Chemical Properties of 1-Propanol, 2-methyl- (CAS 78-83-1)

InChI

InChI=1S/C4H10O/c1-4(2)3-5/h4-5H,3H2,1-2H3

InChI Key

ZXEKIIBDNHEJCQ-UHFFFAOYSA-N

Formula

C4H10O

SMILES

CC(C)CO

Molecular Weight¹

74.12

CAS

78-83-1

Other Names

• 1-Hydroxymethylpropane
• 2-METHYL-1-PROPANOL
• 2-Methylpropan-1-ol
• 2-Methylpropanol
• 2-Methylpropanol-1
• 2-Methylpropyl alcohol
• 2-methyl-1-propanyl alcohol
• 2-methylpropanoI
• Alcool isobutylique
• Butanol-iso
• Fermentation butyl alcohol
• ISOBUTYL ALCOHOL
• ISOPROPYLCARBINOL
• Isobutanol
• Isobutylalkohol
• Isopropyl carbitol
• Methyl-2 propanol-1
• NSC 5708
• Propanol, 2-methyl-
• Rcra waste number U140
• UN 1212
• i-Butanol
• i-Butyl alcohol
• iso-C4H9OH

• 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).
• C_p,solid : Solid phase heat capacity (J/mol×K).
• μ : Dipole Moment (debye).
• η : Dynamic viscosity (Pa×s).
• LFL : Lower Flammability Limit (% in Air).
• UFL : Upper Flammability Limit (% in Air).
• T_flash,cc : Flash Point (Closed Cup Method) (K).
• T_flash,oc : Flash Point (Open Cup Method) (K).
• Δ_fG° : Standard Gibbs free energy of formation (kJ/mol).
• R_g : Radius of Gyration.
• Δ_fH°_gas : Enthalpy of formation at standard conditions (kJ/mol).
• Δ_fH°_liquid : Liquid phase enthalpy of formation at standard conditions (kJ/mol).
• Δ_fusH° : Enthalpy of fusion at standard conditions (kJ/mol).
• Δ_fusH : Enthalpy of fusion at a given temperature (kJ/mol).
• Δ_vapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
• Δ_vapH : Enthalpy of vaporization at a given temperature (kJ/mol).
• IE : Ionization energy (eV).
• ν : Kinematic viscosity (m²/s).
• log₁₀WS : Log10 of Water solubility in mol/l.
• logP_oct/wat : Octanol/Water partition coefficient.
• McVol : McGowan's characteristic volume (ml/mol).
• NFPA Fire : NFPA Fire Rating.
• 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°_gas : Molar entropy at standard conditions (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).
• S°_{solid,1 bar} : Solid phase molar entropy at standard conditions (J/mol×K).
• T_boil : Normal Boiling Point Temperature (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).
• 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. Datasets
4. Correlations
5. Similar Compounds
6. Mixtures
7. Sources

Physical Properties

Property	Value	Unit	Source
ω	0.5920		KDB
PAff	793.70	kJ/mol	NIST
Tig	699.82	K	KDB
BasG	762.20	kJ/mol	NIST
ΔcH°liquid	[-2669.60; -2665.79]	kJ/mol
ΔcH°liquid	-2669.60 ± 0.59	kJ/mol	NIST
ΔcH°liquid	-2668.50 ± 0.84	kJ/mol	NIST
ΔcH°liquid	-2665.79	kJ/mol	NIST
μ	1.70	debye	KDB
η	[0.0033070; 0.0034040]	Pa×s
η	0.0033070	Pa×s	Thermod...
η	0.0034040	Pa×s	Thermop...
LFL	1.60	% in Air	KDB
UFL	10.90	% in Air	KDB
Tflash,cc	305.37	K	KDB
Tflash,oc	300.93	K	KDB
ΔfG°	-167.40	kJ/mol	KDB
Rg	3.1400		KDB
ΔfH°gas	[-284.00; -282.90]	kJ/mol
ΔfH°gas	-283.40	kJ/mol	KDB
ΔfH°gas	-283.80 ± 0.90	kJ/mol	NIST
ΔfH°gas	-282.90	kJ/mol	NIST
ΔfH°gas	-284.00 ± 1.50	kJ/mol	NIST
ΔfH°liquid	[-334.70; -333.60]	kJ/mol
ΔfH°liquid	-334.60 ± 0.90	kJ/mol	NIST
ΔfH°liquid	-333.60 ± 0.63	kJ/mol	NIST
ΔfH°liquid	-334.70 ± 0.84	kJ/mol	NIST
ΔfusH°	6.68	kJ/mol	Joback Calculated Property
ΔvapH°	[42.89; 50.89]	kJ/mol
ΔvapH°	50.89	kJ/mol	NIST
ΔvapH°	48.80	kJ/mol	NIST
ΔvapH°	50.76 ± 0.03	kJ/mol	NIST
ΔvapH°	50.80 ± 0.10	kJ/mol	NIST
ΔvapH°	50.80	kJ/mol	NIST
ΔvapH°	50.79 ± 0.02	kJ/mol	NIST
ΔvapH°	50.80 ± 0.10	kJ/mol	NIST
ΔvapH°	50.84 ± 0.08	kJ/mol	NIST
ΔvapH°	49.80	kJ/mol	NIST
ΔvapH°	50.70	kJ/mol	NIST
ΔvapH°	Outlier 42.89 ± 0.01	kJ/mol	NIST
IE	[10.02; 10.47]	eV
IE	10.02 ± 0.02	eV	NIST
IE	10.02 ± 0.05	eV	NIST
IE	10.11 ± 0.07	eV	NIST
IE	10.12 ± 0.04	eV	NIST
IE	10.09 ± 0.02	eV	NIST
IE	Outlier 10.47 ± 0.03	eV	NIST
log10WS	[0.04; 0.10]
log10WS	0.04		Aq. Sol...
log10WS	0.10		Estimat...
logPoct/wat	0.635		Crippen Calculated Property
McVol	73.090	ml/mol	McGowan Calculated Property
NFPA Fire	3		KDB
NFPA Health	1		KDB
Pc	4295.00	kPa	KDB
ρc	[269.06; 272.17]	kg/m3
ρc	271.29 ± 1.48	kg/m3	NIST
ρc	272.17	kg/m3	NIST
ρc	269.06	kg/m3	NIST
Inp	[580.00; 663.00]
Inp	596.00		NIST
Inp	617.93		NIST
Inp	629.00		NIST
Inp	629.00		NIST
Inp	609.00		NIST
Inp	629.00		NIST
Inp	641.00		NIST
Inp	620.00		NIST
Inp	629.00		NIST
Inp	609.00		NIST
Inp	629.00		NIST
Inp	641.00		NIST
Inp	620.00		NIST
Inp	629.00		NIST
Inp	609.00		NIST
Inp	605.00		NIST
Inp	601.00		NIST
Inp	Outlier 586.00		NIST
Inp	595.00		NIST
Inp	Outlier 584.00		NIST
Inp	Outlier 585.00		NIST
Inp	612.00		NIST
Inp	609.00		NIST
Inp	589.00		NIST
Inp	Outlier 580.00		NIST
Inp	612.00		NIST
Inp	648.00		NIST
Inp	607.00		NIST
Inp	608.00		NIST
Inp	636.00		NIST
Inp	637.00		NIST
Inp	612.00		NIST
Inp	616.00		NIST
Inp	594.60		NIST
Inp	637.00		NIST
Inp	645.00		NIST
Inp	646.00		NIST
Inp	629.00		NIST
Inp	Outlier 654.00		NIST
Inp	622.00		NIST
Inp	629.00		NIST
Inp	622.00		NIST
Inp	626.00		NIST
Inp	624.70		NIST
Inp	626.10		NIST
Inp	590.00		NIST
Inp	621.20		NIST
Inp	592.00		NIST
Inp	609.00		NIST
Inp	617.00		NIST
Inp	592.00		NIST
Inp	644.00		NIST
Inp	627.00		NIST
Inp	611.00		NIST
Inp	611.00		NIST
Inp	611.00		NIST
Inp	612.00		NIST
Inp	609.00		NIST
Inp	609.00		NIST
Inp	612.00		NIST
Inp	614.00		NIST
Inp	627.00		NIST
Inp	627.00		NIST
Inp	600.00		NIST
Inp	640.00		NIST
Inp	626.00		NIST
Inp	612.00		NIST
Inp	612.00		NIST
Inp	Outlier 655.00		NIST
Inp	Outlier 586.00		NIST
Inp	588.00		NIST
Inp	Outlier 580.00		NIST
Inp	616.00		NIST
Inp	621.00		NIST
Inp	626.00		NIST
Inp	632.00		NIST
Inp	628.00		NIST
Inp	618.00		NIST
Inp	612.00		NIST
Inp	626.00		NIST
Inp	622.00		NIST
Inp	618.00		NIST
Inp	642.50		NIST
Inp	624.00		NIST
Inp	622.00		NIST
Inp	622.00		NIST
Inp	622.00		NIST
Inp	625.00		NIST
Inp	625.00		NIST
Inp	626.00		NIST
Inp	610.00		NIST
Inp	647.00		NIST
Inp	647.00		NIST
Inp	608.00		NIST
Inp	612.55		NIST
Inp	611.00		NIST
Inp	641.00		NIST
Inp	620.00		NIST
Inp	621.00		NIST
Inp	Outlier 663.00		NIST
Inp	635.00		NIST
Inp	635.00		NIST
Inp	608.00		NIST
Inp	609.00		NIST
Inp	602.00		NIST
Inp	606.00		NIST
Inp	605.00		NIST
Inp	606.00		NIST
Inp	616.00		NIST
Inp	608.00		NIST
Inp	608.00		NIST
Inp	618.00		NIST
Inp	628.00		NIST
Inp	619.00		NIST
Inp	Outlier 663.00		NIST
Inp	622.00		NIST
Inp	Outlier 654.00		NIST
Inp	614.00		NIST
Inp	621.00		NIST
Inp	614.00		NIST
Inp	618.00		NIST
Inp	625.00		NIST
Inp	612.00		NIST
Inp	617.00		NIST
Inp	617.00		NIST
Inp	612.00		NIST
Inp	629.00		NIST
Inp	622.00		NIST
Inp	622.00		NIST
Inp	612.00		NIST
Inp	622.00		NIST
Inp	622.00		NIST
Inp	616.00		NIST
Inp	623.00		NIST
Inp	619.00		NIST
Inp	619.00		NIST
Inp	621.00		NIST
Inp	623.00		NIST
Inp	614.00		NIST
Inp	647.00		NIST
Inp	647.00		NIST
Inp	635.00		NIST
Inp	625.00		NIST
Inp	619.00		NIST
Inp	619.00		NIST
Inp	614.00		NIST
Inp	619.00		NIST
Inp	608.00		NIST
Inp	624.00		NIST
Inp	608.00		NIST
Inp	617.00		NIST
Inp	601.00		NIST
Inp	614.00		NIST
Inp	619.00		NIST
Inp	620.00		NIST
Inp	616.00		NIST
Inp	618.00		NIST
Inp	642.50		NIST
Inp	625.00		NIST
Inp	647.00		NIST
Inp	620.00		NIST
Inp	608.00		NIST
Inp	606.00		NIST
Inp	628.00		NIST
Inp	614.00		NIST
Inp	612.00		NIST
Inp	622.00		NIST
Inp	623.00		NIST
Inp	648.00		NIST
Inp	Outlier 580.00		NIST
I	[1043.00; 1129.00]
I	1108.00		NIST
I	1100.00		NIST
I	1094.00		NIST
I	1108.00		NIST
I	1100.00		NIST
I	1094.00		NIST
I	1122.00		NIST
I	1088.00		NIST
I	1090.00		NIST
I	1080.00		NIST
I	1092.00		NIST
I	1075.00		NIST
I	1083.00		NIST
I	1094.00		NIST
I	1087.00		NIST
I	1080.00		NIST
I	1101.00		NIST
I	1077.00		NIST
I	1091.00		NIST
I	1077.00		NIST
I	1092.00		NIST
I	1094.00		NIST
I	1094.00		NIST
I	1094.00		NIST
I	1110.00		NIST
I	Outlier 1048.00		NIST
I	1114.00		NIST
I	1101.00		NIST
I	Outlier 1053.00		NIST
I	Outlier 1057.00		NIST
I	1060.00		NIST
I	1062.00		NIST
I	1085.00		NIST
I	1075.00		NIST
I	1108.00		NIST
I	1092.00		NIST
I	1095.00		NIST
I	1086.00		NIST
I	1108.00		NIST
I	1097.00		NIST
I	1094.00		NIST
I	1093.00		NIST
I	1093.00		NIST
I	1098.00		NIST
I	1085.00		NIST
I	1090.00		NIST
I	1090.00		NIST
I	1112.00		NIST
I	1085.00		NIST
I	Outlier 1056.00		NIST
I	1104.00		NIST
I	1097.00		NIST
I	1114.00		NIST
I	Outlier 1043.00		NIST
I	1085.00		NIST
I	1093.00		NIST
I	1089.00		NIST
I	1078.00		NIST
I	1103.40		NIST
I	1065.00		NIST
I	1092.00		NIST
I	1064.00		NIST
I	1092.00		NIST
I	1077.00		NIST
I	1064.00		NIST
I	1078.00		NIST
I	1094.00		NIST
I	1077.00		NIST
I	1094.00		NIST
I	1094.00		NIST
I	1107.00		NIST
I	1098.00		NIST
I	1121.00		NIST
I	1110.00		NIST
I	1075.00		NIST
I	1083.00		NIST
I	1095.00		NIST
I	1093.00		NIST
I	1090.00		NIST
I	1085.00		NIST
I	1068.00		NIST
I	1078.00		NIST
I	1083.00		NIST
I	1081.00		NIST
I	1083.00		NIST
I	1083.00		NIST
I	1079.00		NIST
I	1068.00		NIST
I	1067.00		NIST
I	1097.00		NIST
I	1107.00		NIST
I	1105.00		NIST
I	1116.00		NIST
I	1103.00		NIST
I	1097.00		NIST
I	1098.00		NIST
I	1085.00		NIST
I	1068.00		NIST
I	1116.00		NIST
I	1096.00		NIST
I	1100.00		NIST
I	1077.00		NIST
I	1076.00		NIST
I	1093.00		NIST
I	1084.00		NIST
I	1107.00		NIST
I	1097.00		NIST
I	1096.00		NIST
I	1085.00		NIST
I	1084.00		NIST
I	1078.00		NIST
I	1124.00		NIST
I	1073.00		NIST
I	1113.00		NIST
I	1066.00		NIST
I	1104.00		NIST
I	1108.00		NIST
I	1108.00		NIST
I	1110.00		NIST
I	1092.00		NIST
I	1059.00		NIST
I	1106.00		NIST
I	1119.00		NIST
I	1109.00		NIST
I	1098.00		NIST
I	1081.00		NIST
I	1103.00		NIST
I	1087.00		NIST
I	1087.00		NIST
I	Outlier 1054.00		NIST
I	1087.00		NIST
I	1090.00		NIST
I	1113.00		NIST
I	1059.00		NIST
I	1081.00		NIST
I	1113.00		NIST
I	1081.00		NIST
I	1081.00		NIST
I	1083.00		NIST
I	1087.00		NIST
I	1094.00		NIST
I	1081.00		NIST
I	Outlier 1125.00		NIST
I	1091.00		NIST
I	Outlier 1055.00		NIST
I	1094.00		NIST
I	1094.00		NIST
I	1122.00		NIST
I	1093.00		NIST
I	1085.00		NIST
I	1110.00		NIST
I	1097.00		NIST
I	1086.00		NIST
I	1104.00		NIST
I	1108.00		NIST
I	1110.00		NIST
I	1108.00		NIST
I	1095.00		NIST
I	1087.00		NIST
I	1091.00		NIST
I	1060.00		NIST
I	1103.00		NIST
I	1087.00		NIST
I	1103.00		NIST
I	1108.00		NIST
I	1104.00		NIST
I	1103.00		NIST
I	1103.00		NIST
I	1086.00		NIST
I	1114.00		NIST
I	1062.00		NIST
I	1105.00		NIST
I	1105.00		NIST
I	1110.00		NIST
I	Outlier 1054.00		NIST
I	1094.00		NIST
I	1096.00		NIST
I	1091.00		NIST
I	1099.00		NIST
I	1070.00		NIST
I	1088.00		NIST
I	1094.00		NIST
I	1071.00		NIST
I	1070.00		NIST
I	1090.00		NIST
I	1100.00		NIST
I	Outlier 1054.00		NIST
I	1084.00		NIST
I	1084.00		NIST
I	1084.00		NIST
I	1088.00		NIST
I	1060.00		NIST
I	1063.00		NIST
I	1060.00		NIST
I	1063.00		NIST
I	Outlier 1054.00		NIST
I	1090.00		NIST
I	1092.00		NIST
I	1090.00		NIST
I	1098.00		NIST
I	1096.00		NIST
I	1099.00		NIST
I	1119.00		NIST
I	1099.00		NIST
I	1099.00		NIST
I	1093.00		NIST
I	Outlier 1054.00		NIST
I	1087.00		NIST
I	1113.00		NIST
I	1089.00		NIST
I	1108.00		NIST
I	1113.00		NIST
I	1113.00		NIST
I	1106.00		NIST
I	1108.00		NIST
I	Outlier 1129.00		NIST
I	1097.00		NIST
I	1107.00		NIST
I	1108.00		NIST
I	1091.00		NIST
I	1108.00		NIST
I	1091.00		NIST
I	1086.00		NIST
I	1091.00		NIST
I	1072.00		NIST
I	Outlier 1129.00		NIST
I	1093.00		NIST
I	1091.00		NIST
I	1096.00		NIST
I	Outlier 1054.00		NIST
I	1091.00		NIST
I	1085.00		NIST
I	1084.00		NIST
I	1085.00		NIST
I	1084.00		NIST
I	1089.00		NIST
I	1108.00		NIST
I	1091.00		NIST
I	1083.00		NIST
I	1091.00		NIST
I	1098.00		NIST
I	1094.00		NIST
I	1095.00		NIST
I	1095.00		NIST
I	1095.00		NIST
I	1114.00		NIST
I	1110.00		NIST
I	1110.00		NIST
I	Outlier 1054.00		NIST
I	1090.00		NIST
I	1092.00		NIST
I	1084.00		NIST
I	1089.00		NIST
I	1122.00		NIST
I	1076.00		NIST
I	1086.00		NIST
I	1093.00		NIST
I	1112.00		NIST
I	1114.00		NIST
I	1078.00		NIST
I	1092.00		NIST
I	1077.00		NIST
I	1121.00		NIST
I	1083.00		NIST
I	1068.00		NIST
I	1108.00		NIST
I	1094.00		NIST
I	1080.00		NIST
I	1104.00		NIST
I	1059.00		NIST
I	1081.00		NIST
I	1087.00		NIST
I	1113.00		NIST
I	1110.00		NIST
I	1060.00		NIST
I	1062.00		NIST
I	1088.00		NIST
I	1100.00		NIST
I	Outlier 1054.00		NIST
S°gas	350.00	J/mol×K	NIST
S°liquid	214.50	J/mol×K	NIST
S°solid,1 bar	140.70	J/mol×K	NIST
Tboil	[374.65; 410.55]	K
Tboil	381.04	K	KDB
Tboil	381.05	K	Measure...
Tboil	380.15	K	Liquid-...
Tboil	380.83	K	Isobari...
Tboil	380.98	K	Isobari...
Tboil	380.93	K	Vapor-L...
Tboil	381.00	K	Vapor-L...
Tboil	380.92	K	Vapor-L...
Tboil	380.92	K	Vapor L...
Tboil	380.98	K	High-Pr...
Tboil	380.90 ± 0.40	K	NIST
Tboil	381.30	K	NIST
Tboil	380.97 ± 0.30	K	NIST
Tboil	380.85 ± 0.30	K	NIST
Tboil	Outlier 410.55 ± 0.20	K	NIST
Tboil	381.10	K	NIST
Tboil	380.85 ± 0.40	K	NIST
Tboil	380.85 ± 0.30	K	NIST
Tboil	380.55 ± 0.20	K	NIST
Tboil	381.25 ± 0.30	K	NIST
Tboil	380.94 ± 0.40	K	NIST
Tboil	381.10 ± 0.40	K	NIST
Tboil	380.90 ± 0.40	K	NIST
Tboil	380.90 ± 0.30	K	NIST
Tboil	380.90 ± 0.30	K	NIST
Tboil	381.05 ± 0.20	K	NIST
Tboil	380.90 ± 0.10	K	NIST
Tboil	381.95 ± 0.30	K	NIST
Tboil	381.05	K	NIST
Tboil	381.15 ± 0.40	K	NIST
Tboil	381.03 ± 1.00	K	NIST
Tboil	380.90 ± 0.10	K	NIST
Tboil	379.15 ± 2.00	K	NIST
Tboil	381.45	K	NIST
Tboil	380.65 ± 1.00	K	NIST
Tboil	379.15 ± 2.00	K	NIST
Tboil	380.15 ± 1.00	K	NIST
Tboil	381.15 ± 1.00	K	NIST
Tboil	381.20 ± 0.38	K	NIST
Tboil	379.90 ± 0.70	K	NIST
Tboil	381.15 ± 1.00	K	NIST
Tboil	381.15 ± 2.00	K	NIST
Tboil	381.15 ± 1.00	K	NIST
Tboil	378.65 ± 2.00	K	NIST
Tboil	380.15 ± 2.00	K	NIST
Tboil	379.65 ± 1.00	K	NIST
Tboil	381.15 ± 0.50	K	NIST
Tboil	381.05 ± 0.50	K	NIST
Tboil	381.15 ± 0.50	K	NIST
Tboil	381.20 ± 0.40	K	NIST
Tboil	381.15 ± 0.50	K	NIST
Tboil	381.80 ± 0.50	K	NIST
Tboil	380.15 ± 1.00	K	NIST
Tboil	381.00 ± 1.50	K	NIST
Tboil	381.15 ± 0.50	K	NIST
Tboil	380.15 ± 1.00	K	NIST
Tboil	379.65 ± 1.00	K	NIST
Tboil	380.00 ± 3.00	K	NIST
Tboil	378.15 ± 5.00	K	NIST
Tboil	381.15 ± 0.25	K	NIST
Tboil	375.15 ± 5.00	K	NIST
Tboil	380.65 ± 0.50	K	NIST
Tboil	384.15 ± 3.00	K	NIST
Tboil	380.35 ± 0.50	K	NIST
Tboil	378.15 ± 2.00	K	NIST
Tboil	374.65 ± 2.00	K	NIST
Tboil	380.15 ± 1.00	K	NIST
Tboil	380.65 ± 0.50	K	NIST
Tboil	381.35 ± 0.50	K	NIST
Tboil	380.75 ± 0.50	K	NIST
Tboil	381.04 ± 0.10	K	NIST
Tboil	380.65 ± 0.50	K	NIST
Tboil	379.90 ± 1.50	K	NIST
Tboil	380.55 ± 0.50	K	NIST
Tboil	380.25 ± 0.50	K	NIST
Tboil	380.96 ± 0.20	K	NIST
Tboil	381.10 ± 0.30	K	NIST
Tboil	381.15 ± 0.30	K	NIST
Tboil	381.25 ± 0.15	K	NIST
Tboil	381.00 ± 0.50	K	NIST
Tboil	381.00 ± 0.50	K	NIST
Tboil	381.00 ± 0.50	K	NIST
Tboil	381.30 ± 0.20	K	NIST
Tboil	381.00 ± 1.50	K	NIST
Tboil	381.00 ± 0.50	K	NIST
Tboil	381.20 ± 0.30	K	NIST
Tboil	379.05 ± 1.00	K	NIST
Tboil	380.85 ± 0.20	K	NIST
Tboil	381.00 ± 0.30	K	NIST
Tboil	380.15 ± 0.30	K	NIST
Tboil	381.05 ± 0.50	K	NIST
Tboil	380.62 ± 0.20	K	NIST
Tboil	381.04 ± 0.10	K	NIST
Tboil	380.40 ± 0.30	K	NIST
Tboil	376.30 ± 0.20	K	NIST
Tboil	378.20 ± 0.50	K	NIST
Tboil	380.82 ± 0.30	K	NIST
Tboil	380.79 ± 0.30	K	NIST
Tboil	380.40 ± 0.50	K	NIST
Tboil	379.55 ± 1.00	K	NIST
Tc	[538.20; 556.70]	K
Tc	547.80	K	KDB
Tc	547.80 ± 0.30	K	NIST
Tc	548.60	K	NIST
Tc	547.70	K	NIST
Tc	547.78 ± 1.00	K	NIST
Tc	547.74	K	NIST
Tc	Outlier 556.70	K	NIST
Tc	547.77	K	NIST
Tc	549.85 ± 0.30	K	NIST
Tc	550.80	K	NIST
Tc	Outlier 538.20	K	NIST
Tfus	[165.00; 169.00]	K
Tfus	165.00	K	KDB
Tfus	165.15 ± 2.00	K	NIST
Tfus	165.15	K	NIST
Tfus	169.00 ± 2.00	K	NIST
Ttriple	[171.18; 171.20]	K
Ttriple	171.18	K	KDB
Ttriple	171.20 ± 0.01	K	NIST
Ttriple	171.18 ± 0.02	K	NIST
Vc	[0.274; 0.274]	m3/kmol
Vc	0.274	m3/kmol	KDB
Vc	0.274	m3/kmol	NIST
Zc	0.2583780		KDB
Zra	0.26		KDB

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[133.74; 189.48]	J/mol×K	[379.99; 602.55]
T(K) Ideal gas heat capacity (J/mol×K) 130 140 150 160 170 180 190 400 500 600
Cp,gas	133.74	J/mol×K	379.99	NIST
Cp,gas	134.34	J/mol×K	381.23	NIST
Cp,gas	140.10 ± 0.71	J/mol×K	390.55	NIST
Cp,gas	141.76 ± 0.71	J/mol×K	397.65	NIST
Cp,gas	139.55	J/mol×K	400.03	NIST
Cp,gas	143.92 ± 0.71	J/mol×K	406.95	NIST
Cp,gas	146.25 ± 0.71	J/mol×K	416.95	NIST
Cp,gas	147.91 ± 0.71	J/mol×K	424.05	NIST
Cp,gas	146.35	J/mol×K	425.01	NIST
Cp,gas	152.05 ± 0.71	J/mol×K	441.85	NIST
Cp,gas	152.97	J/mol×K	450.06	NIST
Cp,gas	154.24 ± 0.71	J/mol×K	451.25	NIST
Cp,gas	159.62 ± 0.71	J/mol×K	474.35	NIST
Cp,gas	158.94	J/mol×K	475.09	NIST
Cp,gas	160.41 ± 0.71	J/mol×K	477.75	NIST
Cp,gas	165.96 ± 0.71	J/mol×K	501.55	NIST
Cp,gas	171.62 ± 0.71	J/mol×K	525.85	NIST
Cp,gas	176.39 ± 0.71	J/mol×K	546.35	NIST
Cp,gas	184.92 ± 0.71	J/mol×K	582.95	NIST
Cp,gas	189.48 ± 0.71	J/mol×K	602.55	NIST
Cp,liquid	[181.00; 215.10]	J/mol×K	[298.10; 333.00]
T(K) Liquid phase heat capacity (J/mol×K) 180 185 190 195 200 205 210 215 300 310 320 330
Cp,liquid	184.10	J/mol×K	298.10	NIST
Cp,liquid	181.05	J/mol×K	298.15	NIST
Cp,liquid	181.00	J/mol×K	298.15	NIST
Cp,liquid	182.01	J/mol×K	298.15	NIST
Cp,liquid	185.40	J/mol×K	301.20	NIST
Cp,liquid	187.00	J/mol×K	303.00	NIST
Cp,liquid	185.60	J/mol×K	303.15	NIST
Cp,liquid	201.30	J/mol×K	323.00	NIST
Cp,liquid	215.10	J/mol×K	333.00	NIST
Cp,solid	129.20	J/mol×K	180.00	NIST
η	[0.0008767; 0.0048050]	Pa×s	[288.15; 343.15]
T(K) Dynamic viscosity (Pa×s) 1.00e-3 2.00e-3 3.00e-3 4.00e-3 5.00e-3 300 320 340
η	0.0048050	Pa×s	288.15	Densiti...
η	0.0048050	Pa×s	288.15	Densiti...
η	0.0039940	Pa×s	293.15	Viscosi...
η	0.0039430	Pa×s	293.15	Densiti...
η	0.0040855	Pa×s	293.15	Measure...
η	0.0040366	Pa×s	293.15	Densiti...
η	0.0040850	Pa×s	293.15	Experim...
η	0.0034500	Pa×s	298.15	Measure...
η	0.0034350	Pa×s	298.15	Densiti...
η	0.0034350	Pa×s	298.15	Densiti...
η	0.0033340	Pa×s	298.15	Viscosi...
η	0.0033320	Pa×s	298.15	Densiti...
η	0.0034040	Pa×s	298.15	Volumet...
η	0.0033297	Pa×s	298.15	Densiti...
η	0.0028767	Pa×s	303.15	Measure...
η	0.0028752	Pa×s	303.15	Densiti...
η	0.0027940	Pa×s	303.15	Viscosi...
η	0.0028770	Pa×s	303.15	Experim...
η	0.0026950	Pa×s	303.15	Volumet...
η	0.0026490	Pa×s	303.15	Densiti...
η	0.0028840	Pa×s	303.15	Densiti...
η	0.0023845	Pa×s	308.15	Measure...
η	0.0022798	Pa×s	308.15	Densiti...
η	0.0024207	Pa×s	308.15	Densiti...
η	0.0025080	Pa×s	308.15	Densiti...
η	0.0025080	Pa×s	308.15	Densiti...
η	0.0021880	Pa×s	308.15	Volumet...
η	0.0019666	Pa×s	313.15	Densiti...
η	0.0019653	Pa×s	313.15	Densiti...
η	0.0020909	Pa×s	313.15	Measure...
η	0.0020910	Pa×s	313.15	Experim...
η	0.0018700	Pa×s	318.15	Densiti...
η	0.0018700	Pa×s	318.15	Densiti...
η	0.0018503	Pa×s	318.15	Measure...
η	0.0016921	Pa×s	318.15	Densiti...
η	0.0014825	Pa×s	323.15	Densiti...
η	0.0015760	Pa×s	323.15	Experim...
η	0.0015759	Pa×s	323.15	Measure...
η	0.0012675	Pa×s	328.15	Densiti...
η	0.0012967	Pa×s	328.15	Measure...
η	0.0011243	Pa×s	333.15	Measure...
η	0.0011240	Pa×s	333.15	Experim...
η	0.0011163	Pa×s	333.15	Densiti...
η	0.0009876	Pa×s	338.15	Measure...
η	0.0009851	Pa×s	338.15	Densiti...
η	0.0008767	Pa×s	343.15	Densiti...
ΔfusH	[6.32; 6.32]	kJ/mol	[171.18; 171.20]
ΔfusH	6.32	kJ/mol	171.18	NIST
ΔfusH	6.32	kJ/mol	171.20	NIST
ΔfusH	6.32	kJ/mol	171.20	NIST
ΔfusH	6.32	kJ/mol	171.20	NIST
ΔvapH	[36.20; 55.00]	kJ/mol	[106.90; 515.50]
T(K) Enthalpy of vaporization at a given temperature (kJ/mol) 35 40 45 50 55 200 400
ΔvapH	50.71	kJ/mol	106.90	NIST
ΔvapH	55.00	kJ/mol	222.50	NIST
ΔvapH	49.70 ± 0.10	kJ/mol	313.00	NIST
ΔvapH	48.30 ± 0.10	kJ/mol	328.00	NIST
ΔvapH	52.60	kJ/mol	340.50	NIST
ΔvapH	46.20 ± 0.10	kJ/mol	347.00	NIST
ΔvapH	48.10	kJ/mol	351.00	NIST
ΔvapH	47.00	kJ/mol	357.00	NIST
ΔvapH	45.00 ± 0.10	kJ/mol	358.00	NIST
ΔvapH	49.50	kJ/mol	362.00	NIST
ΔvapH	44.20 ± 0.10	kJ/mol	363.00	NIST
ΔvapH	46.20	kJ/mol	365.50	NIST
ΔvapH	45.20	kJ/mol	370.50	NIST
ΔvapH	45.40	kJ/mol	375.00	NIST
ΔvapH	44.20	kJ/mol	379.00	NIST
ΔvapH	41.90 ± 0.10	kJ/mol	381.00	NIST
ΔvapH	41.82	kJ/mol	381.10	NIST
ΔvapH	42.60	kJ/mol	399.50	NIST
ΔvapH	41.10	kJ/mol	447.00	NIST
ΔvapH	46.00	kJ/mol	452.50	NIST
ΔvapH	40.10	kJ/mol	485.50	NIST
ΔvapH	36.20	kJ/mol	515.50	NIST
ν	[0.0000027; 0.0000042]	m2/s	[298.15; 313.15]
ν	0.0000042	m2/s	298.15	Viscosi...
ν	0.0000027	m2/s	313.15	Viscosi...
Pvap	[0.34; 2505.00]	kPa	[278.15; 513.15]
T(K) Vapor pressure (kPa) 0 500 1000 1500 2000 2500 300 400 500
Pvap	0.34	kPa	278.15	Vapor L...
Pvap	0.51	kPa	283.15	Vapor L...
Pvap	0.74	kPa	288.15	Vapor L...
Pvap	1.06	kPa	293.15	Vapor L...
Pvap	1.50	kPa	298.15	Vapor L...
Pvap	2.13	kPa	303.15	Vapor L...
Pvap	2.96	kPa	308.15	Vapor L...
Pvap	4.03	kPa	313.15	Vapor L...
Pvap	5.44	kPa	318.15	Vapor L...
Pvap	7.24	kPa	323.15	Vapor L...
Pvap	15.00	kPa	336.90	Complem...
Pvap	30.00	kPa	351.20	Complem...
Pvap	40.00	kPa	357.45	Isobari...
Pvap	40.00	kPa	357.70	Complem...
Pvap	50.00	kPa	362.90	Complem...
Pvap	53.33	kPa	364.17	Isobari...
Pvap	60.00	kPa	367.40	Complem...
Pvap	66.66	kPa	369.67	Isobari...
Pvap	70.00	kPa	371.30	Complem...
Pvap	79.99	kPa	374.35	Isobari...
Pvap	80.00	kPa	374.70	Complem...
Pvap	90.00	kPa	377.80	Complem...
Pvap	93.32	kPa	378.45	Isobari...
Pvap	98.66	kPa	379.96	Isobari...
Pvap	100.00	kPa	380.70	Complem...
Pvap	110.00	kPa	383.30	Complem...
Pvap	120.00	kPa	385.80	Complem...
Pvap	130.00	kPa	388.00	Complem...
Pvap	140.00	kPa	390.20	Complem...
Pvap	150.00	kPa	392.20	Complem...
Pvap	1113.00	kPa	468.15	Vapor-L...
Pvap	1506.00	kPa	483.15	Vapor-L...
Pvap	1933.00	kPa	498.15	Vapor-L...
Pvap	2505.00	kPa	513.15	Vapor-L...
n0	[1.38390; 1.39620]		[293.15; 308.15]
T(K) Refractive Index 1.38 1.39 1.39 1.39 1.39 1.39 1.4 295 300 305
n0	1.39540		293.15	Vapor L...
n0	1.39550		293.15	Liquid ...
n0	1.39290		293.15	Volumet...
n0	1.39570		293.15	Solid-L...
n0	1.39580		293.15	Isother...
n0	1.39570		293.15	Isother...
n0	1.39590		293.15	Isother...
n0	1.39620		293.15	Excess ...
n0	1.39563		293.15	Ternary...
n0	1.39580		293.15	Vapour-...
n0	1.39550		293.15	Liquid-...
n0	1.39260		295.15	Isobari...
n0	1.39390		298.15	(Vapor ...
n0	1.39320		298.15	Physico...
n0	1.39380		298.15	Volumet...
n0	1.39380		298.15	Study o...
n0	1.39390		298.15	Excess ...
n0	1.39390		298.15	Isobari...
n0	1.39380		298.15	Liquid ...
n0	1.39390		298.15	Excess ...
n0	1.39390		298.15	Excess ...
n0	1.39390		298.15	Activit...
n0	1.39380		298.15	Vapor l...
n0	1.38390		298.15	Bubble ...
n0	1.39390		298.15	Bubble-...
n0	1.39370		298.15	Density...
n0	1.39370		298.15	Phase e...
n0	1.39370		298.15	Phase e...
n0	1.39370		298.15	Isobari...
n0	1.39170		303.15	Physico...
n0	1.38960		308.15	Physico...
ρl	[756.43; 806.12]	kg/m3	[288.15; 348.15]
T(K) Liquid Density (kg/m3) 760 770 780 790 800 810 300 320 340
ρl	805.88	kg/m3	288.15	Volumet...
ρl	806.12	kg/m3	288.15	Excess ...
ρl	805.60	kg/m3	288.15	Excess ...
ρl	802.00	kg/m3	293.00	KDB
ρl	801.70	kg/m3	293.15	Measure...
ρl	801.80	kg/m3	293.15	Measure...
ρl	802.03	kg/m3	293.15	Volumet...
ρl	801.98	kg/m3	293.15	Density...
ρl	801.98	kg/m3	293.15	Densiti...
ρl	801.85	kg/m3	293.15	Volumet...
ρl	801.82	kg/m3	293.15	Density...
ρl	801.48	kg/m3	293.15	Densiti...
ρl	801.80	kg/m3	293.15	Measure...
ρl	801.96	kg/m3	293.15	Experim...
ρl	795.35	kg/m3	298.15	Vapor L...
ρl	797.80	kg/m3	298.15	Bubble ...
ρl	798.32	kg/m3	298.15	Densiti...
ρl	798.10	kg/m3	298.15	Densiti...
ρl	797.99	kg/m3	298.15	Volumet...
ρl	797.77	kg/m3	298.15	Densiti...
ρl	798.13	kg/m3	298.15	Densiti...
ρl	798.41	kg/m3	298.15	Excess ...
ρl	798.16	kg/m3	298.15	Volumet...
ρl	797.77	kg/m3	298.15	Surface...
ρl	797.84	kg/m3	298.15	Volumet...
ρl	797.82	kg/m3	298.15	Experim...
ρl	801.65	kg/m3	298.15	Liquid-...
ρl	797.83	kg/m3	298.15	Excess ...
ρl	797.54	kg/m3	298.15	Densiti...
ρl	798.10	kg/m3	298.15	Density...
ρl	797.98	kg/m3	298.15	(Vapour...
ρl	798.12	kg/m3	298.15	Experim...
ρl	797.83	kg/m3	298.15	Proposa...
ρl	797.92	kg/m3	298.15	Excess ...
ρl	794.24	kg/m3	303.15	Densiti...
ρl	794.25	kg/m3	303.15	Volumet...
ρl	794.22	kg/m3	303.15	Experim...
ρl	794.20	kg/m3	303.15	Density...
ρl	793.60	kg/m3	303.15	Densiti...
ρl	794.06	kg/m3	303.15	Density...
ρl	794.03	kg/m3	303.15	Volumet...
ρl	794.43	kg/m3	303.15	Densiti...
ρl	790.09	kg/m3	308.15	Volumet...
ρl	790.29	kg/m3	308.15	Densiti...
ρl	789.66	kg/m3	308.15	Densiti...
ρl	790.63	kg/m3	308.15	Experim...
ρl	790.31	kg/m3	308.15	Volumet...
ρl	790.27	kg/m3	308.15	Experim...
ρl	790.12	kg/m3	308.15	Densiti...
ρl	790.25	kg/m3	308.15	Density...
ρl	790.49	kg/m3	308.15	Densiti...
ρl	786.12	kg/m3	313.15	Densiti...
ρl	786.48	kg/m3	313.15	Densiti...
ρl	786.12	kg/m3	313.15	Density...
ρl	786.07	kg/m3	313.15	Excess ...
ρl	786.51	kg/m3	313.15	Excess ...
ρl	786.31	kg/m3	313.15	Volumet...
ρl	785.72	kg/m3	313.15	Densiti...
ρl	786.12	kg/m3	313.15	Volumet...
ρl	786.27	kg/m3	313.15	Experim...
ρl	786.24	kg/m3	313.15	Density...
ρl	786.30	kg/m3	313.15	Densiti...
ρl	781.78	kg/m3	318.15	Densiti...
ρl	781.97	kg/m3	318.15	Volumet...
ρl	782.06	kg/m3	318.15	Densiti...
ρl	782.26	kg/m3	318.15	Volumet...
ρl	781.98	kg/m3	318.15	Experim...
ρl	782.42	kg/m3	318.15	Densiti...
ρl	782.24	kg/m3	318.15	Densiti...
ρl	777.94	kg/m3	323.15	Density...
ρl	778.30	kg/m3	323.15	Densiti...
ρl	777.86	kg/m3	323.15	Volumet...
ρl	777.93	kg/m3	323.15	Densiti...
ρl	778.14	kg/m3	323.15	Volumet...
ρl	778.12	kg/m3	323.15	Densiti...
ρl	774.09	kg/m3	328.15	Densiti...
ρl	773.73	kg/m3	328.15	Densiti...
ρl	773.92	kg/m3	328.15	Densiti...
ρl	774.11	kg/m3	328.15	Excess ...
ρl	773.69	kg/m3	328.15	Excess ...
ρl	769.81	kg/m3	333.15	Densiti...
ρl	769.44	kg/m3	333.15	Densiti...
ρl	769.65	kg/m3	333.15	Densiti...
ρl	769.46	kg/m3	333.15	Density...
ρl	765.07	kg/m3	338.15	Densiti...
ρl	765.45	kg/m3	338.15	Excess ...
ρl	760.61	kg/m3	343.15	Densiti...
ρl	756.43	kg/m3	348.15	Excess ...
ΔfusS	36.93	J/mol×K	171.18	NIST
csound,fluid	[1108.20; 1238.70]	m/s	[283.15; 323.15]
T(K) Speed of sound in fluid (m/s) 1100 1120 1140 1160 1180 1200 1220 1240 290 300 310 320
csound,fluid	1238.70	m/s	283.15	Excess ...
csound,fluid	1204.10	m/s	293.15	Acousti...
csound,fluid	1188.50	m/s	298.15	Densiti...
csound,fluid	1188.00	m/s	298.15	Excess ...
csound,fluid	1174.30	m/s	303.15	Excess ...
csound,fluid	1138.40	m/s	313.15	Densiti...
csound,fluid	1138.00	m/s	313.15	Excess ...
csound,fluid	1108.20	m/s	323.15	Excess ...

Datasets

1. Mass density, kg/m3 (2)
2. Speed of sound, m/s (1)

Mass density, kg/m3

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
283.15	89.40	809.726
283.16	289.90	810.056
283.15	478.20	810.123
283.15	489.90	810.142
283.15	930.20	810.437
283.15	1027.30	810.557
283.15	2172.10	811.348
283.15	2992.90	811.865
283.15	4993.80	813.245
283.15	6906.90	814.669
283.15	8995.70	816.167
283.15	10003.00	816.885
283.15	12183.00	818.287
283.15	14910.00	820.439
283.15	17915.00	822.056
283.15	20110.00	823.875
283.15	22168.00	825.177
283.15	24886.00	826.625
283.15	27713.00	828.29
283.15	30148.00	829.717
283.15	32117.00	830.745
283.15	33086.00	831.522
283.15	33288.00	831.507
283.15	34077.00	832.073
283.15	35107.00	832.469
283.15	38030.00	834.322
283.16	39967.00	835.34
283.16	41406.00	835.909
283.15	44591.00	837.752
283.16	48034.00	839.7
283.16	49830.00	840.462
283.16	51952.00	841.796
283.15	54994.00	843.308
283.15	57756.00	844.723
283.15	59886.00	845.575
283.15	61822.00	846.524
283.15	64894.00	848.158
283.16	66072.00	848.566
288.15	85.30	806.159
288.15	351.10	806.381
288.16	549.30	806.494
288.15	718.60	806.519
288.15	928.30	806.632
288.15	1132.30	807.006
288.15	1931.60	807.42
288.15	3433.90	808.429
288.15	5023.90	809.62
288.15	6893.90	810.983
288.15	8406.40	812.175
288.16	9959.10	813.184
288.15	12498.00	814.345
288.15	13061.00	815.035
288.15	15159.00	815.414
288.15	16159.00	816.818
288.15	17078.00	817.715
288.15	19062.00	818.283
288.15	20120.00	819.399
288.15	21983.00	820.3
288.15	22948.00	821.319
288.15	24955.00	821.837
288.16	27092.00	823.174
288.16	29078.00	824.509
288.15	31002.00	825.774
288.16	33729.00	826.936
288.15	36056.00	828.477
288.15	38602.00	829.859
288.15	40698.00	831.363
288.15	42984.00	832.313
288.15	44991.00	833.694
288.15	46862.00	834.848
288.15	49740.00	835.692
288.15	53748.00	837.321
288.15	55203.00	839.369
288.16	57016.00	840.129
288.15	60810.00	841.135
288.16	62338.00	843.086
288.15	65611.00	844.144
293.15	63.40	802.054
293.15	194.50	802.316
293.16	310.40	802.406
293.16	463.50	802.612
293.15	662.60	802.599
293.16	1059.70	802.921
293.16	2037.10	803.747
293.16	2922.00	804.089
293.16	3431.50	804.593
293.16	5298.80	805.894
293.15	5367.80	806.019
293.15	5979.30	806.327
293.16	7111.40	807.238
293.15	8031.40	807.842
293.16	9968.50	809.474
293.15	12279.00	811.587
293.16	14057.00	812.743
293.15	16110.00	814.191
293.15	18001.00	815.385
293.16	20853.00	817.066
293.16	22118.00	818.157
293.16	24057.00	819.188
293.16	25922.00	820.412
293.16	27187.00	821.228
293.15	30253.00	822.999
293.15	32967.00	824.811
293.16	34602.00	825.683
293.16	38051.00	827.567
293.16	40103.00	828.763
293.15	42984.00	830.218
293.15	44913.00	831.278
293.15	47933.00	833.008
293.15	50078.00	834.047
293.16	52135.00	835.387
293.16	55036.00	836.79
293.16	58004.00	838.271
293.16	60107.00	839.502
293.16	62061.00	840.325
293.16	66037.00	842.335
298.15	122.40	798.281
298.15	162.60	798.371
298.15	405.50	798.562
298.15	632.80	798.678
298.15	956.40	798.832
298.16	1152.20	799.011
298.16	2046.30	799.798
298.16	3021.10	800.42
298.16	5107.40	801.927
298.15	6988.80	803.491
298.16	9044.30	804.777
298.16	9996.80	805.681
298.16	11947.00	807.14
298.15	14555.00	809.311
298.15	18284.00	812.068
298.15	20164.00	813.104
298.15	22781.00	814.894
298.15	25076.00	816.275
298.15	27604.00	817.904
298.15	30046.00	819.519
298.15	32326.00	821.055
298.16	33072.00	821.357
298.15	33317.00	821.248
298.16	34997.00	822.338
298.16	37948.00	823.936
298.16	39972.00	825.207
298.16	41983.00	826.345
298.15	44911.00	827.946
298.16	48045.00	829.528
298.16	49997.00	830.783
298.16	52020.00	832.399
298.16	54851.00	833.381
298.16	57898.00	835.245
298.15	60006.00	836.063
298.15	62079.00	837.121
298.15	65330.00	838.566
298.15	66093.00	839.052
303.15	50.60	793.736
303.16	270.10	793.901
303.16	464.40	794.084
303.16	779.60	794.287
303.15	974.40	794.496
303.15	1922.50	795.367
303.16	2945.00	796.031
303.16	4911.20	797.923
303.16	7058.60	799.569
303.15	9012.30	801.25
303.15	10062.00	802.346
303.16	12047.00	803.47
303.15	14908.00	805.823
303.15	18109.00	808.133
303.15	20042.00	809.402
303.16	22055.00	811.092
303.15	25084.00	812.578
303.16	28094.00	815.049
303.15	30167.00	816.191
303.15	32070.00	817.319
303.15	33147.00	817.694
303.16	32939.00	817.604
303.16	34037.00	818.139
303.15	35162.00	818.815
303.15	38019.00	820.574
303.15	39970.00	821.716
303.15	42004.00	823.024
303.15	45033.00	824.95
303.16	48317.00	826.769
303.15	49864.00	827.592
303.15	52115.00	829.036
303.15	55239.00	830.776
303.15	58089.00	832.479
303.15	60079.00	833.282
303.15	62294.00	834.706
303.15	65137.00	835.715
303.16	66124.00	836.43
308.15	96.70	791.579
308.15	250.60	791.714
308.15	562.20	791.995
308.16	770.20	792.158
308.15	991.90	792.349
308.16	2101.20	793.3
308.16	3195.10	794.224
308.15	5219.30	795.881
308.16	7083.00	797.398
308.16	9108.00	799.011
308.15	10282.00	799.926
308.16	12379.00	801.538
308.15	15083.00	803.575
308.16	18161.00	805.827
308.16	20006.00	807.165
308.16	22192.00	808.686
308.16	25100.00	810.705
308.16	27887.00	812.568
308.16	30041.00	813.99
308.16	31933.00	815.242
308.16	33077.00	815.959
308.15	32866.00	815.75
308.16	34026.00	816.482
308.15	35203.00	817.171
308.16	35193.00	817.245
308.16	38088.00	818.995
308.16	40106.00	820.225
308.16	42282.00	821.541
308.16	45145.00	823.251
308.15	48031.00	824.96
308.16	50089.00	826.126
308.16	52047.00	827.233
308.15	55094.00	828.952
308.16	58085.00	830.585
308.15	60161.00	831.729
308.15	62192.00	832.798
308.16	65217.00	834.405
308.15	66004.00	834.804
313.15	82.90	787.4
313.15	316.80	787.607
313.15	491.80	787.767
313.15	890.90	788.108
313.15	981.50	788.182
313.15	1939.60	789.038
313.15	2951.00	789.905
313.15	4889.10	791.537
313.15	6856.50	793.195
313.15	8886.90	794.841
313.15	10029.00	795.77
313.15	11886.00	797.214
313.15	14927.00	799.577
313.15	17845.00	801.775
313.15	20040.00	803.389
313.15	21942.00	804.76
313.15	24894.00	806.85
313.15	28132.00	809.095
313.15	29974.00	810.333
313.15	32058.00	811.716
313.16	33053.00	812.371
313.16	33131.00	812.356
313.16	34040.00	812.94
313.15	35162.00	813.664
313.15	37952.00	815.444
313.15	40011.00	816.732
313.15	41939.00	817.878
313.15	45098.00	819.95
313.15	47966.00	821.512
313.15	49918.00	822.65
313.15	52024.00	823.857
313.15	54951.00	825.557
313.15	58062.00	827.336
313.15	60202.00	828.515
313.16	62187.00	829.599
313.15	65050.00	831.15
313.15	66082.00	831.7
318.16	128.50	783.253
318.15	368.30	783.457
318.15	589.40	783.667
318.16	858.20	783.902
318.16	1069.50	784.105
318.16	1979.10	784.923
318.16	2997.40	785.79
318.16	4942.60	787.513
318.16	6987.20	789.27
318.16	8967.50	790.929
318.15	9887.60	791.657
318.16	11870.00	793.265
318.16	14863.00	795.639
318.16	17735.00	797.848
318.16	19860.00	799.438
318.16	21987.00	801.004
318.16	25193.00	803.357
318.16	27823.00	805.216
318.16	30119.00	806.799
318.16	32145.00	808.205
318.15	33128.00	808.894
318.15	33065.00	808.852
318.16	34164.00	809.488
318.15	35190.00	810.134
318.16	38074.00	812.009
318.16	40048.00	813.265
318.16	41997.00	814.496
318.16	45096.00	816.426
318.15	48088.00	818.249
318.16	50173.00	819.491
318.15	52184.00	820.67
318.16	55235.00	822.46
318.16	58075.00	824.084
318.15	60194.00	825.273
318.15	62260.00	826.409
318.15	65194.00	828.017
318.15	66060.00	828.484
323.15	62.10	778.89
323.15	338.00	779.159
323.15	557.50	779.374
323.15	917.30	779.697
323.16	1117.80	779.897
323.15	2125.40	780.833
323.15	3154.80	781.778
323.15	5126.40	783.557
323.15	7366.80	785.517
323.15	9081.60	787.01
323.15	10156.00	787.907
323.15	12167.00	789.544
323.15	15030.00	791.876
323.15	18076.00	794.274
323.15	19932.00	795.694
323.15	22079.00	797.333
323.15	25085.00	799.541
323.15	28006.00	801.644
323.15	30029.00	803.084
323.15	31969.00	804.431
323.15	32903.00	805.081
323.15	33102.00	805.154
323.15	33950.00	805.707
323.15	34958.00	806.425
323.15	37883.00	808.369
323.15	39891.00	809.68
323.15	42065.00	811.076
323.15	44846.00	812.852
323.16	47886.00	814.721
323.15	49935.00	815.968
323.15	52064.00	817.249
323.15	54897.00	818.944
323.15	57818.00	820.634
323.15	59855.00	821.787
323.15	61856.00	822.928
323.15	64838.00	824.6
323.15	65957.00	825.209
328.15	96.50	774.907
328.15	395.80	775.157
328.16	515.00	775.262
328.15	904.10	775.603
328.15	1030.60	775.74
328.16	2069.70	776.794
328.15	2999.30	777.646
328.15	5042.00	779.515
328.16	6936.70	781.257
328.16	8874.20	782.985
328.15	10121.00	784.077
328.15	11905.00	785.621
328.16	14954.00	788.149
328.16	17891.00	790.513
328.16	20040.00	792.21
328.16	22054.00	793.773
328.15	24953.00	795.929
328.15	27874.00	798.098
328.15	29949.00	799.588
328.15	31948.00	800.996
328.16	33018.00	801.745
328.15	33061.00	801.681
328.15	34111.00	802.415
328.15	34984.00	803.007
328.15	37913.00	805.001
328.16	39966.00	806.346
328.15	41958.00	807.674
328.15	44806.00	809.5
328.16	47820.00	811.414
328.16	49817.00	812.637
328.16	52099.00	814.145
328.15	55150.00	815.995
328.15	58100.00	817.75
328.15	60045.00	818.881
328.15	62082.00	820.048
328.16	64955.00	821.692
328.15	66095.00	822.334
333.15	95.70	770.629
333.16	295.90	770.818
333.16	574.50	771.11
333.15	913.60	771.467
333.16	1069.50	771.621
333.16	2110.60	772.649
333.16	3100.00	773.622
333.16	5034.00	775.464
333.15	6965.60	777.259
333.15	8937.30	779.076
333.15	9995.10	780.005
333.15	11970.00	781.72
333.15	14915.00	784.255
333.16	17954.00	786.777
333.16	19985.00	788.397
333.15	22033.00	790.027
333.16	24923.00	792.261
333.16	27922.00	794.514
333.15	29996.00	796.045
333.15	31986.00	797.49
333.15	32928.00	798.124
333.16	33031.00	798.137
333.16	34001.00	798.837
333.16	35030.00	799.567
333.16	37925.00	801.558
333.16	39862.00	802.861
333.15	41792.00	804.162
333.16	44782.00	806.126
333.15	47830.00	808.087
333.15	49895.00	809.38
333.15	51876.00	810.61
333.15	54830.00	812.44
333.15	58116.00	814.429
333.15	59975.00	815.509
333.15	61974.00	816.676
333.15	65057.00	818.467
333.15	66042.00	819.039
338.15	72.50	765.803
338.15	267.10	766.009
338.15	496.50	766.255
338.15	821.30	766.6
338.15	1007.70	766.796
338.15	2012.40	767.824
338.15	3039.10	768.845
338.16	5091.10	770.879
338.15	7018.50	772.739
338.15	8987.60	774.596
338.15	10054.00	775.578
338.16	12131.00	777.462
338.16	15171.00	780.113
338.15	18105.00	782.627
338.16	20167.00	784.349
338.15	22120.00	785.947
338.16	25290.00	788.465
338.15	28029.00	790.565
338.16	30041.00	792.069
338.15	32010.00	793.527
338.15	32776.00	794.103
338.15	32995.00	794.184
338.15	33922.00	794.869
338.16	35102.00	795.7
338.15	38056.00	797.798
338.16	39987.00	799.156
338.15	42127.00	800.629
338.16	45109.00	802.623
338.15	48090.00	804.572
338.15	50121.00	805.906
338.15	52094.00	807.168
338.15	55116.00	809.055
338.15	58010.00	810.837
338.15	60191.00	812.149
338.15	62244.00	813.373
338.15	65243.00	815.143
338.15	65986.00	815.583
338.15	66355.00	815.805
343.15	55.60	761.239
343.15	101.80	761.279
343.15	277.30	761.484
343.15	487.70	761.699
343.15	881.60	762.13
343.15	1037.00	762.294
343.15	1941.40	763.263
343.15	3000.30	764.362
343.15	4957.00	766.378
343.15	6956.10	768.377
343.15	8969.50	770.304
343.15	10003.00	771.264
343.15	11997.00	773.149
343.15	14895.00	775.758
343.15	17840.00	778.358
343.15	20135.00	780.417
343.15	21925.00	781.908
343.15	24920.00	784.349
343.15	27949.00	786.755
343.15	29863.00	788.238
343.15	31874.00	789.777
343.15	32981.00	790.602
343.15	32927.00	790.544
343.15	34026.00	791.305
343.15	35028.00	792.011
343.15	38080.00	794.257
343.15	39908.00	795.53
343.15	41973.00	796.98
343.15	44972.00	799.034
343.15	47997.00	801.072
343.15	50016.00	802.401
343.15	52079.00	803.724
343.15	54997.00	805.581
343.15	57987.00	807.46
343.16	60015.00	808.691
343.15	62074.00	809.959
343.15	65051.00	811.734
343.15	66170.00	812.401
348.15	94.00	756.672
348.15	293.80	756.914
348.15	481.90	757.128
348.15	763.50	757.435
348.15	1011.00	757.701
348.15	1981.10	758.826
348.15	3073.20	759.88
348.15	5089.90	762.131
348.15	7034.60	764.092
348.15	9052.50	766.106
348.15	9991.30	767.026
348.16	12060.00	769.03
348.15	15042.00	771.822
348.15	17922.00	774.408
348.15	19893.00	776.137
348.15	22033.00	777.985
348.15	22381.00	778.265
348.16	25066.00	780.513
348.15	28023.00	782.927
348.15	29922.00	784.471
348.16	32007.00	786.046
348.16	32760.00	786.619
348.16	32941.00	786.66
348.15	33999.00	787.493
348.15	34980.00	788.228
348.15	37995.00	790.467
348.15	40072.00	791.973
348.15	41992.00	793.388
348.15	45082.00	795.525
348.15	48031.00	797.589
348.16	50014.00	798.878
348.15	52067.00	800.261
348.15	55099.00	802.242
348.16	58146.00	804.186
348.15	60084.00	805.42
348.15	62302.00	806.758
348.15	65219.00	808.569
348.15	66250.00	809.201
353.15	98.10	752.221
353.15	305.80	752.433
353.15	384.00	752.511
353.15	558.50	752.696
353.15	929.40	753.125
353.15	1073.70	753.289
353.15	2082.70	754.432
353.15	3025.90	755.465
353.15	5017.90	757.656
353.15	6957.80	759.69
353.15	8976.60	761.781
353.15	9990.30	762.812
353.15	11934.00	764.803
353.15	14917.00	767.603
353.15	18020.00	770.471
353.15	19983.00	772.259
353.15	22060.00	773.965
353.15	24899.00	776.429
353.15	27951.00	778.961
353.15	29947.00	780.584
353.15	31942.00	782.185
353.15	32982.00	782.978
353.15	33037.00	783.002
353.15	33907.00	783.604
353.15	35053.00	784.493
353.15	37939.00	786.664
353.15	39830.00	788.076
353.15	41863.00	789.556
353.15	44753.00	791.642
353.15	47880.00	793.816
353.15	49780.00	795.14
353.15	51876.00	796.535
353.15	55023.00	798.765
353.15	55678.00	799.178
353.15	57869.00	800.594
353.15	59971.00	801.962
353.15	62015.00	803.245
353.15	64989.00	805.09
353.15	66151.00	805.82
358.15	91.60	747.694
358.15	304.90	747.895
358.15	517.30	748.147
358.15	850.10	748.568
358.15	1095.50	748.835
358.15	2101.60	750.029
358.15	3210.60	751.303
358.15	5324.20	753.465
358.15	7190.10	755.483
358.15	9074.30	757.505
358.15	10165.00	758.644
358.15	12208.00	760.738
358.15	13986.00	762.552
358.15	15000.00	763.577
358.15	17866.00	766.293
358.15	20104.00	768.379
358.16	22005.00	770.073
358.16	25079.00	772.781
358.15	27962.00	775.177
358.15	30131.00	776.699
358.15	32076.00	778.299
358.15	33039.00	779.08
358.15	32938.00	778.904
358.15	33914.00	779.672
358.15	34978.00	780.53
358.15	37986.00	782.876
358.15	39996.00	784.402
358.15	42079.00	785.976
358.15	45119.00	788.207
358.15	48100.00	790.343
358.15	49987.00	791.672
358.15	52101.00	793.112
358.15	54983.00	795.084
358.15	58017.00	797.106
358.15	60055.00	798.438
358.15	62083.00	799.766
358.15	65016.00	801.626
358.15	66339.00	802.467
363.15	53.20	742.307
363.15	125.50	742.405
363.15	320.30	742.647
363.15	562.50	742.935
363.15	892.50	743.339
363.15	1001.30	743.446
363.15	1911.60	744.576
363.15	2977.30	745.832
363.15	4957.50	748.169
363.15	6937.40	750.436
363.15	8892.90	752.564
363.15	10033.00	753.801
363.15	11914.00	755.769
363.15	14908.00	758.826
363.15	17925.00	761.773
363.15	19995.00	763.754
363.15	21953.00	765.578
363.15	24962.00	768.273
363.15	27932.00	770.858
363.15	30163.00	772.879
363.15	32029.00	774.439
363.15	33151.00	775.369
363.15	33315.00	775.421
363.15	34086.00	776.049
363.15	35189.00	776.934
363.15	37932.00	779.076
363.15	40070.00	780.754
363.15	41883.00	782.107
363.15	44755.00	784.308
363.15	48054.00	786.713
363.15	50037.00	788.134
363.15	51977.00	789.492
363.15	55048.00	791.627
363.15	57990.00	793.615
363.15	60071.00	794.972
363.15	62073.00	796.302
363.15	64996.00	798.178
363.15	66050.00	798.847
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
298.15	1.53	797.775
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	102.00	1347.322
253.15	5144.00	1373.695
253.15	10257.00	1399.134
253.15	15122.00	1422.242
253.15	20400.00	1446.625
253.15	25315.00	1467.969
253.15	30039.00	1488.704
273.15	105.00	1274.213
273.15	5154.00	1302.778
273.15	10139.00	1329.437
273.15	15072.00	1354.721
273.15	20215.00	1379.951
273.15	25138.00	1403.158
273.15	30242.00	1426.375
293.15	102.00	1204.925
293.15	5004.00	1234.867
293.15	10097.00	1264.152
293.15	15140.00	1291.722
293.15	20220.00	1318.237
293.15	25063.00	1342.456
293.15	30100.00	1366.71
313.15	104.00	1138.14
313.15	5135.00	1171.059
313.15	10050.00	1201.432
313.15	15190.00	1231.544
313.15	20126.00	1259.038
313.15	25019.00	1285.053
313.15	30259.00	1311.678
333.15	100.00	1071.814
333.15	5187.00	1108.004
333.15	10181.00	1141.267
333.15	15331.00	1173.58
333.15	20135.00	1202.01
333.15	25174.00	1230.377
333.15	30144.00	1257.018
353.15	104.00	1004.081
353.15	5055.00	1042.847
353.15	10093.00	1079.408
353.15	15238.00	1114.154
353.15	20157.00	1145.379
353.15	25111.00	1175.116
353.15	30108.00	1203.555
Reference

Correlations

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.65]	kPa	[297.75; 401.38]	The Yaw...
Equation			ln(Pvp) = A + B/(T + C)
Coefficient A			1.44742e+01
Coefficient B			-2.68120e+03
Coefficient C			-1.08758e+02
Temperature range, min.			297.75
Temperature range, max.			401.38
T(K) Vapor pressure (kPa) 0 50 100 150 200 300 350 400
Pvap	1.33	kPa	297.75	Calculated Property
Pvap	3.01	kPa	309.26	Calculated Property
Pvap	6.22	kPa	320.78	Calculated Property
Pvap	11.94	kPa	332.29	Calculated Property
Pvap	21.48	kPa	343.81	Calculated Property
Pvap	36.60	kPa	355.32	Calculated Property
Pvap	59.45	kPa	366.84	Calculated Property
Pvap	92.65	kPa	378.35	Calculated Property
Pvap	139.24	kPa	389.87	Calculated Property
Pvap	202.65	kPa	401.38	Calculated Property
Pvap	[4.46e-10; 4532.42]	kPa	[165.15; 547.73]	KDB Vap...
Equation			ln(Pvp) = A + B/T + C*ln(T) + D*T^2
Coefficient A			2.14566e+02
Coefficient B			-1.41062e+04
Coefficient C			-2.96193e+01
Coefficient D			2.12663e-05
Temperature range, min.			165.15
Temperature range, max.			547.73
T(K) Vapor pressure (kPa) 0 1000 2000 3000 4000 200 300 400 500
Pvap	4.46e-10	kPa	165.15	Calculated Property
Pvap	2.77e-05	kPa	207.66	Calculated Property
Pvap	0.02	kPa	250.17	Calculated Property
Pvap	0.98	kPa	292.68	Calculated Property
Pvap	14.06	kPa	335.19	Calculated Property
Pvap	88.93	kPa	377.69	Calculated Property
Pvap	339.80	kPa	420.20	Calculated Property
Pvap	949.79	kPa	462.71	Calculated Property
Pvap	2193.06	kPa	505.22	Calculated Property
Pvap	4532.42	kPa	547.73	Calculated Property

Similar Compounds

Find more compounds similar to 1-Propanol, 2-methyl-.

Mixtures

• Aniline + 1-Propanol, 2-methyl-
• Isobutyl acetate + 1-Propanol, 2-methyl-
• Formamide, N,N-dimethyl- + 1-Propanol, 2-methyl-
• Isobutyl acetate + Formamide, N,N-dimethyl- + 1-Propanol, 2-methyl-
• Piperazine, 1-methyl- + 1-Propanol, 2-methyl-
• 1-Propanol, 2-methyl- + 1-Hexanol
• Isobutyl acetate + 1-Propanol, 2-methyl- + 1-Hexanol
• Propanoic acid, butyl ester + 1-Propanol, 2-methyl-
• Propanoic acid, butyl ester + Isobutyl acetate + 1-Propanol, 2-methyl-
• Diisopropyl ether + 1-Propanol, 2-methyl-
• Benzene + 1-Propanol, 2-methyl-
• Benzene + Diisopropyl ether + 1-Propanol, 2-methyl-
• Phenol, 2-methyl- + 1-Propanol, 2-methyl-
• p-Cresol + 1-Propanol, 2-methyl-
• 2-Pyrrolidinone, 1-methyl- + 1-Propanol, 2-methyl-
• 1-Propanol, 2-methyl- + 1,4-Dioxane
• 1-Propanol, 2-methyl- + Acetylacetone
• Isobutyl acetate + 1-Propanol, 2-methyl- + Water
• Isobutyl acetate + Glycerin + 1-Propanol, 2-methyl-
• 1-Propanol, 2-methyl- + Ethyl Acetate

Find more mixtures with 1-Propanol, 2-methyl-.

Sources

• KDB Pure (Korean Thermophysical Properties Databank)
• KDB Vapor Pressure Data
• Crippen Method
• 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
• Acoustic and Thermophysical Properties of Binary Liquid Mixtures of Primary Butanols with Hexane and Cyclohexane at 293.15 K
• Solubility of Baicalein in Different Solvents from (287 to 323) K
• Isobaric vapor-liquid equilibria for the binary systems isobutyl alcohol + isobutyl acetate and tert-butyl alcohol + tert-butyl acetate at 20 and 101.3 kPa
• Phase equilibria in the systems isobutyl alcohol +N,N-dimethylformamide, isobutyl acetate +N,N-dimethylformamide and isobutyl alcohol + isobutyl acetate +N,N-dimethylformamide at 101.3 kPa
• 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
• Phase equilibria in the ternary system isobutyl alcohol + isobutyl acetate + 1-hexanol and the binary systems isobutyl alcohol + 1-hexanol, isobutyl acetate + 1-hexanol at 101.3 kPa
• Enhancement of the anthracene aqueous solubility by a synergistic effect of alcohols and beta-cyclodextrin
• Vapor liquid equilibria in the ternary system isobutyl alcohol + isobutyl acetate + butyl propionate and the binary systems isobutyl alcohol + butyl propionate, isobutyl acetate + butyl propionate at 101.3 kPa
• Phase equilibria properties of binary and ternary systems containing di-isopropyl ether + isobutanol + benzene at 313.15K
• Activity coefficients of the binary mixtures of a-cresol or p-cresol with C l-C4 aliphatic alcohols near ambient pressure
• Excess Gibbs energies of selected binary mixtures formed by N,N-dimethyl formamide at 95.5 kPa
• Excess volumes and excess enthalpies of N-methyl-2-pyrrolidone with branched alcohols
• Measurement and correlation of binary vapor liquid equilibria of isomeric butanols with 1,4-dioxane
• Determination and correlation of molar excess enthalpies of binary systems 2,4-pentanedione + (1-butanol, + 2-methyl-1-propanol, + 1-pentanol, + 1-heptane, + ethyl acetate, and + water)
• Liquid liquid equilibria of the systems isobutyl acetate + isobutyl alcohol +water and isobutyl acetate + isobutyl alcohol + glycerol at different temperatures
• Isothermal vapor liquid equilibria for different binary mixtures involved in the alcoholic distillation
• Study of liquid liquid equilibrium of the systems isobutyl acetate + acetic acid +water and isobutyl alcohol + acetic acid +water at different temperatures
• Solubility of antioxidant 1010 in pure alkanols
• Excess molar enthalpies of diethyl malonate+ (1-butanol, 2-methyl-1-propanol, 1-pentanol, n-heptane, and ethyl acetate) at T= (288.2, 298.2, 313.2, 328.2, 338.2, and 348.2 K) and p = 101.3 kPa
• Experimental and predicted excess molar enthalpies of binary mixtures containing 2,2'-oxybis[propane], benzene, butan-1-ol, 2-methylpropan-1-ol, 2-methyl-2-ene-1-propanol at 303.15 K
• Isothermal vapour-liquid equilibria in the binary and ternary systems composed of 2,2,4-trimethylpentane, 2-methyl-1-propanol, and 4-methyl-2-pentanone
• Liquid-liquid equilibria of water + 2,3-butanediol + isobutanol at several temperatures
• Measurement and correlation of liquid liquid equilibrium data for 2-methyl-1-propanol + 2-propanol + water at several temperatures
• Volumetric behavior of carbon dioxide + 2-methyl-1-propanol and carbondioxide + 2-methyl-2-propanol mixtures at 313.15 K
• Liquid-liquid equilibrium data for ternary aqueous mixtures containing 1-pentanol and 2-methyl-1-propanol at (298.15, 323.15, and 348.15) K
• Measurement and correlation of solid-liquid equilibrium for abietic acid + alcohol systems at atmospheric pressure
• Experimental and theoretical study of interaction between organic compounds and 1- (4-sulfobutyl)-3-methylimidazolium based ionic liquids
• Vapour-liquid equilibrium of carboxylic acid alcohol binary systems:2-Propanol + butyric acid, 2-butanol + butyric acid and 2-methyl-1-propanol + butyric acid
• Liquid-liquid equilibrium for the ternary system water + 2-methyl-1-propanol + butyl acetate and water + 2-methyl-2-propanol + butyl acetate at (298.15 and 323.15) K
• Study of interaction between organic compounds and mono or dicationic oxygenated ionic liquids using gas chromatography
• 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
• Determination and correlation of solubility and solution thermodynamics of ethenzamide in different pure solvents
• Evaluation of the solvent structural effect upon the vapor-liquid equilibrium of [C4C1im][Cl] + Alcohols
• 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
• Thermodynamic equilibrium of hydrocortisone form I in different solvent systems
• 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
• 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
• Ammonium ionic liquids in extraction of bio-butan-1-ol from water phase using activity coefficients at infinite dilution
• (Vapour + liquid) equilibrium of binary mixtures (1,3-dioxolane or 1,4-dioxane + 2-methyl-1-propanol or 2-methyl-2-propanol) at isobaric conditions
• Henry's constants and infinite dilution activity coefficients of propane, propene, butane, isobutane, 1-butene, isobutene, trans-2-butene, and 1,3-butadiene in isobutanol and tert-butanol
• Densities and speeds of sound for binary mixtures of (1,3-dioxolane or 1,4-dioxane) with (2-methyl-1-propanol or 2-methyl-2-propanol) at the temperatures 298.15 K and 313.15 K
• 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
• 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
• (Vapor + liquid) equilibria of the binary mixtures of m-cresol with C1 C4 aliphatic alcohols at 95.5 kPa
• Excess Gibbs free energies of the binary mixtures of acetonitrile with butanols at 94.83 kPa
• Measurement of activity coefficients at infinite dilution in 1-hexadecyl-3-methylimidazolium tetrafluoroborate ionic liquid
• Isobaric (vapour + liquid) equilibrium for N-methyl-2-pyrrolidone with branched alcohols
• Volumetric, transport, and acoustic properties of binary mixtures of 2-methyl-1-propanol with hexadecane and squalane at T = (298.15, 303.15, and 308.15) K: Experimental results, correlation, and prediction by the ERAS model
• Complementary vapor pressure data for 2-methyl-1-propanol and 3-methyl-1-butanol at a pressure range of (15 to 177) kPa
• Measurement and modeling of high-pressure (vapour + liquid) equilibria of (CO2 + alcohol) binary systems
• Application of ERAS-model and Prigogine-Flory-Patterson theory to excess molar volumes for ternary mixtures of (2-chlorobutane + butylacetate + isobutanol) at T = 298.15 K
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 4-(2-methoxyethyl)-4-methylmorpholinium bis(trifluoromethylsulfonyl)-amide
• Measurements of activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-hexyl-3-methylimidazolium tetracyanoborate
• Measurement and modeling the excess molar properties of binary mixtures of {[C6mim][BF4] + 3-amino-1-propanol} and {[C6mim][BF4] + isobutanol}: Application of Prigogine-Flory-Patterson theory
• 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
• Determination and correlation of the solubility for diosgenin in alcohols solvents
• 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
• 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
• 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 coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-methoxyethyl)- 1-methylpiperidinium trifluorotris(perfluoroethyl)phosphate
• 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
• 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
• 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
• Activity coefficients at infinite dilution of organic solutes in 1-hexyl-3- methylimidazolium trifluoroacetate and influence of interfacial adsorption using gas liquid chromatography
• Determination and correlation of the solubility of four Bronsted-acidic ionic liquids based on benzothiazolium cations in six alcohols
• Thermodynamics and activity coefficients at infinite dilution for organic solutes, water and diols in the ionic liquid choline bis(trifluoromethylsulfonyl)imide
• Experimental and theoretically study of interaction between organic compounds and tricyanomethanide based ionic liquids
• 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
• 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
• 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 modelling and thermodynamic dissolution functions of phthalimide in ten organic solvents
• Mutual diffusion coefficients of isopropanol + n-heptane and isobutanol + n-heptane
• 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
• 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
• Determination and correlation of solubility and thermodynamic properties of pyraclostrobin in pure and binary solvents
• 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
• 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
• Thermodynamics and limiting activity coefficients measurements for organic solutes and water in the ionic liquid 1-dodecyl-3-methylimidzolium bis(trifluoromethylsulfonyl) imide
• 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
• Volumetric, viscometric, spectral studies and viscosity modelling of binary mixtures of esters and alcohols (diethyl succinate, or ethyl octanoate + isobutanol, or isopentanol) at varying temperatures
• Separation of binary mixtures hexane/hex-1-ene, cyclohexane/cyclohexene and ethylbenzene/styrene based on limiting activity coefficients
• 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
• Thermodynamics and activity coefficients at infinite dilution for organic compounds and water in the ionic liquid 1-butyl-3-methylimidazolium perchlorate
• Measurement and correlation of isobaric vapour-liquid equilibria for binary systems of 1-(methoxymethoxy)-2-methyl-propane with 1-butanol and isobutanol at 101.33 kPa
• Separation of water/butan-1-ol based on activity coefficients at infinite dilution in 1,3-didecyl-2-methylimidazolium dicyanamide ionic liquid
• Separation of binary mixtures hexane/hex-1-ene, cyclohexane/cyclohexene and ethylbenzene/styrene based on gamma infinity data measurements
• 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
• Measurement and thermodynamic modelling of ternary liquid-liquid equilibrium for extraction of (1R,2R)-(-)-1,2-Diaminocyclohexane from aqueous solution with C4-C5 alcohols at different temperatures
• Thermodynamic study of molecular interaction-selectivity in separation processes based on limiting activity coefficients
• Liquid-liquid equilibrium for the system of ionic liquid [BMIm][HSO4] catalysed isobutyl isobutyrate formation
• 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
• Thermodynamics and activity coefficients at infinite dilution for organic compounds in the ionic liquid 1-hexyl-3-methylimidazolium chloride
• Separation of binary mixtures based on gamma infinity data using [OMMIM][BF4] ionic liquid and modelling of thermodynamic functions
• Determination of the thermodynamic parameters of ionic liquid 1-propyl-3-methylimidazolium bromide by gas-liquid chromatography
• Volumetric properties of monoethanolamine and alcohol binary mixtures at different temperatures and 0.1 MPa
• Research on the application of 7-chloro-quinaldine adducts in 7-chloro-quinaldine separation process
• Determination and correlation of solubility and solution thermodynamics of saccharin in different pure solvents
• Solubility and mixing thermodynamic properties of levamisole hydrochloride in twelve pure solvents at various temperatures
• Volumetric properties for binary and ternary systems consist of 1-chlorobutane, n-butylamine and isobutanol at 298.15 K with application of the Prigogine-Flory-Patterson theory and ERAS-Model
• Thermodynamic properties of binary liquid mixtures of diethylenetriamine with alcohols at different temperatures
• Measurement and Correlation for Solubility of Dexibuprofen in Different Solvents from (263.15 to 293.15) K
• Experimental and theoretical excess molar properties of imidazolium based ionic liquids with isomers of butanol
• Density, Speed of Sound, Viscosity, Excess Properties, and Prigogine Flory Patterson (PFP) Theory of Binary Mixtures of Amine and Alcohols
• Proposal for a Viscous Test Mixture Densities, Viscosities, and Vapor Liquid Equilibrium Data of the Binary Mixture 2-Methyl-2-butanol + 2-Methyl-1-propanol
• Isobaric Vapor Liquid Equilibrium for the Binary Systems of sec-Butyl Acetate + Methyl Ethyl Ketone, 2-Methoxyethanol, or 1,2-Dimethoxyethane at 101.3 kPa
• Solubility and Dissolution Thermodynamics for 1,3,5- Trichlorobenzene in Organic Solvents
• 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
• 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 Benzoic Acid and Aspirin in Pure Solvents Using Focused Beam Reflective Measurement
• Solid Liquid Phase Equilibrium of trans-Cinnamic Acid in Several Alcohols: Measurements and Thermodynamic Modeling
• Solubility of 1,3,5-Benzenetricarboxylic Acid in Different Solvents
• Solubility of Ethyl p-Aminobenzoate in Six Alcohols within (283.15 to 327.15) K
• Experimental and Computational Studies of Binary Mixtures of Isobutanol + Cyclohexylamine
• 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 Equilibrium for the Binary Systems of sec-Butyl Acetate + n-Butyl Alcohol, Isobutyl Alcohol, or tert-Butyl Alcohol at 101.3 kPa
• Solubility of 4-Methylsulfonylacetophenone in Nine Pure Solvents and (Ethyl Acetate + n-Hexane) Binary Solvent Mixtures from 278.15 K to 328.15 K
• Solubility Correlation and Thermodynamic Analysis of Sorafenib Free Base and Sorafenib Tosylate in Monosolvents and Binary Solvent Mixtures
• Density, Viscosity, and Refractive Index Data for a Ternary System of Wine Congeners (Ethyl Butyrate + Diethyl Succinate + Isobutanol) in the Temperature Range from 288.15 to 323.15 K and at Atmospheric Pressure
• Determination of Ternary Liquid Liquid Equilibria for Dimethyl Carbonate + 2-Methyl-1-propanol or 2-Methyl-2-propanol + Water Systems at T = 303.15 and 313.15 K
• Proposal of Isobutyl Alcohol as Entrainer To Separate Mixtures Formed by Ethanol and Water and 1-Propanol and Water
• Isobaric Vapor Liquid Equilibrium for the Binary and Ternary System with Isobutyl Alcohol, Isobutyl Acetate and Dimethyl Sulfoxide at 101.3 kPa
• Measurement and Correlation of Solubility of Two Isomers of Cyanopyridine in Eight Pure Solvents from 268.15 K to 318.15 K
• Measurement and Correlation of Isobaric Vapor Liquid Equilibrium for Binary Systems of 1-(Ethoxymethoxy)-2-methyl-propane with Isobutyl Alcohol or 1-Butanol at 101.33 kPa
• Densities and Viscosities for Binary Liquid Mixtures of Biodiesel + 1-Butanol, + Isobutyl Alcohol, or + 2-Butanol from 293.15 to 333.15 K at 0.1 MPa
• Determination and Correlation of Solubility of Quetiapine Fumarate in Nine Pure Solvents and Two Aqueous Binary Solvents
• Thermodynamic Functions for the Solubility of 3-Nitrobenzonitrile in 12 Organic Solvents from T/K = (278.15 to 318.15)
• Densities and Viscosities for Binary Liquid Mixtures of Butan-1-ol + Propane-1,2-diol, + Butane-1,2-diol and 2-Methylpropan-1-ol + Propane-1,2-diol, + Butane-1,2-diol from 298.15 to 333.15 K at 0.1 MPa
• Determination and Correlation of Solubility and Thermodynamic Properties of trans-Cinnamyl Alcohol in Pure and Binary Solvents from 253.15 K to 293.15 K
• Measurement and Correlation of the Solubility of Azoxystrobin in Seven Monosolvents and Two Different Binary Mixed Solvents
• Solubility Modeling and Mixing Properties for Benzoin in Different Monosolvents and Solvent Mixtures at the Temperature Range from 273.15 to 313.15 K
• Determination and Correlation of Dipyridamole p-Toluene Sulfonate Solubility in Seven Alcohol Solvents and Three Binary Solvents
• Determination, Correlation, and Application of Sodium l-Ascorbate Solubility in Nine Pure Solvents and Two Binary Solvents at Temperatures from 278.15 to 323.15 K
• Solubility of 2,5-Furandicarboxylic Acid in Eight Pure Solvents and Two Binary Solvent Systems at 313.15-363.15 K
• Measurement and Correlation of the Solubility of Florfenicol Form A in Several Pure and Binary Solvents
• Excess Properties and Phase Equilibria for the Potential Biofuel System of Propan-2-ol and 2-Methyl-propan-1-ol at 333.15, 343.15, and 353.15 K
• Liquid-Liquid Equilibrium for Ternary Systems, Water + 5-Hydroxymethylfurfural + (1-Butanol, Isobutanol, Methyl Isobutyl Ketone), at 313.15, 323.15, and 333.15 K
• Measurement and Correlation of the Solubility of Pyrimethanil in Seven Monosolvents and Two Different Binary Mixed Solvents
• Solubility of Acetylene in Alcohols and Ketones
• Solubility of 2-Chlorophenylacetic Acid in 12 Pure Solvents from T = (273.15/283.15 to 318.15) K: Determination and Modeling
• Determination of Solubility and Thermodynamic Properties of Benzophenone in Different Pure Solvents
• Isothermal Vapor-Liquid Equilibrium for the 2-Pentanone (MPK) + 2-Methyl Propan-1-ol Binary Mixture
• Thermodynamic Study of Solubility for Imatinib Mesylate in Nine Monosolvents and Two Binary Solvent Mixtures from 278.15 to 318.15 K
• Isothermal Vapor-Liquid Equilibrium Measurements of Butan-2-one + 2-Methyl-propan-1-ol/Pentan-1-ol
• Solubility Determination of Nicotinamide and Its Application for the Cocrystallization with Benzoic Acid
• Measurement and Correlation of Solubility of 3-Hydroxy-2-naphthoic Acid in Ten Pure and Binary Mixed Organic Solvents from T = (293.15 to 333.15 K)
• Solubility Measurement and Correlation of Probenecid in 12 Pure Organic Solvents and Thermodynamic Properties of Mixing of Solutions
• Solubility Modeling and Solvent Effect of 2-Amino-6-chloropurine in Twelve Neat Solvents
• Liquid-Liquid Equilibrium of Isobutyl Acetate + Isobutyl Alcohol + Imidazolium-Based Ionic Liquids at 298.15 and 308.15 K
• Solubility Modeling and Solvent Effect for Flubendazole in 12 Neat Solvents
• Liquid-Liquid Extraction of Biobased Isobutanol from an Aqueous Solution
• Determination and Modeling of Solubility of 4-Aminobenzamide in Different Pure Solvents
• Solid-Liquid Equilibrium of Azacyclotridecan-2-one in 15 Pure Solvents from T = 273.15 to 323.15 K: Experimental Determination and Thermodynamic Modeling
• Solubility and Solution Thermodynamics of 3-Nitrophthalonitrile in 12 Neat Solvents at Temperatures from 278.15 to 323.15 K
• Solubility Determination and Modeling of p-Nitrobenzamide Dissolved in Twelve Neat Solvents from 283.15 to 328.15 K
• Isothermal Vapor-Liquid Equilibrium Measurements for Alcohol + Water/n-Hexane Azeotropic Systems Using Both Dynamic and Automated Static-Synthetic Methods
• Solid-Liquid Equilibrium Measurements for Posaconazole and Voriconazole in Several Solvents between T = 278.2 and 323.2 K Using Differential Thermal Analysis/Thermal Gravimetric Analysis
• Measurement and Correlation of Solubility of Hydrochlorothiazide in Monosolvents and Binary Solvent Mixtures from 283.15 to 323.15 K
• Solubility and Solvent Effect of Acetamiprid in Thirteen Pure Solvents and Aqueous Solutions of Ethanol
• Design of a Salt-Free Aqueous Two-Phase System Containing Butanol, n-Butylpyridine Dicyanamide, and Water: Equilibrium Data and Correlation
• Solubility Measurement and Phase Equilibrium Modeling of 2-Aminobenzamide in 15 Pure Solvents
• Solubility Determination, Modeling, and Thermodynamic Dissolution Properties of Benzenesulfonamide in 16 Neat Solvents from 273.15 to 324.45 K
• Solubility Measurement and Thermodynamic Modeling for o-Toluenesulfonamide in 16 Solvents from T = 273.15 to 323.85 K
• Solubility and Solvent Effect of 1-(2-Bromo-phenyl)-pyrrole-2,5-dione in 14 Pure Solvents from 278.15 to 323.15 K
• Solubility of Acetoguanamine in Twelve Neat Solvents from 283.15 to 323.15 K
• Solubility and Thermodynamic Modeling of Dimethyl Terephthalate in Pure Solvents and the Evaluation of the Mixing Properties of the Solutions
• Determination and Modeling of d-Histidine Solubility in Several Pure Solvents from 293.15 to 333.15 K
• Solubility measurement and thermodynamic model correlation of sancycline in twelve pure solvents
• Solubility and Data Correlation of b-Arbutin in Different Monosolvents from 283.15 to 323.15 K
• Thermodynamic Solubility and Mixing Properties of Phenformin in 14 Pure Solvents at Temperatures Ranging from 278.15 to 323.15 K
• Vapor Liquid Equilibrium between (278.15 and 323.15) K and Excess Functions at T = 298.15 K for 1-Bromobutane with 2-Methyl-1-propanol or 2-Butanol
• Solubility of Anthracene in Binary Alcohol + Acetonitrile Solvent Mixtures at 298.2 K
• High-Pressure Vapor-Liquid Equilibria for CO2 + 2-Butanol, CO2 + iso-Butanol and CO2 + tert-Butanol Systems
• Solubility in Binary Solvent Mixtures: Pyrene Dissolved in Alcohol + Acetonitrile Mixtures at 299.2 K
• Bubble Temperatures of the Binary Mixtures of Dimethylcarbonate with Some Alcohols at 95.8 kPa
• Bubble-Temperature Measurements on Some Binary Mixtures Formed by Tetrahydrofuran or Amyl Alcohol with Hydrocarbons, Chlorohydrocarbons, or Butanols at (94.6 or 95.8) kPa
• Vapor-Liquid Equilibria in Alcohol + Cyclohexane + Water Systems
• Viscosities of Binary Mixtures of Isomeric Butanols or Isomeric Chlorobutanes with 2-Methyltetrahydrofuran
• Solubility in Binary Solvent Mixtures: Anthracene Dissolved in Alcohol + 2-Methyl-1-butanol Mixtures at 298.2 K
• Solubility in Binary Solvent Mixtures: Anthracene Dissolved in Alcohol + Carbon Tetrachloride Mixtures at 298.2 K
• Density, Refractive Index, and Speed of Sound at 298.15 K and Vapor-Liquid Equilibria at 101.3 kPa for Binary Mixtures of Ethyl Acetate + 1-Pentanol and Ethanol + 2-Methyl-1-propanol
• Densities and Viscosities of Binary Mixtures of 1-Chlorobutane with Butanol Isomers at Several Temperatures
• Excess Molar Volumes and Surface Tensions of 1,2,4-Trimethylbenzene and 1,3,5-Trimethylbenzene with 1-Butanol, 2-Methyl-1-propanol, 2-Butanol, and 2-Methyl-2-propanol at 298.15 K
• Densities and Viscosities of Binary Mixtures of 1-Bromobutane with Butanol Isomers at Several Temperatures
• Solubility of Potassium Clavulanate in Ethanol, 1-Propanol, 1-Butanol, 2-Propanol, and 2-Methyl-1-propanol between 273 K and 305 K
• Excess Molar Enthalpies of Methyl Acetate and (1-Propanol, 2-Propanol, 1-Butanol, 2-Butanol, and 1-Pentanol) at T = (298.15 and 308.15) K and P = (5.0 and 10.0) MPa
• Thermodynamic Properties of Mixtures Containing Ionic Liquids. 8. Activity Coefficients at Infinite Dilution of Hydrocarbons, Alcohols, Esters, and Aldehydes in 1-Hexyl-3-methylimidazolium Bis(trifluoromethylsulfonyl) Imide Using Gas-Liquid Chromatography
• Vapor-Liquid Equilibrium of Binary Mixtures Containing Ethyl Acetate + 2-Methyl-1-propanol and Ethyl Acetate + 2-Methyl-1-butanol at 101.3 kPa
• Thermodynamic Properties of Mixtures Containing Ionic Liquids. 9. Activity Coefficients at Infinite Dilution of Hydrocarbons, Alcohols, Esters, and Aldehydes in Trimethyl-butylammonium Bis(trifluoromethylsulfonyl) Imide Using Gas-Liquid Chromatography and Static Method
• Vapor-Liquid Equilibria for the n-Pentane + 1-Propanol and n-Pentane + 2-Methyl-1-propanol Systems near the Critical Region
• Thermodynamic Properties of Mixtures Containing Ionic Liquids: Activity Coefficients at Infinite Dilution of Organic Compounds in 1-Propyl Boronic Acid-3-Alkylimidazolium Bromide and 1-Propenyl-3-alkylimidazolium Bromide Using Inverse Gas Chromatography
• Vapor-Liquid Equilibria at 101.3 kPa for Binary Mixtures Containing 2-Methyl-1-propanol + 2-Methyl-1-butanol, 2-Methyl-1-propanol + 3-Methyl-1-butanol, and 2-Methyl-1-propanol + 1-Pentanol
• Experimental Study of Thermodynamic Properties of Mixtures Containing Ionic Liquid 1-Ethyl-3-methylimidazolium Ethyl Sulfate Using Gas-Liquid Chromatography and Transpiration Method
• Activity Coefficients at Infinite Dilution of Polar Solutes in 1-Butyl-3-methylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
• Thermophysical Properties of Binary Mixtures of 2-Methyl-1-propanol with Hexane, Octane, and Decane at 298.15 K
• Excess Molar Volumes of 1,3-Diethyl Propanedioate with Methanol, Ethanol, Propan-1-ol, Propan-2-ol, Butan-2-ol, 2-Methyl-propan-1-ol, and Pentan-1-ol at T = (288.15, 298.15, 313.15, and 328.15) K
• Surface Tensions of the Ternary Mixtures Containing an Isomeric Butanol + n-Hexane + 1-Chlorobutane at 298.15 K
• Solubilities of Ibuprofen in Different Pure Solvents
• Measurement and Study on the Liquid Liquid Equilibrium of Ionic Liquids with Aliphatic Alcohols
• Densities, Viscosities, and Speeds of Sound of Binary Liquid Mixtures of Ethylenediamine with Alcohols at T = (293.15 to 313.15) K
• Activity Coefficients at Infinite Dilution of Organic Compounds in Four New Imidazolium-Based Ionic Liquids
• Partition Coefficients of Organic Compounds in Four New Tetraalkylammonium Bis(trifluoromethylsulfonyl)imide Ionic Liquids Using Inverse Gas Chromatography
• Volumetric Properties of Highly Nonideal Binary Mixtures Containing Ethanoic Acid and Propanoic Acid with Butan-2-ol, Methyl-2-propanol, and 2-Methyl-2-butanol at Different Temperatures
• Evaluation of the Performance of Trigeminal Tricationic Ionic Liquids for Separation Problems
• Liquid Liquid Equilibrium for the Ternary System 2-Methyl-1-propanol + 3-Methyl-1-butanol + Water at (298.15, 323.15, and 348.15) K
• Activity Coefficients at Infinite Dilution for Organic Compounds Dissolved in 1-Alkyl-1-methylpyrrolidinium Bis(trifluoromethylsulfonyl)imide Ionic Liquids Having Six-, Eight-, and Ten-Carbon Alkyl Chains
• Solubility of N-Chloro-4-toluenesulfonamide Sodium and N-Chlorobenzenesulfonamide Sodium in Ethanol, Water, 1-Propanol, and Butan-2-ol
• Isobaric Vapor Liquid Equilibrium Data for Binary Mixtures of 1-Phenylethanone with a Few Alcohols at 95.2 kPa
• Determination and Correlation of Solubility of Tris(3-hydroxypropyl)phosphine Oxide in Selected Solvents
• Density and Viscosity Measurements of Binary Alkanol Mixtures from (293.15 to 333.15) K at Atmospheric Pressure
• Solubility of Veratric Acid in Eight Monosolvents and Ethanol + 1-Butanol at Various Temperatures
• Activity Coefficients at Infinite Dilution for Organic Solutes Dissolved in Three 1-Alkyl-1-methylpyrrolidinium Bis(trifluoromethylsulfonyl)imide Ionic Liquids Bearing Short Linear Alkyl Side Chains of Three to Five Carbons
• Densities and Viscosities of Binary Mixtures of 2-Butanol + Isobutanol, 2-Butanol + tert-Butanol, and Isobutanol + tert-Butanol from (308.15 to 343.15) K
• Vapor Liquid Equilibrium of Mixtures Containing the Following Higher Alcohols: 2-Propanol, 2-Methyl-1-propanol, and 3-Methyl-1-butanol
• Infinite Dilution Activity Coefficients of Solutes Dissolved in Two Trihexyl(tetradecyl)phosphonium Ionic Liquids
• Determination and Correlation of Solubilities of Lauric Acid in Eight Alcohols
• Vapor Liquid Equilibrium Data for Binary Systems of n-Dodecane + {Propan-1-ol, Butan-1-ol, 2-Methylpropan-1-ol} at 40 kPa
• Volumetric and Viscometric Study of Binary Systems of Ethyl Butyrate with Alcohols
• Ternary Liquid Liquid Equilibrium Data for the Water + Acetonitrile + {Butan-1-ol or 2-Methylpropan-1-ol} Systems at (303.2, 323.2, 343.2) K and 1 atm
• Thermodynamic Properties of Polymorphs of 2,2'-Thiodiethylene Bis[3-(3,5-di-tert-butyl-4-hydroxyphenyl)propionate]
• P ? T Data for 1-Butanol and Isobutyl Alcohol from (283.15 to 363.15) K at Pressures up to 66 MPa
• Determination and Modeling of the Solubility of 2,4-Dimethoxybenzoic Acid in Six Pure and Isopropanol + Ethyl Acetate Mixed Organic Solvents at Temperatures From (288.15 to 323.15) K
• Solubility of Anthracene in Binary Diisopropyl Ether + Alcohol Solvent Mixtures at 298.15 K
• Temperature Dependence of Limiting Activity Coefficients, Henry s Law Constants, and Related Infinite Dilution Properties of Branched (C3 and C4) Alkanols in Water. Measurement, Critical Compilation, Correlation, and Recommended Data
• Vapor-Liquid Equilibrium Behaviors of Vanillin in 1-Butanol, 2-Butanol, and 2-Methyl-1-propanol
• Excess Enthalpy, Density, and Speed of Sound for the Mixtures a-Pinene + 2-Methyl-1-propanol or 2-Methyl-2-propanol at Several Temperatures
• Solubility of Anthracene in Binary Propyl Acetate + Alcohol Solvent Mixtures at 298.15 K
• Liquid Liquid Equilibria of the Ternary Systems 3-Methyl-1-butanol + Ethanol + Water and 2-Methyl-1-propanol + Ethanol + Water at 293.15 K
• Activity Coefficients at Infinite Dilution of Polar Solutes in 1-Butyl-3-methylimidazolium Trifluoromethanesulfonate Using Gas Liquid Chromatography
• Activity Coefficients at Infinite Dilution of Polar Solutes in 1-Propyl-2,3-dimethylimidazolium Tetrafluoroborate Using Gas Liquid Chromatography
• Vapor Liquid Equilibrium Behaviors of 5-Methyl-2-(1-methylethyl)phenol in Alcohol
• Densities and Viscosities of the Ternary Mixtures 2-Methyl-1-propanol (or 2-Methyl-2-propanol) + N-Hexane + 1-Chlorobutane at 298.15 K
• Isobaric Vapor-Liquid Equilibria for Tetrahydropyran and Alcohol Systems
• Determination and Correlation of Excess Molar Enthalpies of Eight Binary Systems Containing Acetophenone at Different Temperatures
• Measurement of Infinite Dilution Activity Coefficients of Alcohols, Ketones, and Aromatic Hydrocarbons in 4-Methyl-N-butylpyridinium Tetrafluoroborate and 1-Butyl-3-methylimidazolium Hexafluorophosphate by Gas-Liquid Chromatography
• Activity Coefficients at Infinite Dilution of Alkanols in the Ionic Liquids 1-Butyl-3-methylimidazolium Hexafluorophosphate, 1-Butyl-3-methylimidazolium Methyl Sulfate, and 1-Hexyl-3-methylimidazolium Bis(trifluoromethylsulfonyl) Amide Using the Dilutor Technique
• Solubility of Diphenyl Carbonate in Pure Alcohols from (283 to 333) K
• Densities and Viscosities of Binary Liquid Mixtures of 2-Butanone with Branched Alcohols at (293.15 to 313.15) K
• Activity Coefficients at Infinite Dilution of Organic Compounds in 1-Butyl-3-methylimidazolium Tetrafluoroborate Using Inverse Gas Chromatography
• Solubility of Salol in Pure Alcohols from (283.15 to 308.15) K
• Solubility of Fluorene in Benzene, Chloroform, Acetone, 1-Propanol, Isobutanol, and Methylbenzene from (283 to 323) K
• Solubility of Acenaphthene in Different Solvents from (283.00 to 323.00) K
• Solubility of Indinavir Sulfate in Different Solvents from (278.35 to 314.15) K
• Activity Coefficients at Infinite Dilution of Organic Compounds in Trihexyl(tetradecyl)phosphonium Bis(trifluoromethylsulfonyl)imide Using Inverse Gas Chromatography
• High-Pressure Vapor-Liquid Equilibrium for Ethylene + 2-Methyl-1-propanol
• Densities, Viscosities, and Excess Molar Enthalpies of 2-Pyrrolidone + Butanol Isomers at T ) (293.15, 298.15, and 303.15) K
• Partition Coefficients of Organic Compounds in New Imidazolium and Tetralkylammonium Based Ionic Liquids Using Inverse Gas Chromatography
• Isothermal Vapor-Liquid Equilibrium of Ternary Mixtures Containing 2-Methyl-1-propanol or 2-Methyl-2-propanol, n-Hexane, and 1-Chlorobutane at 298.15 K
• Activity Coefficients at Infinite Dilution of Polar Solutes in 1-(2-Hydroxyethyl)-3-methylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
• Densities and Viscosities of Binary Mixtures of n-Butanol with 2-Butanol, Isobutanol, and tert-Butanol from (303.15 to 343.15) K
• Solubilities of (?,Z)-2-Amino-?-(methoxyimino)-4-thiazole-ethanethioic Acid S-2-Benzothiazolyl Ester in Pure Solvents and a Mixture of Acetonitrile and Dichloromethane
• Study of Ether-, Alcohol-, or Cyano-Functionalized Ionic Liquids Using Inverse Gas Chromatography
• Joback Method
• KDB
• Aqueous Solubility Prediction Method
• Estimated Solubility Method
• McGowan Method
• NIST Webbook
• The Yaws Handbook of Vapor Pressure

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