Chemical Properties of Isopropyl Alcohol (CAS 67-63-0)

InChI

InChI=1S/C3H8O/c1-3(2)4/h3-4H,1-2H3

InChI Key

KFZMGEQAYNKOFK-UHFFFAOYSA-N

Formula

C3H8O

SMILES

CC(C)O

Molecular Weight¹

60.09

CAS

67-63-0

Other Names

• 1-Methylethyl Alcohol
• 1-methylethanol
• 2-Hydroxypropane
• 2-PROPANOL
• 2-Propyl alcohol
• Alcojel
• Alcolo
• Alcool isopropilico
• Alcool isopropylique
• Alcosolve
• Alcosolve 2
• Alkolave
• Arquad DMCB
• Avantin
• Avantine
• Combi-Schutz
• Dimethylcarbinol
• Hartosol
• IPA
• IPS 1
• Imsol A
• Isohol
• Isopropanol
• Isopropyl alcohol, rubbing
• Lavacol
• Lutosol
• PRO
• Petrohol
• Propan-2-ol
• Propane, 2-hydroxy-
• Propanol-2
• Propol
• SEC-PROPYL ALCOHOL
• Spectrar
• Sterisol hand disinfectant
• Takineocol
• UN 1219
• Virahol
• Visco 1152
• i-Propanol
• i-Propylalkohol
• iso-C3H7OH
• iso-Propylalkohol
• n-Propan-2-ol
• sec-Propanol

• ω : Acentric Factor.
• PAff : Proton affinity (kJ/mol).
• T_ig : Autoignition Temperature (K).
• BasG : Gas basicity (kJ/mol).
• Δ_cH°_liquid : Standard liquid enthalpy of combustion (kJ/mol).
• C_p,gas : Ideal gas heat capacity (J/mol×K).
• C_p,liquid : Liquid phase heat capacity (J/mol×K).
• μ : Dipole Moment (debye).
• η : Dynamic viscosity (Pa×s).
• σ_cond : Electrical conductivity (S/m).
• LFL : Lower Flammability Limit (% in Air).
• UFL : Upper Flammability Limit (% in Air).
• T_flash,cc : Flash Point (Closed Cup Method) (K).
• T_flash,oc : Flash Point (Open Cup Method) (K).
• Δ_fG° : Standard Gibbs free energy of formation (kJ/mol).
• R_g : Radius of Gyration.
• Δ_fH°_gas : Enthalpy of formation at standard conditions (kJ/mol).
• Δ_fH°_liquid : Liquid phase enthalpy of formation at standard conditions (kJ/mol).
• Δ_fusH° : Enthalpy of fusion at standard conditions (kJ/mol).
• Δ_fusH : Enthalpy of fusion at a given temperature (kJ/mol).
• Δ_vapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
• Δ_vapH : Enthalpy of vaporization at a given temperature (kJ/mol).
• IE : Ionization energy (eV).
• 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_c : Critical density (kg/m³).
• ρ_l : Liquid Density (kg/m³).
• I_np : Non-polar retention indices.
• I : Polar retention indices.
• Δ_fusS : Entropy of fusion at a given temperature (J/mol×K).
• S°_liquid : Liquid phase molar entropy at standard conditions (J/mol×K).
• c_sound,fluid : Speed of sound in fluid (m/s).
• γ : Surface Tension (N/m).
• T_boil : Normal Boiling Point Temperature (K).
• T_boil : Boiling point at given pressure (K).
• T_c : Critical Temperature (K).
• 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	0.6650		KDB
PAff	[793.00; 796.00]	kJ/mol
PAff	793.00	kJ/mol	NIST
PAff	796.00 ± 6.00	kJ/mol	NIST
Tig	672.04	K	KDB
BasG	762.60	kJ/mol	NIST
ΔcH°liquid	[-2006.90; -2005.10]	kJ/mol
ΔcH°liquid	-2006.90 ± 0.20	kJ/mol	NIST
ΔcH°liquid	-2005.80 ± 0.40	kJ/mol	NIST
ΔcH°liquid	-2005.10	kJ/mol	NIST
μ	1.70	debye	KDB
η	[0.0020443; 0.0020980]	Pa×s
η	0.0020980	Pa×s	Speeds ...
η	0.0020630	Pa×s	Thermod...
η	0.0020443	Pa×s	Densiti...
LFL	2.30	% in Air	KDB
UFL	12.70	% in Air	KDB
Tflash,cc	291.48	K	KDB
Tflash,oc	284.82	K	KDB
ΔfG°	-173.50	kJ/mol	KDB
Rg	2.7260		KDB
ΔfH°gas	[-272.80; -271.10]	kJ/mol
ΔfH°gas	-272.60	kJ/mol	KDB
ΔfH°gas	-272.80	kJ/mol	NIST
ΔfH°gas	-271.10	kJ/mol	NIST
ΔfH°gas	-272.30 ± 0.92	kJ/mol	NIST
ΔfH°gas	-272.80	kJ/mol	NIST
ΔfH°liquid	[-318.70; -317.00]	kJ/mol
ΔfH°liquid	-317.00 ± 0.30	kJ/mol	NIST
ΔfH°liquid	-318.20 ± 0.71	kJ/mol	NIST
ΔfH°liquid	-318.70	kJ/mol	NIST
ΔfusH°	4.09	kJ/mol	Joback Calculated Property
ΔvapH°	[40.00; 45.90]	kJ/mol
ΔvapH°	45.48	kJ/mol	NIST
ΔvapH°	44.00	kJ/mol	NIST
ΔvapH°	45.34 ± 0.02	kJ/mol	NIST
ΔvapH°	45.34 ± 0.02	kJ/mol	NIST
ΔvapH°	45.20 ± 0.10	kJ/mol	NIST
ΔvapH°	45.20 ± 0.10	kJ/mol	NIST
ΔvapH°	45.51	kJ/mol	NIST
ΔvapH°	44.00	kJ/mol	NIST
ΔvapH°	45.90 ± 0.20	kJ/mol	NIST
ΔvapH°	44.40	kJ/mol	NIST
ΔvapH°	Outlier 40.00 ± 0.04	kJ/mol	NIST
IE	[10.10; 10.49]	eV
IE	10.17 ± 0.02	eV	NIST
IE	10.15 ± 0.07	eV	NIST
IE	10.10 ± 0.02	eV	NIST
IE	10.29 ± 0.02	eV	NIST
IE	10.18	eV	NIST
IE	10.12 ± 0.03	eV	NIST
IE	10.15 ± 0.05	eV	NIST
IE	10.44	eV	NIST
IE	10.49 ± 0.03	eV	NIST
IE	10.42	eV	NIST
IE	10.36	eV	NIST
IE	10.42	eV	NIST
log10WS	[0.43; 0.43]
log10WS	0.43		Aq. Sol...
log10WS	0.43		Estimat...
logPoct/wat	0.387		Crippen Calculated Property
McVol	59.000	ml/mol	McGowan Calculated Property
NFPA Fire	3		KDB
NFPA Health	1		KDB
Pc	[4716.00; 5380.00]	kPa
Pc	4764.00	kPa	KDB
Pc	4755.00	kPa	Isother...
Pc	4760.00 ± 20.00	kPa	NIST
Pc	4770.00	kPa	NIST
Pc	4761.00 ± 20.00	kPa	NIST
Pc	4761.00 ± 20.00	kPa	NIST
Pc	4762.00	kPa	NIST
Pc	4716.00 ± 8.00	kPa	NIST
Pc	4762.00 ± 4.75	kPa	NIST
Pc	4764.00	kPa	NIST
Pc	Outlier 5370.23 ± 101.32	kPa	NIST
Pc	Outlier 5380.00	kPa	NIST
ρc	[271.03; 272.83]	kg/m3
ρc	271.03 ± 1.20	kg/m3	NIST
ρc	272.83	kg/m3	NIST
ρc	272.71	kg/m3	NIST
Inp	[444.00; 530.00]
Inp	508.00		NIST
Inp	491.00		NIST
Inp	453.00		NIST
Inp	508.00		NIST
Inp	491.00		NIST
Inp	453.00		NIST
Inp	508.00		NIST
Inp	491.00		NIST
Inp	453.00		NIST
Inp	480.00		NIST
Inp	458.00		NIST
Inp	447.00		NIST
Inp	450.00		NIST
Inp	444.00		NIST
Inp	450.00		NIST
Inp	446.00		NIST
Inp	477.00		NIST
Inp	456.00		NIST
Inp	460.00		NIST
Inp	476.00		NIST
Inp	490.00		NIST
Inp	486.00		NIST
Inp	463.00		NIST
Inp	450.00		NIST
Inp	524.00		NIST
Inp	494.00		NIST
Inp	524.00		NIST
Inp	524.00		NIST
Inp	495.40		NIST
Inp	500.00		NIST
Inp	481.00		NIST
Inp	515.80		NIST
Inp	515.00		NIST
Inp	510.00		NIST
Inp	510.00		NIST
Inp	483.00		NIST
Inp	480.00		NIST
Inp	472.00		NIST
Inp	474.00		NIST
Inp	456.00		NIST
Inp	530.00		NIST
Inp	496.00		NIST
Inp	493.00		NIST
Inp	506.00		NIST
Inp	483.40		NIST
Inp	514.00		NIST
Inp	500.00		NIST
Inp	488.00		NIST
Inp	500.00		NIST
Inp	502.00		NIST
Inp	516.00		NIST
Inp	516.00		NIST
Inp	477.00		NIST
Inp	477.00		NIST
Inp	498.00		NIST
Inp	499.00		NIST
Inp	477.00		NIST
Inp	500.00		NIST
Inp	511.00		NIST
Inp	486.00		NIST
Inp	486.00		NIST
Inp	474.00		NIST
Inp	486.00		NIST
Inp	474.00		NIST
Inp	530.00		NIST
Inp	475.00		NIST
Inp	491.00		NIST
Inp	481.00		NIST
Inp	503.00		NIST
Inp	475.00		NIST
Inp	500.00		NIST
Inp	516.00		NIST
Inp	477.00		NIST
Inp	474.00		NIST
Inp	491.00		NIST
Inp	530.00		NIST
Inp	514.00		NIST
Inp	508.00		NIST
Inp	453.00		NIST
Inp	458.00		NIST
Inp	446.00		NIST
Inp	490.00		NIST
I	[884.00; 975.00]
I	935.00		NIST
I	949.00		NIST
I	957.00		NIST
I	949.00		NIST
I	957.00		NIST
I	962.00		NIST
I	885.00		NIST
I	963.00		NIST
I	935.00		NIST
I	928.00		NIST
I	922.00		NIST
I	912.00		NIST
I	932.00		NIST
I	920.00		NIST
I	910.00		NIST
I	940.00		NIST
I	903.00		NIST
I	927.00		NIST
I	891.00		NIST
I	884.00		NIST
I	920.00		NIST
I	935.00		NIST
I	941.40		NIST
I	950.00		NIST
I	921.00		NIST
I	912.00		NIST
I	884.00		NIST
I	888.00		NIST
I	932.00		NIST
I	938.00		NIST
I	909.00		NIST
I	Outlier 975.00		NIST
I	970.00		NIST
I	935.00		NIST
I	924.00		NIST
I	917.00		NIST
I	928.00		NIST
I	922.00		NIST
I	948.00		NIST
I	923.00		NIST
I	884.00		NIST
I	925.00		NIST
I	926.00		NIST
I	884.00		NIST
I	917.00		NIST
I	885.00		NIST
I	921.00		NIST
I	912.00		NIST
I	925.00		NIST
I	938.00		NIST
I	947.00		NIST
I	970.00		NIST
I	Outlier 975.00		NIST
I	910.00		NIST
I	933.00		NIST
I	884.00		NIST
I	906.00		NIST
I	931.00		NIST
I	931.00		NIST
I	942.00		NIST
I	921.00		NIST
I	884.00		NIST
I	962.00		NIST
I	908.00		NIST
I	927.00		NIST
I	923.00		NIST
I	917.00		NIST
I	935.00		NIST
I	962.00		NIST
I	922.00		NIST
I	940.00		NIST
S°liquid	[179.90; 192.90]	J/mol×K
S°liquid	180.58	J/mol×K	NIST
S°liquid	179.90	J/mol×K	NIST
S°liquid	192.90	J/mol×K	NIST
S°liquid	190.80	J/mol×K	NIST
Tboil	[3.50; 385.20]	K
Tboil	355.40	K	KDB
Tboil	355.37	K	Physica...
Tboil	355.15	K	Multiph...
Tboil	355.53	K	Isobari...
Tboil	355.35	K	Isobari...
Tboil	355.60	K	Isobari...
Tboil	355.40	K	Experim...
Tboil	355.61	K	VLE of ...
Tboil	355.45	K	Isobari...
Tboil	355.25	K	Isobari...
Tboil	355.27	K	Vapour-...
Tboil	355.33	K	Separat...
Tboil	355.71	K	A new a...
Tboil	355.33	K	Vapor L...
Tboil	355.60	K	Acetoni...
Tboil	355.37	K	Vapor L...
Tboil	355.35	K	Measure...
Tboil	355.15	K	Vapor-L...
Tboil	355.41	K	Vapor-L...
Tboil	355.39	K	Vapor-L...
Tboil	355.35	K	Isobari...
Tboil	355.40	K	Vapor-L...
Tboil	355.40	K	Vapor L...
Tboil	355.65	K	Isobari...
Tboil	355.42 ± 0.20	K	NIST
Tboil	355.42 ± 0.30	K	NIST
Tboil	355.42 ± 0.07	K	NIST
Tboil	355.65 ± 0.20	K	NIST
Tboil	355.65 ± 0.30	K	NIST
Tboil	355.42 ± 0.20	K	NIST
Tboil	355.60	K	NIST
Tboil	385.20 ± 0.20	K	NIST
Tboil	355.60 ± 0.10	K	NIST
Tboil	355.40	K	NIST
Tboil	355.45 ± 0.40	K	NIST
Tboil	355.45 ± 0.40	K	NIST
Tboil	355.45 ± 0.30	K	NIST
Tboil	355.06 ± 0.25	K	NIST
Tboil	355.45 ± 0.10	K	NIST
Tboil	354.85 ± 0.30	K	NIST
Tboil	355.45 ± 0.30	K	NIST
Tboil	355.00 ± 0.30	K	NIST
Tboil	355.55 ± 0.30	K	NIST
Tboil	355.20 ± 0.60	K	NIST
Tboil	355.70 ± 0.30	K	NIST
Tboil	355.50 ± 0.40	K	NIST
Tboil	355.39 ± 0.30	K	NIST
Tboil	355.50 ± 0.50	K	NIST
Tboil	353.60 ± 0.50	K	NIST
Tboil	355.45 ± 0.25	K	NIST
Tboil	355.45	K	NIST
Tboil	353.60 ± 0.30	K	NIST
Tboil	355.45 ± 0.40	K	NIST
Tboil	355.45 ± 0.30	K	NIST
Tboil	355.45 ± 0.08	K	NIST
Tboil	355.55 ± 0.15	K	NIST
Tboil	355.54 ± 0.20	K	NIST
Tboil	355.37 ± 0.30	K	NIST
Tboil	355.16 ± 0.20	K	NIST
Tboil	355.48 ± 0.30	K	NIST
Tboil	355.35 ± 0.50	K	NIST
Tboil	355.45	K	NIST
Tboil	355.35 ± 0.50	K	NIST
Tboil	355.55 ± 0.30	K	NIST
Tboil	355.65 ± 1.00	K	NIST
Tboil	355.55 ± 0.50	K	NIST
Tboil	Outlier 3.50 ± 2.00	K	NIST
Tboil	354.70 ± 1.00	K	NIST
Tboil	355.55 ± 0.50	K	NIST
Tboil	355.45 ± 0.10	K	NIST
Tboil	355.55 ± 0.50	K	NIST
Tboil	355.60 ± 0.25	K	NIST
Tboil	355.30 ± 0.50	K	NIST
Tboil	355.25 ± 0.50	K	NIST
Tboil	355.15 ± 1.00	K	NIST
Tboil	355.48 ± 0.33	K	NIST
Tboil	355.35 ± 0.30	K	NIST
Tboil	354.65 ± 1.00	K	NIST
Tboil	357.65 ± 1.00	K	NIST
Tboil	355.48 ± 0.44	K	NIST
Tboil	355.45 ± 0.20	K	NIST
Tboil	353.90 ± 2.00	K	NIST
Tboil	355.40 ± 0.10	K	NIST
Tboil	355.55 ± 0.50	K	NIST
Tboil	364.85 ± 0.50	K	NIST
Tboil	355.65 ± 0.50	K	NIST
Tboil	355.15 ± 1.30	K	NIST
Tboil	355.55 ± 0.50	K	NIST
Tboil	355.65 ± 1.00	K	NIST
Tboil	355.85 ± 0.50	K	NIST
Tboil	355.35 ± 0.30	K	NIST
Tboil	355.45 ± 0.50	K	NIST
Tboil	355.60 ± 0.40	K	NIST
Tboil	355.39 ± 0.20	K	NIST
Tboil	355.57 ± 0.10	K	NIST
Tboil	355.55 ± 0.30	K	NIST
Tboil	355.25 ± 0.30	K	NIST
Tboil	354.87 ± 0.30	K	NIST
Tboil	355.55 ± 0.50	K	NIST
Tboil	355.90 ± 0.40	K	NIST
Tboil	355.15 ± 2.00	K	NIST
Tboil	355.51 ± 0.10	K	NIST
Tboil	355.45 ± 0.30	K	NIST
Tboil	354.95 ± 0.50	K	NIST
Tboil	354.55 ± 0.50	K	NIST
Tboil	355.45 ± 0.50	K	NIST
Tboil	355.54 ± 0.10	K	NIST
Tboil	355.44 ± 0.10	K	NIST
Tboil	355.55 ± 0.10	K	NIST
Tboil	355.46 ± 0.20	K	NIST
Tboil	355.50 ± 0.20	K	NIST
Tboil	355.55 ± 0.50	K	NIST
Tboil	355.45 ± 1.00	K	NIST
Tboil	355.95 ± 1.00	K	NIST
Tboil	355.60 ± 0.50	K	NIST
Tboil	355.60 ± 0.50	K	NIST
Tboil	355.60 ± 0.50	K	NIST
Tboil	355.15 ± 0.20	K	NIST
Tboil	355.60 ± 0.20	K	NIST
Tboil	Outlier 82.21 ± 0.20	K	NIST
Tboil	353.85 ± 0.50	K	NIST
Tboil	355.55 ± 0.30	K	NIST
Tboil	355.50 ± 0.30	K	NIST
Tboil	355.15 ± 0.20	K	NIST
Tboil	355.40 ± 0.05	K	NIST
Tboil	355.55 ± 0.50	K	NIST
Tboil	355.41 ± 0.05	K	NIST
Tboil	355.40 ± 0.05	K	NIST
Tboil	355.43 ± 0.05	K	NIST
Tboil	355.41 ± 0.05	K	NIST
Tboil	355.55 ± 0.20	K	NIST
Tboil	351.65 ± 3.00	K	NIST
Tboil	355.75 ± 0.30	K	NIST
Tboil	354.65 ± 1.50	K	NIST
Tboil	354.20 ± 0.50	K	NIST
Tboil	355.65 ± 1.00	K	NIST
Tboil	355.15 ± 1.50	K	NIST
Tboil	355.59 ± 0.20	K	NIST
Tboil	355.19 ± 0.20	K	NIST
Tboil	356.15 ± 1.00	K	NIST
Tboil	356.00 ± 0.50	K	NIST
Tboil	355.65 ± 1.50	K	NIST
Tboil	356.00 ± 0.50	K	NIST
Tc	[507.36; 516.60]	K
Tc	508.30	K	KDB
Tc	508.72	K	One- an...
Tc	508.30 ± 0.30	K	NIST
Tc	508.60	K	NIST
Tc	508.00 ± 0.60	K	NIST
Tc	508.00 ± 0.60	K	NIST
Tc	508.00	K	NIST
Tc	507.36 ± 0.20	K	NIST
Tc	508.30	K	NIST
Tc	508.30 ± 0.05	K	NIST
Tc	508.30 ± 1.00	K	NIST
Tc	508.30 ± 0.20	K	NIST
Tc	508.30 ± 0.30	K	NIST
Tc	508.30 ± 0.30	K	NIST
Tc	508.26	K	NIST
Tc	511.50	K	NIST
Tc	508.15 ± 0.50	K	NIST
Tc	508.40 ± 0.30	K	NIST
Tc	508.80	K	NIST
Tc	Outlier 516.60	K	NIST
Tc	511.20 ± 3.00	K	NIST
Tc	507.80	K	NIST
Tfus	[183.60; 185.75]	K
Tfus	183.60	K	KDB
Tfus	183.90	K	Aq. Sol...
Tfus	184.65	K	NIST
Tfus	185.75 ± 0.50	K	NIST
Tfus	185.35	K	NIST
Ttriple	[184.60; 185.26]	K
Ttriple	185.26 ± 0.05	K	NIST
Ttriple	185.25 ± 0.06	K	NIST
Ttriple	185.20 ± 0.05	K	NIST
Ttriple	184.67 ± 0.10	K	NIST
Ttriple	184.60 ± 0.30	K	NIST
Ttriple	184.60 ± 0.15	K	NIST
Vc	[0.222; 0.223]	m3/kmol
Vc	0.222	m3/kmol	KDB
Vc	0.222	m3/kmol	NIST
Vc	0.223 ± 0.003	m3/kmol	NIST
Zc	0.2502460		KDB
Zra	0.25		KDB

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[103.06; 148.10]	J/mol×K	[358.72; 597.25]
Cp,gas	103.06	J/mol×K	358.72	NIST
Cp,gas	105.70 ± 1.60	J/mol×K	365.75	NIST
Cp,gas	105.77	J/mol×K	371.15	NIST
Cp,gas	106.29	J/mol×K	373.15	NIST
Cp,gas	108.10 ± 1.60	J/mol×K	378.85	NIST
Cp,gas	109.20 ± 1.60	J/mol×K	384.95	NIST
Cp,gas	110.08	J/mol×K	391.15	NIST
Cp,gas	110.80 ± 1.60	J/mol×K	393.65	NIST
Cp,gas	111.65	J/mol×K	398.15	NIST
Cp,gas	113.00 ± 1.60	J/mol×K	405.35	NIST
Cp,gas	114.35	J/mol×K	411.15	NIST
Cp,gas	117.02	J/mol×K	423.15	NIST
Cp,gas	118.70	J/mol×K	431.15	NIST
Cp,gas	122.10	J/mol×K	448.15	NIST
Cp,gas	122.80	J/mol×K	451.15	NIST
Cp,gas	121.70 ± 1.60	J/mol×K	453.15	NIST
Cp,gas	124.20 ± 1.60	J/mol×K	466.75	NIST
Cp,gas	127.01	J/mol×K	473.15	NIST
Cp,gas	126.70 ± 1.60	J/mol×K	480.55	NIST
Cp,gas	130.30 ± 1.60	J/mol×K	499.75	NIST
Cp,gas	132.90 ± 1.60	J/mol×K	513.95	NIST
Cp,gas	137.50 ± 1.60	J/mol×K	539.05	NIST
Cp,gas	142.60 ± 1.60	J/mol×K	567.05	NIST
Cp,gas	148.10 ± 1.60	J/mol×K	597.25	NIST
Cp,liquid	[149.75; 218.14]	J/mol×K	[292.84; 600.10]
Cp,liquid	149.75	J/mol×K	292.84	NIST
Cp,liquid	152.30	J/mol×K	293.10	NIST
Cp,liquid	151.00	J/mol×K	293.10	NIST
Cp,liquid	154.00	J/mol×K	298.00	NIST
Cp,liquid	163.60	J/mol×K	298.00	NIST
Cp,liquid	159.99	J/mol×K	298.04	NIST
Cp,liquid	180.30	J/mol×K	298.10	NIST
Cp,liquid	154.75	J/mol×K	298.15	NIST
Cp,liquid	154.43	J/mol×K	298.15	NIST
Cp,liquid	161.20	J/mol×K	298.15	NIST
Cp,liquid	162.80	J/mol×K	298.20	NIST
Cp,liquid	169.90	J/mol×K	303.00	NIST
Cp,liquid	172.40	J/mol×K	303.20	NIST
Cp,liquid	165.60	J/mol×K	311.60	NIST
Cp,liquid	180.30	J/mol×K	324.00	NIST
Cp,liquid	218.14	J/mol×K	508.16	Influen...
Cp,liquid	208.53	J/mol×K	508.18	Influen...
Cp,liquid	195.91	J/mol×K	508.28	Influen...
Cp,liquid	187.80	J/mol×K	508.37	Influen...
Cp,liquid	185.69	J/mol×K	508.47	Influen...
Cp,liquid	186.90	J/mol×K	508.57	Influen...
Cp,liquid	192.91	J/mol×K	508.67	Influen...
Cp,liquid	186.90	J/mol×K	508.76	Influen...
Cp,liquid	179.56	J/mol×K	509.35	Influen...
Cp,liquid	180.16	J/mol×K	509.45	Influen...
Cp,liquid	178.84	J/mol×K	509.55	Influen...
Cp,liquid	179.98	J/mol×K	509.64	Influen...
Cp,liquid	177.46	J/mol×K	509.79	Influen...
Cp,liquid	177.28	J/mol×K	509.99	Influen...
Cp,liquid	178.12	J/mol×K	510.14	Influen...
Cp,liquid	177.94	J/mol×K	510.23	Influen...
Cp,liquid	176.68	J/mol×K	510.33	Influen...
Cp,liquid	178.60	J/mol×K	510.48	Influen...
Cp,liquid	176.74	J/mol×K	516.90	Influen...
Cp,liquid	176.80	J/mol×K	516.99	Influen...
Cp,liquid	176.80	J/mol×K	517.08	Influen...
Cp,liquid	172.17	J/mol×K	517.27	Influen...
Cp,liquid	173.13	J/mol×K	521.87	Influen...
Cp,liquid	168.57	J/mol×K	521.96	Influen...
Cp,liquid	173.19	J/mol×K	522.14	Influen...
Cp,liquid	168.63	J/mol×K	522.33	Influen...
Cp,liquid	171.63	J/mol×K	522.42	Influen...
Cp,liquid	173.85	J/mol×K	522.51	Influen...
Cp,liquid	175.18	J/mol×K	522.60	Influen...
Cp,liquid	168.39	J/mol×K	530.01	Influen...
Cp,liquid	168.27	J/mol×K	532.04	Influen...
Cp,liquid	168.33	J/mol×K	535.11	Influen...
Cp,liquid	168.39	J/mol×K	540.06	Influen...
Cp,liquid	168.63	J/mol×K	545.13	Influen...
Cp,liquid	169.77	J/mol×K	560.04	Influen...
Cp,liquid	173.85	J/mol×K	570.09	Influen...
Cp,liquid	174.22	J/mol×K	580.16	Influen...
Cp,liquid	176.38	J/mol×K	590.07	Influen...
Cp,liquid	178.60	J/mol×K	600.10	Influen...
η	[0.0006241; 0.0024050]	Pa×s	[293.00; 343.15]
η	0.0021000	Pa×s	293.00	Ultraso...
η	0.0023840	Pa×s	293.15	Viscosi...
η	0.0022256	Pa×s	293.15	Densiti...
η	0.0023621	Pa×s	293.15	Experim...
η	0.0023820	Pa×s	293.15	Densiti...
η	0.0024050	Pa×s	293.15	Viscosi...
η	0.0023820	Pa×s	293.15	Viscosi...
η	0.0023820	Pa×s	293.15	Viscosi...
η	0.0020450	Pa×s	298.15	Viscosi...
η	0.0020550	Pa×s	298.15	Densiti...
η	0.0020550	Pa×s	298.15	Densiti...
η	0.0020690	Pa×s	298.15	Densiti...
η	0.0019102	Pa×s	298.15	Densiti...
η	0.0020620	Pa×s	298.15	Viscosi...
η	0.0020610	Pa×s	298.15	Studies...
η	0.0020450	Pa×s	298.15	Viscosi...
η	0.0014900	Pa×s	303.00	Ultraso...
η	0.0017430	Pa×s	303.15	Densiti...
η	0.0017370	Pa×s	303.15	Densiti...
η	0.0017694	Pa×s	303.15	Experim...
η	0.0017630	Pa×s	303.15	Viscosi...
η	0.0017919	Pa×s	303.15	Densiti...
η	0.0017630	Pa×s	303.15	Viscosi...
η	0.0017880	Pa×s	303.15	Densiti...
η	0.0017580	Pa×s	303.15	Studies...
η	0.0017880	Pa×s	303.15	Densiti...
η	0.0017520	Pa×s	303.15	Viscosi...
η	0.0017820	Pa×s	303.15	Viscosi...
η	0.0015242	Pa×s	308.15	Densiti...
η	0.0015630	Pa×s	308.15	Densiti...
η	0.0015529	Pa×s	308.15	Densiti...
η	0.0015730	Pa×s	308.15	Studies...
η	0.0015630	Pa×s	308.15	Densiti...
η	0.0011300	Pa×s	313.00	Ultraso...
η	0.0013297	Pa×s	313.15	Experim...
η	0.0013350	Pa×s	313.15	Viscosi...
η	0.0013472	Pa×s	313.15	Densiti...
η	0.0012880	Pa×s	313.15	Densiti...
η	0.0013790	Pa×s	313.15	Densiti...
η	0.0013780	Pa×s	313.15	Densiti...
η	0.0013554	Pa×s	313.15	Densiti...
η	0.0011822	Pa×s	318.15	Densiti...
η	0.0010145	Pa×s	323.15	Experim...
η	0.0010380	Pa×s	323.15	Viscosi...
η	0.0010411	Pa×s	323.15	Densiti...
η	0.0010020	Pa×s	323.15	Densiti...
η	0.0006241	Pa×s	333.15	Experim...
η	0.0007890	Pa×s	333.15	Densiti...
η	0.0006260	Pa×s	343.15	Densiti...
σcond	[5.20e-05; 8.43e-05]	S/m	[298.15; 318.15]
σcond	5.20e-05	S/m	298.15	Electri...
σcond	7.00e-05	S/m	303.15	Electri...
σcond	7.50e-05	S/m	308.15	Electri...
σcond	8.08e-05	S/m	313.15	Electri...
σcond	8.43e-05	S/m	318.15	Electri...
ΔfusH	[5.30; 5.41]	kJ/mol	[184.60; 185.20]
ΔfusH	5.30	kJ/mol	184.60	NIST
ΔfusH	5.30	kJ/mol	184.60	NIST
ΔfusH	5.37	kJ/mol	184.67	NIST
ΔfusH	5.37	kJ/mol	184.70	NIST
ΔfusH	5.41	kJ/mol	185.20	NIST
ΔfusH	5.41	kJ/mol	185.20	NIST
ΔfusH	5.41	kJ/mol	185.20	NIST
ΔvapH	[10.50; 50.30]	kJ/mol	[211.50; 503.00]
ΔvapH	50.30	kJ/mol	211.50	NIST
ΔvapH	45.50	kJ/mol	318.00	NIST
ΔvapH	45.70	kJ/mol	323.50	NIST
ΔvapH	43.20	kJ/mol	324.00	NIST
ΔvapH	43.40 ± 0.08	kJ/mol	324.11	NIST
ΔvapH	44.80	kJ/mol	327.50	NIST
ΔvapH	42.70 ± 0.10	kJ/mol	330.00	NIST
ΔvapH	43.20	kJ/mol	338.50	NIST
ΔvapH	41.70	kJ/mol	339.00	NIST
ΔvapH	43.10	kJ/mol	343.50	NIST
ΔvapH	41.00 ± 0.10	kJ/mol	346.00	NIST
ΔvapH	42.80	kJ/mol	346.00	NIST
ΔvapH	39.80	kJ/mol	355.00	NIST
ΔvapH	39.80 ± 0.10	kJ/mol	355.00	NIST
ΔvapH	39.80	kJ/mol	355.00	NIST
ΔvapH	39.85	kJ/mol	355.40	NIST
ΔvapH	39.83	kJ/mol	355.50	KDB
ΔvapH	42.00	kJ/mol	357.50	NIST
ΔvapH	38.90 ± 0.10	kJ/mol	363.00	NIST
ΔvapH	41.30	kJ/mol	366.50	NIST
ΔvapH	41.10	kJ/mol	387.00	NIST
ΔvapH	39.20	kJ/mol	420.00	NIST
ΔvapH	29.70	kJ/mol	423.00	NIST
ΔvapH	39.10	kJ/mol	451.50	NIST
ΔvapH	23.70	kJ/mol	453.00	NIST
ΔvapH	35.30	kJ/mol	480.50	NIST
ΔvapH	16.50	kJ/mol	483.00	NIST
ΔvapH	10.50	kJ/mol	503.00	NIST
Pvap	[5.78; 4362.00]	kPa	[297.80; 503.15]
Pvap	5.78	kPa	297.80	An expe...
Pvap	5.80	kPa	298.15	Vapor-P...
Pvap	8.00	kPa	303.10	An expe...
Pvap	7.93	kPa	303.15	Solubil...
Pvap	7.86	kPa	303.15	Vapor-P...
Pvap	10.72	kPa	308.15	Solubil...
Pvap	10.52	kPa	308.15	Vapor-P...
Pvap	13.77	kPa	313.11	Vapour ...
Pvap	13.94	kPa	313.15	Vapor-P...
Pvap	16.22	kPa	315.80	An expe...
Pvap	17.46	kPa	317.07	Isobari...
Pvap	17.98	kPa	317.65	Isobari...
Pvap	18.39	kPa	318.10	Isobari...
Pvap	18.24	kPa	318.15	Vapor-P...
Pvap	19.01	kPa	318.73	Isobari...
Pvap	19.48	kPa	319.19	Isobari...
Pvap	20.03	kPa	319.72	Isobari...
Pvap	20.52	kPa	320.19	Isobari...
Pvap	21.00	kPa	320.65	Isobari...
Pvap	21.49	kPa	321.11	Isobari...
Pvap	22.03	kPa	321.58	Isobari...
Pvap	22.55	kPa	322.07	Isobari...
Pvap	23.03	kPa	322.47	Isobari...
Pvap	23.52	kPa	322.91	Isobari...
Pvap	23.64	kPa	323.15	Vapor-P...
Pvap	23.47	kPa	323.16	Isother...
Pvap	23.60	kPa	323.19	Vapor L...
Pvap	24.02	kPa	323.32	Isobari...
Pvap	24.51	kPa	323.71	Isobari...
Pvap	25.03	kPa	324.13	Isobari...
Pvap	25.48	kPa	324.49	Isobari...
Pvap	26.04	kPa	324.94	Isobari...
Pvap	26.52	kPa	325.30	Isobari...
Pvap	27.08	kPa	325.72	Isobari...
Pvap	27.69	kPa	326.18	Isobari...
Pvap	28.19	kPa	326.53	Isobari...
Pvap	28.83	kPa	326.99	Isobari...
Pvap	29.45	kPa	327.46	Isobari...
Pvap	30.08	kPa	327.86	Isobari...
Pvap	30.35	kPa	328.15	Vapor-P...
Pvap	30.96	kPa	328.47	Isobari...
Pvap	31.86	kPa	329.06	Isobari...
Pvap	32.76	kPa	329.64	Isobari...
Pvap	33.77	kPa	330.26	Isobari...
Pvap	34.52	kPa	330.73	Isobari...
Pvap	35.48	kPa	331.32	Isobari...
Pvap	36.37	kPa	331.83	Isobari...
Pvap	36.47	kPa	332.03	Vapor L...
Pvap	36.06	kPa	332.10	An expe...
Pvap	37.45	kPa	332.44	Isobari...
Pvap	38.41	kPa	332.99	Isobari...
Pvap	38.59	kPa	333.15	Vapor-P...
Pvap	39.33	kPa	333.50	Isobari...
Pvap	39.54	kPa	333.72	Vapor-L...
Pvap	40.00	kPa	333.94	Isobari...
Pvap	40.41	kPa	334.10	Isobari...
Pvap	41.44	kPa	334.60	Isobari...
Pvap	42.44	kPa	335.12	Isobari...
Pvap	43.46	kPa	335.64	Isobari...
Pvap	44.38	kPa	336.11	Isobari...
Pvap	45.32	kPa	336.55	Isobari...
Pvap	46.34	kPa	337.07	Isobari...
Pvap	47.28	kPa	337.50	Isobari...
Pvap	48.35	kPa	337.98	Isobari...
Pvap	48.66	kPa	338.15	Vapor-P...
Pvap	49.34	kPa	338.45	Isobari...
Pvap	50.25	kPa	338.86	Isobari...
Pvap	51.26	kPa	339.30	Isobari...
Pvap	52.33	kPa	339.72	Isobari...
Pvap	53.01	kPa	340.04	Isobari...
Pvap	53.33	kPa	340.18	Isobari...
Pvap	53.94	kPa	340.43	Isobari...
Pvap	55.03	kPa	340.89	Isobari...
Pvap	55.03	kPa	340.98	Vapor-L...
Pvap	55.92	kPa	341.25	Isobari...
Pvap	56.96	kPa	341.69	Isobari...
Pvap	58.05	kPa	342.09	Isobari...
Pvap	59.04	kPa	342.48	Isobari...
Pvap	59.93	kPa	342.82	Isobari...
Pvap	60.00	kPa	342.87	Isobari...
Pvap	60.66	kPa	343.15	Vapor-P...
Pvap	60.66	kPa	343.19	Vapor-L...
Pvap	60.91	kPa	343.20	Isobari...
Pvap	61.30	kPa	343.44	Vapor-L...
Pvap	61.94	kPa	343.59	Isobari...
Pvap	62.98	kPa	343.96	Isobari...
Pvap	63.92	kPa	344.32	Isobari...
Pvap	64.96	kPa	344.68	Isobari...
Pvap	63.92	kPa	344.70	An expe...
Pvap	65.23	kPa	344.86	Vapor-L...
Pvap	65.97	kPa	345.05	Isobari...
Pvap	66.66	kPa	345.25	Isobari...
Pvap	66.84	kPa	345.35	Isobari...
Pvap	68.03	kPa	345.75	Isobari...
Pvap	69.14	kPa	346.13	Isobari...
Pvap	69.47	kPa	346.33	Vapor-L...
Pvap	70.12	kPa	346.46	Isobari...
Pvap	72.04	kPa	347.11	Isobari...
Pvap	74.18	kPa	347.79	Isobari...
Pvap	75.22	kPa	348.15	Vapor-P...
Pvap	75.27	kPa	348.21	Vapor-L...
Pvap	75.96	kPa	348.37	Isobari...
Pvap	77.81	kPa	348.95	Isobari...
Pvap	79.34	kPa	349.48	Vapor-L...
Pvap	79.99	kPa	349.55	Isobari...
Pvap	80.00	kPa	349.60	Isobari...
Pvap	79.96	kPa	349.61	Isobari...
Pvap	81.58	kPa	350.08	Isobari...
Pvap	83.94	kPa	350.75	Isobari...
Pvap	85.15	kPa	351.19	Vapor-L...
Pvap	85.47	kPa	351.21	Isobari...
Pvap	87.17	kPa	351.69	Isobari...
Pvap	88.63	kPa	352.09	Isobari...
Pvap	90.24	kPa	352.54	Isobari...
Pvap	90.34	kPa	352.63	Vapor-L...
Pvap	92.44	kPa	353.15	Vapor-P...
Pvap	92.57	kPa	353.16	Isobari...
Pvap	93.80	kPa	353.30	Isother...
Pvap	93.32	kPa	353.30	Isobari...
Pvap	93.41	kPa	353.46	Vapor-L...
Pvap	94.46	kPa	353.66	Isobari...
Pvap	96.15	kPa	354.17	Vapor L...
Pvap	96.49	kPa	354.20	Isobari...
Pvap	98.05	kPa	354.59	Isobari...
Pvap	98.66	kPa	354.67	Isobari...
Pvap	100.00	kPa	355.06	Isobari...
Pvap	100.03	kPa	355.09	Isobari...
Pvap	100.00	kPa	355.09	Isobari...
Pvap	101.30	kPa	355.15	Multiph...
Pvap	101.30	kPa	355.33	Vapor L...
Pvap	101.30	kPa	355.35	Isobari...
Pvap	101.28	kPa	355.38	Isobari...
Pvap	101.06	kPa	355.40	Ammoniu...
Pvap	101.00	kPa	355.40	Experim...
Pvap	101.54	kPa	355.41	Vapor-L...
Pvap	101.07	kPa	355.42	Vapor-L...
Pvap	101.30	kPa	355.45	Isobari...
Pvap	101.32	kPa	355.60	Acetoni...
Pvap	101.32	kPa	355.65	Isobari...
Pvap	101.30	kPa	355.71	A new a...
Pvap	103.44	kPa	355.93	Isobari...
Pvap	105.38	kPa	356.40	Isobari...
Pvap	106.91	kPa	356.76	Isobari...
Pvap	108.63	kPa	357.16	Isobari...
Pvap	110.13	kPa	357.52	Isobari...
Pvap	111.88	kPa	357.93	Isobari...
Pvap	113.79	kPa	358.35	Isobari...
Pvap	115.10	kPa	358.65	Isobari...
Pvap	116.64	kPa	358.98	Isobari...
Pvap	118.64	kPa	359.43	Isobari...
Pvap	120.24	kPa	359.77	Isobari...
Pvap	121.30	kPa	359.95	Isobari...
Pvap	122.11	kPa	360.16	Isobari...
Pvap	124.03	kPa	360.57	Isobari...
Pvap	125.62	kPa	360.90	Isobari...
Pvap	127.12	kPa	361.21	Vapor-L...
Pvap	127.36	kPa	361.26	Isobari...
Pvap	129.08	kPa	361.62	Isobari...
Pvap	130.93	kPa	361.98	Isobari...
Pvap	132.35	kPa	362.26	Isobari...
Pvap	133.65	kPa	362.52	Isobari...
Pvap	144.10	kPa	364.50	Vapour ...
Pvap	144.50	kPa	364.50	Isother...
Pvap	144.10	kPa	364.51	Vapor L...
Pvap	144.20	kPa	364.51	Vapor L...
Pvap	143.90	kPa	364.52	Vapor-L...
Pvap	152.55	kPa	366.10	Vapor-L...
Pvap	161.30	kPa	367.65	Isobari...
Pvap	177.97	kPa	370.40	Vapor-L...
Pvap	200.10	kPa	373.50	Isother...
Pvap	201.30	kPa	373.65	Isobari...
Pvap	203.40	kPa	374.20	Vapor-L...
Pvap	228.82	kPa	377.60	Vapor-L...
Pvap	254.25	kPa	380.80	Vapor-L...
Pvap	593.80	kPa	408.30	Isother...
Pvap	1610.00	kPa	450.00	Pressur...
Pvap	1640.00	kPa	451.50	Pressur...
Pvap	2040.00	kPa	461.50	Pressur...
Pvap	2030.00	kPa	462.50	Pressur...
Pvap	2460.00	kPa	469.00	Pressur...
Pvap	2420.00	kPa	469.00	Pressur...
Pvap	2740.00	kPa	477.00	Pressur...
Pvap	2780.00	kPa	477.00	Pressur...
Pvap	3060.00	kPa	482.00	Pressur...
Pvap	3090.00	kPa	482.00	Pressur...
Pvap	3081.00	kPa	483.15	Measure...
Pvap	3500.00	kPa	489.00	Pressur...
Pvap	3460.00	kPa	489.50	Pressur...
Pvap	3677.00	kPa	493.15	Measure...
Pvap	3970.00	kPa	494.50	Pressur...
Pvap	4362.00	kPa	503.15	Measure...
n0	[1.35540; 1.38000]		[293.15; 323.15]
n0	1.37740		293.15	Vapour-...
n0	1.37800		293.15	Measure...
n0	1.37709		293.15	Liquid ...
n0	1.37707		293.15	Thermod...
n0	1.37740		293.15	Solid-L...
n0	1.37718		293.15	Vapor L...
n0	1.37740		293.15	Excess ...
n0	1.37660		293.15	Densiti...
n0	1.37707		293.15	Mixing ...
n0	1.37740		293.15	Vapor l...
n0	1.37710		293.20	Isobari...
n0	1.37710		293.20	Vapor L...
n0	1.37880		295.15	Isobari...
n0	1.37580		298.00	Determi...
n0	1.37496		298.15	Thermod...
n0	1.37540		298.15	sobaric...
n0	1.37520		298.15	Effect ...
n0	1.37520		298.15	(Vapor ...
n0	1.37450		298.15	Thermod...
n0	1.37540		298.15	Isobari...
n0	1.37500		298.15	Density...
n0	1.37760		298.15	Investi...
n0	1.37496		298.15	Mixing ...
n0	1.37520		298.15	Vapor-L...
n0	1.37510		298.15	(Vapor ...
n0	1.37496		298.15	Ternary...
n0	1.37500		298.15	Isobari...
n0	1.37410		298.15	Applica...
n0	1.37500		298.15	Effect ...
n0	1.37502		298.15	Isobari...
n0	1.37518		298.15	(Vapour...
n0	1.37496		298.15	Ternary...
n0	1.37527		298.15	Densiti...
n0	1.37495		298.15	Physica...
n0	1.35540		298.15	Vapor L...
n0	1.37530		298.15	Molar e...
n0	1.37523		298.15	Effect ...
n0	1.37560		298.15	Ternary...
n0	1.37497		298.15	Isobari...
n0	1.37450		298.15	Densiti...
n0	1.37450		298.15	Thermod...
n0	1.37509		298.15	Vapor-L...
n0	1.37510		298.15	Physica...
n0	1.37500		298.15	Vapor-L...
n0	1.37540		298.15	Isobari...
n0	1.37520		298.15	Activit...
n0	1.37504		298.15	Isother...
n0	1.37504		298.15	Isother...
n0	1.37650		298.15	Physico...
n0	1.37540		298.15	Effect ...
n0	1.38000		298.15	Bubble ...
n0	1.37500		298.15	Densiti...
n0	1.37500		298.15	Excess ...
n0	1.37480		298.15	Excess ...
n0	1.37450		298.15	Densiti...
n0	1.37510		298.20	Isobari...
n0	1.37410		303.15	Physico...
n0	1.37400		303.15	Densiti...
n0	1.37210		303.15	Thermod...
n0	1.37210		303.15	Thermod...
n0	1.37360		303.15	Solute-...
n0	1.37278		303.15	Mixing ...
n0	1.37410		303.15	Experim...
n0	1.37240		303.15	Densiti...
n0	1.37314		303.15	Densiti...
n0	1.37278		303.15	Thermod...
n0	1.37093		308.15	Densiti...
n0	1.37030		308.15	Densiti...
n0	1.37160		308.15	Physico...
n0	1.37020		308.15	Thermod...
n0	1.37020		308.15	Thermod...
n0	1.37300		308.15	Densiti...
n0	1.37063		308.15	Densiti...
n0	1.37200		313.15	Densiti...
n0	1.36870		313.15	Densiti...
n0	1.36040		323.15	Physica...
ρl	[738.91; 810.90]	kg/m3	[263.10; 343.30]
ρl	810.90	kg/m3	263.10	Effect ...
ρl	797.50	kg/m3	278.15	Thermop...
ρl	795.30	kg/m3	283.10	Effect ...
ρl	794.00	kg/m3	283.15	Densiti...
ρl	793.67	kg/m3	283.15	Propert...
ρl	793.31	kg/m3	283.15	Volumet...
ρl	789.40	kg/m3	288.15	Thermop...
ρl	789.34	kg/m3	288.15	Volumet...
ρl	789.58	kg/m3	288.15	Propert...
ρl	789.18	kg/m3	288.15	Mass de...
ρl	789.68	kg/m3	288.15	Densiti...
ρl	789.22	kg/m3	288.15	The exc...
ρl	789.41	kg/m3	288.15	Excess ...
ρl	789.34	kg/m3	288.15	Excess ...
ρl	789.18	kg/m3	288.15	Thermop...
ρl	789.22	kg/m3	288.15	Volumet...
ρl	786.00	kg/m3	293.00	KDB
ρl	785.00	kg/m3	293.15	Density...
ρl	785.10	kg/m3	293.15	Volumet...
ρl	785.40	kg/m3	293.15	Evaluat...
ρl	785.29	kg/m3	293.15	Excess ...
ρl	785.10	kg/m3	293.15	Volumet...
ρl	785.40	kg/m3	293.15	Densiti...
ρl	786.00	kg/m3	293.15	Effect ...
ρl	785.08	kg/m3	293.15	Volumet...
ρl	785.24	kg/m3	293.15	Measure...
ρl	785.09	kg/m3	293.15	The exc...
ρl	785.25	kg/m3	293.15	Density...
ρl	785.90	kg/m3	293.15	Measure...
ρl	785.81	kg/m3	293.15	Investi...
ρl	785.30	kg/m3	293.15	Densiti...
ρl	785.40	kg/m3	293.15	Studies...
ρl	785.40	kg/m3	293.15	Thermod...
ρl	785.40	kg/m3	293.15	Influen...
ρl	785.74	kg/m3	293.15	Molecul...
ρl	785.10	kg/m3	293.15	Densiti...
ρl	784.90	kg/m3	293.15	Density...
ρl	785.20	kg/m3	293.15	Volumet...
ρl	786.00	kg/m3	293.15	Composi...
ρl	785.10	kg/m3	293.15	Osmotic...
ρl	791.50	kg/m3	293.15	Liquid ...
ρl	786.91	kg/m3	293.15	Experim...
ρl	785.44	kg/m3	293.15	Propert...
ρl	785.35	kg/m3	293.15	Density...
ρl	785.18	kg/m3	293.15	Densiti...
ρl	784.96	kg/m3	293.15	Densiti...
ρl	785.76	kg/m3	293.15	Densiti...
ρl	784.30	kg/m3	295.30	Effect ...
ρl	781.40	kg/m3	298.15	Liquid-...
ρl	780.79	kg/m3	298.15	Solid-l...
ρl	781.30	kg/m3	298.15	Bubble ...
ρl	782.45	kg/m3	298.15	Experim...
ρl	781.60	kg/m3	298.15	Thermop...
ρl	781.23	kg/m3	298.15	ACSExce...
ρl	781.05	kg/m3	298.15	Densiti...
ρl	780.99	kg/m3	298.15	Excess ...
ρl	780.80	kg/m3	298.15	Determi...
ρl	780.80	kg/m3	298.15	Density...
ρl	782.45	kg/m3	298.15	Isobari...
ρl	781.31	kg/m3	298.15	Densiti...
ρl	780.90	kg/m3	298.15	Dynamic...
ρl	781.18	kg/m3	298.15	Densiti...
ρl	780.70	kg/m3	298.15	Density...
ρl	781.40	kg/m3	298.15	Phase d...
ρl	782.45	kg/m3	298.15	Experim...
ρl	781.00	kg/m3	298.15	Composi...
ρl	781.40	kg/m3	298.15	Determi...
ρl	781.10	kg/m3	298.15	Density...
ρl	780.95	kg/m3	298.15	Densiti...
ρl	781.08	kg/m3	298.15	Densiti...
ρl	779.36	kg/m3	298.15	Vapor L...
ρl	781.10	kg/m3	298.15	Isobari...
ρl	781.10	kg/m3	298.15	Thermod...
ρl	781.59	kg/m3	298.15	Molecul...
ρl	782.00	kg/m3	298.15	Isobari...
ρl	781.10	kg/m3	298.15	Influen...
ρl	781.08	kg/m3	298.15	Measure...
ρl	780.90	kg/m3	298.15	A combi...
ρl	780.90	kg/m3	298.15	(Liquid...
ρl	780.80	kg/m3	298.15	Measure...
ρl	780.60	kg/m3	298.15	Solubil...
ρl	781.18	kg/m3	298.15	Isobari...
ρl	781.10	kg/m3	298.15	Thermod...
ρl	781.10	kg/m3	298.15	Studies...
ρl	782.70	kg/m3	298.15	Solubil...
ρl	781.18	kg/m3	298.15	Liquid ...
ρl	780.84	kg/m3	298.15	Thermop...
ρl	782.70	kg/m3	298.15	Liquid ...
ρl	781.20	kg/m3	298.15	Excess ...
ρl	781.10	kg/m3	298.15	Solubil...
ρl	781.20	kg/m3	298.15	Measure...
ρl	781.11	kg/m3	298.15	Experim...
ρl	781.59	kg/m3	298.15	Thermod...
ρl	781.34	kg/m3	298.15	Investi...
ρl	798.00	kg/m3	298.15	Liquid ...
ρl	781.05	kg/m3	298.15	Density...
ρl	781.21	kg/m3	298.15	Liquid ...
ρl	781.21	kg/m3	298.15	Modifie...
ρl	781.05	kg/m3	298.15	The stu...
ρl	780.89	kg/m3	298.15	The exc...
ρl	780.89	kg/m3	298.15	Refract...
ρl	781.09	kg/m3	298.15	Densiti...
ρl	781.10	kg/m3	298.15	Densiti...
ρl	781.32	kg/m3	298.15	Liquid ...
ρl	781.08	kg/m3	298.15	Excess ...
ρl	781.10	kg/m3	298.15	Evaluat...
ρl	780.87	kg/m3	298.15	Volumet...
ρl	780.99	kg/m3	298.15	Volumet...
ρl	781.00	kg/m3	298.15	Thermop...
ρl	780.91	kg/m3	298.15	Isother...
ρl	781.40	kg/m3	298.15	Liquid-...
ρl	781.40	kg/m3	298.15	Effect ...
ρl	781.35	kg/m3	298.15	Binary ...
ρl	780.98	kg/m3	298.15	Topolog...
ρl	780.35	kg/m3	298.15	Excess ...
ρl	781.34	kg/m3	298.15	Binary ...
ρl	781.24	kg/m3	298.15	Propert...
ρl	781.50	kg/m3	298.15	Solubil...
ρl	780.90	kg/m3	298.15	Apparen...
ρl	781.00	kg/m3	298.15	Density...
ρl	780.69	kg/m3	298.15	Liquid-...
ρl	780.75	kg/m3	298.15	Densiti...
ρl	780.86	kg/m3	298.15	Mass de...
ρl	781.91	kg/m3	298.15	Speeds ...
ρl	780.95	kg/m3	298.15	Excess ...
ρl	780.91	kg/m3	298.15	Volumet...
ρl	780.60	kg/m3	298.15	Densiti...
ρl	780.85	kg/m3	298.20	A green...
ρl	776.63	kg/m3	303.15	Volumet...
ρl	776.80	kg/m3	303.15	Densiti...
ρl	776.66	kg/m3	303.15	Densiti...
ρl	777.28	kg/m3	303.15	Densiti...
ρl	776.54	kg/m3	303.15	Densiti...
ρl	776.60	kg/m3	303.15	Densiti...
ρl	776.80	kg/m3	303.15	Influen...
ρl	776.80	kg/m3	303.15	Studies...
ρl	776.80	kg/m3	303.15	Thermod...
ρl	777.00	kg/m3	303.15	Density...
ρl	776.97	kg/m3	303.15	Propert...
ρl	776.80	kg/m3	303.15	Thermod...
ρl	777.00	kg/m3	303.15	Liquid ...
ρl	776.79	kg/m3	303.15	Densiti...
ρl	777.06	kg/m3	303.15	Investi...
ρl	777.00	kg/m3	303.15	Composi...
ρl	776.78	kg/m3	303.15	Density...
ρl	776.60	kg/m3	303.15	Volumet...
ρl	776.40	kg/m3	303.15	Density...
ρl	776.76	kg/m3	303.15	Measure...
ρl	776.57	kg/m3	303.15	Volumet...
ρl	776.63	kg/m3	303.15	Densiti...
ρl	776.72	kg/m3	303.15	Volumet...
ρl	776.86	kg/m3	303.15	Density...
ρl	777.50	kg/m3	303.15	Density...
ρl	776.62	kg/m3	303.15	The exc...
ρl	776.81	kg/m3	303.15	Excess ...
ρl	777.47	kg/m3	303.15	Molecul...
ρl	777.30	kg/m3	303.15	Viscous...
ρl	776.80	kg/m3	303.15	Densiti...
ρl	776.80	kg/m3	303.15	Evaluat...
ρl	776.80	kg/m3	303.15	Measure...
ρl	777.50	kg/m3	303.60	Effect ...
ρl	772.40	kg/m3	308.15	Evaluat...
ρl	772.41	kg/m3	308.15	The stu...
ρl	772.46	kg/m3	308.15	Excess ...
ρl	772.27	kg/m3	308.15	The exc...
ρl	772.51	kg/m3	308.15	Density...
ρl	772.31	kg/m3	308.15	Osmotic...
ρl	772.02	kg/m3	308.15	Investi...
ρl	772.40	kg/m3	308.15	Thermop...
ρl	772.10	kg/m3	308.15	Density...
ρl	772.45	kg/m3	308.15	Measure...
ρl	772.42	kg/m3	308.15	Density...
ρl	772.48	kg/m3	308.15	Densiti...
ρl	772.30	kg/m3	308.15	Densiti...
ρl	772.26	kg/m3	308.15	Mass de...
ρl	773.15	kg/m3	308.15	Molecul...
ρl	772.23	kg/m3	308.15	Thermop...
ρl	772.62	kg/m3	308.15	Propert...
ρl	772.39	kg/m3	308.15	Densiti...
ρl	772.40	kg/m3	308.15	Densiti...
ρl	772.40	kg/m3	308.15	Thermod...
ρl	772.40	kg/m3	308.15	Thermod...
ρl	772.43	kg/m3	308.15	Densiti...
ρl	772.32	kg/m3	308.15	Densiti...
ρl	772.40	kg/m3	308.15	Studies...
ρl	772.25	kg/m3	308.15	Volumet...
ρl	772.32	kg/m3	308.15	Densiti...
ρl	772.24	kg/m3	308.15	Volumet...
ρl	772.40	kg/m3	308.15	Influen...
ρl	772.37	kg/m3	308.15	Volumet...
ρl	768.02	kg/m3	313.15	Measure...
ρl	768.45	kg/m3	313.15	Molecul...
ρl	768.00	kg/m3	313.15	Influen...
ρl	767.92	kg/m3	313.15	Excess ...
ρl	768.00	kg/m3	313.15	Studies...
ρl	768.00	kg/m3	313.15	Thermod...
ρl	768.00	kg/m3	313.15	Experim...
ρl	767.76	kg/m3	313.15	Densiti...
ρl	768.00	kg/m3	313.15	Densiti...
ρl	767.85	kg/m3	313.15	Densiti...
ρl	769.70	kg/m3	313.15	Investi...
ρl	767.96	kg/m3	313.15	Measure...
ρl	767.81	kg/m3	313.15	Volumet...
ρl	767.83	kg/m3	313.15	The exc...
ρl	768.00	kg/m3	313.15	Evaluat...
ρl	768.07	kg/m3	313.15	Density...
ρl	768.80	kg/m3	313.15	Density...
ρl	768.00	kg/m3	313.15	Total P...
ρl	767.93	kg/m3	313.15	Volumet...
ρl	768.02	kg/m3	313.15	Excess ...
ρl	767.90	kg/m3	313.15	Densiti...
ρl	768.00	kg/m3	313.15	Composi...
ρl	767.84	kg/m3	313.15	Volumet...
ρl	767.60	kg/m3	313.15	Density...
ρl	768.11	kg/m3	313.15	Densiti...
ρl	767.99	kg/m3	313.15	Densiti...
ρl	767.83	kg/m3	313.15	Densiti...
ρl	768.18	kg/m3	313.15	Propert...
ρl	768.20	kg/m3	313.15	Liquid ...
ρl	768.00	kg/m3	313.15	Density...
ρl	767.82	kg/m3	313.15	Volumet...
ρl	767.80	kg/m3	313.15	Thermod...
ρl	767.99	kg/m3	313.15	Density...
ρl	768.48	kg/m3	313.15	Densiti...
ρl	763.47	kg/m3	318.15	Densiti...
ρl	763.30	kg/m3	318.15	Densiti...
ρl	763.51	kg/m3	318.15	Density...
ρl	763.28	kg/m3	318.15	Volumet...
ρl	763.88	kg/m3	318.15	Densiti...
ρl	763.40	kg/m3	318.15	Studies...
ρl	763.49	kg/m3	318.15	Measure...
ρl	763.40	kg/m3	318.15	Influen...
ρl	763.27	kg/m3	318.15	Thermop...
ρl	763.40	kg/m3	318.15	Thermod...
ρl	763.40	kg/m3	318.15	Densiti...
ρl	763.29	kg/m3	318.15	The exc...
ρl	763.41	kg/m3	318.15	The stu...
ρl	763.40	kg/m3	318.15	Evaluat...
ρl	763.65	kg/m3	318.15	Propert...
ρl	763.40	kg/m3	318.15	Thermop...
ρl	763.90	kg/m3	318.15	Densiti...
ρl	763.61	kg/m3	318.15	Densiti...
ρl	763.30	kg/m3	318.15	Mass de...
ρl	763.19	kg/m3	318.15	Volumet...
ρl	763.10	kg/m3	318.15	Density...
ρl	763.48	kg/m3	318.15	Excess ...
ρl	758.71	kg/m3	323.15	Densiti...
ρl	758.55	kg/m3	323.15	Volumet...
ρl	758.84	kg/m3	323.15	Measure...
ρl	759.31	kg/m3	323.15	Densiti...
ρl	759.00	kg/m3	323.15	Density...
ρl	758.89	kg/m3	323.15	Density...
ρl	759.00	kg/m3	323.15	Composi...
ρl	759.01	kg/m3	323.15	Propert...
ρl	758.80	kg/m3	323.15	Studies...
ρl	758.68	kg/m3	323.15	Densiti...
ρl	758.63	kg/m3	323.15	Osmotic...
ρl	758.80	kg/m3	323.15	Densiti...
ρl	759.70	kg/m3	323.15	Density...
ρl	758.80	kg/m3	323.15	Influen...
ρl	758.68	kg/m3	323.15	Volumet...
ρl	758.85	kg/m3	323.15	Densiti...
ρl	758.79	kg/m3	323.15	Measure...
ρl	758.80	kg/m3	323.15	Evaluat...
ρl	758.64	kg/m3	323.15	Volumet...
ρl	758.70	kg/m3	323.15	Osmotic...
ρl	758.60	kg/m3	323.15	Densiti...
ρl	759.00	kg/m3	323.15	Liquid ...
ρl	758.50	kg/m3	323.15	Density...
ρl	758.80	kg/m3	323.15	Thermod...
ρl	760.10	kg/m3	323.40	Effect ...
ρl	754.10	kg/m3	328.15	Thermop...
ρl	753.88	kg/m3	328.15	Volumet...
ρl	753.12	kg/m3	328.15	The stu...
ρl	754.19	kg/m3	328.15	Density...
ρl	754.26	kg/m3	328.15	Propert...
ρl	754.00	kg/m3	328.15	Excess ...
ρl	753.80	kg/m3	328.15	Densiti...
ρl	754.84	kg/m3	328.15	Densiti...
ρl	753.89	kg/m3	328.15	Thermop...
ρl	753.91	kg/m3	328.15	Mass de...
ρl	749.39	kg/m3	333.15	Propert...
ρl	749.25	kg/m3	333.15	Density...
ρl	750.00	kg/m3	333.15	Density...
ρl	749.06	kg/m3	333.15	Densiti...
ρl	750.00	kg/m3	333.15	Composi...
ρl	749.16	kg/m3	333.15	Measure...
ρl	748.90	kg/m3	333.15	Densiti...
ρl	749.68	kg/m3	333.15	Densiti...
ρl	749.01	kg/m3	333.15	Volumet...
ρl	744.02	kg/m3	338.15	Thermop...
ρl	743.66	kg/m3	338.15	Density...
ρl	739.50	kg/m3	343.15	Density...
ρl	739.53	kg/m3	343.15	Densiti...
ρl	738.91	kg/m3	343.15	Densiti...
ρl	741.00	kg/m3	343.30	Effect ...
ΔfusS	[28.70; 29.21]	J/mol×K	[184.60; 185.20]
ΔfusS	28.72	J/mol×K	184.60	NIST
ΔfusS	28.70	J/mol×K	184.60	NIST
ΔfusS	29.09	J/mol×K	184.67	NIST
ΔfusS	29.21	J/mol×K	185.20	NIST
csound,fluid	[1032.57; 1208.50]	m/s	[278.15; 328.15]
csound,fluid	1208.50	m/s	278.15	Ultraso...
csound,fluid	1191.88	m/s	283.15	Thermop...
csound,fluid	1173.07	m/s	288.15	Ultraso...
csound,fluid	1157.30	m/s	293.15	Acousti...
csound,fluid	1138.16	m/s	298.15	Ultraso...
csound,fluid	1139.17	m/s	298.15	Thermop...
csound,fluid	1104.80	m/s	308.15	Acousti...
csound,fluid	1103.25	m/s	308.15	Ultraso...
csound,fluid	1086.62	m/s	313.15	Thermop...
csound,fluid	1068.09	m/s	318.15	Ultraso...
csound,fluid	1051.60	m/s	323.15	Acousti...
csound,fluid	1032.57	m/s	328.15	Ultraso...
γ	[0.02; 0.02]	N/m	[288.15; 333.20]
γ	0.02	N/m	288.15	Densiti...
γ	0.02	N/m	288.15	Densiti...
γ	0.02	N/m	288.15	The mol...
γ	0.02	N/m	293.15	The mol...
γ	0.02	N/m	293.15	Surface...
γ	0.02	N/m	293.20	Surface...
γ	0.02	N/m	293.20	KDB
γ	0.02	N/m	298.15	Densiti...
γ	0.02	N/m	298.15	Surface...
γ	0.02	N/m	298.15	Densiti...
γ	0.02	N/m	298.15	Densiti...
γ	0.02	N/m	298.15	Effect ...
γ	0.02	N/m	298.15	Experim...
γ	0.02	N/m	298.15	The mol...
γ	0.02	N/m	303.15	Surface...
γ	0.02	N/m	303.15	The mol...
γ	0.02	N/m	303.20	Surface...
γ	0.02	N/m	308.15	Effect ...
γ	0.02	N/m	308.15	Densiti...
γ	0.02	N/m	308.15	The mol...
γ	0.02	N/m	308.15	Densiti...
γ	0.02	N/m	308.15	Surface...
γ	0.02	N/m	308.15	Densiti...
γ	0.02	N/m	313.15	Surface...
γ	0.02	N/m	313.15	The mol...
γ	0.02	N/m	313.20	Surface...
γ	0.02	N/m	318.15	Surface...
γ	0.02	N/m	318.15	Effect ...
γ	0.02	N/m	318.15	The mol...
γ	0.02	N/m	318.15	Densiti...
γ	0.02	N/m	323.15	Surface...
γ	0.02	N/m	323.20	Surface...
γ	0.02	N/m	328.15	Effect ...
γ	0.02	N/m	333.20	Surface...

Pressure Dependent Properties

Property	Value	Unit	Pressure (kPa)	Source
Tboil	355.01	K	100.00	Isobari...

Datasets

1. Molar heat capacity at constant pressure, J/K/mol (1)
2. Viscosity, Pa*s (1)
3. Refractive index (Na D-line) (2)
4. Mass density, kg/m3 (8)
5. Speed of sound, m/s (2)
6. Molar volume, m3/mol (1)

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

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Molar heat capacity at constant pressure, J/K/mol - Liquid
253.15	100.00	129.40
253.15	20000.00	126.10
253.15	40000.00	125.80
258.15	100.00	130.60
258.15	20000.00	128.30
258.15	40000.00	127.30
263.15	100.00	132.60
263.15	20000.00	130.70
263.15	40000.00	129.20
268.15	100.00	135.00
268.15	20000.00	133.40
268.15	40000.00	131.50
273.15	100.00	138.00
273.15	20000.00	136.30
273.15	40000.00	134.00
278.15	100.00	141.40
278.15	20000.00	139.40
278.15	40000.00	136.80
283.15	100.00	145.10
283.15	20000.00	142.60
283.15	40000.00	140.00
288.15	100.00	148.90
288.15	20000.00	146.00
288.15	40000.00	143.30
293.15	100.00	152.90
293.15	20000.00	149.60
293.15	40000.00	146.90
298.15	100.00	157.00
298.15	20000.00	153.30
298.15	40000.00	150.70
303.15	100.00	161.10
303.15	20000.00	157.10
303.15	40000.00	154.70
308.15	100.00	165.00
308.15	20000.00	161.10
308.15	40000.00	159.00
313.15	100.00	168.60
313.15	20000.00	165.00
313.15	40000.00	163.30
318.15	100.00	171.90
318.15	20000.00	169.10
318.15	40000.00	167.80
323.15	100.00	174.90
323.15	20000.00	173.20
323.15	40000.00	172.40
Reference

Viscosity, Pa*s

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Viscosity, Pa*s - Liquid
298.15	81.50	0.0021
Reference

Refractive index (Na D-line)

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Refractive index (Na D-line) - Liquid
298.15	101.33	1.3752
293.15	101.00	1.3772
303.15	101.00	1.3729
313.15	101.00	1.3685
323.15	101.00	1.3636
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Refractive index (Na D-line) - Liquid
298.15	100.00	1.375
Reference

Mass density, kg/m3

Fixed		Measured
Pressure, kPa - Liquid	Temperature, K - Liquid	Mass density, kg/m3 - Liquid
100.00	313.15	767.67
5000.00	313.15	772.3
10000.00	313.15	776.83
15000.00	313.15	781.04
20000.00	313.15	785.09
25000.00	313.15	788.94
30000.00	313.15	792.51
35000.00	313.15	796.05
40000.00	313.15	799.39
50000.00	313.15	805.89
60000.00	313.15	811.8
70000.00	313.15	817.44
80000.00	313.15	822.71
90000.00	313.15	827.67
100000.00	313.15	832.64
110000.00	313.15	837.15
120000.00	313.15	841.57
130000.00	313.15	845.79
140000.00	313.15	849.83
100.00	323.15	758.87
5000.00	323.15	763.96
10000.00	323.15	768.84
15000.00	323.15	773.34
20000.00	323.15	777.63
25000.00	323.15	781.69
30000.00	323.15	785.6
35000.00	323.15	789.17
40000.00	323.15	792.74
50000.00	323.15	799.4
60000.00	323.15	805.57
70000.00	323.15	811.34
80000.00	323.15	816.78
90000.00	323.15	822.03
100000.00	323.15	826.88
110000.00	323.15	831.63
120000.00	323.15	836.11
130000.00	323.15	840.39
140000.00	323.15	844.6
100.00	333.15	749.24
5000.00	333.15	754.45
10000.00	333.15	759.66
15000.00	333.15	764.42
20000.00	333.15	768.95
25000.00	333.15	773.18
30000.00	333.15	777.21
35000.00	333.15	781.18
40000.00	333.15	784.88
50000.00	333.15	791.92
60000.00	333.15	798.25
70000.00	333.15	804.32
80000.00	333.15	810.15
90000.00	333.15	815.49
100000.00	333.15	820.8
110000.00	333.15	825.59
120000.00	333.15	830.23
130000.00	333.15	834.5
140000.00	333.15	838.74
100.00	343.15	738.88
5000.00	343.15	744.75
10000.00	343.15	750.17
15000.00	343.15	755.4
20000.00	343.15	760.17
25000.00	343.15	764.81
30000.00	343.15	769.03
35000.00	343.15	773.28
40000.00	343.15	777.23
50000.00	343.15	784.53
60000.00	343.15	791.22
70000.00	343.15	797.48
80000.00	343.15	803.44
90000.00	343.15	808.87
100000.00	343.15	814.1
110000.00	343.15	819.16
120000.00	343.15	823.87
130000.00	343.15	828.44
140000.00	343.15	832.84
100.00	353.15	728.44
5000.00	353.15	734.66
10000.00	353.15	740.52
15000.00	353.15	745.99
20000.00	353.15	751.21
25000.00	353.15	756.02
30000.00	353.15	760.43
35000.00	353.15	764.79
40000.00	353.15	768.87
50000.00	353.15	777.01
60000.00	353.15	783.94
70000.00	353.15	790.65
80000.00	353.15	796.56
90000.00	353.15	802.3
100000.00	353.15	807.6
110000.00	353.15	812.87
120000.00	353.15	817.76
130000.00	353.15	822.37
140000.00	353.15	826.85
5000.00	363.15	723.93
10000.00	363.15	730.44
15000.00	363.15	736.42
20000.00	363.15	741.95
25000.00	363.15	747.05
30000.00	363.15	751.95
35000.00	363.15	756.37
40000.00	363.15	760.76
50000.00	363.15	769.06
60000.00	363.15	776.43
70000.00	363.15	783.33
80000.00	363.15	789.52
90000.00	363.15	795.58
100000.00	363.15	801.38
110000.00	363.15	806.5
120000.00	363.15	811.57
130000.00	363.15	816.39
140000.00	363.15	820.9
5000.00	373.15	712.57
10000.00	373.15	719.75
15000.00	373.15	726.13
20000.00	373.15	732.08
25000.00	373.15	737.65
30000.00	373.15	742.73
35000.00	373.15	747.59
40000.00	373.15	752.29
50000.00	373.15	760.75
60000.00	373.15	768.5
70000.00	373.15	775.82
80000.00	373.15	782.24
90000.00	373.15	788.49
100000.00	373.15	794.34
110000.00	373.15	799.85
120000.00	373.15	805.17
130000.00	373.15	810.06
140000.00	373.15	814.94
5000.00	383.15	700.32
10000.00	383.15	708.06
15000.00	383.15	715.03
20000.00	383.15	721.43
25000.00	383.15	727.35
30000.00	383.15	732.77
35000.00	383.15	737.95
40000.00	383.15	742.76
50000.00	383.15	751.85
60000.00	383.15	760.06
70000.00	383.15	767.53
80000.00	383.15	774.49
90000.00	383.15	780.94
100000.00	383.15	786.9
110000.00	383.15	792.77
120000.00	383.15	798.27
130000.00	383.15	803.3
140000.00	383.15	808.26
5000.00	393.15	687.82
10000.00	393.15	696.15
15000.00	393.15	703.77
20000.00	393.15	710.73
25000.00	393.15	717.07
30000.00	393.15	722.91
35000.00	393.15	728.4
40000.00	393.15	733.66
50000.00	393.15	743.39
60000.00	393.15	751.87
70000.00	393.15	759.71
80000.00	393.15	766.86
90000.00	393.15	773.67
100000.00	393.15	779.96
110000.00	393.15	785.9
120000.00	393.15	791.54
130000.00	393.15	796.8
140000.00	393.15	801.97
5000.00	403.15	674.03
10000.00	403.15	683.54
15000.00	403.15	691.9
20000.00	403.15	699.4
25000.00	403.15	706.26
30000.00	403.15	712.66
35000.00	403.15	718.38
40000.00	403.15	724.01
50000.00	403.15	734.72
60000.00	403.15	743.58
70000.00	403.15	751.89
80000.00	403.15	759.17
90000.00	403.15	766.2
100000.00	403.15	772.7
110000.00	403.15	778.85
120000.00	403.15	784.7
130000.00	403.15	790.2
140000.00	403.15	795.51
Reference

Fixed		Measured
Pressure, kPa - Liquid	Temperature, K - Liquid	Mass density, kg/m3 - Liquid
117.90	280.21	797.61
186.70	300.09	780.22
202.70	325.12	757.05
220.40	350.14	731.92
349.50	375.01	702.23
407.60	392.57	679.26
439.60	280.21	797.89
609.40	325.12	757.49
610.50	300.09	780.62
663.40	350.14	732.49
703.30	375.01	702.82
888.70	392.57	680.18
938.70	280.21	798.29
953.40	300.09	780.94
960.00	325.12	757.87
1046.80	375.01	703.38
1071.20	350.14	733.03
1171.40	392.57	680.72
1253.90	325.12	758.21
1328.40	280.21	798.62
1339.50	300.09	781.31
1412.60	350.14	733.49
1437.50	375.01	704.01
1526.60	392.57	681.39
1638.80	325.12	758.63
1656.60	280.21	798.89
1722.10	300.09	781.66
1791.60	375.01	704.58
1844.70	350.14	734.07
1897.40	392.57	682.08
1944.90	280.21	799.14
2021.00	325.12	759.06
2044.80	300.09	781.96
2161.70	375.01	705.16
2226.70	350.14	734.58
2272.30	392.57	682.77
2328.80	325.12	759.39
2440.60	280.21	799.56
2446.40	300.09	782.34
2545.70	375.01	705.76
2619.10	392.57	683.41
2644.70	350.14	735.11
2655.80	325.15	759.75
2834.60	300.09	782.7
2842.70	350.14	735.41
2850.60	280.21	799.88
2909.90	375.01	706.34
3014.90	325.12	760.15
3050.40	392.57	684.2
3198.00	280.21	800.17
3224.90	300.09	783.06
3286.90	350.14	735.99
3321.40	325.12	760.48
3364.10	375.01	707.04
3411.20	392.57	684.86
3630.70	350.14	736.45
3659.40	325.12	760.85
3671.10	300.09	783.47
3677.60	375.01	707.53
3679.10	280.21	800.56
3835.00	392.57	685.63
4004.10	325.12	761.22
4012.20	350.14	736.94
4071.10	280.21	800.9
4074.10	300.09	783.84
4083.20	375.01	708.16
4095.70	392.57	686.12
4362.50	300.09	784.11
4394.60	350.14	737.43
4399.20	325.12	761.65
4437.70	280.21	801.19
4515.70	375.01	708.82
4524.90	392.57	686.89
4691.20	325.12	761.97
4757.60	350.14	737.91
4771.80	300.09	784.48
4832.60	280.21	801.5
4853.50	375.01	709.33
4902.80	392.57	687.57
5010.70	325.12	762.32
5182.10	280.21	801.8
5197.90	350.14	738.48
5226.50	300.09	784.89
5280.20	375.01	709.98
5283.50	392.57	688.24
5383.40	325.12	762.71
5559.10	280.21	802.1
5577.90	350.14	738.96
5579.20	300.09	785.21
5646.90	375.01	710.53
5730.50	325.12	763.08
5775.90	392.57	689.09
5910.00	280.21	802.39
5939.30	350.14	739.42
6001.60	300.09	785.59
6039.60	392.57	689.55
6138.10	375.01	711.26
6143.60	325.12	763.52
6321.30	350.14	739.89
6334.90	280.21	802.73
6427.20	300.09	785.98
6447.10	375.01	711.73
6476.60	392.57	690.3
6525.60	325.12	763.91
6730.90	350.14	740.41
6750.90	280.21	803.06
6780.30	300.09	786.29
6880.90	375.01	712.37
6889.70	392.57	691.01
6903.20	325.12	764.31
7119.70	350.14	740.89
7166.50	281.21	803.39
7214.70	300.09	786.68
7269.80	375.01	712.94
7293.80	325.12	764.72
7348.00	392.57	691.78
7564.40	350.14	741.45
7592.00	280.21	803.74
7629.90	300.09	787.05
7661.90	325.12	765.11
7728.00	392.57	692.42
7772.40	375.01	713.68
7918.60	325.12	765.38
7988.50	350.14	741.97
7999.00	280.21	804.07
8020.30	300.09	787.4
8119.20	375.01	714.18
8172.70	392.57	693.17
8254.40	325.12	765.72
8329.00	280.21	804.33
8417.50	300.09	787.75
8472.50	350.14	742.55
8557.20	375.01	714.81
8598.30	392.57	693.88
8755.50	325.12	766.24
8805.70	300.09	788.1
8817.00	280.21	804.7
8925.80	350.14	743.13
8987.30	375.01	715.42
9018.50	392.57	694.57
9212.90	300.09	788.45
9280.80	350.14	743.56
9350.60	280.21	805.11
9405.00	392.57	695.2
9423.80	375.01	716.04
9621.50	300.09	788.81
9658.50	280.21	805.38
9676.30	350.14	744.05
9837.90	392.57	695.89
9842.20	375.01	716.64
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
293.15	100.00	785.0
293.15	10000.00	793.2
293.15	20000.00	800.6
293.15	30000.00	807.4
293.15	40000.00	813.7
293.15	50000.00	819.6
293.15	60000.00	825.1
293.15	70000.00	830.4
293.15	80000.00	835.3
293.15	90000.00	840.1
293.15	100000.00	844.6
293.15	110000.00	848.9
293.15	120000.00	853.1
293.15	130000.00	857.1
293.15	140000.00	861.0
303.15	100.00	776.6
303.15	10000.00	785.3
303.15	20000.00	793.3
303.15	30000.00	800.2
303.15	40000.00	806.9
303.15	50000.00	813.1
303.15	60000.00	818.9
303.15	70000.00	824.3
303.15	80000.00	829.1
303.15	90000.00	834.2
303.15	100000.00	838.8
303.15	110000.00	843.1
303.15	120000.00	847.3
303.15	130000.00	851.4
303.15	140000.00	855.2
313.15	100.00	767.8
313.15	10000.00	777.1
313.15	20000.00	785.4
313.15	30000.00	792.9
313.15	40000.00	799.8
313.15	50000.00	806.2
313.15	60000.00	812.1
313.15	70000.00	817.6
313.15	80000.00	822.8
313.15	90000.00	827.8
313.15	100000.00	832.6
313.15	110000.00	837.3
313.15	120000.00	841.5
313.15	130000.00	845.8
313.15	140000.00	849.7
323.15	100.00	758.7
323.15	10000.00	768.6
323.15	20000.00	777.3
323.15	30000.00	785.2
323.15	40000.00	792.4
323.15	50000.00	799.0
323.15	60000.00	805.2
323.15	70000.00	811.0
323.15	80000.00	816.4
323.15	90000.00	821.6
323.15	100000.00	826.6
323.15	110000.00	831.3
323.15	120000.00	835.7
323.15	130000.00	840.0
323.15	140000.00	844.2
333.15	100.00	749.2
333.15	10000.00	759.7
333.15	20000.00	769.1
333.15	30000.00	777.4
333.15	40000.00	785.0
333.15	50000.00	792.0
333.15	60000.00	798.5
333.15	70000.00	804.5
333.15	80000.00	810.1
333.15	90000.00	815.6
333.15	100000.00	820.6
333.15	110000.00	825.4
333.15	120000.00	830.0
333.15	130000.00	834.4
333.15	140000.00	838.5
343.15	100.00	738.8
343.15	10000.00	750.2
343.15	20000.00	760.1
343.15	30000.00	768.8
343.15	40000.00	776.8
343.15	50000.00	784.1
343.15	60000.00	790.9
343.15	70000.00	797.1
343.15	80000.00	803.0
343.15	90000.00	808.6
343.15	100000.00	813.9
343.15	110000.00	818.9
343.15	120000.00	823.8
343.15	130000.00	828.3
343.15	140000.00	832.7
353.15	100.00	728.3
353.15	10000.00	740.5
353.15	20000.00	751.1
353.15	30000.00	760.6
353.15	40000.00	768.9
353.15	50000.00	776.6
353.15	60000.00	783.7
353.15	70000.00	790.3
353.15	80000.00	796.4
353.15	90000.00	802.1
353.15	100000.00	807.5
353.15	110000.00	812.6
353.15	120000.00	817.5
353.15	130000.00	822.3
353.15	140000.00	826.7
363.15	10000.00	730.2
363.15	20000.00	741.7
363.15	30000.00	751.7
363.15	40000.00	760.6
363.15	50000.00	768.7
363.15	60000.00	776.0
363.15	70000.00	782.8
363.15	80000.00	789.2
363.15	90000.00	795.2
363.15	100000.00	800.8
363.15	110000.00	806.2
363.15	120000.00	811.3
363.15	130000.00	816.2
363.15	140000.00	820.8
373.15	10000.00	719.5
373.15	20000.00	731.9
373.15	30000.00	742.6
373.15	40000.00	752.1
373.15	50000.00	760.5
373.15	60000.00	768.2
373.15	70000.00	775.4
373.15	80000.00	782.1
373.15	90000.00	788.4
373.15	100000.00	794.2
373.15	110000.00	799.8
373.15	120000.00	805.0
373.15	130000.00	810.0
373.15	140000.00	814.7
383.15	10000.00	708.0
383.15	20000.00	721.5
383.15	30000.00	732.9
383.15	40000.00	743.1
383.15	50000.00	752.0
383.15	60000.00	760.1
383.15	70000.00	767.6
383.15	80000.00	774.6
383.15	90000.00	781.0
383.15	100000.00	787.1
383.15	110000.00	792.8
383.15	120000.00	798.3
383.15	130000.00	803.5
383.15	140000.00	808.5
393.15	10000.00	696.3
393.15	20000.00	710.9
393.15	30000.00	723.2
393.15	40000.00	733.7
393.15	50000.00	743.1
393.15	60000.00	751.7
393.15	70000.00	759.6
393.15	80000.00	766.6
393.15	90000.00	773.6
393.15	100000.00	779.9
393.15	110000.00	785.9
393.15	120000.00	791.5
393.15	130000.00	796.8
393.15	140000.00	801.6
403.15	10000.00	683.7
403.15	20000.00	699.5
403.15	30000.00	712.8
403.15	40000.00	724.1
403.15	50000.00	734.2
403.15	60000.00	743.2
403.15	70000.00	751.4
403.15	80000.00	758.9
403.15	90000.00	766.0
403.15	100000.00	772.5
403.15	110000.00	778.7
403.15	120000.00	784.5
403.15	130000.00	790.1
403.15	140000.00	795.4
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
302.90	1040.00	778.1
302.90	2000.00	778.9
302.90	2990.00	779.8
302.90	4060.00	780.8
302.90	5010.00	781.6
302.90	6000.00	782.5
302.90	7020.00	783.4
302.90	8020.00	784.3
302.90	9000.00	785.1
302.90	10000.00	786.0
323.00	1000.00	760.6
323.00	2020.00	761.6
323.00	3000.00	762.7
323.00	4070.00	763.7
323.00	5000.00	764.7
323.00	6010.00	765.7
323.00	7020.00	766.7
323.00	8010.00	767.7
323.00	9010.00	768.6
323.00	10020.00	769.6
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
293.15	100.00	785.4
293.15	1000.00	786.2
293.15	5000.00	789.6
293.15	10000.00	793.6
293.15	15000.00	797.4
293.15	20000.00	801.1
293.15	25000.00	804.5
293.15	30000.00	807.9
293.15	35000.00	811.2
293.15	40000.00	814.2
293.15	45000.00	817.2
293.15	50000.00	820.1
293.15	55000.00	822.9
293.15	60000.00	825.6
293.15	65000.00	828.2
293.15	70000.00	830.8
293.15	80000.00	835.8
293.15	90000.00	840.5
293.15	100000.00	845.0
293.15	110000.00	849.4
293.15	120000.00	853.5
293.15	130000.00	857.6
293.15	140000.00	861.2
298.15	100.00	781.4
298.15	1000.00	782.1
298.15	5000.00	785.6
298.15	10000.00	789.8
298.15	15000.00	793.7
298.15	20000.00	797.3
298.15	25000.00	800.9
298.15	30000.00	804.3
298.15	35000.00	807.7
298.15	40000.00	810.8
298.15	45000.00	813.8
298.15	50000.00	816.7
298.15	55000.00	819.7
298.15	60000.00	822.5
298.15	65000.00	825.2
298.15	70000.00	827.6
298.15	80000.00	832.8
298.15	90000.00	837.5
298.15	100000.00	842.3
298.15	110000.00	846.4
298.15	120000.00	850.8
298.15	130000.00	854.8
298.15	140000.00	858.7
313.15	100.00	768.2
313.15	1000.00	769.1
313.15	5000.00	773.0
313.15	10000.00	777.4
313.15	15000.00	781.8
313.15	20000.00	785.7
313.15	25000.00	789.5
313.15	30000.00	793.3
313.15	35000.00	796.9
313.15	40000.00	800.1
313.15	45000.00	803.4
313.15	50000.00	806.5
313.15	55000.00	809.6
313.15	60000.00	812.5
313.15	65000.00	815.4
313.15	70000.00	818.2
313.15	80000.00	823.4
313.15	90000.00	828.5
313.15	100000.00	833.1
313.15	110000.00	837.8
313.15	120000.00	842.1
313.15	130000.00	846.4
313.15	140000.00	850.4
333.15	100.00	749.4
333.15	1000.00	750.5
333.15	5000.00	754.9
333.15	10000.00	760.0
333.15	15000.00	764.9
333.15	20000.00	769.3
333.15	25000.00	773.6
333.15	30000.00	777.7
333.15	35000.00	781.5
333.15	40000.00	785.3
333.15	45000.00	788.9
333.15	50000.00	792.3
333.15	55000.00	795.6
333.15	60000.00	798.7
333.15	65000.00	801.8
333.15	70000.00	804.8
333.15	80000.00	810.5
333.15	90000.00	815.9
333.15	100000.00	820.9
333.15	110000.00	825.8
333.15	120000.00	830.4
333.15	130000.00	834.8
333.15	140000.00	839.2
353.15	1000.00	729.8
353.15	5000.00	735.0
353.15	10000.00	741.0
353.15	15000.00	746.5
353.15	20000.00	751.7
353.15	25000.00	756.5
353.15	30000.00	761.0
353.15	35000.00	765.4
353.15	40000.00	769.3
353.15	45000.00	773.3
353.15	50000.00	777.0
353.15	55000.00	780.6
353.15	60000.00	784.0
353.15	65000.00	787.4
353.15	70000.00	790.6
353.15	80000.00	796.7
353.15	90000.00	802.6
353.15	100000.00	808.0
353.15	110000.00	813.2
353.15	120000.00	818.1
353.15	130000.00	822.8
353.15	140000.00	827.3
373.15	1000.00	706.6
373.15	5000.00	712.8
373.15	10000.00	719.9
373.15	15000.00	726.3
373.15	20000.00	732.0
373.15	25000.00	737.7
373.15	30000.00	742.9
373.15	35000.00	747.8
373.15	40000.00	752.2
373.15	45000.00	756.6
373.15	50000.00	760.7
373.15	55000.00	764.7
373.15	60000.00	768.6
373.15	65000.00	772.1
373.15	70000.00	775.6
373.15	80000.00	782.3
373.15	90000.00	788.5
373.15	100000.00	794.4
373.15	110000.00	799.9
373.15	120000.00	805.3
373.15	130000.00	810.2
373.15	140000.00	815.1
393.15	1000.00	680.4
393.15	5000.00	688.2
393.15	10000.00	696.7
393.15	15000.00	704.4
393.15	20000.00	711.4
393.15	25000.00	717.6
393.15	30000.00	723.5
393.15	35000.00	729.0
393.15	40000.00	734.2
393.15	45000.00	739.0
393.15	50000.00	743.5
393.15	55000.00	747.9
393.15	60000.00	752.1
393.15	65000.00	756.1
393.15	70000.00	760.0
393.15	80000.00	767.2
393.15	90000.00	773.9
393.15	100000.00	780.2
393.15	110000.00	786.2
393.15	120000.00	791.8
393.15	130000.00	797.2
393.15	140000.00	802.3
303.15	100.00	777.0
293.15	100.00	785.46
313.15	100.00	768.21
323.15	100.00	759.07
298.15	100.00	781.27
333.15	100.00	749.42
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
298.15	81.50	780.99
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
298.15	100.00	781.3
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
283.15	100.00	793.7
283.15	5000.00	797.5
283.15	10000.00	801.3
283.15	20000.00	808.9
283.18	15000.00	805.2
298.15	100.00	781.2
298.15	5000.00	785.5
298.15	10000.00	789.7
298.15	15000.00	793.8
298.15	20000.00	797.6
313.15	100.00	768.1
313.15	5000.00	773.0
313.15	10000.00	777.5
313.15	15000.00	781.9
313.15	20000.00	786.1
328.15	100.00	754.4
328.15	5000.00	759.6
328.15	15000.00	769.5
328.15	20000.00	774.0
328.18	10000.00	764.8
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	99.00	1300.967
253.15	5138.00	1328.819
253.15	10106.00	1354.875
253.15	15136.00	1380.021
253.15	20143.00	1404.015
253.15	25229.00	1427.462
253.15	30036.00	1448.868
273.15	100.00	1227.88
273.15	5275.00	1258.803
273.15	10173.00	1286.447
273.15	15164.00	1313.265
273.15	20289.00	1339.577
273.15	25102.00	1363.26
273.15	30264.00	1387.65
293.15	100.00	1157.361
293.15	5085.00	1189.739
293.15	10183.00	1220.822
293.15	15273.00	1250.197
293.15	20239.00	1277.428
293.15	25220.00	1303.56
293.15	30278.00	1328.856
313.15	100.00	1087.156
313.15	5177.00	1123.06
313.15	10104.00	1155.744
313.15	15187.00	1187.465
313.15	20126.00	1216.587
313.15	25138.00	1244.664
313.15	30110.00	1271.13
333.15	100.00	1015.957
333.15	5048.00	1054.493
333.15	10038.00	1090.587
333.15	15065.00	1124.563
333.15	20102.00	1156.534
333.15	25093.00	1186.433
333.15	30014.00	1214.42
353.15	100.00	940.503
353.15	5080.00	983.885
353.15	10091.00	1023.857
353.15	15114.00	1060.82
353.15	20132.00	1095.253
353.15	25164.00	1127.605
353.15	30380.00	1159.239
Reference

Operational condition: Frequency, MHz = 8 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Speed of sound, m/s - Liquid
299.79	86.00	1132.8
349.93	138.00	950.4
217.77	143.00	1445.1
249.84	159.00	1317.8
399.64	492.00	745.0
299.80	865.00	1138.2
249.86	992.00	1322.3
217.84	1031.00	1449.0
399.63	1090.00	752.7
349.94	1099.00	958.9
450.06	1639.00	499.2
349.97	1915.00	966.0
399.63	1986.00	764.1
249.87	2039.00	1328.0
299.81	2097.00	1146.6
450.04	2190.00	512.0
217.84	2256.00	1454.8
249.85	4937.00	1343.6
349.97	5044.00	992.5
299.81	5133.00	1166.5
399.62	5275.00	802.7
217.88	6084.00	1472.2
500.17	7568.00	371.1
217.00	8951.00	1489.1
249.85	9128.00	1365.3
500.15	9582.00	424.0
299.79	9677.00	1195.1
349.97	9682.00	1029.2
399.62	9782.00	850.0
249.86	10803.00	1373.6
249.85	19905.00	1417.6
299.80	20194.00	1256.1
399.61	20985.00	948.9
349.98	21490.00	1111.7
450.02	22115.00	792.1
500.11	22653.00	636.6
216.95	24689.00	1556.1
399.63	38384.00	1071.2
299.80	39488.00	1353.7
500.25	40483.00	812.4
216.87	41140.00	1619.7
249.85	41768.00	1512.2
349.98	42396.00	1232.7
449.97	42419.00	957.3
249.85	59235.00	1579.4
216.89	60566.00	1688.1
299.81	60935.00	1447.1
349.97	61179.00	1324.0
449.98	61580.00	1076.2
500.27	61769.00	961.8
399.63	61965.00	1203.3
216.90	78557.00	1746.2
249.85	80375.00	1653.1
500.27	80461.00	1067.0
399.61	80647.00	1291.3
349.97	81377.00	1409.9
299.89	81993.00	1527.9
449.99	82381.00	1183.6
249.85	96644.00	1705.5
349.97	96752.00	1469.0
299.88	97237.00	1581.4
399.60	97607.00	1362.4
450.00	97646.00	1252.6
500.27	98305.00	1153.8
216.97	98400.00	1805.5
216.96	121241.00	1868.7
399.66	122092.00	1454.2
450.00	122429.00	1352.4
299.85	123509.00	1665.9
349.94	123510.00	1562.0
500.28	123715.00	1261.3
249.85	124462.00	1787.6
Reference

Molar volume, m3/mol

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

Correlations

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 4733.35]	kPa	[272.89; 508.31]	The Yaw...
Equation			ln(Pvp) = A + B/(T + C)
Coefficient A			1.60031e+01
Coefficient B			-3.41274e+03
Coefficient C			-5.57370e+01
Temperature range, min.			272.89
Temperature range, max.			508.31
Pvap	1.33	kPa	272.89	Calculated Property
Pvap	7.22	kPa	299.05	Calculated Property
Pvap	28.18	kPa	325.21	Calculated Property
Pvap	86.40	kPa	351.36	Calculated Property
Pvap	220.84	kPa	377.52	Calculated Property
Pvap	490.18	kPa	403.68	Calculated Property
Pvap	973.21	kPa	429.84	Calculated Property
Pvap	1766.54	kPa	455.99	Calculated Property
Pvap	2980.40	kPa	482.15	Calculated Property
Pvap	4733.35	kPa	508.31	Calculated Property
Pvap	[3.30e-05; 4751.86]	kPa	[185.28; 508.31]	KDB Vap...
Equation			ln(Pvp) = A + B/T + C*ln(T) + D*T^2
Coefficient A			7.13411e+01
Coefficient B			-7.69090e+03
Coefficient C			-7.69405e+00
Coefficient D			7.65635e-07
Temperature range, min.			185.28
Temperature range, max.			508.31
Pvap	3.30e-05	kPa	185.28	Calculated Property
Pvap	7.19e-03	kPa	221.17	Calculated Property
Pvap	0.29	kPa	257.06	Calculated Property
Pvap	4.27	kPa	292.96	Calculated Property
Pvap	31.34	kPa	328.85	Calculated Property
Pvap	143.80	kPa	364.74	Calculated Property
Pvap	471.71	kPa	400.63	Calculated Property
Pvap	1209.10	kPa	436.53	Calculated Property
Pvap	2574.02	kPa	472.42	Calculated Property
Pvap	4751.86	kPa	508.31	Calculated Property

Similar Compounds

Find more compounds similar to Isopropyl Alcohol.

Mixtures

• 1-Propanol + Isopropyl Alcohol
• Isopropyl Alcohol + 1-Butanol
• Isopropyl Alcohol + 1-Octanol
• Isopropyl Alcohol + 1-Hexanol
• Aniline + Isopropyl Alcohol
• Isopropyl Alcohol + (S)-Isopropyl lactate
• Isopropyl Alcohol + Isobutane
• Isopropyl Alcohol + Piperazine, 1-methyl-
• Methyl Isobutyl Ketone + Isopropyl Alcohol
• Methyl Isobutyl Ketone + Diisopropyl ether + Isopropyl Alcohol
• Isopropyl Alcohol + Tetrahydrofuran
• 1,3-Dioxolane + Isopropyl Alcohol + Water
• Phenol, 2-methyl- + Isopropyl Alcohol
• p-Cresol + Isopropyl Alcohol
• Isopropyl Alcohol + 2-Pyrrolidinone, 1-methyl-
• Isopropyl Alcohol + Butane
• Isopropyl Alcohol + Carbon dioxide
• Diisopropyl ether + Isopropyl Alcohol
• Isopropyl Alcohol + Ethanol, 2-methoxy-
• Diisopropyl ether + Isopropyl Alcohol + Ethanol, 2-methoxy-

Find more mixtures with Isopropyl Alcohol.

Sources

• KDB Pure (Korean Thermophysical Properties Databank)
• KDB Vapor Pressure Data
• Crippen Method
• Dortmund Data Bank Vapor-Liquid Equilibrium Data
• Speeds of Sound and Isentropic Compressibilities in Binary Mixtures of 2-Propanol with Several 1-Alkanols at 298.15K
• Densities and Volumetric Properties of Binary Mixtures of Aniline with 1-Propanol, 2-Propanol, 2-Methyl-1-Propanol, and 2-Methyl-2-Propanol at Temperatures from 293.15 to 318.15 K
• Solubility of Baicalein in Different Solvents from (287 to 323) K
• Effect of Al2O3 Nanoparticles Additives on the Density, Saturated Vapor Pressure, Surface Tension and Viscosity of Isopropyl Alcohol
• Measurement and prediction of vapor-liquid equilibria of ternary systems containing ionic liquids
• 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
• Vapor liquid equilibria and excess volumes of the binary systems ethanol + ethyl lactate, isopropanol + isopropyl lactate and n-butanol + n-butyl lactate at 101.325 kPa
• Vapour liquid equilibrium for the 2-methylpropane + methanol, +ethanol, +2-propanol, +2-butanol and +2-methyl-2-propanol systems at 313.15K
• 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
• Isothermal vapour liquid equilibria in the binary and ternary systems composed of 2-propanol, diisopropyl ether and 4-methyl-2-pentanone
• Ultrasonic velocity, viscosity and excess properties of binary mixture of tetrahydrofuran with 1-propanol and 2-propanol
• Salt effect on vapor liquid equilibria for binary systems of propanol/CaCl2 and butanol/CaCl2
• Enhancement of the anthracene aqueous solubility by a synergistic effect of alcohols and beta-cyclodextrin
• Vapor liquid equilibria for nitrogen with 2-propanol, 2-butanol, or 2-pentanol binary systems
• 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
• Bubble points of the systems isopropanol-water, isopropanol-water-sodium acetate and isopropanol-water-sodium oleate at high pressure
• Excess volumes and excess enthalpies of N-methyl-2-pyrrolidone with branched alcohols
• Co-solvent effects in LLE of 1-hydroxyethyl-3-methylimidazolium based ionic liquids + 2-propanol + dichloromethane or 1,2-dichloroethane
• Vapour liquid equilibrium for the systems butane + methanol, +2-propanol, +1-butanol, +2-butanol, +2-methyl-2-propanol at 364.5K
• Selection of ionic liquids as entrainers for separation of water and 2-propanol
• High-pressure vapor liquid equilibria for CO2 + alkanol systems and densities of n-dodecane and n-tridecane
• 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
• Determination of partial molar excess enthalpies at infinite dilution for the systems four alcohols + [bmim]PF6 at different temperatures by isothermal titration calorimeter
• Solubilities of rutin in eight solvents at T = 283.15, 298.15, 313.15, 323.15, and 333.15K
• Effect of pressure and the capability of 2-methoxyethanol as a solvent in the behaviour of a diisopropyl ether isopropyl alcohol azeotropic mixture
• Isothermal vapour liquid equilibria in the binary and ternary systems composed of 2-propanol, 3-methyl-2-butanone and 2,2,4-trimethylpentane
• Excess molar enthalpies of ethyl acetoacetate + (methanol, +ethanol, +1-propanol, and +2-propanol) at T = (298.15, 313.15 and 328.15)K and p = (0.1 and 10.0)MPa
• Liquid liquid equilibria for the binary system of di-isopropyl ether (DIPE) +water in between 288.15 and 323.15K and the ternary systems of DIPE +water + C1 C4 alcohols at 298.15K
• Solubility of l-serine, l-threonine and l-isoleucine in aqueous aliphatic alcohol solutions
• Isobaric vapour liquid equilibria for binary systems of 2-butanone with ethanol, 1-propanol, and 2-propanol at 20 and 101.3 kPa
• Solubility of antioxidant 1010 in pure alkanols
• Phase equilibria of glycerol containing systems and their description with the Cubic-Plus-Association (CPA) Equation of State
• Physical properties and phase equilibria of the system isopropyl acetate + isopropanol + 1-octyl-3-methyl-imidazolium bis(trifluoromethylsulfonyl)imide
• Solubility and density measurements of palmitic acid in supercritical carbon dioxide + alcohol mixtures
• Phase equilibrium for the systems diisopropyl ether, isopropyl alcohol + 2,2,4-trimethylpentane and + n-heptane at 101.3 kPa
• New analytic apparatus for experimental determination of vapor-liquid equilibria and saturation densities
• Solubility of benzoic acid in acetone, 2-propanol, acetic acid and cyclohexane: Experimental measurement and thermodynamic modeling
• Solubilities of cefodizime disodium in aqueous alcohol mixtures at atmospheric pressure and different temperatures
• Isobaric vapour liquid equilibria and physical properties for isopropyl acetate + isopropanol + 1-butyl-3-methyl-imidazolium bis(trifluoromethylsulfonyl)imide mixtures
• Activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-ethyl-3-methylimidazolium methanesulfonate
• Multiphase equilibria for mixtures containing water, isopropanol, propionic acid, and isopropyl propionate
• Experimental measurement and modeling of solubility of LiBr and LiNO3 in methanol, ethanol, 1-propanol, 2-propanol and 1-butanol
• Solubility of itaconic acid in different organic solvents: Experimental measurement and thermodynamic modeling
• Solubility of citric, malonic, and malic acids in different solvents from 303.2 to 333.2 K
• Study of the influence of the structure of the alcohol on vapor pressures and osmotic coefficients of binary mixtures alcohol + 1-hexyl-3-methylimidazolium bis(trifluoromethylsulfonyl)imide at T = 323.15 K
• Study of the liquid-liquid equilibrium of 1-propanol + manganese sulphate and 2-propanol + lithium sulphate aqueous two-phase systems at different temperatures: Experiment and correlation
• Solubility of caprolactam in different organic solvents
• Liquid-liquid equilibria of aqueous systems containing alcohol and ammonium sulfate
• 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
• Thermodynamic study of aqueous two phase systems for some aliphatic alcohols + sodium thiosulfate + water
• Activity coefficients at infinite dilution of organic solutes in the ionic liquid ethyl(2-hydroxyethyl)dimethyl-ammonium diethylphosphate using gas liquid chromatography
• Solid-liquid phase equilibrium of glyphosate in selected solvents
• Activity coefficients at infinite dilution of organic solutes in 1-octyl-3-methylimidazolium nitrate using gas-liquid chromatography
• Liquid liquid equilibrium of 1-propanol, 2-propanol, 2-methyl-2-propanol or 2-butanol + sodium sulfite + water aqueous two phase systems
• Measurement and correlation for solubility of levofloxacin in six solvents at temperatures from 288.15 to 328.15 K
• Solubility of chlocyphos in different solvents
• Solubility of lansoprazole in different solvents
• Determination of the solubility, dissolution enthalpy and entropy of suberic acid in different solvents
• Isobaric VLE at 0.6 MPa for binary systems isobutyl acetate + ethanol, + 1-propanol or + 2-propanol
• The study of phase behavior of aqueous 1-propanol/2-propanol/2-butanol/2-methyl-2-propanol systems in the presence of disodium tartrate or disodium succinate at T = 298.15 K
• Solid liquid equilibrium of 1-hydroxyethane-1,1-diphosphonic acid in different solvents
• Prediction of different thermodynamic properties for systems of alcohols and sulfate-based anion Ionic Liquids using modified UNIFAC
• Measurement and correlation of liquid liquid equilibrium data for 2-methyl-1-propanol + 2-propanol + water at several temperatures
• Investigation on vapor liquid equilibrium for 2-propanol + 1-butanol + 1-pentanol at 101.3 kPa
• 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
• Measurement and correlation of solubility of N-chlorobenzenesulfonamide sodium and N-chloro-4-toluenesulfonamide sodium in binary ethanol + propan-2-ol mixtures from 278.00 K to 323.00 K
• Thermodynamics of solubility of thiomalic acid in different organicsolvents from 278.15 K to 333.15 K
• The effect of temperature on the liquid-liquid equilibria of somealiphatic alcohols + di-sodium hydrogen citrate + water systems: Experimental and correlation
• Thermodynamic and spectral investigations of binary liquid mixturesof 2-butoxy ethanol with alcohols at temperature range of 293.15-313.15 K
• Solubilities of crotonic acid in different organic solvents at severaltemperatures from (278.15 to 333.15) K
• Excess second-order thermodynamic derivatives of the {2-propanol + water} system from 313.15 K to 403.15 K up to 140 MPa. Experimental and Monte Carlo simulation study
• Determination and correlation of solubilities of 1,2-bis(2-oxo-5,5-dimethyl-1,3,2-dioxyphosphacyclohexyl-2-imino) ethane in selected solvents
• Measurement and correlation solubility and mixing properties of L-malic acid in pure and mixture organic solvents
• Liquid liquid equilibria of 4-methyl-2-pentanone + 1-propanol or 2-propanol + water ternary systems: Measurements and correlation at different temperatures
• Determination and correlation of cefoperazone solubility in different pure solvents and binary mixture
• Solubility of androstenedione in lower alcohols
• (p, VE, T) Measurements of mixtures (DBE + alcohol) at temperaturesfrom (293.15 to 353.15) K and at pressures up to 140 MPa
• Measurement and correlation of the solubility of maleic anhydride in different organic solvents
• Measurement and correlation of solid-liquid equilibrium for abietic acid + alcohol systems at atmospheric pressure
• 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
• Isobaric vapor-liquid equilibria for the binary and ternary mixtures of 2-propanol, water, and 1,3-propanediol at p = 101.3 kPa: Effect of the 1,3-propanediol addition
• Determination and correlation of solubility and solution thermodynamics of valnemulin hydrogen tartrate in different pure solvents
• Solubility and polymorphic forms of antibiotic lasalocid sodium in different organic solvents
• Thermodynamics of risperidone and solubility in pure organic solvents
• Solid-liquid equilibrium and thermodynamic of 2,5-thiophenedicarboxylic acid in different organic solvents
• Measurement and modeling of volumetric properties and speeds of sound of several mixtures of alcohol liquids containing 1-propanol and 2-propanol at T= (298.15 - 323.15) K and ambient pressure
• Experimental and theoretical study of interaction between organic compounds and 1- (4-sulfobutyl)-3-methylimidazolium based ionic liquids
• Ternary liquid-liquid equilibria of bis(trifluoromethylsulfonyl)-amidebased ionic liquids + 2-propanol + di-iso-propyl ether
• Solubility of N-Ethylcarbazole in different organic solvent at 279.15 - 319.15 K
• Vapour-liquid equilibrium of carboxylic acid alcohol binary systems:2-Propanol + butyric acid, 2-butanol + butyric acid and 2-methyl-1-propanol + butyric acid
• 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.
• Measurement, correlation, and prediction of vapor pressure for binary and ternary systems containing an ionic liquid 1,3-dimethylimidazolium methylsulfate
• Isothermal vapor liquid equilibrium for binary mixtures containing furfural and its derivatives
• 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
• Densities, surface tensions, and isobaric vapor-liquid equilibria for the mixtures of 2-propanol, water, and 1,2-propanediol
• Solubility of methylphosphonic acid in selected organic solvents
• 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
• Measurement, correlation, and prediction of vapor pressure for binary and ternary systems containing an alkylsulfate-based ionic liquid
• Measurement and correlation of solubility and dissolution properties of flunixin meglumine in pure and binary solvents
• 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
• Activity coefficients at infinite dilution for different alcohols and ketones in [EMpy][ESO4]: Experimental data and modeling with PC-SAFT
• Solubility correlation and thermodynamic analysis of two forms of Metaxalone in different pure solvents
• 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.
• Effect of imidazolium-based ionic liquid on vapor-liquid equilibria of 2-propanol + acetonitrile binary system at 101.3 kPa
• Separation of 2-propanol and water azeotropic system using ionic liquids as entrainers
• Solubility of L-asparagine monohydrate in water and water-isopropanol mixed solvents: Measurements and thermodynamic modelling
• Liquid-liquid equilibrium for the ternary system of isopropyl acetate + 2-propanol + glycerol at different temperatures under atmospheric pressure
• Liquid-liquid equilibria for ternary mixtures of water + 2-propanol + 1-alkyl-3-methylimidazolium bis(trifluoromethylsulfonyl)imide ionic liquids at 298.15 K
• Study of the phase equilibrium of the water + 2-propanol + 1- undecanol ternary system between 275.15 K and 288.15 K. Comparison with the water + ethanol + 1-undecanol System
• Activity coefficients at infinite dilution of organic solvents and water in 1-butyl-3-methylimidazolium dicyanamide. A literature review of hexane/hex-1-ene separation
• Solid-liquid phase equilibrium and ternary phase diagrams of ethenzamide-saccharin cocrystals in different solvents
• A model to calculate concentration-dependent surface tension of binary systems
• The influence of temperature on liquid-liquid-solid equilibria for (water + 2-propanol + KCl +NH4Cl) quaternary system
• Separation of ethyl acetate and 2-propanol azeotropic mixture using ionic liquids as entrainers
• Liquid density of mixtures methyl nonafluorobutyl Ether (HFE-7100) + 2-propanol at pressures up to 140 MPa and temperatures from 298.15 K to 393.15 K.
• Determination and correlation of solubility of linezolid form II in different pure and binary solvents
• Equilibrium study and diversified models of drug Norfloxacin in eight pure organic and binary solvents at T = (278.15 to 328.15) K
• Evaluation of the solvent structural effect upon the vapor-liquid equilibrium of [C4C1im][Cl] + Alcohols
• Application of 1-hexyl-3-methylimidazolium trifluoromethanesulfonate to the removal of alcohol from mixtures with heptane
• Determination and correlation of solubility of N-methyl-3,4,5- trinitropyrazole (MTNP) in ten pure solvents from 283.15 K to 323.15 K
• High selective water/butan-1-ol separation on investigation of limiting activity coefficients with [P8,8,8,8][[NTf2] ionic liquid
• Evaluation of salting-out effect in the liquid-liquid equilibrium of aqueous two-phase systems composed of 2-propanol and Na2SO4/ MgSO4 at different temperatures
• Experimental studies and thermodynamic analysis of isobaric vapor-liquid-liquid equilibria of 2-propanol + water system using n-propyl acetate and isopropyl acetate as entrainers
• Separation of the isopropanol-water azeotropic mixture using ionic liquids
• Liquid-liquid equilibrium determination and thermodynamics modeling for extraction of isopropanol from its aqueous solution
• 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
• 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
• Measurement and correlation of aqueous biphasic systems composed of alcohol (1-propanol/ 2-propanol/tert-butanol) + (NH4)2SO4 + H2O at 298 K and a textile dye partition.
• Isobaric vapor-liquid equilibrium for chloroform + isopropanol + 1,3-dimethylimidazolium dimethylphosphate at 101.3 kPa
• High pressure and high temperature volumetric properties of (2-propanol + diisopropyl ether) system
• 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
• 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
• 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
• Solid-liquid equilibria for selected binary systems containing diphenyl carbonate
• Ammonium ionic liquids in extraction of bio-butan-1-ol from water phase using activity coefficients at infinite dilution
• 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
• Dissolution behavior and thermodynamic properties of lapatinib ditosylate in pure and mixed organic solvents from T = (283.15-323.15) K
• Creating efficient novel aqueous two-phase systems: Salting-out effect and high solubility of salt
• Separation of isopropyl acetate + isopropanol azeotropic mixture using ionic liquids with acetate anion as entrainers
• Excess molar enthalpies of ternary mixtures of (methanol, ethanol + 2-propanol + 1,4-dioxane) at T ? 298:15 K
• A thermodynamic study of the ketoreductase-catalyzed reduction of 2-alkanones in non-aqueous solvents
• VLE of the binary systems (dimethyl carbonate with 2-propanol or 2-butanol) and (diethyl carbonate with methylcyclohexane) at 101.3 kPa
• Systems with ionic liquids: Measurement of VLE and c1 data and prediction of their thermodynamic behavior using original UNIFAC, mod. UNIFAC(Do) and COSMO-RS(Ol)
• Excess molar enthalpies of ethylformate and (1-propanol, 2-propanol, 1-butanol, 2-butanol, and 1-pentanol) at T = (298.15 and 308.15) K and p = (5 and 10) MPa
• Speeds of sound, isentropic compressibilities, viscosities and excess molar volumes of binary mixtures of methylcyclohexane + 2-alkanols or ethanol at T = 298.15 K
• Excess molar volumes and partial molar volumes for (propionitrile + an alkanol) at T = 298.15 K and p = 0.1 MPa
• Physico-chemical and excess properties of the binary mixtures of methylcyclohexane + ethanol, + propan-1-ol, + propan-2-ol, + butan-1-ol, + 2-methyl-1-propanol, or 3-methyl-1-butanol at T = (298.15, 303.15, and 308.15) K
• Quaternary (liquid + liquid) equilibria for (water + 2-propanol + 1,1-dimethylethyl methyl ether + diisopropyl ether) at the temperature 298.15 K
• (Liquid + liquid) equilibrium of (water + 2-propanol + 1-butanol + salt) systems at T = 313.15 K and T = 353.15 K: Experimental data and correlation
• 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
• Thermodynamic properties of (tetradecane + benzene, + toluene, + chlorobenzene, + bromobenzene, + anisole) binary mixtures at T = (298.15, 303.15, and 308.15) K
• Viscosity, density, and speed of sound of methylcyclopentane with primary and secondary alcohols at T = (293.15, 298.15, and 303.15) K
• (Vapor + liquid) equilibria of the binary mixtures of m-cresol with C1 C4 aliphatic alcohols at 95.5 kPa
• Thermodynamic interactions in binary mixtures of anisole with ethanol, propan-1-ol, propan-2-ol, butan-1-ol, pentan-1-ol, and 3-methylbutan-1-ol at T = (298.15, 303.15, and 308.15) K
• Isobaric (vapour + liquid) equilibrium for (2-propanol + water + ammonium thiocyanate): Fitting the data by an empirical equation
• Densities and derived thermodynamic properties of (2-methoxyethanol + 1-propanol, or 2-propanol, or 1,2-propandiol) at temperatures from T = (293.15 to 343.15) 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
• Measurement of activity coefficients at infinite dilution in 1-hexadecyl-3-methylimidazolium tetrafluoroborate ionic liquid
• Mixing properties of binary mixtures presenting azeotropes at several temperatures
• (Vapor + liquid) equilibrium of the binary mixtures formed by acetonitrile with selected compounds at 95.5 kPa
• Density and speed of sound of lithium bromide with organic solvents: Measurement and correlation
• Ternary (liquid + liquid) equilibria of the azeotrope (ethyl acetate + 2-propanol) with different ionic liquids at T = 298.15 K
• Measurement and correlation of solubility of trans-resveratrol in 11 solvents at T = (278.2, 288.2, 298.2, 308.2, and 318.2) K
• Densities and volumetric properties of (N-(2-hydroxyethyl)morpholine + ethanol, + 1-propanol, + 2-propanol, + 1-butanol, and + 2-butanol) at (293.15, 298.15, 303.15, 313.15, and 323.15) K
• (Vapour + liquid + liquid) equilibria and excess molar enthalpies of binary and ternary mixtures of isopropanol, water, and propylene
• Isobaric (vapour + liquid + liquid) equilibrium data for (di-n-propyl ether + n-propyl alcohol + water) and (diisopropyl ether + isopropyl alcohol + water) systems at 100 kPa
• Studies of mixing properties of binary systems of 2-propanol with hexadecane and squalane at T = (298.15, 303.15, and 308.15) K
• Isobaric (vapour + liquid) equilibrium for N-methyl-2-pyrrolidone with branched alcohols
• Phase diagrams of (hexane + methanol + 2,2,2-trifluoroethanol) at three temperatures: Measurement and correlation
• Density measurements of liquid 2-propanol at temperatures between (280 and 393) K and at pressures up to 10 MPa
• Osmotic coefficients of binary mixtures of 1-butyl-3-methylimidazolium methylsulfate and 1,3-dimethylimidazolium methylsulfate with alcohols at T = 323.15 K
• Vapour pressures and osmotic coefficients of binary mixtures of 1-ethyl-3-methylimidazolium ethylsulfate and 1-ethyl-3-methylpyridinium ethylsulfate with alcohols at T = 323.15 K
• Vapour pressures, osmotic and activity coefficients for binary mixtures containing (1-ethylpyridinium ethylsulfate + several alcohols) at T = 323.15 K
• Cloud point measurements of 1-butyl-2,3-dimethylimidazolium tetrafluoroborate with alcohols
• Densities, viscosities, refractive indices, and surface tensions for binary and ternary mixtures of 2-propanol, tetrahydropyran, and 2,2,4-trimethylpentane
• Application of the ERAS model to volumetric properties of binary mixtures of banana oil with primary and secondary alcohols (C1- C4) at different temperatures
• Measurement and modeling of osmotic coefficients of binary mixtures (alcohol + 1,3-dimethylpyridinium methylsulfate) at T = 323.15 K
• 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
• Determination and modelling of osmotic coefficients and vapour pressures of binary systems 1- and 2-propanol with CnMimNTf2 ionic liquids (n = 2, 3, and 4) at T = 323.15 K
• 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
• Isothermal (vapour + liquid) equilibria in the binary and ternary systems composed of 2-propanol, 2,2,4-trimethylpentane, and 2,4-dimethyl-3-pentanone
• Interactions of volatile organic compounds with the ionic liquid 1-ethyl-3-methylimidazolium tetracyanoborate
• The buffering-out effect and phase separation in aqueous solutions of EPPS buffer with 1-propanol, 2-propanol, or 2-methyl-2-propanol at T = 298.15 K
• (Vapour + liquid) equilibria for binary and ternary mixtures of 2-propanol, tetrahydropyran, and 2,2,4-trimethylpentane at P = 101.3 kPa
• Solubilities of some organic solutes in 1-ethyl-3-methylimidazolium acetate. Chromatographic measurements and predictions from COSMO-RS
• 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
• Volumetric properties of ternary (IL + 2-propanol or 1-butanol or 2-butanol + ethyl acetate) systems and binary (IL + 2-propanol or 1-butanol or 2-butanol) and (1-butanol or 2-butanol + ethyl acetate) systems
• 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
• Acoustic, volumetric and osmotic properties of binary mixtures containing the ionic liquid 1-butyl-3-methylimidazolim dicyanamide mixed with primary and secondary alcohols
• Ternary (liquid + liquid) equilibria for (water + 2-propanol + a-pinene, or a-pinene) mixtures at four temperatures
• Experimental excess molar properties of binary mixtures of (3-amino-1-propanol + isobutanol, 2-propanol) at T = (293.15 to 333.15) K and modelling the excess molar volume by Prigogine-Flory-Patterson theory
• Experimental study on the calorimetric data of cyclohexanol with alkanols (C1-C4) and correlation with Wilson, NRTL and UNIQUAC models at 300 K
• 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
• Liquid density of oxygenated additive 2-propanol at pressures up to 140 MPa and from 293.15 K to 403.15 K
• 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
• Activity coefficient at infinite dilution measurements for organic solutes (polar and non-polar) in fatty compounds: Saturated fatty acids
• Thermodynamic investigation of the ATPSs composed of some (aliphatic alcohol + sodium carbonate + water) ternary systems
• 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
• 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
• Solubilities of evodiamine in twelve organic solvents from T = (283.2 to 323.2) K
• Activity coefficient at infinite dilution measurements for organic solutes (polar and non-polar) in fatty compounds Part II: C18 fatty acids
• 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
• Osmotic and apparent molar properties of binary mixtures alcohol + 1-butyl-3-methylimidazolium trifluoromethanesulfonate ionic liquid
• Activity coefficients at infinite dilution of organic solutes in N-formylmorpholine and N-methylpyrrolidone from gas-liquid chromatography
• 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
• Vapour pressures and osmotic coefficients of binary mixtures containing alcohol and pyrrolidinium-based ionic liquids
• Infinite dilution activity coefficients of volatile organic compounds in two ionic liquids composed of the tris(pentafluoroethyl) trifluorophosphate ([FAP]) anion and a functionalized cation
• Experimental and modeling investigations of solubility and saturated liquid densities and viscosities for binary systems (methane +, ethane +, and carbon dioxide + 2-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
• Thermodynamics and activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-butyl-1-methylmorpholinium tricyanomethanide
• Osmotic coefficients and apparent molar volumes of 1-hexyl-3-methylimidazolium trifluoromethanesulfonate ionic liquid in alcohols
• Densities and viscosities of the mixtures (formamide + 2-alkanol): Experimental and theoretical approaches
• 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
• Osmotic coefficients of alcoholic mixtures containing BMpyrDCA: Experimental determination and correlation
• Determination and correlation of the solubility of four Bronsted-acidic ionic liquids based on benzothiazolium cations in six alcohols
• 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
• Thermodynamics and activity coefficients at infinite dilution for organic solutes, water and diols in the ionic liquid choline bis(trifluoromethylsulfonyl)imide
• (Solid + liquid) phase equilibria of tetraphenyl piperazine-1,4-diyldiphosphonate in pure solvents
• Determination and correlation of solubility of spironolactone form II in pure solvents and binary solvent mixtures
• Molecular interactions in binary mixtures of 1-butoxy-2-propanol with alcohols at different temperatures: A thermophysical and spectroscopic approach
• Determination and correlation of solubility of tylosin tartrate in alcohol mixtures
• A combined experimental and computational investigation of excess molar enthalpies of (nitrobenzene + alkanol) mixtures
• (Liquid + liquid) equilibria for mixtures of dodecane and ethanol with alkylsulfate-based ionic liquids
• Thermodynamics of 4'-bromomethyl-2-cyanobiphenyl in different solvents
• 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
• 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)
• Thermodynamic models for determination of the solubility of DL-malic acid in methanol plus (acetonitrile, N,N-dimethylformamide, isopropyl alcohol) binary solvent mixtures
• Isopropanol dehydration via extractive distillation using low transition temperature mixtures as entrainers
• Solubility and solution thermodynamics of sorbic acid in eight pure organic solvents
• Activity coefficients at infinite dilution of organic solutes in methylphosphonate based ionic liquids using gas-liquid chromatography
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 4-(3-hydroxypropyl)-4-methylmorpholinium bis(trifluoromethylsulfonyl)-amide
• Thermodynamic models for determination of the solubility of (-)-shikimic acid in different pure solvents and in (H2O + ethanol) binary solvent mixtures
• Thermodynamic and transport properties of binary mixtures; friction theory coupled with PC-SAFT model
• Solubility of daidzin in different organic solvents and (ethyl alcohol + water) mixed solvents
• Excess molar enthalpies of R-fenchone + propan-1-ol or +propan-2-ol. Modeling with COSMO-RS and UNIFAC
• Measurement and correlation of the solubility of genistin in eleven organic solvents from T = (283.2 to 323.2) K
• Activity coefficients at infinite dilution, physicochemical and thermodynamic properties for organic solutes and water in the ionic liquid ethyl-dimethyl-(2-methoxyethyl)ammonium trifluorotris-(perfluoroethyl)phosphate
• Solubility measurement and prediction of clopidogrel hydrogen sulfate polymorphs in isopropanol and ethyl acetate
• Solubility measurement and modelling of 1,8-dinitronaphthalene in nine organic solvents from T = (273.15 to 308.15) K and mixing properties of solutions
• Solution thermodynamics of valnemulin hydrogen fumarate in different pure solvents
• Screening of environmental friendly ionic liquid as a solvent for the different types of separations problem: Insight from activity coefficients at infinite dilution measurement using (gas + liquid) chromatography technique
• Solubility and solution thermodynamics of thymol in six pure organic solvents
• Solubility modelling and thermodynamic dissolution functions of phthalimide in ten organic solvents
• Ternary (liquid + liquid) equilibria for the extraction of ethanol, or 2-propanol from aqueous solutions with 1,1'-oxybis(butane) at different temperatures
• Determination and correlation of solubility and solution thermodynamics of oxiracetam in three (alcohol + water) binary solvents
• Solubility of rosuvastatin calcium in different neat solvents at different temperatures
• Measurement and correlation of solubility of cefmenoxime hydrochloride in pure solvents and binary solvent mixtures
• Solubility and solution thermodynamics of ethyl 5-amino-4-cyano-3-(2-ethoxy-2-oxoethyl)-2-thiophenecarboxylate in nine organic solvents at evaluated temperatures
• Mutual diffusion coefficients of isopropanol + n-heptane and isobutanol + n-heptane
• Measurement and correlation of solubility and solution thermodynamics of 1,3-dimethylurea in different solvents from T = (288.15 to 328.15) K
• Solubility of 3-chloro-N-phenylphthalimide in ten organic solvents from T = (288.15 to 323.15) K: Determination and modelling
• A 1-alkylcyanopyridinium-based ionic liquid in the separation processes
• Solubility measurement and thermodynamic functions of dehydroepiandrosterone acetate in different solvents at evaluated temperatures
• (Vapor + liquid) equilibria of alcohol + 1-methyl-1-propylpiperidinium triflate ionic liquid: VPO measurements and modeling
• Determination and thermodynamic modeling of solid-liquid phase equilibrium for 3,5-dichloroaniline in pure solvents and ternary 3,5-dichloroaniline + 1,3,5-trichlorobenzene + toluene system
• Solubility determination and thermodynamic dissolution functions of 1,3-diphenylguanidine in nine organic solvents at evaluated temperatures
• Measurement and correlation of solubility of pronamide in five organic solvents at (278.15-323.15) K
• 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
• Solubility determination and thermodynamic modeling of 5-nitro-8- hydroxyquinoline in ten organic solvents from T = (278.15 to 313.15) K and mixing properties of solutions
• Solubility and thermodynamic function of a bioactive compound bergenin in various pharmaceutically acceptable neat solvents at different temperatures
• Determination and correlation of solubility and thermodynamic properties of pyraclostrobin in pure and binary solvents
• Solubility and solution thermodynamics of 2-methyl-6-nitroaniline in ten organic solvents at elevated temperatures
• Speed of sound in saturated aliphatic alcohols (propan-2-ol, butan-2-ol, and 2-methylpropan-1-ol) and alkanediols (ethane-1,2-diol, propane-1,2- and -1,3-diol) at temperature between 253.15 K and 353.15 K and pressures up to 30 MPa
• Effect of temperature and composition on the surface tension and surface properties of binary mixtures containing DMSO and short chain alcohols
• 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
• Solubility determination and thermodynamic modelling of terephthaldialdehyde in ten organic solvents from T = (273.15 to 318.15) K and mixing properties of solutions
• Separation of aliphatic from aromatic hydrocarbons and sulphur compounds from fuel based on measurements of activity coefficients at infinite dilution for organic solutes and water in the ionic liquid N,N-diethyl-N-methyl-N-(2-methoxy-ethyl)ammonium bis(trifluoromethylsulfonyl)imide
• Solubility determination and thermodynamic modeling of 3-methyl-4- nitrobenzoic acid in twelve organic solvents from T = (283.15-318.15) K and mixing properties of solutions
• Measurement and modelling of econazole nitrate in twelve pure organic solvents at temperatures from 278.15 K to 318.15 K
• Solubility of cefoxitin acid in different solvent systems
• Solid-liquid phase equilibrium and mixing properties of 2-Cyano-4'-methylbiphenyl in pure solvents
• 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 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
• 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 measurement and correlation of the form A of ibrutinib in organic solvents from 278.15 to 323.15 K
• Solubility measurement and modelling of ethyl 5-amino-4-cyano-3-(2-ethoxy-2-oxoethyl)-2-thiophenecarboxylate in four groups mixed solvents
• 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
• Solubility determination and thermodynamic modelling of 3-amino-1,2,4-triazole in ten organic solvents from T = 283.15 K to T = 318.15 K and mixing properties of solutions
• Investigation on molecular interactions of antibiotics in alcohols using volumetric and acoustic studies at different temperatures
• Solubility determination and thermodynamic modeling of paclobutrazol in nine organic solvents from T = (278.15 to 318.15) K and mixing properties of solutions
• Solubility of L-histidine in different aqueous binary solvent mixtures from 283.15 K to 318.15 K with experimental measurement and thermodynamic modelling
• A green process for recovery of 1-propanol/2-propanol from their aqueous solutions: Experimental and MD simulation studies
• Thermodynamic modelling for solubility of 5-chloro-1-methyl-4-nitroimidazole in eleven organic solvents from T = (283.15 to 318.15) K
• Measurement and correlation of solubility of ciclesonide in seven pure organic solvents
• 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
• Determination and correlation of Avermectin B1a solubility in different binary solvent mixtures at temperatures from (283.15 to 313.15) K
• Solid-liquid phase equilibrium and dissolution properties of ethyl vanillin in pure solvents
• Solubility and solution thermodynamics of 2-methyl-4-nitroaniline in eleven organic solvents at elevated temperatures
• Solubility measurement and thermodynamic functions of 3-nitrobenzaldehyde in different solvents at elevated temperatures
• Determination and thermodynamic modelling for 2-methyl-6-nitroaniline solubility in binary solvent mixtures of ethyl acetate + (methanol, ethanol, n-propanol and isopropanol)
• Determination and correlation of terephthaldialdehyde solubility in (ethanol, isopropanol, ethyl acetate, isopentanol) + N,Ndimethylformamide mixed solvents at temperatures from 273.15 K to 318.15 K
• Solubility determination and modelling of 4-nitro-1,2-phenylenediamine in eleven organic solvents from T = (283.15 to 318.15) K and thermodynamic properties of solutions
• Solubility determination and thermodynamic modelling for 2-amino-4-chlorobenzoic acid in eleven organic solvents from T = (278.15 to 313.15) K and mixing properties of solutions
• Liquid-liquid equilibrium measurements and correlation for phase behaviors of alcohols + heptane + ILs ternary systems
• Solubility determination and thermodynamic functions of 2-chlorophenothiazine in nine organic solvents from T = 283.15 K to T = 318.15 K and mixing properties of solutions
• Solubility and thermodynamic properties of vanillyl alcohol in some pure solvents
• Solubility and thermodynamic functions of tebuconazole in nine organic solvents from T = (278.15 to 313.15) K and mixing properties of solutions
• Solubility of 2-isopropylimidazole in nine pure organic solvents and liquid mixture of (methanol + ethyl acetate) from T = (278.15 to 313.15) K: Experimental measurement and thermodynamic modelling
• Excess molar enthalpies of ethane-1,2-diamine plus primary and secondary alkanols (C1-C4) and correlation with Redlich-Kister, Wilson, NRTL and UNIQUAC models at T = 298 K
• Thermodynamic equilibrium of hydroxyacetic acid in pure and binary solvent systems
• Solubility of 2-nitro-p-phenylenediamine in nine pure solvents and mixture of (methanol + N-methyl-2-pyrrolidone) from T = (283.15 to 318.15) K: Determination and modelling
• Isobaric vapor-liquid equilibria for the extractive distillation of 2-propanol + water mixtures using 1-ethyl-3-methylimidazolium dicyanamide ionic liquid
• 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
• The study of physico-chemical properties of binary systems consisting of N-Methylcyclohexylamine with 2-alkanols at T = (298.15-328.15) K
• Separation of binary mixtures hexane/hex-1-ene, cyclohexane/cyclohexene and ethylbenzene/styrene based on limiting activity coefficients
• Thermodynamic properties of enantiotropic polymorphs of glycolide
• Thermodynamic models for determination of the solid-liquid equilibrium of istradefylline in ethyl acetate plus (isopropanol, tetrahydrofuran, acetone) binary solvent mixtures
• Hydrogen solubility in furfural and 2-propanol: Experiments and modeling
• 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
• 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)
• Solubility and preferential solvation of 2-methyl-4-nitroaniline in mixed solvents of ethyl acetate + (methanol, ethanol, n-propanol and isopropanol)
• Physical properties of systems of interest to the edible oil industry: Viscosities and densities of model systems formed by (triacylglycerol + fatty acid + solvent)
• Studies on physicochemical behavior of binary mixtures containing propanal and Alkan-2-ol
• Thermodynamics and activity coefficients at infinite dilution for organic compounds and water in the ionic liquid 1-butyl-3-methylimidazolium perchlorate
• Excess molar volume and excess Gibbs energy of activation for viscous flow for the binary mixtures of N-ethylpyridinium dicyanamide [C2py][DCA] with alcohols
• Study of separation of water + 2-propanol mixture using different ionic liquids: 1-Butyl-3-methylimidazolium bis(trifluoromethylsulfonyl)imide or 1-butyl-1-methylpyrrolidinium bis(trifluoromethylsulfonyl)imide
• Separation of water/butan-1-ol based on activity coefficients at infinite dilution in 1,3-didecyl-2-methylimidazolium dicyanamide ionic liquid
• Estimation and confirmation of the thermodynamic stability relationships of the enantiotropic polymorphs of glycolide
• Separation of binary mixtures hexane/hex-1-ene, cyclohexane/cyclohexene and ethylbenzene/styrene based on gamma infinity data measurements
• Thermophysical properties of binary mixtures of 1-butyl-1-methylpyrrolidinium trifluoromethanesulfonate ionic liquid with alcohols at several temperatures
• Separation of binary mixtures based on gamma infinity data using [OMMIM][NTf2] ionic liquid and modelling of thermodynamic functions
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid trihexyl-tetradecyl-phosphonium tricyanomethanide
• Solubility and thermodynamics of vitamin C in binary liquid mixtures involving water, methanol, ethanol and isopropanol at different temperatures
• Thermodynamic study of molecular interaction-selectivity in separation processes based on limiting activity coefficients
• Equilibrium solubility and preferential solvation of 1,1'-sulfonylbis(4-aminobenzene) in binary aqueous solutions of n-propanol, isopropanol and 1,4-dioxane
• Consistency of experimental data in SLLV equilibrium of ternary systems with electrolyte. Application to the water + NaCl + 2-propanol system at 101.3 kPa
• Abraham model correlations for describing the thermodynamic properties of solute transfer into pentyl acetate based on headspace chromatographic and solubility measurements
• Thermodynamics and selectivity of separation based on activity coefficients at infinite dilution of various solutes in ionic liquid [HMMIM][BF4]
• The use of ionic liquids for separation of binary hydrocarbons mixtures based on gamma infinity data measurements
• The molar surface Gibbs energy and its application to the binary mixtures of N-butylpyridinium dicyanamide [C4py][DCA] with alcohols
• Experimental solubility evaluation and thermodynamic analysis of biologically active D-tryptophan in aqueous mixtures of N,N-dimethylformamide and several alcohols
• Thermodynamics and activity coefficients at infinite dilution for organic compounds in the ionic liquid 1-hexyl-3-methylimidazolium chloride
• Density, speed of sound and refractive index of mixtures containing 2-phenoxyethanol with propanol or butanol at various temperatures
• Separation of binary mixtures based on gamma infinity data using [OMMIM][BF4] ionic liquid and modelling of thermodynamic functions
• Determination of the thermodynamic parameters of ionic liquid 1-propyl-3-methylimidazolium bromide by gas-liquid chromatography
• Influence of the temperature on the equilibrium phase diagram of the ternary system water + ammonium chloride + 2-propanol at 101.3 kPa
• Liquid-liquid equilibria and density data for pseudoternary systems of refined soybean oil + (hexanal, or heptanal, or butyric acid, or valeric acid, or caproic acid, or caprylic acid) + dimethyl sulfoxide at 298.15 K
• Vapour-liquid equilibrium and extractive distillation for separation of azeotrope isopropyl alcohol and diisopropyl ether
• Experimental solubility evaluation and thermodynamic analysis of quinocetone in aqueous co-solvent solutions of ethanol, isopropanol, dimethyl sulfoxide and N,N-dimethylformamide
• Thermodynamic solubility modeling, solvent effect and preferential solvation of curcumin in aqueous co-solvent mixtures of ethanol, n-propanol, isopropanol and propylene glycol
• The dissolution behavior and apparent thermodynamic analysis of temozolomide in pure and mixed solvents
• Solubility modelling, solvent effect and preferential solvation of allopurinol in aqueous co-solvent mixtures of ethanol, isopropanol, N,N-dimethylformamide and 1-methyl-2-pyrrolidone
• Influence of nanofluid instability on thermodynamic properties near the critical point
• Thermodynamics of binary mixtures 1-ethoxy-1,1,2,2,3,3,4,4,4-nonafluorobutane (HFE-7200) + 2-propanol: High pressure density, speed of sound and derivative properties
• 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
• 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
• Equilibrium solubility determination, modelling and preferential solvation of bioactive iminodibenzyl in aqueous co-solvent mixtures at various temperatures
• Equilibrium solubility of dinitolmide in several neat solvents and binary aqueous co-solvent mixtures: Experimental determination and thermodynamic analysis
• Volumetric properties of monoethanolamine and alcohol binary mixtures at different temperatures and 0.1 MPa
• Equilibrium solubility investigation and thermodynamic aspects of biologically active gimeracil (form P) dissolved in aqueous co-solvent mixtures of isopropanol, N,N-dimethylformamide, ethylene glycol and dimethylsulfoxide
• Research on the application of 7-chloro-quinaldine adducts in 7-chloro-quinaldine separation process
• Thermodynamic properties of paracetamol impurities 4-nitrophenol and 4'-chloroacetanilide and the impact of such impurities on the crystallisation of paracetamol from solution
• Determination and correlation of solubility and solution thermodynamics of saccharin in different pure solvents
• Thermodynamic solubility modelling, solvent effect and preferential solvation of naftopidil in aqueous co-solvent solutions of (n-propanol, ethanol, isopropanol and dimethyl sulfoxide)
• Excess volumes and partial molar volumes of binary liquid mixtures of furfural or 2-methylfuran with alcohols at 298.15 K
• Properties of pure 1-(3-(trimethylammonio)prop-1-yl)-3-methylimidazolium bis(dicyanamide) asymmetrical gemini ionic liquid and its binary mixture with isopropanol at T = (283.15 333.15) K
• Equilibrium solubility determination, modelling and thermodynamic aspects of 6-chloroguanine in aqueous co-solvent mixtures of N,N-dimethylformamide, isopropanol, 1,4-dioxane and dimethyl sulfoxide
• Surface tension and interfacial compositions of binary glycerol/alcohol mixtures
• Separation of the mixture (isopropyl alcohol + diisopropyl ether + n-propanol): Entrainer selection, interaction exploration and vapour-liquid equilibrium measurements
• Cosolvent effect on solubility of aripiprazole in mixed solvents and apparent thermodynamic analysis of dissolution process
• One- and two-phase isochoric heat capacities and saturated densities of 2-propanol in the critical and supercritical regions
• Determination and correlation of solubility and solution thermodynamics of musk xylene in different pure solvents
• Solubility and preferential solvation of flubendazole dissolved in aqueous co-solvent mixtures of 1,4-dioxane, dimethyl sulfoxide, N,N-dimethylformamide and isopropanol
• Thermophysical study of binary mixtures of 1-butyl-3-methylimidazolium nitrate ionic liquid + alcohols at different temperatures
• Effect of temperature on the phase-separation ability of KCl in aqueous two-phase systems composed of propanols: Determination of the critical temperature and extension of the results to other salts
• Thermodynamic solubility modelling, solvent effect and preferential solvation of p-nitrobenzamide in aqueous co-solvent mixtures of dimethyl sulfoxide, ethanol, isopropanol and ethylene glycol
• The dissolution behaviour and apparent thermodynamic analysis of diprophylline in pure and mixed solvents
• Solubility behaviour and thermodynamic analysis of methyleneaminoacetonitrile in binary (ethanol + water, ethanol + 2-propanol, ethanol + n-butanol) solvents
• Co-solvence phenomenon and thermodynamic properties of edaravone in pure and mixed solvents
• Solvent effect on solubility and preferential solvation analysis of buprofezin dissolved in aqueous co-solvent mixtures of N,N-dimethylformamide, ethanol, acetonitrile and isopropanol
• Improving the solubility of temozolomide by cosolvent and its correlation with the Jouyban-Acree and CNIBS/R-K models
• Volumetric, acoustic and viscometric investigation of ceftriaxone disodium in aqueous solutions of 1-propanol and 2-propanol
• Solubility and mixing thermodynamic properties of levamisole hydrochloride in twelve pure solvents at various temperatures
• Molar excess enthalpies of ethyl acetate + alkanols at T=298.15K, p=10MPa
• Ternary excess molar enthalpies of (1-propanol + 2-propanol + 1,4-dioxane) mixture at 298.15 K
• Enthalpies of solution of l-threonine in aqueous alcohol solutions
• Excess molar enthalpies of methylformate + (1-propanol, 2-propanol, 1-butanol, 2-butanol and 1-pentanol) at T = 298.15 K, p = (5.0, 10.0)MPa, and methylformate + 1-propanol at T = 333.15 K, p = 10.0MPa
• Excess enthalpies of binary mixtures of some propylamines + some propanols at 298.15K
• Topological investigations of the molecular species and molecular interactions that characterize pyrrolidin-2-one + lower alkanol mixtures
• Densities, viscosities, excess molar volumes, and refractive indices of acetonitrile and 2-alkanols binary mixtures at different temperatures: Experimental results and application of the Prigogine Flory Patterson theory
• Solute-Solvent and Solvent-Solvent Interactions of Menthol in Isopropyl Alcohol and its Binary Mixtures with Methyl Salicylate by Volumetric, Viscometric, Interferometric and Refractive Index Techniques.
• Calibration of a low temperature calorimeter and application in the determination ofisobaric heat capacity of 2-propanol
• Thermodynamic properties of binary liquid mixtures of diethylenetriamine with alcohols at different temperatures
• Solubilities of succinimide in different pure solvents and binary methanol+ethyl acetate solvent mixtures
• Solubilities of 1,3-dimethyl-1,1,3,3-tetraphenyldisiloxane in different solvents from (288.15 to 313.15) K
• Volumetric properties of binary liquid mixtures of alcohols with 1,2-dichloroethane at different temperatures and atmospheric pressure
• Liquid-Liquid Equilibrium of Aqueous Two-Phase Systems Composed of Hydrophilic Alcohols (Ethanol/2-Propanol/1-Propanol) and MgSO4 /ZnSO4 at (303.15 and 313.15) K and Correlation
• Thermodynamic behavior of binary mixtures CnMpyNTf2 ionic liquids with primary and secondary alcohols
• Solubility in binary solvent mixtures: pyrene dissolved in alcohol + toluene mixtures
• Densities and viscosities of binary mixtures of ethylmethylketone and 2-alkanols; application of the ERAS model and cubic EOS
• Molar excess enthalpies and molar excess volumes of formamide + 1-propanol or 2-propanol and thermodynamic modeling by Prigogine-Flory-Patterson theory and Treszczanowicz-Benson association model
• Liquid liquid equilibria of hydrophilic alcohol + sodiumhydroxide + water systems: Experimental and correlation
• Evaluation of thermodynamic properties of fluid mixtures by PC-SAFT model
• Measurement and correlation of the solubility of (1-benzyl-1H-1,2,3-triazole-4-yl)methanol in water and alcohols at temperatures from 292.15 K to 310.15 K
• Determination and correlation of solubility and mixing properties of isonicotinamide (form II) in some pure solvents
• Thermophysical study of the binary mixtures of N,N-dimethylacetamide with 2-propanol and 2-butanol
• 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
• An experimental investigation and modelling of the thermal and caloric properties of nanofluids isopropyl alcohol - Al2O3 nanoparticles
• Apparent thermodynamic analysis and the dissolution behavior of levamisole hydrochloride in three binary solvent mixtures
• The excess molar volume and the molar surface Gibbs energy of the binary of the ether-functionalized ionic liquids [C22O1IM][TfO] with ethanol and isomeric propanols at T = (288.15-318.15) K
• Solubility and Caloric Properties of Cinnarizine
• 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
• Thermodynamic Behaviour of Binary Mixtures of 1-Butyl-1- methylpyrrolidinium Iodide and Alcohols
• Solubility and Solution Thermodynamics of Gibberellin A4 in Different Organic Solvents from 278.15 K to 333.15 K
• Liquid-Liquid Equilibrium of Alcohols + Ammonium/Potassium/Sodium Acetate + Water Systems: Experimental and Correlation
• Density, Speed of Sound, Viscosity, Excess Properties, and Prigogine Flory Patterson (PFP) Theory of Binary Mixtures of Amine and Alcohols
• Solubility of Amorphous Clopidogrel Hydrogen Sulfate in Different Pure Solvents
• Vapor-Liquid Equilibrium of Binary Mixtures Containing Isopropyl Acetate and Alkanols at 101.32 kPa
• Solubility Measurement and Correlation for 2- Naphthaldehyde in Pure Organic Solvents and Methanol + Ethanol Mixtures
• Solubility and Thermodynamic Analysis of Tenoxicam in Different Pure Solvents at Different Temperatures
• Liquid Liquid Equilibrium data for the ternary systems of Water, Isopropyl alcohol, and selected entrainers
• Measurement and Correlation of the Solubility of Maltitol in Different Pure Solvents, Methanol Water Mixtures, and Ethanol Water Mixtures
• Solubility of Agomelatine Crystal Form I and Form II in Pure Solvents and (Isopropanol + Water) Mixtures
• Solubility and Dissolution Thermodynamics for 1,3,5- Trichlorobenzene in Organic Solvents
• Solubility of Trimethoprim in Selected Pure Solvents and (Water + Ethanol/2-Propanol) Mixed-Solvent Systems
• Measurement and Correlation of Solubility of Cefathiamidine in Water + (Acetone, Ethanol, or 2-Propanol) from (278.15 to 308.15) K
• Measurement and Correlation of the Solubility of Vanillic Acid in Eight Pure and Water + Ethanol Mixed Solvents at Temperatures from (293.15 to 323.15) K
• Determination and Modeling of MgCl2 Solubility in Methanol, Ethanol, 2-Propanol and Their Mixtures from 283 to 343 K
• Solubility Measurement and Simulation of Rivaroxaban (Form I) in Solvent Mixtures from 273.15 to 323.15 K
• Solubility of Hydrogen Sulfide in Ethanediol, 1,2-Propanediol, 1-Propanol, and 2-Propanol: Experimental Measurement and Modeling
• 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
• Liquid-Liquid Equilibrium of Hydrophilic Alcohols with Three Different Salts of Chloride: Experimental and Correlation
• Liquid-Liquid Equilibria for Ternary Systems of Water + Methoxycyclopentane (CPME) + Alcohol; Methanol, Ethanol, 1-Propanol, or 2-Propanol
• Solid Liquid Phase Equilibrium of trans-Cinnamic Acid in Several Alcohols: Measurements and Thermodynamic Modeling
• Measurement and Correlation of the Solubility of Antioxidant 626 in Alcohols
• Measurement and Correlation of Solubility of -Aminobutyric Acid in Different Binary Solvents
• Solubility of 1,3,5-Benzenetricarboxylic Acid in Different Solvents
• Thermophysical Characterization of the Mixtures of the Ionic Liquid 1-Ethyl-3-Methylimidazolium Acetate with 1-Propanol or 2-Propanol
• Solubility Modeling of 4-(Methylsulfonyl)benzaldehyde in Nine Organic Solvents at Elevated Temperatures
• Liquid Liquid Equilibria, Equilibrium Phase Densities, and Refractive Indices for the Quaternary Mixtures Containing 2-Propanol or 2-Methyl-2-Propanol of Fuel Oxygenate at T = 298.15 and 318.15 K
• Vapor Liquid Equilibria for Ternary Mixtures of Isopropyl Alcohol, Isopropyl Acetate, and DMSO at 101.3 kPa
• Studies on Thermodynamic and Transport Properties of Binary Mixtures Containing Alcohols and Aniline
• Determination and Correlation of Solubility of 3,4-Dinitro-1H-pyrazole in Different Pure Solvents from 298.15 K to 338.15 K
• Solubility Measurement and Thermodynamic Modeling of 4-Nitrophthalimide in Twelve Pure Solvents at Elevated Temperatures Ranging from (273.15 to 323.15) K
• Experimental Measurement and Modeling of Vapor Liquid Equilibrium for the Ternary Systems Water + Ethanol + Ethylene Glycol, Water + 2-Propanol + Ethylene Glycol, and Water + 1-Propanol + Ethylene Glycol
• Solubility of 3,7,9,11-Tetraoxo-2,4,6,8,10-pentaaza[3.3.3] Propellane (TOPAP) in Different Pure Solvents at Temperatures between 273.15 and 318.15 K
• Measurement and Correlation of the Solubility of p-Coumaric Acid in Nine Pure and Water + Ethanol Mixed Solvents at Temperatures from 293.15 to 333.15 K
• Isobaric Vapor Liquid Equilibria for Binary Mixtures of .gamma.-Valerolactone + Methanol, Ethanol, and 2-Propanol
• Measurement and Correlation of Solubility on Reactive Crystallization of Methyl D-(-)-4-Hydroxy-phenylglycinate
• Measurement of Solubility of Thiamine Hydrochloride Hemihydrate in Three Binary Solvents and Mixing Properties of Solutions
• S