.20	J/mol×K	521.35	NIST
Cp,gas	64.30 ± 1.20	J/mol×K	555.95	NIST
Cp,gas	66.40 ± 1.20	J/mol×K	581.35	NIST
Cp,gas	66.80 ± 1.20	J/mol×K	585.35	NIST
Cp,liquid	[75.77; 206.35]	J/mol×K	[270.00; 512.78]
Cp,liquid	78.20	J/mol×K	270.00	NIST
Cp,liquid	75.77	J/mol×K	270.00	NIST
Cp,liquid	78.60	J/mol×K	283.15	Heat ca...
Cp,liquid	79.50	J/mol×K	288.15	Heat ca...
Cp,liquid	78.90	J/mol×K	288.15	NIST
Cp,liquid	79.90	J/mol×K	290.10	NIST
Cp,liquid	79.90	J/mol×K	292.00	NIST
Cp,liquid	80.80	J/mol×K	293.15	NIST
Cp,liquid	80.40	J/mol×K	293.15	Heat ca...
Cp,liquid	83.70	J/mol×K	298.00	NIST
Cp,liquid	83.30	J/mol×K	298.00	NIST
Cp,liquid	81.32	J/mol×K	298.00	NIST
Cp,liquid	81.13	J/mol×K	298.15	NIST
Cp,liquid	81.00	J/mol×K	298.15	NIST
Cp,liquid	81.17	J/mol×K	298.15	Thermod...
Cp,liquid	81.92	J/mol×K	298.15	NIST
Cp,liquid	81.30	J/mol×K	298.15	Heat ca...
Cp,liquid	81.47	J/mol×K	298.15	NIST
Cp,liquid	80.35	J/mol×K	298.15	NIST
Cp,liquid	81.56	J/mol×K	298.15	NIST
Cp,liquid	79.50	J/mol×K	298.15	NIST
Cp,liquid	81.11	J/mol×K	298.15	NIST
Cp,liquid	80.24	J/mol×K	298.15	NIST
Cp,liquid	80.22	J/mol×K	298.15	NIST
Cp,liquid	80.28	J/mol×K	298.15	NIST
Cp,liquid	85.80	J/mol×K	298.20	NIST
Cp,liquid	86.60	J/mol×K	300.80	NIST
Cp,liquid	82.30	J/mol×K	303.15	Heat ca...
Cp,liquid	83.40	J/mol×K	308.15	Heat ca...
Cp,liquid	83.01	J/mol×K	308.15	Thermod...
Cp,liquid	80.80	J/mol×K	311.00	NIST
Cp,liquid	84.50	J/mol×K	313.15	Heat ca...
Cp,liquid	83.56	J/mol×K	313.15	NIST
Cp,liquid	85.80	J/mol×K	313.20	NIST
Cp,liquid	85.70	J/mol×K	318.15	Heat ca...
Cp,liquid	85.51	J/mol×K	318.15	Thermod...
Cp,liquid	86.20	J/mol×K	323.00	NIST
Cp,liquid	87.00	J/mol×K	323.15	Heat ca...
Cp,liquid	88.64	J/mol×K	328.15	Thermod...
Cp,liquid	92.43	J/mol×K	338.15	Thermod...
Cp,liquid	96.88	J/mol×K	348.15	Thermod...
Cp,liquid	166.94	J/mol×K	512.35	Thermod...
Cp,liquid	184.24	J/mol×K	512.73	Thermod...
Cp,liquid	194.49	J/mol×K	512.77	Thermod...
Cp,liquid	202.18	J/mol×K	512.78	Thermod...
Cp,liquid	206.35	J/mol×K	512.78	Thermod...
Cp,solid	[5.40; 105.00]	J/mol×K	[20.50; 173.00]
Cp,solid	5.40	J/mol×K	20.50	NIST
Cp,solid	68.39	J/mol×K	120.00	NIST
Cp,solid	105.00	J/mol×K	173.00	NIST
η	[0.0003450; 0.0008699]	Pa×s	[278.15; 333.85]
η	0.0007418	Pa×s	278.15	Density...
η	0.0006890	Pa×s	283.15	Density...
η	0.0006781	Pa×s	283.15	Excess ...
η	0.0006315	Pa×s	288.15	Excess ...
η	0.0006410	Pa×s	288.15	Density...
η	0.0005910	Pa×s	293.00	Thermop...
η	0.0005930	Pa×s	293.15	Viscosi...
η	0.0005884	Pa×s	293.15	Excess ...
η	0.0005820	Pa×s	293.15	Densiti...
η	0.0005880	Pa×s	293.15	Propert...
η	0.0005770	Pa×s	293.15	Density...
η	0.0005850	Pa×s	293.15	Density...
η	0.0005870	Pa×s	293.15	Volumet...
η	0.0005810	Pa×s	293.15	Dynamic...
η	0.0005833	Pa×s	293.15	Viscosi...
η	0.0005950	Pa×s	293.15	Densiti...
η	0.0005676	Pa×s	293.15	Viscosi...
η	0.0005850	Pa×s	293.15	Dynamic...
η	0.0006075	Pa×s	293.15	Densiti...
η	0.0005840	Pa×s	293.15	Densiti...
η	0.0005990	Pa×s	293.15	Density...
η	0.0005320	Pa×s	298.15	Densiti...
η	0.0005510	Pa×s	298.15	Densiti...
η	0.0005585	Pa×s	298.15	Density...
η	0.0005530	Pa×s	298.15	Dynamic...
η	0.0005318	Pa×s	298.15	Viscosi...
η	0.0005446	Pa×s	298.15	Electri...
η	0.0008699	Pa×s	298.15	Volumet...
η	0.0005510	Pa×s	298.15	Viscosi...
η	0.0005450	Pa×s	298.15	Density...
η	0.0005500	Pa×s	298.15	Densiti...
η	0.0005470	Pa×s	298.15	Volumet...
η	0.0005510	Pa×s	298.15	Propert...
η	0.0005509	Pa×s	298.15	Excess ...
η	0.0005520	Pa×s	298.15	Densiti...
η	0.0005450	Pa×s	298.15	Dynamic...
η	0.0005770	Pa×s	298.15	Tempera...
η	0.0005560	Pa×s	298.15	Densiti...
η	0.0005520	Pa×s	298.15	Densiti...
η	0.0005580	Pa×s	298.15	Densiti...
η	0.0005130	Pa×s	302.45	Density...
η	0.0005180	Pa×s	303.00	Thermop...
η	0.0005090	Pa×s	303.15	Viscosi...
η	0.0005080	Pa×s	303.15	Dynamic...
η	0.0005070	Pa×s	303.15	Viscosi...
η	0.0005008	Pa×s	303.15	Viscosi...
η	0.0005261	Pa×s	303.15	Densiti...
η	0.0005130	Pa×s	303.15	Viscome...
η	0.0005140	Pa×s	303.15	Densiti...
η	0.0005120	Pa×s	303.15	Densiti...
η	0.0005154	Pa×s	303.15	Excess ...
η	0.0005100	Pa×s	303.15	Volumet...
η	0.0005240	Pa×s	303.15	Densiti...
η	0.0005150	Pa×s	303.15	Densiti...
η	0.0005060	Pa×s	303.15	Dynamic...
η	0.0005199	Pa×s	303.15	Density...
η	0.0005120	Pa×s	303.15	Density...
η	0.0005080	Pa×s	303.15	Density...
η	0.0005178	Pa×s	303.15	Densiti...
η	0.0005535	Pa×s	303.15	Densiti...
η	0.0005170	Pa×s	303.15	Propert...
η	0.0004760	Pa×s	308.15	Excess ...
η	0.0004840	Pa×s	308.15	Densiti...
η	0.0004849	Pa×s	308.15	Excess ...
η	0.0004860	Pa×s	308.15	Propert...
η	0.0004966	Pa×s	308.15	Densiti...
η	0.0005250	Pa×s	308.15	Tempera...
η	0.0004800	Pa×s	308.15	Viscome...
η	0.0004729	Pa×s	308.15	Viscosi...
η	0.0004900	Pa×s	308.15	Densiti...
η	0.0004780	Pa×s	308.15	Densiti...
η	0.0004650	Pa×s	308.15	Densiti...
η	0.0007287	Pa×s	308.15	Volumet...
η	0.0004930	Pa×s	308.15	Densiti...
η	0.0004747	Pa×s	308.15	Electri...
η	0.0004747	Pa×s	308.15	Electri...
η	0.0004843	Pa×s	308.15	Densiti...
η	0.0004760	Pa×s	308.15	Densiti...
η	0.0004857	Pa×s	308.15	Density...
η	0.0004500	Pa×s	313.00	Thermop...
η	0.0004470	Pa×s	313.15	Density...
η	0.0004430	Pa×s	313.15	Dynamic...
η	0.0004450	Pa×s	313.15	Densiti...
η	0.0004482	Pa×s	313.15	Viscosi...
η	0.0004559	Pa×s	313.15	Density...
η	0.0004480	Pa×s	313.15	Densiti...
η	0.0004450	Pa×s	313.15	Excess ...
η	0.0005010	Pa×s	313.15	Densiti...
η	0.0004440	Pa×s	313.15	Electri...
η	0.0004576	Pa×s	313.15	Excess ...
η	0.0004600	Pa×s	313.15	Propert...
η	0.0004500	Pa×s	313.15	Viscome...
η	0.0004410	Pa×s	313.15	Densiti...
η	0.0004702	Pa×s	313.15	Densiti...
η	0.0004470	Pa×s	313.15	Volumet...
η	0.0004490	Pa×s	313.15	Densiti...
η	0.0004590	Pa×s	313.15	Densiti...
η	0.0004515	Pa×s	313.15	Densiti...
η	0.0004438	Pa×s	313.15	Viscosi...
η	0.0004430	Pa×s	313.50	Density...
η	0.0004185	Pa×s	318.15	Electri...
η	0.0004324	Pa×s	318.15	Excess ...
η	0.0004259	Pa×s	318.15	Viscosi...
η	0.0005962	Pa×s	318.15	Volumet...
η	0.0004210	Pa×s	318.15	Densiti...
η	0.0004240	Pa×s	318.15	Densiti...
η	0.0004233	Pa×s	318.15	Densiti...
η	0.0004810	Pa×s	318.15	Tempera...
η	0.0004185	Pa×s	318.15	Electri...
η	0.0004390	Pa×s	318.15	Densiti...
η	0.0004220	Pa×s	318.15	Viscome...
η	0.0004210	Pa×s	318.15	Excess ...
η	0.0003950	Pa×s	323.15	Densiti...
η	0.0003950	Pa×s	323.15	Excess ...
η	0.0003873	Pa×s	323.15	Viscosi...
η	0.0003950	Pa×s	323.15	Densiti...
η	0.0004170	Pa×s	323.15	Densiti...
η	0.0003940	Pa×s	323.15	Volumet...
η	0.0003940	Pa×s	323.15	Densiti...
η	0.0003950	Pa×s	323.15	Densiti...
η	0.0004093	Pa×s	323.15	Excess ...
η	0.0004055	Pa×s	323.15	Viscosi...
η	0.0004601	Pa×s	323.15	Densiti...
η	0.0003970	Pa×s	323.15	Viscome...
η	0.0003860	Pa×s	323.55	Density...
η	0.0004430	Pa×s	328.15	Tempera...
η	0.0003720	Pa×s	328.15	Excess ...
η	0.0003872	Pa×s	328.15	Viscosi...
η	0.0003903	Pa×s	328.15	Excess ...
η	0.0004792	Pa×s	328.15	Volumet...
η	0.0003720	Pa×s	328.15	Densiti...
η	0.0003720	Pa×s	328.15	Densiti...
η	0.0003510	Pa×s	333.15	Densiti...
η	0.0003724	Pa×s	333.15	Excess ...
η	0.0003710	Pa×s	333.15	Viscosi...
η	0.0003490	Pa×s	333.15	Densiti...
η	0.0003450	Pa×s	333.85	Density...
ΔfusH	[0.59; 3.22]	kJ/mol	[157.30; 176.00]
ΔfusH	0.64	kJ/mol	157.30	NIST
ΔfusH	0.59	kJ/mol	161.10	NIST
ΔfusH	3.18	kJ/mol	175.30	NIST
ΔfusH	3.18	kJ/mol	175.30	NIST
ΔfusH	3.22	kJ/mol	175.60	NIST
ΔfusH	2.20	kJ/mol	176.00	NIST
ΔvapH	[7.40; 43.70]	kJ/mol	[208.00; 510.00]
ΔvapH	43.70	kJ/mol	208.00	NIST
ΔvapH	39.20	kJ/mol	224.00	NIST
ΔvapH	38.90	kJ/mol	257.00	NIST
ΔvapH	38.40	kJ/mol	300.50	NIST
ΔvapH	38.70	kJ/mol	305.50	NIST
ΔvapH	37.00 ± 0.10	kJ/mol	306.00	NIST
ΔvapH	38.30	kJ/mol	312.50	NIST
ΔvapH	36.70 ± 0.10	kJ/mol	313.00	NIST
ΔvapH	38.30	kJ/mol	315.00	NIST
ΔvapH	36.20 ± 0.10	kJ/mol	321.00	NIST
ΔvapH	38.30	kJ/mol	322.50	NIST
ΔvapH	36.20 ± 0.10	kJ/mol	323.00	NIST
ΔvapH	37.50	kJ/mol	326.00	NIST
ΔvapH	35.60 ± 0.10	kJ/mol	331.00	NIST
ΔvapH	35.60 ± 0.10	kJ/mol	333.00	NIST
ΔvapH	35.21	kJ/mol	337.70	NIST
ΔvapH	35.25	kJ/mol	337.80	KDB
ΔvapH	35.30 ± 0.10	kJ/mol	338.00	NIST
ΔvapH	35.20 ± 0.10	kJ/mol	338.00	NIST
ΔvapH	34.70 ± 0.10	kJ/mol	343.00	NIST
ΔvapH	37.00	kJ/mol	355.50	NIST
ΔvapH	37.00	kJ/mol	360.00	NIST
ΔvapH	32.70	kJ/mol	373.00	NIST
ΔvapH	36.90	kJ/mol	412.50	NIST
ΔvapH	36.10	kJ/mol	415.50	NIST
ΔvapH	36.30	kJ/mol	418.00	NIST
ΔvapH	28.10	kJ/mol	423.00	NIST
ΔvapH	20.60	kJ/mol	473.00	NIST
ΔvapH	35.10	kJ/mol	483.00	NIST
ΔvapH	7.40	kJ/mol	510.00	NIST
Pvap	[4.25; 1754.90]	kPa	[274.15; 433.15]
Pvap	4.25	kPa	274.15	Vapor P...
Pvap	5.50	kPa	278.15	Vapor P...
Pvap	6.70	kPa	282.55	Thermop...
Pvap	7.41	kPa	283.15	Vapor P...
Pvap	13.00	kPa	293.15	Vapor P...
Pvap	13.30	kPa	293.75	Thermop...
Pvap	16.95	kPa	298.15	Vapor-P...
Pvap	17.00	kPa	298.15	Measuri...
Pvap	16.97	kPa	298.15	Thermod...
Pvap	16.96	kPa	298.15	Thermod...
Pvap	16.97	kPa	298.15	Vapor p...
Pvap	20.00	kPa	301.45	Thermop...
Pvap	21.88	kPa	303.15	Thermod...
Pvap	21.88	kPa	303.15	Thermod...
Pvap	21.90	kPa	303.15	Measuri...
Pvap	21.88	kPa	303.15	Vapor-P...
Pvap	21.93	kPa	303.15	Thermod...
Pvap	21.93	kPa	303.15	Thermod...
Pvap	21.86	kPa	303.15	Vapor P...
Pvap	21.88	kPa	303.15	Vapor p...
Pvap	26.70	kPa	307.35	Thermop...
Pvap	27.96	kPa	308.15	Thermod...
Pvap	27.90	kPa	308.15	Measuri...
Pvap	27.98	kPa	308.15	Vapor-P...
Pvap	27.96	kPa	308.15	Thermod...
Pvap	27.96	kPa	308.15	Vapor p...
Pvap	30.33	kPa	309.79	Vapor-L...
Pvap	33.30	kPa	311.85	Thermop...
Pvap	35.42	kPa	313.06	Vapor-L...
Pvap	35.27	kPa	313.07	Vapour ...
Pvap	35.43	kPa	313.15	Vapor P...
Pvap	35.60	kPa	313.15	Measuri...
Pvap	35.45	kPa	313.15	Thermod...
Pvap	35.52	kPa	313.15	Vapor-L...
Pvap	35.51	kPa	313.15	Vapor-P...
Pvap	35.44	kPa	313.15	Thermod...
Pvap	35.44	kPa	313.15	Vapor p...
Pvap	38.33	kPa	315.00	Isobari...
Pvap	40.00	kPa	315.73	Vapor-L...
Pvap	40.00	kPa	315.75	Isobari...
Pvap	40.00	kPa	315.75	Thermop...
Pvap	40.41	kPa	316.02	Vapor-L...
Pvap	43.97	kPa	318.00	Isobari...
Pvap	44.54	kPa	318.15	Thermod...
Pvap	44.54	kPa	318.15	Vapor p...
Pvap	44.86	kPa	318.15	Isother...
Pvap	44.59	kPa	318.15	Vapor-P...
Pvap	45.11	kPa	318.43	Vapor-L...
Pvap	46.70	kPa	319.05	Thermop...
Pvap	50.30	kPa	320.90	Vapor-L...
Pvap	50.29	kPa	321.00	Isobari...
Pvap	53.30	kPa	322.05	Thermop...
Pvap	53.33	kPa	322.15	Isobari...
Pvap	55.50	kPa	323.13	Vapor L...
Pvap	55.57	kPa	323.14	Isother...
Pvap	55.39	kPa	323.14	Vapor-L...
Pvap	55.58	kPa	323.15	Vapor p...
Pvap	55.30	kPa	323.15	Vapor-L...
Pvap	55.61	kPa	323.15	Isother...
Pvap	55.58	kPa	323.15	Thermod...
Pvap	55.78	kPa	323.15	Thermod...
Pvap	55.78	kPa	323.15	Thermod...
Pvap	55.65	kPa	323.15	Vapor-P...
Pvap	55.54	kPa	323.15	Vapor P...
Pvap	55.69	kPa	323.15	Vapor-L...
Pvap	57.36	kPa	324.00	Isobari...
Pvap	60.00	kPa	324.65	Thermop...
Pvap	60.00	kPa	324.92	Isobari...
Pvap	59.99	kPa	324.96	Vapor-L...
Pvap	65.28	kPa	326.95	Vapor-L...
Pvap	65.25	kPa	327.00	Isobari...
Pvap	66.70	kPa	327.25	Thermop...
Pvap	66.66	kPa	327.34	Isobari...
Pvap	68.94	kPa	328.15	Vapor-P...
Pvap	74.02	kPa	330.00	Isobari...
Pvap	79.99	kPa	331.73	Isobari...
Pvap	80.97	kPa	332.08	Vapor L...
Pvap	83.76	kPa	333.00	Isobari...
Pvap	85.00	kPa	333.15	Experim...
Pvap	84.72	kPa	333.15	Vapor-L...
Pvap	84.93	kPa	333.15	Vapor P...
Pvap	84.62	kPa	333.15	Vapor-P...
Pvap	85.40	kPa	333.42	Isother...
Pvap	89.50	kPa	334.56	Isother...
Pvap	93.32	kPa	335.57	Isobari...
Pvap	94.55	kPa	336.00	Isobari...
Pvap	98.66	kPa	336.98	Isobari...
Pvap	99.91	kPa	337.35	Measure...
Pvap	100.00	kPa	337.42	Influen...
Pvap	100.00	kPa	337.42	1-Ethyl...
Pvap	101.30	kPa	337.45	Measure...
Pvap	101.30	kPa	337.45	Effect ...
Pvap	101.30	kPa	337.57	Vapor-L...
Pvap	101.30	kPa	337.65	Isother...
Pvap	101.33	kPa	337.65	Experim...
Pvap	101.30	kPa	337.65	Isobari...
Pvap	101.33	kPa	337.68	Determi...
Pvap	101.30	kPa	337.68	Isobari...
Pvap	101.30	kPa	337.68	Experim...
Pvap	101.30	kPa	337.69	Isobari...
Pvap	101.30	kPa	337.75	Vapor L...
Pvap	101.00	kPa	337.75	Isobari...
Pvap	101.30	kPa	337.78	A new a...
Pvap	101.30	kPa	337.82	Isobari...
Pvap	101.30	kPa	337.83	Isobari...
Pvap	101.30	kPa	337.83	Isobari...
Pvap	101.32	kPa	337.84	Organic...
Pvap	101.32	kPa	337.84	Organic...
Pvap	101.32	kPa	337.85	Isobari...
Pvap	101.00	kPa	337.85	Vapor L...
Pvap	101.30	kPa	337.85	Measure...
Pvap	101.32	kPa	337.85	Vapor L...
Pvap	101.30	kPa	337.90	Vapor-L...
Pvap	106.47	kPa	339.00	Isobari...
Pvap	119.61	kPa	342.00	Isobari...
Pvap	120.90	kPa	342.17	Isother...
Pvap	124.80	kPa	343.06	Isother...
Pvap	125.74	kPa	343.15	Vapor P...
Pvap	125.65	kPa	343.15	Vapor L...
Pvap	134.07	kPa	345.00	Isobari...
Pvap	142.60	kPa	346.64	Isother...
Pvap	150.69	kPa	348.15	Measure...
Pvap	150.67	kPa	348.15	Measure...
Pvap	150.71	kPa	348.15	Measure...
Pvap	163.20	kPa	350.25	Isother...
Pvap	181.00	kPa	353.10	Experim...
Pvap	181.56	kPa	353.15	Vapor P...
Pvap	180.50	kPa	353.15	Vapor-L...
Pvap	182.61	kPa	353.15	Measure...
Pvap	181.00	kPa	353.17	Isother...
Pvap	181.70	kPa	353.27	Isother...
Pvap	202.70	kPa	356.35	Isother...
Pvap	221.30	kPa	358.91	Isother...
Pvap	241.40	kPa	361.45	Isother...
Pvap	256.27	kPa	363.15	Vapor P...
Pvap	255.90	kPa	363.19	Isother...
Pvap	261.60	kPa	363.85	Isother...
Pvap	267.00	kPa	364.47	Isother...
Pvap	268.10	kPa	364.50	Vapour ...
Pvap	267.50	kPa	364.51	Vapor L...
Pvap	267.30	kPa	364.52	Vapor-L...
Pvap	267.60	kPa	364.52	Vapor L...
Pvap	288.90	kPa	366.88	Isother...
Pvap	321.30	kPa	370.13	Isother...
Pvap	341.20	kPa	372.04	Isother...
Pvap	350.90	kPa	372.90	Isother...
Pvap	352.62	kPa	373.15	Measure...
Pvap	352.64	kPa	373.15	Measure...
Pvap	352.80	kPa	373.15	Vapor-L...
Pvap	354.35	kPa	373.15	Vapor P...
Pvap	352.70	kPa	373.15	Measure...
Pvap	385.40	kPa	375.89	Isother...
Pvap	400.41	kPa	377.15	Measure...
Pvap	480.82	kPa	383.15	Vapor P...
Pvap	604.68	kPa	391.15	Measure...
Pvap	635.00	kPa	393.10	Experim...
Pvap	641.27	kPa	393.15	Vapor P...
Pvap	641.30	kPa	393.15	Vapor-L...
Pvap	840.10	kPa	403.15	Vapor-L...
Pvap	841.83	kPa	403.15	Vapor P...
Pvap	1042.57	kPa	411.15	Measure...
Pvap	1087.30	kPa	413.15	Vapor-L...
Pvap	1089.15	kPa	413.15	Vapor P...
Pvap	1565.62	kPa	428.15	Measure...
Pvap	1754.90	kPa	433.15	Vapor-L...
n0	[1.31670; 1.33030]		[288.15; 323.15]
n0	1.33030		288.15	Excess ...
n0	1.32890		293.00	Liquid-...
n0	1.32853		293.10	Vapor-L...
n0	1.32850		293.15	Measure...
n0	1.32870		293.15	A novel...
n0	1.33010		293.15	Solubil...
n0	1.32930		293.15	Liquid-...
n0	1.32870		293.15	Isother...
n0	1.32862		293.15	Liquid ...
n0	1.32860		293.15	Liquid ...
n0	1.32890		293.15	Isother...
n0	1.32880		293.15	Study o...
n0	1.32858		293.15	Synergi...
n0	1.32800		293.15	Experim...
n0	1.32860		293.15	Isobari...
n0	1.32850		293.15	Vapor-l...
n0	1.32850		293.15	Isobari...
n0	1.33010		293.15	Solubil...
n0	1.32870		293.15	Solubil...
n0	1.33010		293.15	Solubil...
n0	1.32843		293.15	Refract...
n0	1.32910		293.15	Measure...
n0	1.32900		293.20	Isobari...
n0	1.32640		298.10	PHYSICA...
n0	1.32640		298.15	Propert...
n0	1.32610		298.15	Mixing ...
n0	1.32649		298.15	Effect ...
n0	1.32700		298.15	Densiti...
n0	1.32720		298.15	Densiti...
n0	1.32648		298.15	Effect ...
n0	1.32690		298.15	Viscosi...
n0	1.32570		298.15	Applica...
n0	1.32655		298.15	Sucrose...
n0	1.32900		298.15	Volumet...
n0	1.32645		298.15	Excess ...
n0	1.32650		298.15	(Vapor ...
n0	1.32670		298.15	Binary ...
n0	1.32750		298.15	Isobari...
n0	1.32650		298.15	Excess ...
n0	1.32750		298.15	Excess ...
n0	1.32700		298.15	Tempera...
n0	1.32620		298.15	Experim...
n0	1.32634		298.15	Density...
n0	1.32687		298.15	Physica...
n0	1.32667		298.15	Density...
n0	1.32700		298.15	Excess ...
n0	1.32687		298.15	Physica...
n0	1.32660		298.15	Effect ...
n0	1.32610		298.15	Vapor-L...
n0	1.32630		298.15	Isobari...
n0	1.32660		298.15	Excess ...
n0	1.32640		298.15	Excess ...
n0	1.32700		298.15	Vapor-L...
n0	1.32640		298.15	Excess ...
n0	1.32880		298.15	Investi...
n0	1.32620		298.15	Liquid ...
n0	1.32650		298.15	Density...
n0	1.32650		298.15	Activit...
n0	1.32640		298.15	(Liquid...
n0	1.32640		298.15	Effect ...
n0	1.32668		298.15	Isother...
n0	1.32680		298.20	Isobari...
n0	1.32552		303.15	Densiti...
n0	1.32550		303.15	Experim...
n0	1.32433		303.15	Refract...
n0	1.32362		308.15	Densiti...
n0	1.32540		308.15	Excess ...
n0	1.32171		313.15	Densiti...
n0	1.32015		313.15	Refract...
n0	1.31670		323.15	Refract...
ρl	[752.83; 866.84]	kg/m3	[273.00; 333.15]
ρl	800.00	kg/m3	273.00	Saturat...
ρl	809.77	kg/m3	273.15	Molar C...
ρl	807.18	kg/m3	276.15	Volumet...
ρl	806.25	kg/m3	277.15	Volumet...
ρl	805.40	kg/m3	278.15	Volumet...
ρl	805.10	kg/m3	278.15	Thermop...
ρl	805.11	kg/m3	278.15	Molar C...
ρl	800.45	kg/m3	283.15	Molar C...
ρl	800.71	kg/m3	283.15	Density...
ρl	801.08	kg/m3	283.15	Volumet...
ρl	801.44	kg/m3	283.15	Densiti...
ρl	800.64	kg/m3	283.15	Volumet...
ρl	800.67	kg/m3	283.15	Volumet...
ρl	800.62	kg/m3	283.15	Excess ...
ρl	801.25	kg/m3	283.15	Densiti...
ρl	795.99	kg/m3	288.15	Volumet...
ρl	796.00	kg/m3	288.15	Volumet...
ρl	796.13	kg/m3	288.15	Mass de...
ρl	796.09	kg/m3	288.15	Effect ...
ρl	796.04	kg/m3	288.15	The mol...
ρl	795.50	kg/m3	288.15	Tempera...
ρl	796.41	kg/m3	288.15	Excess ...
ρl	796.09	kg/m3	288.15	Volumet...
ρl	795.96	kg/m3	288.15	Volumet...
ρl	795.77	kg/m3	288.15	Molar C...
ρl	795.70	kg/m3	288.15	Thermop...
ρl	795.97	kg/m3	288.15	Thermod...
ρl	796.41	kg/m3	288.15	Volumet...
ρl	797.30	kg/m3	290.15	Density...
ρl	791.00	kg/m3	293.00	KDB
ρl	791.26	kg/m3	293.15	Volumet...
ρl	791.30	kg/m3	293.15	Volumet...
ρl	793.60	kg/m3	293.15	Investi...
ρl	791.72	kg/m3	293.15	Excess ...
ρl	791.34	kg/m3	293.15	A Volum...
ρl	791.20	kg/m3	293.15	(Liquid...
ρl	791.82	kg/m3	293.15	Isobari...
ρl	791.10	kg/m3	293.15	Measure...
ρl	791.87	kg/m3	293.15	Densiti...
ρl	791.71	kg/m3	293.15	Volumet...
ρl	792.60	kg/m3	293.15	Densiti...
ρl	792.07	kg/m3	293.15	Densiti...
ρl	791.41	kg/m3	293.15	Electro...
ρl	793.50	kg/m3	293.15	Density...
ρl	791.49	kg/m3	293.15	Volume ...
ρl	791.29	kg/m3	293.15	Volumet...
ρl	791.40	kg/m3	293.15	Effect ...
ρl	791.90	kg/m3	293.15	Effect ...
ρl	791.35	kg/m3	293.15	Propert...
ρl	791.62	kg/m3	293.15	Experim...
ρl	791.33	kg/m3	293.15	Density...
ρl	791.28	kg/m3	293.15	Viscosi...
ρl	791.34	kg/m3	293.15	Density...
ρl	791.55	kg/m3	293.15	Thermod...
ρl	791.24	kg/m3	293.15	Thermop...
ρl	792.20	kg/m3	293.15	Isobari...
ρl	792.12	kg/m3	293.15	Densiti...
ρl	791.35	kg/m3	293.15	The mol...
ρl	791.40	kg/m3	293.15	Volumet...
ρl	791.35	kg/m3	293.15	Thermod...
ρl	791.08	kg/m3	293.15	Molar C...
ρl	791.28	kg/m3	293.15	Speed o...
ρl	790.80	kg/m3	295.15	Density...
ρl	787.00	kg/m3	298.00	Saturat...
ρl	787.50	kg/m3	298.10	Activit...
ρl	786.58	kg/m3	298.15	Speed o...
ρl	791.00	kg/m3	298.15	Tie-Lin...
ρl	786.53	kg/m3	298.15	Volumet...
ρl	786.40	kg/m3	298.15	Bubble ...
ρl	786.40	kg/m3	298.15	Tempera...
ρl	786.56	kg/m3	298.15	Excess ...
ρl	786.42	kg/m3	298.15	Isother...
ρl	786.70	kg/m3	298.15	Liquid ...
ρl	786.60	kg/m3	298.15	Thermod...
ρl	786.61	kg/m3	298.15	Density...
ρl	786.71	kg/m3	298.15	Density...
ρl	786.55	kg/m3	298.15	Volumet...
ρl	786.00	kg/m3	298.15	Excess ...
ρl	786.61	kg/m3	298.15	Explora...
ρl	787.00	kg/m3	298.15	Solubil...
ρl	786.62	kg/m3	298.15	Tempera...
ρl	787.00	kg/m3	298.15	Phase d...
ρl	785.30	kg/m3	298.15	Volumet...
ρl	786.63	kg/m3	298.15	Partial...
ρl	786.62	kg/m3	298.15	Isother...
ρl	787.21	kg/m3	298.15	Densiti...
ρl	786.79	kg/m3	298.15	Volume ...
ρl	786.37	kg/m3	298.15	Molar C...
ρl	786.10	kg/m3	298.15	Liquid ...
ρl	786.64	kg/m3	298.15	Binary ...
ρl	786.57	kg/m3	298.15	Binary ...
ρl	786.61	kg/m3	298.15	Isobari...
ρl	787.20	kg/m3	298.15	Thermod...
ρl	786.74	kg/m3	298.15	Study o...
ρl	786.60	kg/m3	298.15	Probing...
ρl	786.40	kg/m3	298.15	Density...
ρl	786.68	kg/m3	298.15	Density...
ρl	866.84	kg/m3	298.15	Tempera...
ρl	786.62	kg/m3	298.15	Effect ...
ρl	786.88	kg/m3	298.15	Effect ...
ρl	787.00	kg/m3	298.15	Effect ...
ρl	786.66	kg/m3	298.15	Physica...
ρl	786.56	kg/m3	298.15	Vapor-l...
ρl	786.69	kg/m3	298.15	Volumet...
ρl	786.90	kg/m3	298.15	Cation ...
ρl	786.61	kg/m3	298.15	Partial...
ρl	786.62	kg/m3	298.15	Density...
ρl	787.00	kg/m3	298.15	Liquid-...
ρl	786.58	kg/m3	298.15	Ionic m...
ρl	786.67	kg/m3	298.15	Non-cov...
ρl	786.62	kg/m3	298.15	Experim...
ρl	786.44	kg/m3	298.15	Thermod...
ρl	786.20	kg/m3	298.15	Measure...
ρl	786.30	kg/m3	298.15	Solubil...
ρl	787.10	kg/m3	298.15	Isobari...
ρl	786.67	kg/m3	298.15	Propert...
ρl	787.52	kg/m3	298.15	Modifie...
ρl	786.59	kg/m3	298.15	Determi...
ρl	786.99	kg/m3	298.15	Excess ...
ρl	786.60	kg/m3	298.15	Measure...
ρl	786.62	kg/m3	298.15	Isobari...
ρl	786.59	kg/m3	298.15	Isobari...
ρl	786.60	kg/m3	298.15	Volumet...
ρl	786.20	kg/m3	298.15	Dynamic...
ρl	786.50	kg/m3	298.15	Density...
ρl	786.20	kg/m3	298.15	Measure...
ρl	786.60	kg/m3	298.15	Solubil...
ρl	786.59	kg/m3	298.15	Excess ...
ρl	786.56	kg/m3	298.15	Separat...
ρl	786.38	kg/m3	298.15	Partial...
ρl	786.80	kg/m3	298.15	Density...
ρl	786.30	kg/m3	298.15	Volumet...
ρl	786.56	kg/m3	298.15	Excess ...
ρl	791.81	kg/m3	298.15	Liquid-...
ρl	786.59	kg/m3	298.15	Ternary...
ρl	785.90	kg/m3	298.15	Solubil...
ρl	786.69	kg/m3	298.15	Isobari...
ρl	786.57	kg/m3	298.15	Liquid ...
ρl	786.97	kg/m3	298.15	Experim...
ρl	786.55	kg/m3	298.15	Thermod...
ρl	786.64	kg/m3	298.15	Thermod...
ρl	786.49	kg/m3	298.15	Refract...
ρl	787.35	kg/m3	298.15	Excess ...
ρl	786.58	kg/m3	298.15	Volumet...
ρl	786.50	kg/m3	298.15	Fully a...
ρl	786.46	kg/m3	298.15	Measure...
ρl	789.27	kg/m3	298.15	Investi...
ρl	786.59	kg/m3	298.15	Vapor P...
ρl	786.30	kg/m3	298.15	Thermod...
ρl	786.40	kg/m3	298.15	Liquid ...
ρl	786.67	kg/m3	298.15	Ebullio...
ρl	786.70	kg/m3	298.15	Liquid-...
ρl	786.30	kg/m3	298.15	Thermop...
ρl	787.01	kg/m3	298.15	Volumet...
ρl	786.58	kg/m3	298.15	Liquid ...
ρl	786.55	kg/m3	298.15	Liquid-...
ρl	786.55	kg/m3	298.15	Surface...
ρl	789.70	kg/m3	298.15	Phase e...
ρl	786.67	kg/m3	298.15	Density...
ρl	786.00	kg/m3	298.15	Ternary...
ρl	786.65	kg/m3	298.15	Electro...
ρl	786.59	kg/m3	298.15	Liquid ...
ρl	786.58	kg/m3	298.15	Volumet...
ρl	786.62	kg/m3	298.15	Experim...
ρl	786.60	kg/m3	298.15	Dynamic...
ρl	786.75	kg/m3	298.15	Mass de...
ρl	786.58	kg/m3	298.15	Volumet...
ρl	786.69	kg/m3	298.15	Effect ...
ρl	786.55	kg/m3	298.15	Liquid ...
ρl	786.62	kg/m3	298.15	Mutual ...
ρl	786.55	kg/m3	298.15	Volumet...
ρl	786.53	kg/m3	298.15	Volumet...
ρl	786.64	kg/m3	298.15	The mol...
ρl	786.50	kg/m3	298.15	Excess ...
ρl	787.43	kg/m3	298.15	Densiti...
ρl	786.80	kg/m3	298.15	Vapor-L...
ρl	796.00	kg/m3	298.20	Solubil...
ρl	791.00	kg/m3	298.20	Phase e...
ρl	786.27	kg/m3	298.20	Ternary...
ρl	786.00	kg/m3	303.00	Saturat...
ρl	781.85	kg/m3	303.15	Speed o...
ρl	782.07	kg/m3	303.15	Volume ...
ρl	781.83	kg/m3	303.15	Volumet...
ρl	783.40	kg/m3	303.15	Ternary...
ρl	781.86	kg/m3	303.15	Volumet...
ρl	781.97	kg/m3	303.15	Effect ...
ρl	781.96	kg/m3	303.15	Density...
ρl	781.85	kg/m3	303.15	Electro...
ρl	783.00	kg/m3	303.15	Densiti...
ρl	782.43	kg/m3	303.15	Densiti...
ρl	781.91	kg/m3	303.15	Densiti...
ρl	781.81	kg/m3	303.15	Excess ...
ρl	782.68	kg/m3	303.15	Densiti...
ρl	784.59	kg/m3	303.15	Investi...
ρl	782.40	kg/m3	303.15	Viscous...
ρl	782.24	kg/m3	303.15	Excess ...
ρl	781.91	kg/m3	303.15	Thermod...
ρl	781.91	kg/m3	303.15	The mol...
ρl	782.29	kg/m3	303.15	Volumet...
ρl	781.86	kg/m3	303.15	Volumet...
ρl	781.90	kg/m3	303.15	A Volum...
ρl	781.40	kg/m3	303.15	Density...
ρl	782.44	kg/m3	303.15	Thermod...
ρl	781.97	kg/m3	303.15	Volumet...
ρl	781.81	kg/m3	303.15	Isobari...
ρl	781.81	kg/m3	303.15	Thermop...
ρl	781.94	kg/m3	303.15	Propert...
ρl	782.16	kg/m3	303.15	Effect ...
ρl	781.65	kg/m3	303.15	Molar C...
ρl	781.89	kg/m3	303.15	Density...
ρl	782.75	kg/m3	303.15	Densiti...
ρl	781.81	kg/m3	303.15	Vapor-l...
ρl	782.00	kg/m3	303.15	Liquid ...
ρl	781.95	kg/m3	303.15	Physica...
ρl	783.40	kg/m3	303.15	Excess ...
ρl	782.61	kg/m3	303.15	Densiti...
ρl	777.10	kg/m3	308.15	Speed o...
ρl	776.90	kg/m3	308.15	Density...
ρl	777.18	kg/m3	308.15	Effect ...
ρl	777.20	kg/m3	308.15	Propert...
ρl	777.20	kg/m3	308.15	Physica...
ρl	777.20	kg/m3	308.15	Tempera...
ρl	777.56	kg/m3	308.15	Densiti...
ρl	777.14	kg/m3	308.15	Density...
ρl	777.15	kg/m3	308.15	Partial...
ρl	777.41	kg/m3	308.15	Effect ...
ρl	777.18	kg/m3	308.15	Non-cov...
ρl	777.21	kg/m3	308.15	Volumet...
ρl	777.45	kg/m3	308.15	Study o...
ρl	776.89	kg/m3	308.15	Molar C...
ρl	777.10	kg/m3	308.15	Density...
ρl	777.07	kg/m3	308.15	Thermod...
ρl	777.30	kg/m3	308.15	Density...
ρl	777.21	kg/m3	308.15	Density...
ρl	777.11	kg/m3	308.15	Volumet...
ρl	777.55	kg/m3	308.15	Volumet...
ρl	777.33	kg/m3	308.15	Volume ...
ρl	777.16	kg/m3	308.15	Thermod...
ρl	777.87	kg/m3	308.15	Investi...
ρl	776.90	kg/m3	308.15	Thermop...
ρl	777.21	kg/m3	308.15	Effect ...
ρl	777.10	kg/m3	308.15	Volumet...
ρl	776.95	kg/m3	308.15	Electro...
ρl	777.08	kg/m3	308.15	Volumet...
ρl	777.29	kg/m3	308.15	Mass de...
ρl	777.91	kg/m3	308.15	Densiti...
ρl	777.16	kg/m3	308.15	The mol...
ρl	777.10	kg/m3	308.15	Volumet...
ρl	779.00	kg/m3	313.00	Saturat...
ρl	772.31	kg/m3	313.14	Volumet...
ρl	772.32	kg/m3	313.15	Speed o...
ρl	772.70	kg/m3	313.15	Liquid ...
ρl	772.36	kg/m3	313.15	A Volum...
ρl	772.31	kg/m3	313.15	Density...
ρl	772.33	kg/m3	313.15	Volumet...
ρl	772.42	kg/m3	313.15	Propert...
ρl	772.37	kg/m3	313.15	Density...
ρl	772.55	kg/m3	313.15	Volume ...
ρl	772.44	kg/m3	313.15	Volumet...
ρl	771.97	kg/m3	313.15	Electro...
ρl	773.50	kg/m3	313.15	Densiti...
ρl	772.74	kg/m3	313.15	Excess ...
ρl	772.78	kg/m3	313.15	Volumet...
ρl	772.44	kg/m3	313.15	Effect ...
ρl	772.32	kg/m3	313.15	Excess ...
ρl	772.73	kg/m3	313.15	Excess ...
ρl	774.60	kg/m3	313.15	Ternary...
ρl	772.89	kg/m3	313.15	Thermod...
ρl	772.90	kg/m3	313.15	Densiti...
ρl	772.29	kg/m3	313.15	Thermop...
ρl	772.11	kg/m3	313.15	Molar C...
ρl	772.64	kg/m3	313.15	Effect ...
ρl	772.10	kg/m3	313.15	Density...
ρl	772.32	kg/m3	313.15	Volumet...
ρl	772.38	kg/m3	313.15	Thermod...
ρl	773.14	kg/m3	313.15	Densiti...
ρl	772.97	kg/m3	313.15	Densiti...
ρl	772.44	kg/m3	313.15	Investi...
ρl	772.38	kg/m3	313.15	The mol...
ρl	774.60	kg/m3	313.15	Excess ...
ρl	773.05	kg/m3	313.15	Densiti...
ρl	767.51	kg/m3	318.15	Speed o...
ρl	767.52	kg/m3	318.15	Volumet...
ρl	768.32	kg/m3	318.15	Densiti...
ρl	768.09	kg/m3	318.15	Thermod...
ρl	767.71	kg/m3	318.15	Mass de...
ρl	767.40	kg/m3	318.15	Thermop...
ρl	767.57	kg/m3	318.15	The mol...
ρl	767.84	kg/m3	318.15	Effect ...
ρl	767.74	kg/m3	318.15	Effect ...
ρl	767.70	kg/m3	318.15	Density...
ρl	767.52	kg/m3	318.15	Volumet...
ρl	767.97	kg/m3	318.15	Volumet...
ρl	767.20	kg/m3	318.15	Density...
ρl	767.74	kg/m3	318.15	Volume ...
ρl	768.01	kg/m3	318.15	Study o...
ρl	767.56	kg/m3	318.15	Density...
ρl	767.50	kg/m3	318.15	Density...
ρl	767.75	kg/m3	318.15	Non-cov...
ρl	768.04	kg/m3	318.15	Thermod...
ρl	767.74	kg/m3	318.15	Partial...
ρl	767.60	kg/m3	318.15	Volumet...
ρl	768.03	kg/m3	318.15	Densiti...
ρl	768.00	kg/m3	323.00	Saturat...
ρl	762.67	kg/m3	323.15	Speed o...
ρl	764.00	kg/m3	323.15	Densiti...
ρl	763.47	kg/m3	323.15	Densiti...
ρl	762.70	kg/m3	323.15	A Volum...
ρl	762.72	kg/m3	323.15	Density...
ρl	762.83	kg/m3	323.15	Thermop...
ρl	763.03	kg/m3	323.15	Effect ...
ρl	762.61	kg/m3	323.15	Vapor-l...
ρl	762.67	kg/m3	323.15	Volumet...
ρl	763.24	kg/m3	323.15	Thermod...
ρl	763.12	kg/m3	323.15	Volumet...
ρl	762.10	kg/m3	323.15	Density...
ρl	763.24	kg/m3	323.15	Densiti...
ρl	763.36	kg/m3	323.15	Densiti...
ρl	758.23	kg/m3	328.15	Volumet...
ρl	758.20	kg/m3	328.15	Excess ...
ρl	757.97	kg/m3	328.15	Mass de...
ρl	757.77	kg/m3	328.15	Volumet...
ρl	752.83	kg/m3	333.15	Volumet...
ρl	753.39	kg/m3	333.15	Densiti...
ρl	753.51	kg/m3	333.15	Densiti...
ρl	753.29	kg/m3	333.15	Volumet...
ρl	752.86	kg/m3	333.15	A Volum...
ΔfusS	[3.70; 18.30]	J/mol×K	[157.30; 176.00]
ΔfusS	4.00	J/mol×K	157.30	NIST
ΔfusS	3.70	J/mol×K	161.10	NIST
ΔfusS	18.10	J/mol×K	175.30	NIST
ΔfusS	18.30	J/mol×K	175.60	NIST
ΔfusS	12.50	J/mol×K	176.00	NIST
csound,fluid	[1020.46; 1169.50]	m/s	[278.15; 323.15]
csound,fluid	1169.50	m/s	278.15	Volumet...
csound,fluid	1135.85	m/s	288.15	Densiti...
csound,fluid	1136.34	m/s	288.15	Thermop...
csound,fluid	1135.49	m/s	288.15	Volumet...
csound,fluid	1134.45	m/s	288.15	Effect ...
csound,fluid	1126.20	m/s	290.65	Effect ...
csound,fluid	1127.69	m/s	290.65	Thermop...
csound,fluid	1117.95	m/s	293.15	Effect ...
csound,fluid	1119.49	m/s	293.15	Thermop...
csound,fluid	1118.91	m/s	293.15	Densiti...
csound,fluid	1111.28	m/s	295.65	Thermop...
csound,fluid	1109.77	m/s	295.65	Effect ...
csound,fluid	1101.58	m/s	298.15	Effect ...
csound,fluid	1102.68	m/s	298.15	Volumet...
csound,fluid	1102.98	m/s	298.15	Thermop...
csound,fluid	1102.62	m/s	298.15	Densiti...
csound,fluid	1102.29	m/s	298.15	Volumet...
csound,fluid	1104.60	m/s	298.15	Ultraso...
csound,fluid	1102.41	m/s	298.15	Apparen...
csound,fluid	1109.00	m/s	298.15	Densiti...
csound,fluid	1103.80	m/s	298.15	Compres...
csound,fluid	1101.24	m/s	298.15	Thermod...
csound,fluid	1094.69	m/s	300.65	Thermop...
csound,fluid	1093.44	m/s	300.65	Effect ...
csound,fluid	1092.00	m/s	303.15	Densiti...
csound,fluid	1085.45	m/s	303.15	Effect ...
csound,fluid	1086.37	m/s	303.15	Volumet...
csound,fluid	1086.03	m/s	303.15	Densiti...
csound,fluid	1086.46	m/s	303.15	Thermop...
csound,fluid	1086.37	m/s	303.15	Applica...
csound,fluid	1077.33	m/s	305.65	Effect ...
csound,fluid	1078.30	m/s	305.65	Thermop...
csound,fluid	1074.00	m/s	308.15	Densiti...
csound,fluid	1069.80	m/s	308.15	Densiti...
csound,fluid	1070.15	m/s	308.15	Thermop...
csound,fluid	1070.11	m/s	308.15	Applica...
csound,fluid	1069.78	m/s	308.15	Volumet...
csound,fluid	1070.11	m/s	308.15	Volumet...
csound,fluid	1069.19	m/s	308.15	Effect ...
csound,fluid	1061.07	m/s	310.65	Effect ...
csound,fluid	1062.07	m/s	310.65	Thermop...
csound,fluid	1053.96	m/s	313.15	Applica...
csound,fluid	1053.97	m/s	313.15	Thermop...
csound,fluid	1053.96	m/s	313.15	Volumet...
csound,fluid	1060.00	m/s	313.15	Densiti...
csound,fluid	1052.93	m/s	313.15	Effect ...
csound,fluid	1045.91	m/s	315.65	Thermop...
csound,fluid	1044.90	m/s	315.65	Effect ...
csound,fluid	1037.91	m/s	318.15	Applica...
csound,fluid	1037.91	m/s	318.15	Volumet...
csound,fluid	1036.74	m/s	318.15	Effect ...
csound,fluid	1037.71	m/s	318.15	Volumet...
csound,fluid	1037.93	m/s	318.15	Thermop...
csound,fluid	1028.60	m/s	320.65	Effect ...
csound,fluid	1029.90	m/s	320.65	Thermop...
csound,fluid	1020.46	m/s	323.15	Effect ...
csound,fluid	1021.99	m/s	323.15	Thermop...
γ	[0.02; 0.02]	N/m	[278.20; 343.15]
γ	0.02	N/m	278.20	Thermop...
γ	0.02	N/m	279.11	Measure...
γ	0.02	N/m	282.59	Measure...
γ	0.02	N/m	288.15	Physico...
γ	0.02	N/m	288.15	Surface...
γ	0.02	N/m	288.20	Thermop...
γ	0.02	N/m	288.30	Measure...
γ	0.02	N/m	293.15	Thermod...
γ	0.02	N/m	293.15	Density...
γ	0.02	N/m	293.20	KDB
γ	0.02	N/m	293.37	Measure...
γ	0.02	N/m	296.97	Measure...
γ	0.02	N/m	298.15	Effect ...
γ	0.02	N/m	298.15	Surface...
γ	0.02	N/m	298.15	Physico...
γ	0.02	N/m	298.20	Thermop...
γ	0.02	N/m	301.54	Measure...
γ	0.02	N/m	303.15	Measuri...
γ	0.02	N/m	303.15	Thermod...
γ	0.02	N/m	303.20	Investi...
γ	0.02	N/m	307.31	Measure...
γ	0.02	N/m	308.15	Effect ...
γ	0.02	N/m	308.15	Physico...
γ	0.02	N/m	308.15	Surface...
γ	0.02	N/m	308.20	Thermop...
γ	0.02	N/m	311.76	Measure...
γ	0.02	N/m	313.15	Measuri...
γ	0.02	N/m	313.15	Thermod...
γ	0.02	N/m	313.20	Investi...
γ	0.02	N/m	317.66	Measure...
γ	0.02	N/m	318.15	Surface...
γ	0.02	N/m	318.15	Effect ...
γ	0.02	N/m	318.20	Thermop...
γ	0.02	N/m	322.90	Measure...
γ	0.02	N/m	323.15	Measuri...
γ	0.02	N/m	323.15	Thermod...
γ	0.02	N/m	323.20	Investi...
γ	0.02	N/m	326.56	Measure...
γ	0.02	N/m	328.15	Effect ...
γ	0.02	N/m	330.01	Measure...
γ	0.02	N/m	333.15	Measuri...
γ	0.02	N/m	333.81	Measure...
γ	0.02	N/m	343.15	Measuri...
λ	0.19	W/m×K	298.15	Measure...

Pressure Dependent Properties

Property	Value	Unit	Pressure (kPa)	Source
Tboil	[315.70; 337.65]	K	[40.00; 96.60]
Tboil	315.70	K	40.00	Vapor-L...
Tboil	319.00	K	46.66	Vapor-L...
Tboil	324.30	K	58.80	Vapor-L...
Tboil	327.50	K	67.59	Vapor-L...
Tboil	330.60	K	76.13	Vapor-L...
Tboil	337.65	K	96.60	Low cos...

Datasets

1. Molar heat capacity at constant pressure, J/K/mol (2)
2. Viscosity, Pa*s (5)
3. Refractive index (Na D-line) (2)
4. Mass density, kg/m3 (10)
5. Speed of sound, m/s (2)
6. Thermal diffusivity, m2/s (1)
7. 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
248.15	500.00	74.02
248.15	1000.00	74.02
248.15	2500.00	73.95
248.15	5000.00	73.89
248.15	7500.00	73.79
248.15	10000.00	73.79
248.15	12500.00	73.76
273.15	500.00	77.03
273.15	1000.00	77.00
273.15	2500.00	76.93
273.15	5000.00	76.84
273.15	7500.00	76.80
273.15	10000.00	76.77
273.15	12500.00	76.74
298.15	500.00	81.39
298.15	1000.00	81.35
298.15	2500.00	81.19
298.15	5000.00	81.07
298.15	7500.00	81.03
298.15	10000.00	80.91
298.15	12500.00	80.91
323.15	500.00	86.87
323.15	1000.00	86.80
323.15	2500.00	86.64
323.15	5000.00	86.45
323.15	7500.00	86.29
323.15	10000.00	86.13
323.15	12500.00	86.00
348.15	500.00	93.66
348.15	1000.00	93.59
348.15	2500.00	93.43
348.15	5000.00	93.18
348.15	7500.00	92.92
348.15	10000.00	92.73
348.15	12500.00	92.41
373.15	500.00	101.83
373.15	1000.00	101.76
373.15	2500.00	101.41
373.15	5000.00	101.00
373.15	7500.00	100.64
373.15	10000.00	100.23
373.15	12500.00	99.97
398.15	1000.00	111.86
398.15	2500.00	111.28
398.15	5000.00	110.38
398.15	7500.00	109.58
398.15	10000.00	108.97
398.15	12500.00	108.33
423.15	2500.00	122.98
423.15	5000.00	121.41
423.15	7500.00	120.03
423.15	10000.00	118.84
423.15	12500.00	117.85
473.15	5000.00	162.32
473.15	7500.00	152.94
473.15	10000.00	146.91
473.15	12500.00	142.75
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Molar heat capacity at constant pressure, J/K/mol - Liquid
280.00	100.00	77.22
280.00	1000.00	74.02
280.00	5000.00	73.70
320.00	100.00	87.15
320.00	1000.00	85.87
320.00	5000.00	84.27
360.00	1000.00	97.41
360.00	5000.00	94.20
360.00	10000.00	94.52
360.00	15000.00	97.09
Reference

Viscosity, Pa*s

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Viscosity, Pa*s - Liquid
293.15	100.00	0.0006
293.15	20000.00	0.0006
293.15	40000.00	0.0007
293.15	60000.00	0.0008
293.15	80000.00	0.0008
293.15	100000.00	0.0009
313.15	100.00	0.0004
313.15	20000.00	0.0005
313.15	40000.00	0.0005
313.15	60000.00	0.0006
313.15	80000.00	0.0006
313.15	100000.00	0.0007
333.15	100.00	0.0003
333.15	20000.00	0.0004
333.15	40000.00	0.0004
333.15	60000.00	0.0005
333.15	80000.00	0.0005
333.15	100000.00	0.0005
353.15	20000.00	0.0003
353.15	40000.00	0.0003
353.15	60000.00	0.0004
353.15	80000.00	0.0004
353.15	100000.00	0.0004
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Viscosity, Pa*s - Liquid
298.15	81.50	0.0006
Reference

Fixed		Measured
Temperature, K - Gas	Amount density, mol/m3 - Gas	Viscosity, Pa*s - Gas
297.64	3.79	9.5940e-06
312.54	3.79	0.0000
324.75	3.79	0.0000
338.69	3.79	0.0000
352.91	3.79	0.0000
352.93	3.79	0.0000
366.84	3.79	0.0000
381.27	3.79	0.0000
395.39	3.79	0.0000
411.30	3.79	0.0000
423.50	3.79	0.0000
440.61	3.79	0.0000
468.85	3.79	0.0000
496.65	3.79	0.0000
525.41	3.79	0.0000
547.13	3.79	0.0000
569.26	3.79	0.0000
597.60	3.79	0.0000
298.16	6.32	9.5940e-06
312.25	6.32	0.0000
325.91	6.32	0.0000
339.77	6.32	0.0000
353.30	6.32	0.0000
355.50	6.32	0.0000
367.84	6.32	0.0000
382.15	6.32	0.0000
396.23	6.32	0.0000
411.31	6.32	0.0000
424.73	6.32	0.0000
440.07	6.32	0.0000
297.43	8.17	9.5510e-06
311.23	8.17	0.0000
325.15	8.17	0.0000
338.47	8.17	0.0000
352.62	8.17	0.0000
353.05	8.17	0.0000
366.82	8.17	0.0000
381.38	8.17	0.0000
394.76	8.17	0.0000
412.33	8.17	0.0000
423.31	8.17	0.0000
437.81	8.17	0.0000
496.40	8.17	0.0000
525.42	8.17	0.0000
546.79	8.17	0.0000
602.56	8.17	0.0000
297.41	10.1	9.5320e-06
313.89	10.1	0.0000
325.22	10.1	0.0000
338.62	10.1	0.0000
352.86	10.1	0.0000
353.44	10.1	0.0000
366.59	10.1	0.0000
380.86	10.1	0.0000
394.63	10.1	0.0000
409.51	10.1	0.0000
423.96	10.1	0.0000
437.60	10.1	0.0000
467.33	10.1	0.0000
496.56	10.1	0.0000
298.54	13.2	9.5790e-06
314.18	13.2	0.0000
325.76	13.2	0.0000
339.34	13.2	0.0000
353.22	13.2	0.0000
353.26	13.2	0.0000
367.10	13.2	0.0000
380.97	13.2	0.0000
395.40	13.2	0.0000
409.39	13.2	0.0000
423.77	13.2	0.0000
438.41	13.2	0.0000
467.74	13.2	0.0000
496.43	13.2	0.0000
526.39	13.2	0.0000
546.84	13.2	0.0000
567.40	13.2	0.0000
596.93	13.2	0.0000
301.53	17.93	9.6720e-06
311.12	17.93	9.9590e-06
325.59	17.93	0.0000
339.25	17.93	0.0000
353.58	17.93	0.0000
355.67	17.93	0.0000
366.93	17.93	0.0000
381.53	17.93	0.0000
395.23	17.93	0.0000
412.01	17.93	0.0000
424.38	17.93	0.0000
439.47	17.93	0.0000
468.08	17.93	0.0000
496.41	17.93	0.0000
527.99	17.93	0.0000
548.52	17.93	0.0000
571.83	17.93	0.0000
597.15	17.93	0.0000
299.92	24.58	9.6180e-06
310.88	24.58	9.9480e-06
325.98	24.58	0.0000
340.14	24.58	0.0000
353.71	24.58	0.0000
355.05	24.58	0.0000
368.03	24.58	0.0000
383.55	24.58	0.0000
395.18	24.58	0.0000
409.75	24.58	0.0000
424.41	24.58	0.0000
439.20	24.58	0.0000
466.95	24.58	0.0000
496.44	24.58	0.0000
526.84	24.58	0.0000
299.79	32.22	9.6020e-06
311.60	32.22	9.9690e-06
324.78	32.22	0.0000
338.66	32.22	0.0000
353.78	32.22	0.0000
355.04	32.22	0.0000
366.99	32.22	0.0000
381.92	32.22	0.0000
395.16	32.22	0.0000
410.18	32.22	0.0000
423.88	32.22	0.0000
439.16	32.22	0.0000
467.62	32.22	0.0000
496.97	32.22	0.0000
526.17	32.22	0.0000
547.30	32.22	0.0000
567.53	32.22	0.0000
597.12	32.22	0.0000
297.92	38.68	9.5550e-06
311.60	38.68	9.9710e-06
326.88	38.68	0.0000
338.72	38.68	0.0000
353.06	38.68	0.0000
353.18	38.68	0.0000
367.87	38.68	0.0000
381.90	38.68	0.0000
395.37	38.68	0.0000
410.35	38.68	0.0000
425.10	38.68	0.0000
441.61	38.68	0.0000
467.34	38.68	0.0000
496.21	38.68	0.0000
527.02	38.68	0.0000
547.49	38.68	0.0000
568.11	38.68	0.0000
598.60	38.68	0.0000
298.71	49.53	9.5760e-06
314.20	49.53	0.0000
324.77	49.53	0.0000
338.81	49.53	0.0000
352.35	49.53	0.0000
353.20	49.53	0.0000
367.81	49.53	0.0000
381.27	49.53	0.0000
394.88	49.53	0.0000
411.32	49.53	0.0000
423.52	49.53	0.0000
439.56	49.53	0.0000
467.49	49.53	0.0000
496.48	49.53	0.0000
525.14	49.53	0.0000
548.04	49.53	0.0000
569.93	49.53	0.0000
597.28	49.53	0.0000
Reference

Fixed		Measured
Pressure, kPa - Liquid	Temperature, K - Liquid	Viscosity, Pa*s - Liquid
101.00	297.80	0.0005
Reference

Fixed		Measured
Pressure, kPa - Liquid	Temperature, K - Liquid	Viscosity, Pa*s - Liquid
101.00	303.15	0.0005
Reference

Refractive index (Na D-line)

Fixed		Measured
Pressure, kPa - Liquid	Temperature, K - Liquid	Refractive index (Na D-line) - Liquid
100.00	298.15	1.3267
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Refractive index (Na D-line) - Liquid
298.15	100.00	1.3265
Reference

Mass density, kg/m3

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
298.26	235.00	785.98
298.26	5000.00	790.69
298.26	9999.00	795.4
298.26	15013.00	799.88
298.26	19987.00	804.1
298.26	25008.00	808.17
298.26	29997.00	812.04
298.26	34991.00	815.76
298.26	39981.00	819.34
323.22	270.00	762.14
323.22	4990.00	767.53
323.22	9984.00	772.87
323.22	14982.00	777.91
323.22	19989.00	782.69
323.22	24986.00	787.21
323.22	29995.00	791.53
323.22	34987.00	795.64
323.22	39993.00	799.6
348.25	366.00	737.29
348.25	4987.00	743.46
348.25	9986.00	749.65
348.25	14991.00	755.42
348.25	20004.00	760.84
348.25	25020.00	765.94
348.25	30013.00	770.76
348.25	34989.00	775.32
348.25	40000.00	779.7
373.26	534.00	710.55
373.26	4983.00	717.67
373.26	9990.00	724.99
373.26	14998.00	731.69
373.26	19985.00	737.88
373.26	24994.00	743.68
373.26	29997.00	749.13
373.26	35001.00	754.27
373.26	39996.00	759.14
398.28	934.00	680.93
398.28	4984.00	689.0
398.28	9998.00	697.91
398.28	14986.00	705.88
398.28	19987.00	713.16
398.28	24992.00	719.87
398.28	29991.00	726.11
398.28	35005.00	731.99
398.28	40004.00	737.47
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
298.15	100.00	792.6
298.15	5000.00	796.2
298.15	9900.00	801.0
298.15	19700.00	808.4
298.15	29500.00	816.0
298.15	39300.00	823.8
298.15	49100.00	830.0
298.15	58900.00	836.3
323.15	100.00	770.3
323.15	5000.00	774.2
323.15	9900.00	778.2
323.15	19700.00	787.0
323.15	29500.00	795.0
323.15	39300.00	803.4
323.15	49100.00	811.0
323.15	58900.00	818.2
348.15	5000.00	748.9
348.15	9900.00	753.9
348.15	19700.00	764.1
348.15	29500.00	773.1
348.15	39300.00	782.6
348.15	49100.00	790.9
348.15	58900.00	798.9
373.15	5000.00	721.1
373.15	9900.00	727.7
373.15	19700.00	739.3
373.15	29500.00	750.4
373.15	39300.00	760.2
373.15	49100.00	769.6
373.15	58900.00	778.2
398.15	5000.00	690.0
398.15	9900.00	697.6
398.15	19700.00	712.8
398.15	29500.00	725.4
398.15	39300.00	736.0
398.15	49100.00	747.2
398.15	58900.00	757.0
423.15	5000.00	652.8
423.15	9900.00	665.2
423.15	19700.00	683.6
423.15	29500.00	698.8
423.15	39300.00	710.8
423.15	49100.00	723.9
423.15	58900.00	735.0
448.15	5000.00	610.4
448.15	9900.00	628.9
448.15	19700.00	652.4
448.15	29500.00	670.8
448.15	39300.00	685.6
448.15	49100.00	700.0
448.15	58900.00	713.0
473.15	5000.00	553.4
473.15	9900.00	585.0
473.15	19700.00	620.2
473.15	29500.00	642.0
473.15	39300.00	660.6
473.15	49100.00	677.2
473.15	58900.00	691.2
498.15	9900.00	525.0
498.15	19700.00	584.8
498.15	29500.00	613.4
498.15	39300.00	636.0
498.15	49100.00	655.0
498.15	58900.00	670.0
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
298.26	235.00	785.98
298.26	5000.00	790.69
298.26	9999.00	795.4
298.26	15013.00	799.88
298.26	19987.00	804.1
298.26	25008.00	808.17
298.26	29997.00	812.04
298.26	34991.00	815.76
298.26	39981.00	819.34
323.22	270.00	762.14
323.22	4990.00	767.53
323.22	9984.00	772.87
323.22	14982.00	777.91
323.22	19989.00	782.69
323.22	24986.00	787.21
323.22	29995.00	791.53
323.22	34987.00	795.64
323.22	39993.00	799.6
348.25	366.00	737.29
348.25	4987.00	743.46
348.25	9986.00	749.65
348.25	14991.00	755.42
348.25	20004.00	760.84
348.25	25020.00	765.94
348.25	30013.00	770.76
348.25	34989.00	775.32
348.25	40000.00	779.7
373.26	534.00	710.55
373.26	4983.00	717.67
373.26	9990.00	724.99
373.26	14998.00	731.69
373.26	19985.00	737.88
373.26	24994.00	743.68
373.26	29997.00	749.13
373.26	35001.00	754.27
373.26	39996.00	759.14
398.28	934.00	680.93
398.28	4984.00	689.0
398.28	9998.00	697.91
398.28	14986.00	705.88
398.28	19987.00	713.16
398.28	24992.00	719.87
398.28	29991.00	726.11
398.28	35005.00	731.99
398.28	40004.00	737.47
Reference

Fixed		Measured
Pressure, kPa - Liquid	Temperature, K - Liquid	Mass density, kg/m3 - Liquid
1000.00	303.20	783.0
2000.00	303.20	784.0
3000.00	303.20	785.0
4000.00	303.20	786.0
5000.00	303.20	787.0
6000.00	303.20	788.0
7000.00	303.20	788.9
8000.00	303.20	789.9
9000.00	303.20	790.9
10000.00	303.20	791.8
1000.00	323.20	762.8
2000.00	323.20	763.9
3000.00	323.20	765.0
4000.00	323.20	766.2
5000.00	323.20	767.3
6000.00	323.20	768.3
7000.00	323.20	769.4
8000.00	323.20	770.5
9000.00	323.20	771.5
10000.00	323.20	772.6
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
298.15	100.00	786.57
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
298.15	100.00	786.53
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
288.15	100.00	796.19
288.15	5000.00	800.57
288.15	10000.00	804.93
288.15	15000.00	808.85
288.15	20000.00	812.92
288.15	25000.00	816.56
288.15	30000.00	820.09
288.15	35000.00	823.62
288.15	40000.00	827.04
293.15	100.00	791.18
293.15	5000.00	795.97
293.15	10000.00	800.47
293.15	15000.00	804.52
293.15	20000.00	808.43
293.15	25000.00	812.34
293.15	30000.00	815.93
293.15	35000.00	819.32
293.15	40000.00	822.48
298.15	100.00	786.76
298.15	5000.00	791.52
298.15	10000.00	795.8
298.15	15000.00	800.13
298.15	20000.00	804.18
298.15	25000.00	808.04
298.15	30000.00	811.69
298.15	35000.00	815.2
298.15	40000.00	818.33
303.15	100.00	782.07
303.15	5000.00	786.79
303.15	10000.00	791.31
303.15	15000.00	795.85
303.15	20000.00	800.16
303.15	25000.00	804.08
303.15	30000.00	807.78
303.15	35000.00	811.31
303.15	40000.00	814.7
308.15	100.00	777.09
308.15	5000.00	781.85
308.15	10000.00	786.63
308.15	15000.00	791.23
308.15	20000.00	795.58
308.15	25000.00	799.85
308.15	30000.00	803.73
308.15	35000.00	807.42
308.15	40000.00	811.08
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
298.15	81.50	786.55
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
293.15	100.00	791.15
293.15	5000.00	795.92
293.15	10000.00	800.41
293.15	15000.00	804.64
293.15	20000.00	808.67
293.15	25000.00	812.52
293.15	30000.00	816.25
293.15	35000.00	819.89
303.15	100.00	781.84
303.15	5000.00	786.9
303.15	10000.00	791.61
303.15	15000.00	796.01
303.15	20000.00	800.14
303.15	25000.00	804.05
303.15	30000.00	807.78
303.15	35000.00	811.37
313.15	100.00	772.35
313.15	5000.00	777.48
313.15	10000.00	782.37
313.15	15000.00	786.99
313.15	20000.00	791.38
313.15	25000.00	795.59
313.15	30000.00	799.69
313.15	35000.00	803.73
Reference

Fixed		Measured
Pressure, kPa - Liquid	Temperature, K - Liquid	Mass density, kg/m3 - Liquid
100.00	283.15	800.54
100.00	293.15	791.23
100.00	298.15	786.51
100.00	303.15	781.96
100.00	313.15	772.43
100.00	318.15	767.47
100.00	323.15	762.78
100.00	328.15	757.83
100.00	333.15	752.96
2500.00	283.15	802.75
2500.00	293.15	793.52
2500.00	298.15	788.81
2500.00	303.15	784.36
2500.00	313.15	774.99
2500.00	318.15	770.09
2500.00	323.15	765.48
2500.00	328.15	760.61
2500.00	333.15	755.84
5000.00	283.15	804.88
5000.00	293.15	795.8
5000.00	298.15	791.18
5000.00	303.15	786.78
5000.00	313.15	777.53
5000.00	318.15	772.74
5000.00	323.15	768.2
5000.00	328.15	763.41
5000.00	333.15	758.73
10000.00	283.15	809.06
10000.00	293.15	800.17
10000.00	298.15	795.7
10000.00	303.15	791.48
10000.00	313.15	782.45
10000.00	318.15	777.79
10000.00	323.15	773.39
10000.00	328.15	768.75
10000.00	333.15	764.21
15000.00	283.15	813.06
15000.00	293.15	804.36
15000.00	298.15	800.02
15000.00	303.15	795.84
15000.00	313.15	787.08
15000.00	318.15	782.57
15000.00	323.15	778.3
15000.00	328.15	773.73
15000.00	333.15	769.39
20000.00	283.15	816.88
20000.00	293.15	808.39
20000.00	298.15	804.15
20000.00	303.15	799.97
20000.00	313.15	791.5
20000.00	318.15	787.09
20000.00	323.15	782.93
20000.00	328.15	778.49
20000.00	333.15	774.25
25000.00	283.15	820.6
25000.00	293.15	812.25
25000.00	298.15	808.1
25000.00	303.15	803.95
25000.00	313.15	795.74
25000.00	318.15	791.43
25000.00	323.15	787.34
25000.00	328.15	783.03
25000.00	333.15	778.87
30000.00	283.15	824.14
30000.00	293.15	815.94
30000.00	298.15	811.88
30000.00	303.15	807.83
30000.00	313.15	799.72
30000.00	323.15	791.56
30000.00	333.15	783.33
35000.00	283.15	827.58
35000.00	293.15	819.55
35000.00	298.15	815.52
35000.00	303.15	811.51
35000.00	313.15	803.62
35000.00	323.15	795.6
35000.00	333.15	787.53
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	1259.391
253.15	5031.00	1283.569
253.15	10064.00	1307.272
253.15	15070.00	1329.88
253.15	20048.00	1351.494
253.15	25130.00	1372.789
253.15	30260.00	1393.514
273.15	101.00	1187.324
273.15	5017.00	1213.77
273.15	10158.00	1240.041
273.15	15070.00	1264.004
273.15	20132.00	1287.633
273.15	25155.00	1310.139
273.15	30074.00	1331.42
293.15	101.00	1119.106
293.15	5028.00	1147.798
293.15	10032.00	1175.493
293.15	15145.00	1202.422
293.15	20159.00	1227.564
293.15	25062.00	1251.109
293.15	30276.00	1275.096
313.15	101.00	1053.178
313.15	5046.00	1084.848
313.15	10127.00	1115.409
313.15	15085.00	1143.55
313.15	19989.00	1169.962
313.15	25090.00	1196.105
313.15	30009.00	1220.145
333.15	101.00	988.923
333.15	5029.00	1023.676
333.15	10110.00	1056.926
333.15	15215.00	1088.157
333.15	20093.00	1116.297
333.15	25061.00	1143.501
333.15	30122.00	1169.869
353.15	197.00	925.583
353.15	5097.00	963.758
353.15	10106.00	999.623
353.15	15143.00	1033.012
353.15	20216.00	1064.48
353.15	25221.00	1093.69
353.15	30092.00	1120.591
Reference

Operational condition: Frequency, MHz = 8 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Speed of sound, m/s - Liquid
299.95	99.00	1096.3
220.38	100.00	1387.9
244.25	125.00	1294.5
349.98	201.00	935.8
244.27	761.00	1297.5
399.94	798.00	770.2
299.94	963.00	1101.7
349.98	970.00	941.9
399.94	1015.00	772.5
220.41	1023.00	1391.8
244.28	1200.00	1299.5
220.39	1839.00	1395.3
244.30	1980.00	1303.2
349.98	1998.00	949.9
399.94	2112.00	784.4
299.94	2240.00	1109.5
450.22	2562.00	568.3
349.98	4864.00	971.5
450.19	4910.00	608.8
244.31	5110.00	1317.8
399.93	5110.00	815.0
299.95	5128.00	1126.7
399.92	9339.00	854.2
500.06	9535.00	412.8
244.32	9712.00	1338.5
349.97	9858.00	1006.8
299.95	9896.00	1153.8
220.96	10454.00	1428.5
450.22	14312.00	730.4
499.98	19828.00	611.1
349.99	19881.00	1070.5
220.46	20095.00	1467.9
450.20	20347.00	794.1
299.96	21093.00	1212.5
399.92	21337.00	948.3
499.94	28092.00	708.5
500.06	30612.00	733.2
450.18	39568.00	943.1
499.94	40326.00	818.5
220.39	40357.00	1540.1
299.96	40780.00	1302.9
350.00	41608.00	1186.3
399.89	42375.00	1078.3
299.95	58877.00	1375.6
450.17	59905.00	1062.6
499.94	60313.00	955.4
349.95	60336.00	1270.3
220.26	60890.00	1606.5
399.90	61164.00	1172.4
220.38	69376.00	1631.5
220.37	69581.00	1632.2
450.20	72355.00	1124.9
299.94	80229.00	1452.1
399.91	81158.00	1258.6
349.96	82312.00	1356.2
399.93	84741.00	1273.4
399.73	98358.00	1325.1
299.95	98460.00	1511.3
349.96	99275.00	1415.9
220.37	111490.00	1746.8
399.91	122977.00	1409.6
299.96	123414.00	1585.5
349.97	124114.00	1495.1
Reference

Thermal diffusivity, m2/s

Fixed		Measured
Pressure, kPa - Liquid	Temperature, K - Liquid	Thermal diffusivity, m2/s - Liquid
0.00	299.15	9.7000e-08
370000.00	300.15	1.3500e-07
400000.00	299.85	1.3200e-07
860000.00	300.95	1.5700e-07
880000.00	299.15	1.5900e-07
1290000.00	301.05	1.7000e-07
1290000.00	301.05	1.6600e-07
1750000.00	300.75	1.8000e-07
2430000.00	299.15	1.8600e-07
3100000.00	299.15	1.9200e-07
3120000.00	299.15	1.9900e-07
4220000.00	298.15	2.1700e-07
5000000.00	299.75	2.3700e-07
5300000.00	297.95	2.1900e-07
Reference

Molar volume, m3/mol

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Molar volume, m3/mol - Liquid
298.15	100.00	0.0000
298.15	10000.00	0.0000
313.15	100.00	0.0000
313.15	10000.00	0.0000
328.15	100.00	0.0000
328.15	10000.00	0.0000
Reference

Correlations

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 4027.94]	kPa	[257.16; 472.60]	The Yaw...
Equation			ln(Pvp) = A + B/(T + C)
Coefficient A			1.65992e+01
Coefficient B			-3.63914e+03
Coefficient C			-3.40540e+01
Temperature range, min.			257.16
Temperature range, max.			472.60
Pvap	1.33	kPa	257.16	Calculated Property
Pvap	6.48	kPa	281.10	Calculated Property
Pvap	23.80	kPa	305.04	Calculated Property
Pvap	70.79	kPa	328.97	Calculated Property
Pvap	178.78	kPa	352.91	Calculated Property
Pvap	396.68	kPa	376.85	Calculated Property
Pvap	793.19	kPa	400.79	Calculated Property
Pvap	1456.93	kPa	424.72	Calculated Property
Pvap	2494.65	kPa	448.66	Calculated Property
Pvap	4027.94	kPa	472.60	Calculated Property
Pvap	[1.06e-04; 8099.01]	kPa	[175.47; 512.58]	KDB Vap...
Equation			ln(Pvp) = A + B/T + C*ln(T) + D*T^2
Coefficient A			7.90941e+01
Coefficient B			-7.02920e+03
Coefficient C			-9.37282e+00
Coefficient D			7.99273e-06
Temperature range, min.			175.47
Temperature range, max.			512.58
Pvap	1.06e-04	kPa	175.47	Calculated Property
Pvap	0.02	kPa	212.93	Calculated Property
Pvap	0.78	kPa	250.38	Calculated Property
Pvap	9.61	kPa	287.84	Calculated Property
Pvap	61.07	kPa	325.30	Calculated Property
Pvap	251.59	kPa	362.75	Calculated Property
Pvap	771.81	kPa	400.21	Calculated Property
Pvap	1927.87	kPa	437.67	Calculated Property
Pvap	4162.73	kPa	475.12	Calculated Property
Pvap	8099.01	kPa	512.58	Calculated Property

Similar Compounds

Find more compounds similar to Methyl Alcohol.

Mixtures

• Benzene, chloro- + Methyl Alcohol
• Benzene, bromo- + Methyl Alcohol
• Dimethyl methylphosphonate + Methyl Alcohol
• Methyl Alcohol + Dimethyl phosphonate
• 2,6-Lutidine + Methyl Alcohol
• Pyridine, 2-methyl- + Methyl Alcohol
• Pyridine, 2,4,6-trimethyl- + Methyl Alcohol
• Isobutane + Methyl Alcohol
• Butane, 2-ethoxy-2-methyl- + Methyl Alcohol
• Butane, 2-ethoxy-2-methyl- + Methyl Alcohol + Water
• Carbonic acid, dimethyl ester + Methyl Alcohol
• Piperazine, 1-methyl- + Methyl Alcohol
• Pentane, 2-methyl- + Methyl Alcohol
• Cyclohexane, methyl- + Methyl Alcohol
• Formamide, N,N-dimethyl- + Pentane, 2-methyl- + Methyl Alcohol
• Formamide, N,N-dimethyl- + Cyclohexane, methyl- + Methyl Alcohol
• Benzene + Methyl Alcohol
• n-Hexane + Methyl Alcohol
• Butane, 2-methoxy-2-methyl- + Methyl Alcohol
• n-Hexane + Butane, 2-methoxy-2-methyl- + Methyl Alcohol

Find more mixtures with Methyl Alcohol.

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
• Thermodynamic Properties of Methanol in the Critical and Supercritical Regions
• Volumetric Properties of the Ionic Liquid, 1-Butyl-3-methylimidazolium Tetrafluoroborate, in Organic Solvents at T = 298.15 K
• Thermophysical Properties of Binary Mixtures of Methanol with Chlorobenzene and Bromobenzene from 293K to 313K
• Densities and Viscosities of Binary Mixtures of Methanol with Dimethyl Methylphosphonate and Dimethyl Phosphite from (293.15 to 333.15) K
• Viscosity of Associated Mixtures Approximated by the Grunberg-Nissan Model
• Volumetric Properties of Binary Mixtures of 2,4,6-Trimethylpyridine with 1,2-Ethanediol, Methanol, and Water, and the Association Energies of the O-H***N Bonded Complexes
• Solubility of Baicalein in Different Solvents from (287 to 323) K
• Liquid liquid equilibria for pseudoternary systems: isooctane benzene (methanol +water)
• 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
• 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
• Determination of activity coefficients at infinite dilution of organic solutes in the ionic liquid, trihexyl(tetradecyl)-phosphonium tris(pentafluoroethyl) trifluorophosphate, by gas liquid chromatography
• Measurements of isothermal vapor-liquid equilibrium of binary methanol/dimethyl carbonate system under pressure
• 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
• Study of thermodynamic properties of binary solutions of lithium bromide or lithium chloride with methanol
• 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
• Solubility of aspirin in supercritical carbon dioxide/alcohol mixtures
• 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
• Liquid liquid equilibrium in ternary systems N,N-dimethylformamide + 2-methylpentane + methanol and N,N-dimethylformamide + methylcyclohexane + methanol
• Phase equilibria of methanol triolein system at elevated temperature and pressure
• Effect of temperature on the excess molar volumes of some alcohol + aromatic mixtures and modelling by cubic EOS mixing rules
• Vapour liquid equilibrium of octane enhancing additives in gasolines 7: Total pressure data and gE for the ternary mixture tert-amyl methyl ether (TAME), methanol and hexane at 313.15K
• Henry s law constants of propane, propene, butane, and 2-methylpropane in methanol at 374-490K
• Excess molar enthalpies for mixtures of carbon dioxide + a modifier (5 mol% methanol or 1-octanol) and hexane at 308.15K and 12.40MPa
• Vapor liquid liquid equilibria of perfluorohexane +CO2 + methanol, +toluene, and +acetone at 313K
• Effect of anion fluorination in 1-ethyl-3-methylimidazolium as solvent for the liquid extraction of ethanol from ethyl tert-butyl ether
• 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
• Volumetric behavior of water methanol mixtures in the vicinity of the critical region
• Liquid liquid equlibria of the system dimethyl carbonate + methanol +water at different temperatures
• Isothermal vapour liquid equilibrium with chemical reaction in the quaternary water + methanol + acetic acid + methyl acetate system, and in five binary subsystems
• Henry s law constants of 1-butene, 2-methylpropene, trans-2-butene, and 1,3-butadiene in methanol at 374 490K
• Vapor pressure measurement for binary and ternary systems containing a phosphoric ionic liquid
• Liquid liquid equilibria of aqueous mixtures containing selected dibasic esters and/or methanol
• Activity coefficients of the species in the methanol solutions of acetaminophen and two silylated derivatives at 298.15K
• Isobaric vapor liquid equilibria for acetone + methanol + lithium nitrate at 100 kPa
• Isochoric heat capacity measurements for H2O+CH3OH mixture in the near-critical and supercritical regions
• Measurement and correlation of vapor liquid equilibria for methanol + methyl laurate and methanol + methyl myristate systems near critical temperature of methanol
• Isobaric vapor liquid equilibria of 1,1-dimethylethoxy-butane + methanol or ethanol +water at 101.32 kPa
• Vapour liquid equilibrium for the systems butane + methanol, +2-propanol, +1-butanol, +2-butanol, +2-methyl-2-propanol at 364.5K
• Vapor pressure measurement for water, methanol, ethanol, and their binary mixtures in the presence of an ionic liquid 1-ethyl-3-methylimidazolium dimethylphosphate
• 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
• Solubilities of rutin in eight solvents at T = 283.15, 298.15, 313.15, 323.15, and 333.15K
• Solubility of ammonia in liquid mixtures of (water + methanol)
• Limiting activity coefficients in binary mixtures of 1-alkanols and ethylbenzene
• Thermodynamic properties of mixtures containing alkoxypropanol and n-alkanol
• Solubilities of betulin in chloroform + methanol mixed solvents at T = (278.2, 288.2, 293.2, 298.2, 308.2 and 313.2) K
• Vapour liquid equilibria, azeotropic data, excess enthalpies, activity coefficients at infinite dilution and solid liquid equilibria for binary alcohol ketone systems
• 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
• A new high-pressure vapour liquid equilibrium apparatus
• Isobaric vapour liquid equilibria of binary 1-propoxy-2-propanol mixtures with water and alcohols at reduced pressure
• 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
• Solubility of antioxidant 1010 in pure alkanols
• Vapor liquid equilibrium in the n-butane +methanol system, measurement and modeling from 323.2 to 443.2K
• Activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid 1-butyl-1-methylpyrrolidinium trifluoromethanesulfonate using GLC
• Phase equilibria of glycerol containing systems and their description with the Cubic-Plus-Association (CPA) Equation of State
• Ultrasonic study on binary mixture containing dimethylformamide and methanol over the entire miscibility range (0less thanxless than1) at temperatures 303 323K
• Measurement and calculation of vapor liquid equilibria for methanol + glycerol and ethanol + glycerol systems at 493 573K
• 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
• (Liquid + liquid) equilibria of the quaternary sysytem methanol + isooctane + cyclohexane + benzene at T = 303.15 K
• Solubilities of N-[(4-bromo- 3,5 - difluorine) phenyl]-acrylamide in methanol-ethanol solution
• Compact apparatus for rapid measurement of high-pressure phase equilibria of carbon dioxide expanded liquids
• Volumetric properties of ionic liquid 1,3-dimethylimidazolium methyl sulfate + molecular solvents at T = (298.15 - 328.15) K
• Phase behavior of the ternary 1-hexyl-3-methylimidazolium tetrafluoroborate + carbon dioxide + methanol system
• Solubility of CF4 in lower alcohols
• High-pressure phase behavior of ternary systems (carbon dioxide + alkanol + hydrophobic ionic liquid)
• Thermodynamic properties of new heat pump working pairs: 1,3-Dimethylimidazolium dimethylphosphate and water, ethanol and methanol
• Gas-liquid chromatography measurements of activity coefficients at infinite dilution of hydrocarbons and alkanols in 1-alkyl-3-methylimidazolium bis(oxalato)borate
• Volumetric behavior and solution microstructure of methanol-water mixture in sub- and supercritical state via density measurement and MD simulation
• Activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-ethyl-3-methylimidazolium methanesulfonate
• Liquid-liquid equilibria for mixtures containing water, methanol, fatty acid methyl esters, and glycerol
• Vapor-liquid and liquid-liquid equilibrium properties of ethane + methanol system at ambient temperature
• Solubility of HFCs in lower alcohols
• Effect of mono-, di- and tri-ethanolammonium tetrafluoroborate protonic ionic liquids on the volatility of water, ethanol, and methanol
• The viscosity of the binary vapor mixture methanol triethylamine at low densities and in the saturated vapor phase of the vapor liquid equilibrium
• Influence of temperature on the (liquid + liquid) equilibria of {methanol + benzene + hexane} ternary system
• Thermophysical properties of pure 1-ethyl-3-methylimidazolium methylsulfate and its binary mixtures with alcohols
• Experimental measurement and modeling of solubility of LiBr and LiNO3 in methanol, ethanol, 1-propanol, 2-propanol and 1-butanol
• Vapor-liquid equilibria of ternary systems with 1-ethyl-3-methylimidazolium ethyl sulfate using headspace gas chromatography
• Liquid-liquid equilibria for systems of water + methanol + methyl anthranilate at several temperatures
• Isothermal vapor-liquid equilibria for methanol and 2,3-dimethyl-2-butene at 343.15 K, 353.15 K, 363.15 K, 373.15 K
• Selection of entrainers for the separation of the binary azeotropic system methanol + dimethyl carbonate by extractive distillation
• A new semi-empirical model for correlating the solubilities of solids in supercritical carbon dioxide with cosolvents
• Solubility of L-phenylalanine in water and different binary mixtures from 288.15 to 318.15 K
• Solid-liquid equilibrium data for the binary system methacrylic acid + methanol in the high methacrylic acid concentration range
• 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
• Ternary liquid-liquid equilibria of bis(trifluoromethylsulfonyl)-amide based ionic liquids + methanol + heptane
• Determination of the solubility, dissolution enthalpy and entropy of pyrene in different solvents
• Thermodynamics of the solubility of lomefloxacin in methanol, ethanol, 1-propanol, 2-propanol, acetone, and chloroform from 293.15 to 323.15 K
• Phase behavior for carbon dioxide/tetraalkoxysilane systems
• 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
• 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
• Solubility of chlocyphos in different solvents
• Determination of the solubility, dissolution enthalpy and entropy of suberic acid in different solvents
• Prediction of different thermodynamic properties for systems of alcohols and sulfate-based anion Ionic Liquids using modified UNIFAC
• A novel static analytical apparatus for phase equilibrium measurements
• Ternary liquid liquid equilibria of trifluorotris(perfluoroethyl)phosphate based ionic liquids + methanol + heptane
• Solubility of puerarin in the binary system of methanol and acetic acid solvent mixtures
• Isobaric vapor liquid equilibrium for binary system of methanol and acetonitrile
• Influence of sulfate-based anion ionic liquids on the separation factor of the binary azeotropic system acetone + methanol
• 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
• Solubility of succinic acid in different aqueous solvent mixtures: Experimental measurement and thermodynamic modeling
• Investigation on vapor liquid equilibrium for 2-propanol + 1-butanol + 1-pentanol at 101.3 kPa
• Solubility of dimethyl fumarate in water + (methanol, ethanol, 1-propanol) from (278.15 to 333.15) K
• 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
• (Liquid-liquid) equilibria for ternary and quaternary systems of representative compounds of gasoline + methanol at 293.15 K: Experimental data and correlation
• Solubility and pseudopolymorphic transitions in mixed solvent: Meropenem in methanol-water solution
• 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
• Isobaric vapor-liquid equilibrium for methanol + dimethylcarbonate + phosphoric-based ionic liquids
• Using binary mixtures of dicationic ionic liquids for determination ofactivity coefficients at infinite dilution by gas-liquid chromatography
• 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
• Measurement and correlation of the solubility of 4,4'-oxydianiline in different organic solvents
• 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
• Isobaric vapor-liquid equilibrium at 101.3 kPa and excess properties at 298.15 K for binary mixtures of methyl phenyl carbonate with methanol or dimethyl carbonate
• Determination and correlation of solubilities of 1,2-bis(2-oxo-5,5-dimethyl-1,3,2-dioxyphosphacyclohexyl-2-imino) ethane in selected solvents
• Vapor-Liquid Equilibrium for Tetrahydrofuran + Methanol + Tetrafluoroborate-based ionic liquids at 101.3 kPa
• Measurements of activity coefficients at infinite dilution in vegetable oils and capric acid using the dilutor technique
• Towards automated characterisation of liquid-liquid equilibria
• The solubility of mercaptosuccinic acid in water + (methanol, ethanol, acetone) mixtures from (278.15 to 333.15 K)
• Solubility of androstenedione in lower alcohols
• Excess molar volumes and excess molar enthalpies in binary systems N-alkyl-triethylammonium bis(trifluoromethylsulfonyl)imide +methanol
• Solid-liquid equilibrium of dicyandiamide in different solvents
• Measurement and correlation of the solubility of maleic anhydride in different organic solvents
• Isobaric vapor-liquid equilibria of the binary mixtures propylene glycol methyl ether + propylene glycol methyl ether acetate, methyl acetate + propylene glycol methyl ether and methanol + propylene glycol methyl ether acetate at 101.3 kPa
• Thermodynamics of fenofibrate and solubility in pure organic solvents
• Thermodynamic models for determination of the solubility of 2, 5-bis(2-furylmethylidene) cyclopentan-1-one in different solvents at temperatures ranging from 308.15 to 403.15 K.
• Measurement and correlation of the solubilities of tetra(5,5-dimethyl-1,3-dioxaphosphorinanyl-2-oxy) neopentane in different pure solvents
• Present status of the modified UNIFAC Model for the prediction of phase equilibria and excess enthalpies for systems with ionic liquids
• Thermostabilities and solubilities of flame retardant bisphenol S-bis (5,5-dimethyl-1,3-dioxaphosphorinanyl-2-oxy phosphate ester) as a function of temperature
• Solubility and polymorphic forms of antibiotic lasalocid sodium in different organic solvents
• Measurement and correlation for the solubility of dimethyl succinylsuccinate in (methanol + water) and (methanol + dimethyl succinate) binary solvent mixtures
• Thermodynamics of risperidone and solubility in pure organic solvents
• Solid-liquid equilibrium and thermodynamic of 2,5-thiophenedicarboxylic acid in different organic solvents
• Solid-liquid equilibria and the physical properties of binary systems of diphenyl carbonate, dimethyl carbonate, methyl phenyl carbonate, anisole, methanol and phenol
• 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
• Ternary liquid-liquid equilibria and binary excess and deviation properties at constant temperature for mixtures of dimethyl carbonate, anisole, methanol, phenol and water
• Effect of bivalent cation inorganic salts on isobaric vapor-liquidequilibrium of methyl acetate - methanol system
• Solubility and preferential solvation of sulfadiazine inmethanol + water mixtures at several temperatures
• 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
• Experimental isobaric vapor-liquid equilibrium at atmospheric and sub-atmospheric pressures, excess molar volumes and deviations in molar refractivity from 293.15 K to 318.15 K of diisopropyl ether with methanol and isopropyl alcohol.
• A study on the liquid-liquid equilibrium of 1-alkyl-3-methylimidazolium dialkylphosphate with methanol and dimethyl carbonate
• Separation of acetone and methanol azeotropic system using ionic liquid as entrainer
• Thermodynamic properties of cyclohexane methanol liquid mixture from shear viscosity measurements
• Study of interaction between organic compounds and mono or dicationic oxygenated ionic liquids using gas chromatography
• Solubility and thermodynamic functions of cefazolin acid in pure and mixed solvents at (278.15 308.15) K
• 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
• Temperature dependent solubility of sodium cyclamate in selected pure solvents and binary methanol + water mixed solvents
• Absorption of CO2 with methanol and ionic liquid mixture at low temperatures
• Thermodynamic analysis for solid liquid equilibrium of mercaptosuccinic acid in a binary solvent of methanol and ethyl acetate at temperatures between (278.15 and 333.15) K
• 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
• Separation of methyl acetate + methanol azeotropic mixture using ionic liquids as entrainers
• Excess volumes and excess heat capacities of {1,2- alkanediol + methanol} mixtures and ionic volumes in these systems
• Phase equilibria of (water + propionic acid or butyric acid + 2-methoxy- 2-methylpropane) ternary systems at 298.2 K and 323.2 K
• Measurement and correlation of solubility and dissolution properties of flunixin meglumine in pure and binary solvents
• Measurement of vapor-liquid-liquid phase equilibrium - Equipment and results
• 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
• Isobaric (vapor-liquid) equilibria for binary systems of methanol + 1-(methoxymethoxy)- propane and 1-propanol + 1-(methoxymethoxy)-propane at 101.33 kPa
• Isobaric ternary vapour-liquid equilibrium of methanol(1) + diisopropyl ether(2) + isopropyl alcohol(3) along with methanol + isopropyl alcohol binary data at atmospheric and sub-atmospheric pressures
• Determination and prediction of solubilities of active pharmaceutical ingredients in selected organic solvents
• Isobaric vapor-liquid equilibrium for methyl acetate + methanol system containing different ionic liquids at 101.3 kPa
• Experimental isobaric vapor-liquid equilibrium for the binary and ternary systems with methanol, methyl acetate and dimethyl sulfoxide at 101.3 kPa
• Activity coefficients at infinite dilution for different alcohols and ketones in [EMpy][ESO4]: Experimental data and modeling with PC-SAFT
• Phase equilibria of triolein to biodiesel reactor systems
• Experimental vapour - liquid equilibrium data of the quaternary system Methanol (1) + Isopropyl Alcohol (2) + Water (3) + Glycerol (4) along with Isopropyl Alcohol (2) + Glycerol (4) and Isopropyl Alcohol (2) + Water (3) binary data at atmospheric and sub-atmospheric pressures.
• Measurement and correlation of liquid-liquid equilibrium for the ternary system 2,2,3,3,4,4,5,5-octafluoro-1-pentanol + methanol + water at (298.15, 308.15, and 318.15) K
• Thermal properties and solubility of methyl a-D-glucopyranoside in methanol at different temperatures
• Limiting activity coefficient measurements in binary mixtures of dichloromethane and 1-alkanols (C1 - C4)
• Vapor-liquid equilibria of binary and ternary mixtures containing ethyl lactate and effect of ethyl lactate as entrainer
• Measurement of binary diffusion coefficient and solubility estimation for dyes in supercritical carbon dioxide by CIR method
• 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
• Bubble point pressures of binary system of methanol and methyl propionate
• High pressure vapor-liquid equilibria for binary methane and protic ionic liquid based on propionate anions
• Measurement and correlation of isobaric vapor-liquid equilibria of methanol + tetrahydrofuran + 1-alkyl-3-methylimidazolium bis(trifluoromethylsulfonyl)imide at 101.3 kPa
• Ionic liquid 1-ethyl-3-methylimidazolium tetracyanoborate: An efficient entrainer to separate methanol + dimethyl carbonate azeotropic mixture
• Measurement and correlation of ternary vapor-liquid equilibria for methanol + glycerol + fatty acid methyl ester (methyl laurate, methyl myristate, methyl palmitate) systems at elevated temperatures and pressures
• Liquid-liquid equilibrium in binary and ternary mixtures containing formaldehyde, water, methanol, methylal, and poly(oxymethylene) dimethyl ethers
• Isobaric vapor-liquid equilibrium for methanol + methyl ethyl ketone + bis(trifluoromethylsulfonyl)imide-based ionic liquids at 101.3 kPa
• Determination and correlation of solubility and solution thermodynamics of ethenzamide in different pure solvents
• Measurement and prediction of phase equilibria of ethylene + vinyl acetate + methanol + poly(ethylene-co-vinyl acetate) systems
• Determination and correlation of solubility of linezolid form II in different pure and binary solvents
• Separation of methanol + dimethyl carbonate azeotropic mixture using ionic liquids as entrainers
• Effect of composition and temperature variations on thermophysical properties of binary and ternary mixtures of 1-ethyl-3-methylimidazolium ethylsulfate with 1-butanol and /or methanol
• In situ measurement of liquid-liquid equilibria by medium field nuclear magnetic resonance
• Evaluation of the solvent structural effect upon the vapor-liquid equilibrium of [C4C1im][Cl] + Alcohols
• Isobaric vapor-liquid equilibrium for ternary mixtures of acetone + methanol + ionic liquids at 101.3kPa
• 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
• 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
• Partial molar volume of NaCl and CsCl in mixtures of water and methanol by experiment and molecular simulation
• Isobaric vapor-liquid equilibrium for acetone + methanol system containing different ionic liquids at 101.3 kPa
• Gas solubilities of carbon dioxide in methanol, acetone, mixtures of methanol and water, and mixtures of methanol and acetone
• 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
• Ternary liquid-liquid equilibrium of an azeotropic mixture (hexane + methanol) with different imidazolium-based ionic liquids at T = 298.15 K and 101.325 kPa
• 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
• Extractive distillation of methylal/methanol mixture using ethylene glycol as entrainer
• Solubility of carbon dioxide in methanol from 213.15 K to 273.15 K: Measurement and modeling
• Liquid-liquid equilibria of water + solutes (acetic acid/ acetol/furfural/guaiacol/methanol/phenol/propanal) + solvents (isopropyl acetate/toluene) ternary systems for pyrolysis oil fractionation
• Solubility evaluation and thermodynamic modeling of beta-lapachone in water and ten organic solvents at different temperatures
• Solubility of 1-methyl-4-nitropyrazole in seventeen pure solvents at temperatures from 283.15 K to 323.15 K
• Isobaric vapor-liquid equilibrium for methanol + methyl acetate with ionic liquids [OMMIM][Tf2N] and [OMIM][Tf2N] as entrainers at 101.3 kPa
• Tetramethylammonium chloride + glycerol deep eutectic solvent as separation agent for organic liquid mixtures: Assessment from experimental limiting activity coefficients
• Thermodynamics and activity coefficients at infinite dilution for organic solutes in the ionic liquid 1-butyl-1-methylpyrrolidinium dicyanamide
• Density, excess molar volume, and COSMO-RS study of reactive aqueous solutions containing formaldehyde
• 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
• Separation of acetonitrile and methanol azeotropic mixture using imidazolium-based ionic liquids as entrainers
• Liquid-liquid equilibria of n-heptane, methanol and deep eutectic solvents composed of carboxylic acid and monocyclic terpenes
• Measurement and correlation of the isobaric vapor-liquid equilibria of methanol + methyl carbonate + Bis(trifluoromethylsulfonyl)imide-based ionic liquidsat 101.3 kPa
• Ammonium ionic liquids in extraction of bio-butan-1-ol from water phase using activity coefficients at infinite dilution
• Densities, viscosities, and refractive indices of binary and ternary mixtures of methanol, acetone, and chloroform at temperatures from (298.15-318.15) K and ambient pressure
• Experimental measurements and thermodynamic modeling of Coumarin-7 solid solubility in supercritical carbon dioxide: Production of nanoparticles via RESS method
• 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
• Measurement and modeling of infinite dilution activity coefficients of organic compounds in an equimolar ionic liquid mixture of [Bmim]Cl and [Bmim][Tf2N]
• 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
• Separation abilities of three acetate-based ionic liquids for benzene-methanol mixture through vapor-liquid equilibrium experiment at 101.3 kPa
• Application of trihexyltetradecylphosphonium dicyanamide ionic liquid for various types of separations problems: Activity coefficients at infinite dilution measurements utilizing GLC method
• New vapour-liquid equilibrium data on the ternary system carbon dioxide - methanol - dimethyl sulphoxide
• Solubility measurements and thermodynamic modeling of pyrazinamide in five different solvent-antisolvent mixtures
• Temperature dependence of the volumetric properties of some alkoxypropanols + n-alkanol mixtures
• Liquid--liquid equilibria for mixtures of {methyl acetate + methanol + n-alkane (C10--C12)} at several temperatures and 1 atm
• Excess molar volumes V , isothermal compressibilities k, and thermal expansivities alpha of {(1- x)H2O+xCH3OH} at T =(298.15 to 523.15) K and pressures up to 60 MPa
• Excess molar enthalpies of ternary mixtures of (methanol, ethanol + 2-propanol + 1,4-dioxane) at T ? 298:15 K
• (Liquid + liquid) equilibrium of (dibutyl ether + methanol + water) at different temperatures
• 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
• Activity coefficients at infinite dilution measurements for organic solutes in the ionic liquid 1-butyl-3-methyl-imidazolium 2-(2-methoxyethoxy) ethyl sulfate using g.l.c. at T = (298.15, 303.15, and 308.15) K
• (p, q, T) properties, and apparent molar volumes V/ of ZnBr2 in methanol at T = (298.15 to 398.15) K and pressures up to p = 40 MPa
• Vapor pressure of heat transfer fluids of absorption refrigeration machines and heat pumps: Binary solutions of lithium nitrate with methanol
• The (p,q,T) of (methanol + benzene) and (methanol + ethylbenzene)
• Excess enthalpy HE and massic heat capacity cp of (water + methanol) at temperatures between 323 K and 513 K and pressures up to 10 MPa
• Activity coefficients at infinite dilution measurements for organic solutes in the ionic liquid hexyl-3-methyl-imidazolium bis(trifluoromethylsulfonyl)-imide using g.l.c. at T = (298.15, 313.15, and 333.15) K
• (Liquid + liquid) equilibria for ternary mixtures of (methanol or ethanol + toluene or m-xylene + n-dodecane)
• 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
• (p, rho , T) properties and apparent molar volumes of CaCl2 in methanol at T=(298.15 to 398.15) K and pressures up to 40 MPa
• 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
• Investigation of the vapor pressure p of zinc bromide or zinc chloride solutions with methanol by static method
• Measurement of activity coefficients at infinite dilution using polar and non-polar solutes in the ionic liquid 1-methyl-3-octyl-imidazolium diethyleneglycolmonomethylethersulfate at T = (288.15, 298.15, and 313.15) K
• Dynamic viscosities of the ternary liquid mixtures (dimethyl carbonate + methanol + ethanol) and (dimethyl carbonate + methanol + hexane) at several temperatures
• Volumetric and compressibility behaviour of ionic liquid, 1-n-butyl-3-methylimidazolium hexafluorophosphate and tetrabutylammonium hexafluorophosphate in organic solvents at T = 298.15 K
• Henry's law constants and infinite dilution activity coefficients of cis-2-butene, dimethylether, chloroethane, and 1,1-difluoroethane in methanol, 1-propanol, 2-propanol, 1-butanol, 2-butanol, isobutanol, tert-butanol, 1-pentanol, 2-pentanol, 3-pentanol, 2-methyl-1-butanol, 3-methyl-1-butanol, and 2-methyl-2-butanol
• Bubble point temperatures of the binary mixtures of nitrobenzene with C1 C4 aliphatic alcohols at 94.95 kPa
• (p, rho, T) properties and apparent molar volumes V/ of LiNO3 in methanol
• Application of Prigogine Flory Patterson theory to excess molar volume and speed of sound of 1-n-butyl-3-methylimidazolium hexafluorophosphate or 1-n-butyl-3-methylimidazolium tetrafluoroborate in methanol and acetonitrile
• (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
• Study of activity coefficients for sodium iodide in (methanol + benzene) system by (vapour + liquid) equilibrium measurements
• Molar excess enthalpies of binary mixtures of [tributyl phosphate + {CH3(CH2)nOH (n = 0 to 3)}] at 298.15 K
• 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
• Isobaric specific heat capacity of {xCH3OH + (1-x)H2O} with x = (1.0000, 0.7943, 0.4949, 0.2606, 0.1936, 0.1010, and 0.0496) at T = (280, 320, and 360) K in the pressure range from (0.1 to 15) MPa
• 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
• Liquid densities and excess molar volumes for (ionic liquids + methanol + water) ternary system at atmospheric pressure and at various 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
• Effect of temperature on mixing thermodynamics of a new ionic liquid: {2-Hydroxy ethylammonium formate (2-HEAF) + short hydroxylic solvents}
• Ternary (liquid + liquid) equilibria for mixtures of (methanol + aniline + n-octane or n-dodecane) at T = 298.15 K
• Heat capacities of the mixtures of ionic liquids with methanol at temperatures from 283.15 K to 323.15 K
• 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, excess volumes, isobaric expansivity, and isothermal compressibility of the (1-ethyl-3-methylimidazolium ethylsulfate + methanol) system at temperatures (283.15 to 333.15) K and pressures from (0.1 to 35) MPa
• Measurements of activity coefficients at infinite dilution of aromatic and aliphatic hydrocarbons, alcohols, and water in the new ionic liquid [EMIM][SCN] using GLC
• Volumetric, acoustic, and viscometric studies of molecular interactions in binary mixtures of dipropylene glycol dimethyl ether with 1-alkanols at 298.15 K
• Densities, excess molar volumes, speeds of sound and isothermal compressibilities for {2-(2-hexyloxyethoxy)ethanol + n-alkanol} systems at temperatures between (288.15 and 308.15) K
• 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
• Apparent molar volumes, expansibilities, and isentropic compressibilities of selected electrolytes in methanol
• High-pressure densities and derived volumetric properties (excess, apparent, and partial molar volumes) of binary mixtures of {methanol (1) + [BMIM][BF4] (2)}
• Thermodynamic properties of mixtures of N-methyl-2-pyrrolidinone and methanol at temperatures between 298.15 K and 343.15 K and pressures up to 60 MPa
• 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
• Phase diagrams of (hexane + methanol + 2,2,2-trifluoroethanol) at three temperatures: Measurement and correlation
• 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
• Influence of temperature on the (liquid + liquid) equilibria of {3-methyl pentane + cyclopentane + methanol} ternary system at T = (293.15, 297.15, and 299.15) K
• Physical and excess properties of (methyl acetate + methanol + 1-octyl-3-methyl-imidazolium bis(trifluoromethylsulfonyl)imide) and its binary mixtures at T = 298.15 K and atmospheric pressure
• Activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid 4-methyl-N-butyl-pyridinium bis(trifluoromethylsulfonyl)-imide
• Molar excess enthalpies at T = 298.15 K for (1-alkanol + dibutylether) systems
• (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
• Experimental (vapour + liquid) equilibrium data of (methanol + water), (water + glycerol) and (methanol + glycerol) systems at atmospheric and sub-atmospheric pressures
• 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
• 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
• Volumetric, ultrasonic speed, and viscometric studies of salbutamol sulphate in aqueous methanol solution at different temperatures
• Apparent molar volumes and compressibilities of alkaline earth metal ions in methanol and dimethylsulfoxide
• 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
• Thermodynamic study of binary mixtures containing 1-butylpyridinium tetrafluoroborate and methanol, or ethanol
• Measurement and correlation of solubilities of apigenin and apigenin 7-O-rhamnosylglucoside in seven solvents at different temperatures
• Phase equilibrium data and thermodynamic modelling of the system (propane + DMF + methanol) at high pressures
• 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
• 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
• Phase behavior of (CO2 + methanol + lauric acid) system
• 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
• 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
• 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
• 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
• Ebulliometric determination and prediction of (vapor + liquid) equilibria for binary and ternary mixtures containing alcohols (C1 C4) and dimethyl carbonate
• 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 and surface properties of pure ionic liquid n-octyl-pyridinium nitrate and its binary mixture with alcohol
• 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
• 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
• 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 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 study on the calorimetric data of cyclohexanol with alkanols (C1-C4) and correlation with Wilson, NRTL and UNIQUAC models at 300 K
• 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
• H2 solubility in methanol in the presence of CO2 and O2
• 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
• Effect of alkanolammonium formates ionic liquids on vapour liquid equilibria of binary systems containing water, methanol, and ethanol
• Measurement of (vapor + liquid) equilibrium for the systems {methanol + dimethyl carbonate} and {methanol + dimethyl carbonate + tetramethylammonium bicarbonate} at p = (34.43, 67.74) kPa
• 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
• Partial molar volume of tertiary amines in methanol at T = 298.15 K. Solvation, shape and specific interactions
• Measurement and correlation of solubility of Tetracycline hydrochloride in six organic solvents
• 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
• Densities, speeds of sound, and refractive indices for binary mixtures of 1-butyl-3-methylimidazolium methyl sulphate ionic liquid with alcohols at T = (298.15, 303.15, 308.15, and 313.15) K
• 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
• Solubilities of evodiamine in twelve organic solvents from T = (283.2 to 323.2) K
• Volume effects for binary mixtures of propane-1,2-diol with methanol, propan-1-ol, hexan-1-ol, octan-1-ol, or nonan-1-ol at temperatures (293.15 to 318.15) K
• Thermodynamics of 1-alkanol + linear polyether mixtures
• Activity coefficient at infinite dilution measurements for organic solutes (polar and non-polar) in fatty compounds Part II: C18 fatty acids
• 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
• Probing subsistence of ion-pair and triple-ion of an ionic salt in liquid environments by means of conductometric contrivance
• 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
• 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
• Activity coefficients at infinite dilution of organic solutes in the ionic liquid trihexyltetradecylphosphonium bis(trifluoromethylsulfonyl)imide using gas-liquid chromatography at T = (313.15, 333.15, 353.15 and 373.15) K
• 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
• Effect of tetrabutylammonium bromide on solution behavior of salicylaldehyde anil zinc (II) in methanol at T = (298.15, 308.15 and 318.15) K
• 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
• Partial molar volumes and viscosity B-coefficients for N,N'-ethylenebis(salicylideneiminato)-diaquochromium(III) chloride in methanolic solutions of 1-butyl-2,3-dimethylimidazolium tetrafluoroborate at T = (298.15, 308.15, and 318.15) K
• 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
• Physicochemical properties of two 1-alkyl-1-methylpyrrolidinium bis[(trifluoromethyl)sulfonyl]imide ionic liquids and of binary mixtures of 1-butyl-1-methylpyrrolidinium bis[(trifluoromethyl)sulfonyl]imide with methanol or acetonitrile
• Isobaric (vapor + liquid) equilibrium data for the binary system methanol + 2-butyl alcohol and the quaternary system methyl acetate + methanol + 2-butyl alcohol + 2-butyl acetate at P = 101.33 kPa
• 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
• Ionic molar volumes in methanol mixtures with acetonitrile, N,N-dimethylformamide and propylene carbonate at T = 298.15 K
• Non-covalent interactions between {N,N'-bis[(2-pyridinyl)methylene]-1,2-benzenediamine]-bis(nitrato)}Cu(II) with pyridoxine hydrochloride in methanol at T = (298.15, 308.15 and 318.15) K
• Measurement, correlation and dissolution thermodynamics of biological active chalcone in organic solvents 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
• Thermodynamic study of the surface of liquid mixtures containing pyridinium-based ionic liquids and alkanols
• Determination and correlation of solubility of spironolactone form II in pure solvents and binary solvent mixtures
• Molar heat capacities for {isomer of butanediol + methanol} as function of mixture composition and temperature
• Thermodynamic models for determination of the solubility of dibenzothiophene in (methanol + acetonitrile) binary solvent mixtures
• VLE measurements using a static cell vapor phase manual sampling method accompanied with an empirical data consistency test
• Determination and correlation of solubility of tylosin tartrate in alcohol mixtures
• Measurement and correlation of solubility of 4-chloro-2,5-dimethoxynitrobenzene and 4-chloro-2,5- dimethoxyaniline in methanol, ethanol, xylene and toluene
• 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
• Measuring the solubility of CO2 and H2S in sulfolane and the density and viscosity of saturated liquid binary mixtures of (sulfolane + CO2) and (sulfolane + H2S)
• Measurements and modeling of LLE and HE for (methanol + 2,4,4-trimethyl-1-pentene), and LLE for (water + methanol + 2,4,4-trimethyl-1-pentene)
• (Solid + liquid) phase diagram for (indomethacin + nicotinamide)- methanol or methanol/ethyl acetate mixture and solubility behavior of 1:1 (indomethacin + nicotinamide) co-crystal at T = (298.15 and 313.15) K
• Thermodynamic models for determination of the solubility of DL-malic acid in methanol plus (acetonitrile, N,N-dimethylformamide, isopropyl alcohol) binary solvent mixtures
• Solubility and solution thermodynamics of sorbic acid in eight pure organic solvents
• Isothermal (vapor + liquid) equilibria for the binary mixtures of (propylene oxide + ethanol) and (propylene oxide + 1-propanol) at several temperatures
• Mixing thermodynamic properties of ester-containing solutions: A study on the ternary (methyl alkanoate (pentanoate and methanoate) + methanol) and the corresponding binaries. New contributions to the (ester + ester) interactions
• Density, viscosity, and saturated vapor pressure of ethyl trifluoroacetate
• 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
• (Liquid + liquid) extraction of methanol from alkanes using dialkylphosphate-based ionic liquids as solvents
• 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
• 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
• Measurement, correlation of the solubility and solution thermodynamics of 2-cyanoguanidine in (methanol + water) binary solvent systems from T = (283.15 to 343.15) K
• 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
• Volumetric properties, viscosities and refractive indices of binary liquid mixtures of tetrafluoroborate-based ionic liquids with methanol at several 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
• Measurements and modeling for the density of 2-methoxy-2,4,4- trimethylpentane, HE for (methanol + 2-methoxy-2,4,4- trimethylpentane), LLE for (water + 2-methoxy-2,4,4-trimethylpentane) and LLE for (water + methanol + 2-methoxy-2,4,4-trimethylpentane)
• 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
• Solubility and solution thermodynamics of thymol in six pure organic solvents
• Determination and correlation of pyridoxine hydrochloride solubility in different binary mixtures at temperatures from (278.15 to 313.15) K
• Density, viscosity and excess properties in the trihexyltetradecylphosphonium chloride ionic liquid/methanol cosolvent system
• Correlation and thermodynamic analysis of solubility of diphenhydramine hydrochloride in pure and binary solvents
• Speed of sound measurements of liquid C1-C4 alkanols
• Solubility determination and correlation for 1,8-dinitronaphthalene in (acetone + methanol), (toluene + methanol) and (acetonitrile + methanol) mixed solvents
• 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
• Determination and correlation of solubility and solution thermodynamics of oxiracetam in three (alcohol + water) binary solvents
• 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)
• Solubility of 3-chloro-N-phenylphthalimide in ten organic solvents from T = (288.15 to 323.15) K: Determination and modelling
• 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
• Solution thermodynamics and preferential solvation of sulfamethazine in (methanol + water) mixtures
• Experimental measurement and correlation of the solubility of aloe-emodin in seven pure solvents
• Thermodynamic properties of a CO2-rich mixture (CO2 + CH3OH) in conditions of interest for carbon dioxide capture and storage technology and other applications
• Determination and modeling of the solubility of (limonin in methanol or acetone + water) binary solvent mixtures at T = 283.2 K to 318.2 K
• 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
• Equilibrium solubility of sodium 2,4-diaminobenzene sulfonate in liquid mixtures (methanol + water, isopropanol + water, and 1,2-propanediol + water) from 273.15 K to 323.15 K
• Thermodynamic models for determination of 3-chloro-N-phenylphthalimide solubility in binary solvent mixtures of (acetone, ethyl acetate or 1,4-dioxane + methanol)
• 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
• Measurement and correlation of the vapor-liquid equilibrium for methanol + acetonitrile + imidazolium-based ionic liquids at 101.3 kPa
• 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
• 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
• Measurements and correlations of density, viscosity, and vapour-liquid equilibrium for fluoro alcohols
• Determination and correlation of solubility and thermodynamics of mixing of 4-aminobutyric acid in mono-solvents and binary solvent mixtures
• 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
• The standard molar enthalpy of the base catalysed hydrolysis of methyl paraben revisited
• 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
• Solubility determination and thermodynamic modelling of allisartan isoproxil in different binary solvent mixtures from T = (278.15 to 313.15) K and mixing properties of solutions
• 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
• 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
• Thermodynamic modelling for solubility of 5-chloro-1-methyl-4-nitroimidazole in eleven organic solvents from T = (283.15 to 318.15) K
• 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
• Solubility of 3-methyl-4-nitrobenzoic acid in binary solvent mixtures of {(1,4-dioxane, N-methyl-2-pyrrolidone, N,N-dimethylformamide) + methanol} from T = (283.15 to 318.15) K: Experimental determination and thermodynamic modelling
• 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 of carbon monoxide in bio-oil compounds
• 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 solubility of 11alpha,17alpha-dihydroxy-4-pregnene-3,20-dione in different solvents
• Effect of beta-alanine and the solvent composition on the solubility of solvate of calcium D-pantothenate containing four molecules of methanol and one molecule of water (D-PC*4MeOH*1H2O)
• 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 modelling for phthalimide in mixed solvents of (acetone, ethyl acetate or acetonitrile + methanol) from (278.15 to 313.15) K
• 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 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
• 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
• Solubility and preferential solvation of some n-alkyl-parabens in methanol + water mixtures at 298.15 K
• 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
• 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, solution thermodynamics and preferential solvation for 4- bromopyrazole in mixed solvents of (methanol/ethanol + water) from T = (283.15 to 318.15) K
• Thermodynamic functions for solubility of 2-mercaptobenzothiazole in eleven pure organic solvents at temperatures from 273.15 K to 318.15 K and mixing properties of solutions
• 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)
• Thermodynamics and activity coefficients at infinite dilution for organic compounds and water in the ionic liquid 1-butyl-3-methylimidazolium perchlorate
• Conformational analysis of branched alkanes using limiting partial molar volumes
• Thermodynamic modelling of solubility and preferential solvation for ribavirin (II) in co-solvent mixtures of (methanol, n-propanol, acetonitrile or 1,4-dioxane) + water
• Investigation of surface tension and viscosity for aqueous solutions of MEA-MeOH and DEA-MeOH
• Separation of water/butan-1-ol based on activity coefficients at infinite dilution in 1,3-didecyl-2-methylimidazolium dicyanamide ionic liquid
• 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
• Equilibrium solubility, dissolution thermodynamics and preferential solvation of 6-methyl-2-thiouracil in aqueous co-solvent mixtures of methanol, N-methyl-2-pyrrolidone, N,N-dimethyl formamide and dimethylsulfoxide
• Solubility and thermodynamics of vitamin C in binary liquid mixtures involving water, methanol, ethanol and isopropanol at different temperatures
• Ternary liquid-liquid equilibria for systems containing (dimethyl carbonate or methyl acetate + methanol + 1-methylmidazole hydrogen sulfate) at 298.15 K and 318.15 K
• Thermodynamic study of molecular interaction-selectivity in separation processes based on limiting activity coefficients
• Densities and volumetric properties of (choline chloride+urea) deep eutectic solvent and methanol mixtures in the temperature range of 293.15-323.15 K
• 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
• Thermodynamic behaviour of alkyl lactate-alkanol systems
• The use of ionic liquids for separation of binary hydrocarbons mixtures based on gamma infinity data measurements
• 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
• 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)
• Determination of the thermodynamic parameters of ionic liquid 1-propyl-3-methylimidazolium bromide by gas-liquid chromatography
• The dissolution behavior and apparent thermodynamic analysis of temozolomide in pure and mixed solvents
• 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
• Liquid-liquid equilibria for azeotropic mixture of methyl tert-butyl ether and methanol with ionic liquids at different temperatures
• 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
• Effect of 1-ethyl-3-methylimidazolium tetrafluoroborate on the phase equilibria for systems containing 5-hydroxymethylfurfural, water, organic solvent in the absence and presence of sodium chloride
• Experimental determination of vapor liquid equilibrium for methanol + methyl propionate + 1-butyl-3-methylimidazo-lium bis(trifluoromethylsulfonyl)imide at atmospheric pressure
• 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
• Research on the application of 7-chloro-quinaldine adducts in 7-chloro-quinaldine separation process
• 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
• Research and comparison of solid-liquid phase equilibrium and ternary phase diagrams of 1-(3-nitrophenyl)ethanone + 1-(4-nitrophenyl)ethanone in different solvents
• 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
• Experimental isobaric vapour-liquid equilibrium data for the binary system (N, N-dimethyl acetamide + dimethyl sulfoxide) and the quaternary system (sec-butyl acetate + sec-butyl alcohol + N, N-dimethyl acetamide + dimethyl sulfoxide) at 101.3 kPa
• Separation of (water/butan-1-ol) binary systems based on activity coefficients at infinite dilution with phosphonium ionic liquid
• Synergistic effect of salts and methanol in thermodynamic inhibition of sII gas hydrates
• 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
• Co-solvence phenomenon and thermodynamic properties of edaravone in pure and mixed solvents
• Liquid-liquid extraction of methanol from its mixtures with hexane using three imidazolium-based ionic liquids
• 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
• Volumetric properties of the monoethanolamine methanol mixture at atmospheric pressure from 283.15 to 353.15K
• Solubility of hydrogen in methanol at temperatures from 248.41 to 308.20K
• 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.
• Thermochemistry of adducts of some bivalent transition metal bromides with triphenylphosphine
• Construction of solid liquid phase diagrams in ternary systems by titration calorimetry
• 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
• DSC determination of partial ternary phase diagrams of methanol/sodium chloride/water and propylene glycol/sodium chloride/water and their applications for synthesized diagrams
• Excess molar volumes of Diisopropylamine + (C1-C5) Alkan-1-ols: application of the ERAS model and cubic EOS
• 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
• Measurement and Correlation for Solubility of Dexibuprofen in Different Solvents from (263.15 to 293.15) K
• Solubilities of 1,3-dimethyl-1,1,3,3-tetraphenyldisiloxane in different solvents from (288.15 to 313.15) K
• Solubility in binary solvent mixtures: pyrene dissolved in alcohol + toluene mixtures
• Measurement of thermal conductivities of [mmim]DMP/CH3OH and [mmim]DMP/H2O by freestanding sensor-based 3w technique
• Probing molecular interactions of ionic liquid in industrially important solvents by means of conductometric and spectroscopic approach
• Solubility of disodium cytidine 5'-monophosphate in different binarymixtures from 288.15 K to 313.15 K
• 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
• THERMODYNAMICS OF MIXTURES CONTAINING AMINES. XIV. CpEm OF BENZYLAMINE WITH HEPTANE AT 293.15 K OR WITH METHANOL, 1-PROPANOL OR 1-PENTANOL AT (293.15-308.15) K
• Study of intermolecular interactions in binary mixtures of 2-(dimethylamino)ethanol with methanol and ethanol at various temperatures
• 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
• Vapor-liquid equilibria, density and sound velocity measurements of (water or methanol or ethanol + 1,3-propanediol) binary systems at different temperatures
• Low cost apparatus for rapid boiling point determination of small air sensitive samples under inert atmosphere
• Renewable platform chemicals: Thermochemical study of levulinic acid esters
• Measurement and correlation of solubility of carbendazim in lower alcohols
• A new analysis method for improving collection of vapor-liquid equilibrium (VLE) data of binary mixtures using differential scanning calorimetry (DSC)
• 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
• Solubilities of Phosphoramidic Acid, N-(phenylmethyl)-, Diphenyl Ester in Selected Solvents
• Solubility of 3,7-Dinitro-1,3,5,7-tetraazabicyclo [3.3.1] Nonane in Ethanenitrile, Methanol, 1,1-Dichloroethane, Dimethyl Sulfoxide, Acetone, and Mixed Solvents
• Dissociation Constants and Solubilities of Dalbergin and Nordalbergin in Different Solvents
• Modified Method for Measuring the Solubility of Pharmaceutical Compounds in Organic Solvents by Visual Camera
• Experimental and Computational Thermodynamic Properties of (Benzyl alcohol + Alkanols) Mixtures
• Solubility and Saturation Apparent Volume of Propranolol Hydrochloride in Some Binary Aqueous Cosolvent Mixtures at 298.15 K
• Solubility and Solution Thermodynamics of Gibberellin A4 in Different Organic Solvents from 278.15 K to 333.15 K
• 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
• Density and Excess Molar Volumes of 1-Butanol + Methanol + Electrolyte Systems in the Temperature Range (293.15 308.15) K
• Solubility Measurement and Correlation for 2- Naphthaldehyde in Pure Organic Solvents and Methanol + Ethanol Mixtures
• Investigation of Surface and Solubility Properties of N-Vinylimidazolium Tetrahalogenidoferrate(III) Magnetic Ionic Liquids Using Density Functional Theory
• Solubilities of 3-Chlorophthalic Anhydride and 4-Chlorophthalic Anhydride in Different Pure Solvents
• Tie-Line Data for Aqueous Mixtures of Butyric Acid with Diisopropyl Ether at Various Temperatures
• Isobaric Vapor - Liquid Equilibrium for Ethyl acetate + Methanol + Ionic Liquids Ternary systems at 101.3 kPa
• Measurement and Correlation of the Solubility of Maltitol in Different Pure Solvents, Methanol Water Mixtures, and Ethanol Water Mixtures
• 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
• Exploration of Solvation Consequence of Ionic Liquid [Bu4PCH3SO3] in Various Solvent Systems by Conductance and FTIR Study
• 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
• Solubility of (S)-3-(Aminomethyl)-5-Methylhexanoic Acid in Pure and Binary Solvent Mixtures
• Solubility of Benzoic Acid and Aspirin in Pure Solvents Using Focused Beam Reflective Measurement
• 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
• Isothermal Vapor Liquid Equilibrium Data for the Methanol + Benzene + Tetraphenylphosphonium Chloride System
• Experimental Measurement and Modeling of the Solubility of Methane in Methanol and Ethanol
• Vapor Liquid Equilibria Measurement of (Methanol + Ethanenitrile + Bis(trifluoromethylsulfonyl) Imide)-Based Ionic Liquids at 101.3 kPa
• 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
• Vapor-Liquid Equilibrium Study of the Gamma- Valerolactone-Water Binary System
• Solubility Measurement and Correlation of (+)-Biotin Intermediate Lactone in Different Organic Solvents from (287.15 to 323.75) K
• Vapor Liquid Equilibrium for Methanol + Methyl Palmitate near the Critical Temperature of Methanol
• Solubility of 1,3,5-Benzenetricarboxylic Acid in Different Solvents
• Thermodynamics of 1,3-dimethylurea in eight alcohols
• 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
• Thermophysical Characterization of the Mixtures of the Ionic Liquid 1-Ethyl-3-Methylimidazolium Acetate with 1-Propanol or 2-Propanol
• 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 Equilibria of Binary and Ternary Systems Methanol/Water + n-Hexane, + n-Octane, + n-Dodecane, and + n-Hexadecane in the Temperature Range between T = 283.15 K and T = 333.15 K
• Solubility of Ethyl p-Aminobenzoate in Six Alcohols within (283.15 to 327.15) K
• Measurement and Thermodynamic Modeling of the Solubility of Lamotrigine, Deferiprone, Cefixime Trihydrate, and Cephalexin Monohydrate in Different Pure Solvents from 283.1 to 323.1 K
• Isobaric Vapor Liquid Equilibrium for Nine Binary Systems of Cracking C5 Fraction at 250 kPa
• Solubility Measurement and Thermodynamic Modeling of 4-Nitrophthalimide in Twelve Pure Solvents at Elevated Temperatures Ranging from (273.15 to 323.15) K
• Isothermal Vapor Liquid Equilibrium Data for the Toluene + Methanol + N-Butylpyridinium Bromide System
• Liquid Liquid Equilibria for the Ternary System n-Butyl Acetate + Pyrocatechol + Water at Different Temperatures at 101.3 kPa
• 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
• Phase Equilibria for the Hydroesterification of 10-Undecenoic Acid Methyl Ester
• 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
• 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
• Isobaric Vapor Liquid Equilibrium for Two Binary Systems (Methanol + Dibutyl Carbonate) and (n-Butanol + Dibutyl Carbonate) at p = 40.0, 70.0, and 100.0 kPa
• Solubilities of Naringin Dihydrochalcone in Pure Solvents and Mixed Solvents at Different Temperatures
• Solubility of 4-Methylsulfonylacetophenone in Nine Pure Solvents and (Ethyl Acetate + n-Hexane) Binary Solvent Mixtures from 278.15 K to 328.15 K
• Measurement and Correlation of Solubility of Loratadine in Different Pure Solvents and Binary Mixtures
• 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
• Solubility Measurement and Correlation of Two Erlotinib Hydrochloride Polymorphs in Alcohols and Ketones from 273.15 to 323.15 K
• Solubility Measurement and the Correlation of 1-Naphthaleneacetic Acid in Pure and Methanol + Water Binary Solvents from T = (278.25 to 323.55) K
• Determination of Vapor Liquid Equilibrium of Methyl Acetate + Methanol + 1-Alkyl-3-methylimidazolium Dialkylphosphates at 101.3 kPa
• 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
• 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
• Isobaric Vapor Liquid Equilibria for Two Binary Systems {Propylene Glycol Methyl Ether Acetate + Methanol} and {Propylene Glycol Methyl Ether Acetate + N,N-Dimethylformamide} at p = 30.0, 50.0, and 70.0 kPa
• 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
• 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
• Phase Behavior Data of (CO2 + Toluene + Phenanthrene) and (CO2 + (Methanol + Phenanthrene) Systems at High Pressure<