Chemical Properties of 1-Octanol (CAS 111-87-5)

InChI

InChI=1S/C8H18O/c1-2-3-4-5-6-7-8-9/h9H,2-8H2,1H3

InChI Key

KBPLFHHGFOOTCA-UHFFFAOYSA-N

Formula

C8H18O

SMILES

CCCCCCCCO

Molecular Weight¹

130.23

CAS

111-87-5

Other Names

• 1-Hydroxyoctane
• 1-Octyl alcohol
• Alcohol C-8
• Alfol 8
• Caprylic alcohol
• Dytol M-83
• Emery 3322
• Emery 3324
• Epal 8
• HEPTYL CARBINOL
• Lorol 20
• Lorol C 8-98
• N-OCTYL ALCOHOL
• NSC 9823
• OCTYL ALCOHOL
• Octan-1-ol
• Octanol
• Octanol-(1)
• Octilin
• Octyl alcohol, normal-primary
• Prim-n-octyl alcohol
• Primary octyl alcohol
• Sipol L8
• capryl alcohol
• n-Heptyl carbinol
• n-Octan-1-ol
• n-Octanol

• ω : Acentric Factor.
• PAff : Proton affinity (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).
• Δ_fG° : Standard Gibbs free energy of formation (kJ/mol).
• 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_subH° : Enthalpy of sublimation at standard conditions (kJ/mol).
• Δ_vapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
• Δ_vapH : Enthalpy of vaporization at a given temperature (kJ/mol).
• 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.
• c_sound,fluid : Speed of sound in fluid (m/s).
• γ : Surface Tension (N/m).
• T_boil : Normal Boiling Point Temperature (K).
• T_boilr : Boiling point at reduced pressure (K).
• T_c : Critical Temperature (K).
• λ : Liquid thermal conductivity (W/m×K).
• T_fus : Normal melting (fusion) point (K).
• V_c : Critical Volume (m³/kmol).
• Z_c : Critical Compressibility.
• 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	0.5870		KDB
PAff	799.00	kJ/mol	NIST
ΔcH°liquid	[-5295.50; -5285.60]	kJ/mol
ΔcH°liquid	-5294.00 ± 0.60	kJ/mol	NIST
ΔcH°liquid	-5295.50 ± 1.00	kJ/mol	NIST
ΔcH°liquid	-5285.70 ± 2.70	kJ/mol	NIST
ΔcH°liquid	-5285.60	kJ/mol	NIST
μ	2.00	debye	KDB
η	[0.0071430; 0.0075080]	Pa×s
η	0.0075080	Pa×s	Study o...
η	0.0071430	Pa×s	Volumet...
ΔfG°	-120.20	kJ/mol	KDB
ΔfH°gas	-360.10	kJ/mol	KDB
ΔfH°liquid	[-435.00; -425.20]	kJ/mol
ΔfH°liquid	-426.60 ± 0.60	kJ/mol	NIST
ΔfH°liquid	-428.00 ± 1.10	kJ/mol	NIST
ΔfH°liquid	-425.20 ± 1.10	kJ/mol	NIST
ΔfH°liquid	-435.00 ± 2.70	kJ/mol	NIST
ΔfusH°	[23.70; 25.14]	kJ/mol
ΔfusH°	25.14	kJ/mol	Heat Ca...
ΔfusH°	23.70	kJ/mol	Measure...
ΔsubH°	100.40	kJ/mol	NIST
ΔvapH°	50.08	kJ/mol	Joback Calculated Property
log10WS	[-2.39; -2.39]
log10WS	-2.39		Aq. Sol...
log10WS	-2.39		Estimat...
logPoct/wat	2.339		Crippen Calculated Property
McVol	129.450	ml/mol	McGowan Calculated Property
NFPA Fire	2		KDB
NFPA Health	1		KDB
Pc	[1777.00; 2860.00]	kPa
Pc	2777.00	kPa	KDB
Pc	2780.00 ± 30.00	kPa	NIST
Pc	2850.00 ± 50.00	kPa	NIST
Pc	Outlier 1777.00 ± 20.00	kPa	NIST
Pc	2777.00 ± 20.00	kPa	NIST
Pc	2860.00	kPa	NIST
Pc	2860.00	kPa	NIST
ρc	[256.55; 265.66]	kg/m3
ρc	261.76 ± 3.91	kg/m3	NIST
ρc	265.66	kg/m3	NIST
ρc	256.55 ± 6.51	kg/m3	NIST
ρc	265.66 ± 2.60	kg/m3	NIST
Inp	[175.63; 1095.00]
Inp	1051.43		NIST
Inp	1051.79		NIST
Inp	1052.54		NIST
Inp	1052.35		NIST
Inp	1060.90		NIST
Inp	1060.50		NIST
Inp	1059.90		NIST
Inp	1059.70		NIST
Inp	1060.90		NIST
Inp	1060.50		NIST
Inp	1059.90		NIST
Inp	1059.70		NIST
Inp	1052.99		NIST
Inp	1055.41		NIST
Inp	1053.90		NIST
Inp	1034.80		NIST
Inp	1042.30		NIST
Inp	1051.70		NIST
Inp	1082.00		NIST
Inp	1051.00		NIST
Inp	1052.00		NIST
Inp	1053.00		NIST
Inp	1053.00		NIST
Inp	1053.00		NIST
Inp	1054.00		NIST
Inp	1054.00		NIST
Inp	1054.00		NIST
Inp	1055.00		NIST
Inp	1057.00		NIST
Inp	1060.00		NIST
Inp	1061.00		NIST
Inp	1066.00		NIST
Inp	1049.00		NIST
Inp	1050.00		NIST
Inp	1049.00		NIST
Inp	1042.00		NIST
Inp	1057.00		NIST
Inp	1060.00		NIST
Inp	1058.00		NIST
Inp	1044.00		NIST
Inp	1064.00		NIST
Inp	1058.00		NIST
Inp	1060.00		NIST
Inp	1042.00		NIST
Inp	1061.00		NIST
Inp	1057.00		NIST
Inp	1073.00		NIST
Inp	1059.00		NIST
Inp	1059.00		NIST
Inp	1068.00		NIST
Inp	1071.00		NIST
Inp	1062.00		NIST
Inp	1053.00		NIST
Inp	1060.00		NIST
Inp	1078.00		NIST
Inp	1078.00		NIST
Inp	1060.00		NIST
Inp	1053.00		NIST
Inp	1060.00		NIST
Inp	1059.00		NIST
Inp	1061.00		NIST
Inp	1063.00		NIST
Inp	1061.00		NIST
Inp	1062.00		NIST
Inp	1067.00		NIST
Inp	1070.00		NIST
Inp	1061.00		NIST
Inp	1063.00		NIST
Inp	1055.00		NIST
Inp	1060.00		NIST
Inp	1065.00		NIST
Inp	1061.00		NIST
Inp	1059.00		NIST
Inp	1061.00		NIST
Inp	1070.00		NIST
Inp	1061.00		NIST
Inp	1093.00		NIST
Inp	1093.00		NIST
Inp	1071.00		NIST
Inp	1074.00		NIST
Inp	1064.00		NIST
Inp	1082.00		NIST
Inp	1054.00		NIST
Inp	1070.00		NIST
Inp	1076.00		NIST
Inp	1069.00		NIST
Inp	1079.00		NIST
Inp	1074.00		NIST
Inp	1070.00		NIST
Inp	1068.00		NIST
Inp	1052.00		NIST
Inp	1073.00		NIST
Inp	1065.00		NIST
Inp	1076.00		NIST
Inp	1070.60		NIST
Inp	1072.00		NIST
Inp	1068.00		NIST
Inp	1074.00		NIST
Inp	1084.00		NIST
Inp	1050.00		NIST
Inp	1068.00		NIST
Inp	1065.00		NIST
Inp	1070.00		NIST
Inp	1064.00		NIST
Inp	1063.00		NIST
Inp	1066.90		NIST
Inp	1066.90		NIST
Inp	1066.50		NIST
Inp	1075.00		NIST
Inp	1070.00		NIST
Inp	1070.00		NIST
Inp	1071.00		NIST
Inp	1068.00		NIST
Inp	1072.00		NIST
Inp	1057.00		NIST
Inp	1074.00		NIST
Inp	1073.00		NIST
Inp	1054.00		NIST
Inp	1068.00		NIST
Inp	1053.20		NIST
Inp	1080.00		NIST
Inp	1071.00		NIST
Inp	1068.70		NIST
Inp	1051.00		NIST
Inp	1064.00		NIST
Inp	1073.00		NIST
Inp	1070.00		NIST
Inp	1072.00		NIST
Inp	1070.00		NIST
Inp	1054.00		NIST
Inp	1054.00		NIST
Inp	1069.00		NIST
Inp	1070.00		NIST
Inp	1065.00		NIST
Inp	1065.00		NIST
Inp	1064.00		NIST
Inp	1065.00		NIST
Inp	1067.00		NIST
Inp	1056.00		NIST
Inp	1055.40		NIST
Inp	1067.00		NIST
Inp	1054.00		NIST
Inp	1052.00		NIST
Inp	1080.00		NIST
Inp	1068.00		NIST
Inp	1061.00		NIST
Inp	1070.00		NIST
Inp	1072.00		NIST
Inp	1061.70		NIST
Inp	1061.70		NIST
Inp	1069.00		NIST
Inp	1069.00		NIST
Inp	1071.00		NIST
Inp	1071.00		NIST
Inp	1071.00		NIST
Inp	1060.00		NIST
Inp	1051.00		NIST
Inp	1069.00		NIST
Inp	1083.00		NIST
Inp	1081.00		NIST
Inp	1054.00		NIST
Inp	1072.00		NIST
Inp	1072.00		NIST
Inp	1071.00		NIST
Inp	1052.00		NIST
Inp	1053.00		NIST
Inp	1052.00		NIST
Inp	1068.00		NIST
Inp	1069.00		NIST
Inp	1071.00		NIST
Inp	1071.00		NIST
Inp	1071.00		NIST
Inp	1072.00		NIST
Inp	1072.00		NIST
Inp	1072.00		NIST
Inp	1072.00		NIST
Inp	1072.00		NIST
Inp	1074.00		NIST
Inp	1076.00		NIST
Inp	1058.00		NIST
Inp	1060.00		NIST
Inp	1057.00		NIST
Inp	1084.00		NIST
Inp	1070.00		NIST
Inp	1080.10		NIST
Inp	1068.00		NIST
Inp	1068.00		NIST
Inp	1080.00		NIST
Inp	1068.00		NIST
Inp	1072.00		NIST
Inp	1051.00		NIST
Inp	1070.00		NIST
Inp	1070.00		NIST
Inp	1074.00		NIST
Inp	1074.00		NIST
Inp	1052.00		NIST
Inp	1058.00		NIST
Inp	1081.00		NIST
Inp	1070.00		NIST
Inp	1059.00		NIST
Inp	1052.00		NIST
Inp	1054.00		NIST
Inp	1054.00		NIST
Inp	1052.00		NIST
Inp	1051.00		NIST
Inp	1051.00		NIST
Inp	1053.00		NIST
Inp	1071.00		NIST
Inp	1055.00		NIST
Inp	1057.00		NIST
Inp	1071.00		NIST
Inp	1072.00		NIST
Inp	1078.00		NIST
Inp	1095.00		NIST
Inp	1069.00		NIST
Inp	1063.00		NIST
Inp	1068.00		NIST
Inp	1071.00		NIST
Inp	1073.00		NIST
Inp	1076.00		NIST
Inp	1076.00		NIST
Inp	1055.00		NIST
Inp	1074.00		NIST
Inp	1072.00		NIST
Inp	1061.00		NIST
Inp	1069.00		NIST
Inp	1069.00		NIST
Inp	1070.00		NIST
Inp	1067.00		NIST
Inp	1082.00		NIST
Inp	1071.00		NIST
Inp	1068.00		NIST
Inp	1052.00		NIST
Inp	1091.00		NIST
Inp	1069.00		NIST
Inp	1046.00		NIST
Inp	1076.00		NIST
Inp	1074.00		NIST
Inp	1077.00		NIST
Inp	1076.00		NIST
Inp	1069.00		NIST
Inp	1057.00		NIST
Inp	1053.00		NIST
Inp	1070.00		NIST
Inp	1070.00		NIST
Inp	1054.00		NIST
Inp	1075.00		NIST
Inp	1048.00		NIST
Inp	1073.00		NIST
Inp	1070.00		NIST
Inp	1069.00		NIST
Inp	1069.00		NIST
Inp	1060.00		NIST
Inp	1068.00		NIST
Inp	1070.00		NIST
Inp	1051.00		NIST
Inp	1069.00		NIST
Inp	1068.00		NIST
Inp	1089.00		NIST
Inp	1039.00		NIST
Inp	1065.00		NIST
Inp	1065.00		NIST
Inp	1061.00		NIST
Inp	1048.00		NIST
Inp	1066.00		NIST
Inp	1069.00		NIST
Inp	1070.00		NIST
Inp	1076.00		NIST
Inp	1069.00		NIST
Inp	1059.00		NIST
Inp	1075.00		NIST
Inp	1039.00		NIST
Inp	1052.00		NIST
Inp	1054.00		NIST
Inp	1066.00		NIST
Inp	1077.00		NIST
Inp	1091.00		NIST
Inp	1070.00		NIST
Inp	1070.00		NIST
Inp	1067.00		NIST
Inp	1067.00		NIST
Inp	1070.00		NIST
Inp	1061.00		NIST
Inp	1052.00		NIST
Inp	1070.00		NIST
Inp	1069.00		NIST
Inp	1072.00		NIST
Inp	1048.00		NIST
Inp	1073.00		NIST
Inp	1052.00		NIST
Inp	1052.00		NIST
Inp	1050.00		NIST
Inp	1076.00		NIST
Inp	1053.00		NIST
Inp	1053.00		NIST
Inp	1056.80		NIST
Inp	1056.00		NIST
Inp	1074.00		NIST
Inp	1072.00		NIST
Inp	1072.00		NIST
Inp	1084.00		NIST
Inp	1073.00		NIST
Inp	1069.00		NIST
Inp	1053.00		NIST
Inp	1068.00		NIST
Inp	1075.00		NIST
Inp	1074.00		NIST
Inp	1048.00		NIST
Inp	1050.00		NIST
Inp	1074.00		NIST
Inp	1074.00		NIST
Inp	1068.00		NIST
Inp	1059.00		NIST
Inp	1061.00		NIST
Inp	1068.34		NIST
Inp	1095.00		NIST
Inp	1072.00		NIST
Inp	1072.00		NIST
Inp	1052.00		NIST
Inp	1053.00		NIST
Inp	1060.00		NIST
Inp	1079.00		NIST
Inp	1073.00		NIST
Inp	1051.00		NIST
Inp	1061.00		NIST
Inp	1054.00		NIST
Inp	1054.00		NIST
Inp	1054.00		NIST
Inp	1054.00		NIST
Inp	1053.00		NIST
Inp	1054.00		NIST
Inp	1069.00		NIST
Inp	1075.00		NIST
Inp	1058.00		NIST
Inp	1057.00		NIST
Inp	1056.00		NIST
Inp	1052.00		NIST
Inp	1057.00		NIST
Inp	1061.00		NIST
Inp	1083.00		NIST
Inp	1057.00		NIST
Inp	1061.00		NIST
Inp	1052.00		NIST
Inp	1063.00		NIST
Inp	1074.00		NIST
Inp	1077.00		NIST
Inp	1080.00		NIST
Inp	1060.00		NIST
Inp	1069.00		NIST
Inp	1060.00		NIST
Inp	1068.00		NIST
Inp	1056.00		NIST
Inp	1070.00		NIST
Inp	1065.00		NIST
Inp	1066.00		NIST
Inp	1082.00		NIST
Inp	1080.00		NIST
Inp	1076.00		NIST
Inp	1068.00		NIST
Inp	1074.00		NIST
Inp	1074.00		NIST
Inp	1071.00		NIST
Inp	1074.00		NIST
Inp	1072.00		NIST
Inp	1075.00		NIST
Inp	1049.00		NIST
Inp	1072.00		NIST
Inp	1064.00		NIST
Inp	1044.00		NIST
Inp	1070.00		NIST
Inp	1052.00		NIST
Inp	1071.00		NIST
Inp	1073.00		NIST
Inp	1045.00		NIST
Inp	1069.00		NIST
Inp	1067.00		NIST
Inp	1073.00		NIST
Inp	1064.00		NIST
Inp	1072.00		NIST
Inp	1072.00		NIST
Inp	1038.00		NIST
Inp	1070.00		NIST
Inp	1063.00		NIST
Inp	1069.00		NIST
Inp	1070.00		NIST
Inp	1064.00		NIST
Inp	1072.00		NIST
Inp	1070.00		NIST
Inp	1055.00		NIST
Inp	1064.00		NIST
Inp	1071.00		NIST
Inp	1071.00		NIST
Inp	1070.00		NIST
Inp	1066.00		NIST
Inp	1061.00		NIST
Inp	1071.00		NIST
Inp	1075.00		NIST
Inp	1084.00		NIST
Inp	1057.00		NIST
Inp	1061.00		NIST
Inp	1069.70		NIST
Inp	1075.00		NIST
Inp	1077.00		NIST
Inp	1087.00		NIST
Inp	1065.00		NIST
Inp	1080.00		NIST
Inp	1053.00		NIST
Inp	1079.00		NIST
Inp	1052.00		NIST
Inp	1056.00		NIST
Inp	1056.00		NIST
Inp	1056.00		NIST
Inp	1084.00		NIST
Inp	1053.00		NIST
Inp	1053.00		NIST
Inp	1061.00		NIST
Inp	1061.00		NIST
Inp	1056.00		NIST
Inp	1050.00		NIST
Inp	1058.00		NIST
Inp	1059.00		NIST
Inp	1083.00		NIST
Inp	Outlier 175.63		NIST
Inp	Outlier 177.62		NIST
Inp	Outlier 176.31		NIST
Inp	1061.00		NIST
Inp	1080.00		NIST
Inp	1056.00		NIST
Inp	1071.00		NIST
Inp	1072.00		NIST
Inp	1073.00		NIST
Inp	1070.00		NIST
Inp	1075.00		NIST
Inp	1053.00		NIST
Inp	1083.00		NIST
Inp	1052.00		NIST
Inp	1051.00		NIST
Inp	1069.00		NIST
Inp	1076.00		NIST
Inp	1082.00		NIST
Inp	1039.00		NIST
Inp	1066.00		NIST
Inp	1059.00		NIST
Inp	1067.00		NIST
Inp	1068.00		NIST
Inp	1074.00		NIST
Inp	1068.34		NIST
Inp	1057.00		NIST
Inp	1084.00		NIST
Inp	1081.00		NIST
I	[1507.00; 1605.00]
I	1559.00		NIST
I	Outlier 1517.00		NIST
I	1554.00		NIST
I	1528.00		NIST
I	1551.00		NIST
I	1528.00		NIST
I	1557.00		NIST
I	1555.00		NIST
I	1550.00		NIST
I	1556.00		NIST
I	1556.00		NIST
I	1555.68		NIST
I	1554.38		NIST
I	1553.35		NIST
I	1556.05		NIST
I	1537.00		NIST
I	1530.00		NIST
I	1560.00		NIST
I	1547.00		NIST
I	1523.00		NIST
I	1540.00		NIST
I	Outlier 1518.00		NIST
I	1522.00		NIST
I	1555.00		NIST
I	1552.00		NIST
I	1526.00		NIST
I	1547.00		NIST
I	Outlier 1519.00		NIST
I	1546.00		NIST
I	1547.00		NIST
I	1561.00		NIST
I	1564.00		NIST
I	1564.00		NIST
I	1523.00		NIST
I	1565.00		NIST
I	1522.00		NIST
I	Outlier 1519.00		NIST
I	1530.00		NIST
I	1530.00		NIST
I	1530.00		NIST
I	Outlier 1519.00		NIST
I	1521.00		NIST
I	1567.00		NIST
I	1562.00		NIST
I	1567.00		NIST
I	1546.00		NIST
I	1560.00		NIST
I	1569.00		NIST
I	1573.00		NIST
I	1556.00		NIST
I	1557.00		NIST
I	1561.00		NIST
I	1561.00		NIST
I	1566.00		NIST
I	1546.00		NIST
I	1558.00		NIST
I	1563.00		NIST
I	1552.00		NIST
I	1540.00		NIST
I	1537.00		NIST
I	1520.00		NIST
I	1566.00		NIST
I	1553.00		NIST
I	1550.00		NIST
I	1565.00		NIST
I	1559.00		NIST
I	1553.00		NIST
I	Outlier 1507.00		NIST
I	1538.00		NIST
I	1555.00		NIST
I	1559.00		NIST
I	1566.00		NIST
I	1545.00		NIST
I	1534.00		NIST
I	1569.00		NIST
I	1566.00		NIST
I	1565.00		NIST
I	1544.00		NIST
I	1566.00		NIST
I	1558.00		NIST
I	1557.00		NIST
I	1546.00		NIST
I	1546.00		NIST
I	1559.00		NIST
I	1584.00		NIST
I	1544.00		NIST
I	1559.00		NIST
I	1558.00		NIST
I	1551.00		NIST
I	1544.00		NIST
I	1538.00		NIST
I	Outlier 1589.00		NIST
I	1555.00		NIST
I	1562.00		NIST
I	1540.00		NIST
I	1558.00		NIST
I	1566.00		NIST
I	1578.00		NIST
I	1546.00		NIST
I	1559.00		NIST
I	1549.00		NIST
I	1560.00		NIST
I	1551.00		NIST
I	1520.00		NIST
I	1537.00		NIST
I	1555.00		NIST
I	1579.00		NIST
I	1579.00		NIST
I	1579.00		NIST
I	1562.00		NIST
I	1573.00		NIST
I	1562.00		NIST
I	1541.00		NIST
I	1554.00		NIST
I	1554.00		NIST
I	1565.00		NIST
I	1565.00		NIST
I	1530.00		NIST
I	1567.00		NIST
I	1550.00		NIST
I	1538.00		NIST
I	1550.00		NIST
I	1550.00		NIST
I	1550.00		NIST
I	1562.00		NIST
I	1562.00		NIST
I	1560.00		NIST
I	1564.00		NIST
I	1563.00		NIST
I	1565.00		NIST
I	1544.00		NIST
I	1526.00		NIST
I	1533.00		NIST
I	1565.00		NIST
I	1561.00		NIST
I	1566.00		NIST
I	1552.00		NIST
I	1565.00		NIST
I	1566.00		NIST
I	1563.00		NIST
I	1540.00		NIST
I	1547.00		NIST
I	1576.00		NIST
I	1549.00		NIST
I	1574.00		NIST
I	1576.00		NIST
I	1553.00		NIST
I	1560.00		NIST
I	1553.00		NIST
I	1556.00		NIST
I	1563.00		NIST
I	1568.00		NIST
I	1540.00		NIST
I	1550.00		NIST
I	1584.40		NIST
I	1584.40		NIST
I	1552.00		NIST
I	1556.00		NIST
I	1552.00		NIST
I	1548.00		NIST
I	1580.00		NIST
I	1558.00		NIST
I	1572.00		NIST
I	1568.00		NIST
I	1555.00		NIST
I	1560.00		NIST
I	1542.00		NIST
I	Outlier 1594.00		NIST
I	1528.00		NIST
I	Outlier 1515.00		NIST
I	1562.00		NIST
I	1551.00		NIST
I	1567.00		NIST
I	1539.00		NIST
I	1566.00		NIST
I	1539.00		NIST
I	1558.00		NIST
I	1558.00		NIST
I	1557.00		NIST
I	1531.00		NIST
I	1528.00		NIST
I	1557.00		NIST
I	1555.00		NIST
I	1567.00		NIST
I	1559.00		NIST
I	1563.00		NIST
I	1573.00		NIST
I	1543.00		NIST
I	1546.00		NIST
I	1556.00		NIST
I	1557.00		NIST
I	1543.00		NIST
I	1562.00		NIST
I	1573.00		NIST
I	1572.00		NIST
I	1530.00		NIST
I	1558.00		NIST
I	1562.00		NIST
I	1562.00		NIST
I	1554.00		NIST
I	1558.00		NIST
I	1541.00		NIST
I	1564.00		NIST
I	1547.00		NIST
I	1554.00		NIST
I	1560.00		NIST
I	1555.00		NIST
I	1566.00		NIST
I	1550.00		NIST
I	1560.00		NIST
I	1556.00		NIST
I	1556.00		NIST
I	1562.00		NIST
I	1555.00		NIST
I	1560.00		NIST
I	1562.00		NIST
I	1565.00		NIST
I	1540.00		NIST
I	1555.00		NIST
I	Outlier 1519.00		NIST
I	1563.00		NIST
I	1562.00		NIST
I	1562.00		NIST
I	1562.00		NIST
I	Outlier 1510.00		NIST
I	1552.00		NIST
I	1560.00		NIST
I	1564.00		NIST
I	1560.00		NIST
I	1569.00		NIST
I	1566.00		NIST
I	1564.00		NIST
I	1565.00		NIST
I	1558.00		NIST
I	1534.00		NIST
I	1546.00		NIST
I	1551.00		NIST
I	Outlier 1507.00		NIST
I	1531.00		NIST
I	1534.00		NIST
I	1575.00		NIST
I	Outlier 1519.00		NIST
I	1534.00		NIST
I	1534.00		NIST
I	Outlier 1519.00		NIST
I	1554.00		NIST
I	1553.00		NIST
I	1568.00		NIST
I	Outlier 1516.00		NIST
I	Outlier 1519.00		NIST
I	1562.00		NIST
I	1562.00		NIST
I	Outlier 1516.00		NIST
I	Outlier 1519.00		NIST
I	1530.00		NIST
I	1585.00		NIST
I	1530.00		NIST
I	1530.00		NIST
I	1561.00		NIST
I	1555.00		NIST
I	1563.00		NIST
I	1570.00		NIST
I	1557.00		NIST
I	1558.00		NIST
I	1568.00		NIST
I	1561.00		NIST
I	1566.00		NIST
I	1561.00		NIST
I	1564.00		NIST
I	1562.00		NIST
I	1566.00		NIST
I	1565.00		NIST
I	1568.00		NIST
I	1559.00		NIST
I	1540.00		NIST
I	1548.00		NIST
I	Outlier 1605.00		NIST
I	1561.00		NIST
I	1574.00		NIST
I	1543.00		NIST
I	1562.00		NIST
I	1557.00		NIST
I	1563.00		NIST
I	1562.00		NIST
I	1562.00		NIST
I	1562.00		NIST
I	1550.00		NIST
I	1562.00		NIST
I	1536.00		NIST
I	1538.00		NIST
I	1539.00		NIST
I	1562.00		NIST
I	1562.00		NIST
I	1562.00		NIST
I	1562.00		NIST
I	1551.00		NIST
I	1549.00		NIST
I	1562.00		NIST
I	1562.00		NIST
I	1567.00		NIST
I	Outlier 1519.00		NIST
I	1556.00		NIST
I	1562.00		NIST
I	1562.00		NIST
I	1562.00		NIST
I	1562.00		NIST
I	1562.00		NIST
I	1549.00		NIST
I	Outlier 1519.00		NIST
I	1562.00		NIST
I	1562.00		NIST
I	1562.00		NIST
I	1562.00		NIST
I	1562.00		NIST
I	1562.00		NIST
I	1548.00		NIST
I	1568.00		NIST
I	Outlier 1519.00		NIST
I	1553.00		NIST
I	Outlier 1507.00		NIST
I	1554.00		NIST
I	1573.00		NIST
I	1573.00		NIST
I	1557.00		NIST
I	1557.00		NIST
I	Outlier 1519.00		NIST
I	Outlier 1513.00		NIST
I	1565.00		NIST
I	1566.00		NIST
I	1549.00		NIST
I	1553.00		NIST
I	1550.00		NIST
I	1526.00		NIST
I	1561.00		NIST
I	1522.00		NIST
I	Outlier 1519.00		NIST
I	1556.00		NIST
I	1572.00		NIST
I	Outlier 1594.00		NIST
I	1567.00		NIST
I	1558.00		NIST
I	1555.00		NIST
I	1543.00		NIST
I	1562.00		NIST
I	1564.00		NIST
I	1540.00		NIST
I	Outlier 1507.00		NIST
I	1534.00		NIST
I	1568.00		NIST
I	Outlier 1516.00		NIST
I	1530.00		NIST
I	1546.00		NIST
I	1557.00		NIST
I	1520.00		NIST
I	1559.00		NIST
I	1544.00		NIST
I	1538.00		NIST
I	1573.00		NIST
Tboil	[466.00; 468.31]	K
Tboil	468.31	K	KDB
Tboil	468.20	K	Ternary...
Tboil	466.00	K	The rol...
Tboil	468.00	K	(Liquid...
Tboil	468.00	K	(Liquid...
Tc	[650.56; 668.00]	K
Tc	652.50	K	KDB
Tc	652.50 ± 0.50	K	NIST
Tc	652.20 ± 0.80	K	NIST
Tc	652.40 ± 0.60	K	NIST
Tc	652.40 ± 0.60	K	NIST
Tc	652.60	K	NIST
Tc	650.56 ± 0.30	K	NIST
Tc	652.50	K	NIST
Tc	Outlier 668.00 ± 2.00	K	NIST
Tc	657.80	K	NIST
Tc	658.60	K	NIST
Tfus	[256.20; 259.15]	K
Tfus	257.60	K	KDB
Tfus	257.65	K	Aq. Sol...
Tfus	257.70	K	SLE and...
Tfus	258.20	K	Phase e...
Tfus	258.03	K	Experim...
Tfus	259.15	K	Phase E...
Tfus	257.85	K	Solid-L...
Tfus	258.35 ± 0.05	K	NIST
Tfus	258.03 ± 0.08	K	NIST
Tfus	256.20 ± 0.50	K	NIST
Tfus	256.25 ± 0.40	K	NIST
Tfus	256.40 ± 0.50	K	NIST
Tfus	256.90 ± 0.40	K	NIST
Vc	[0.497; 0.497]	m3/kmol
Vc	0.497	m3/kmol	KDB
Vc	0.497	m3/kmol	NIST
Zc	0.2543990		KDB

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[290.08; 353.18]	J/mol×K	[474.62; 634.38]
Cp,gas	290.08	J/mol×K	474.62	Joback Calculated Property
Cp,gas	301.62	J/mol×K	501.25	Joback Calculated Property
Cp,gas	312.74	J/mol×K	527.87	Joback Calculated Property
Cp,gas	323.45	J/mol×K	554.50	Joback Calculated Property
Cp,gas	333.75	J/mol×K	581.13	Joback Calculated Property
Cp,gas	343.66	J/mol×K	607.75	Joback Calculated Property
Cp,gas	353.18	J/mol×K	634.38	Joback Calculated Property
Cp,liquid	[284.50; 379.00]	J/mol×K	[286.00; 313.15]
Cp,liquid	284.50	J/mol×K	286.00	NIST
Cp,liquid	312.10	J/mol×K	298.00	NIST
Cp,liquid	324.30	J/mol×K	298.00	NIST
Cp,liquid	304.00	J/mol×K	298.15	Volumet...
Cp,liquid	305.55	J/mol×K	298.15	NIST
Cp,liquid	304.00	J/mol×K	298.15	NIST
Cp,liquid	329.00	J/mol×K	303.15	Volumet...
Cp,liquid	329.50	J/mol×K	303.20	NIST
Cp,liquid	354.00	J/mol×K	308.15	Volumet...
Cp,liquid	318.30	J/mol×K	310.67	NIST
Cp,liquid	379.00	J/mol×K	313.15	Volumet...
η	[0.0017820; 0.0134930]	Pa×s	[283.15; 348.15]
η	0.0134930	Pa×s	283.15	Measure...
η	0.0134930	Pa×s	283.15	Density...
η	0.0110700	Pa×s	288.15	Densiti...
η	0.0108720	Pa×s	288.15	Measure...
η	0.0089440	Pa×s	293.15	Measure...
η	0.0090160	Pa×s	293.15	Density...
η	0.0091610	Pa×s	293.15	Densiti...
η	0.0074980	Pa×s	298.15	Measure...
η	0.0073980	Pa×s	298.15	Density...
η	0.0073900	Pa×s	298.15	Density...
η	0.0073650	Pa×s	298.15	Density...
η	0.0076880	Pa×s	298.15	Densiti...
η	0.0076610	Pa×s	298.15	Acousti...
η	0.0064020	Pa×s	303.15	Acousti...
η	0.0064330	Pa×s	303.15	Densiti...
η	0.0064460	Pa×s	303.15	Densiti...
η	0.0063060	Pa×s	303.15	Density...
η	0.0062730	Pa×s	303.15	Measure...
η	0.0064040	Pa×s	303.15	Densiti...
η	0.0054250	Pa×s	308.15	Acousti...
η	0.0052510	Pa×s	308.15	Density...
η	0.0053420	Pa×s	308.15	Measure...
η	0.0052850	Pa×s	308.15	Density...
η	0.0046200	Pa×s	313.15	Densiti...
η	0.0046030	Pa×s	313.15	Densiti...
η	0.0046040	Pa×s	313.15	Densiti...
η	0.0045400	Pa×s	313.15	Measure...
η	0.0045870	Pa×s	313.15	Density...
η	0.0046280	Pa×s	313.15	Acousti...
η	0.0038650	Pa×s	318.15	Density...
η	0.0038870	Pa×s	318.15	Density...
η	0.0029310	Pa×s	328.15	Density...
η	0.0022620	Pa×s	338.15	Density...
η	0.0017820	Pa×s	348.15	Density...
ΔfusH	25.24	kJ/mol	258.40	NIST
ΔvapH	[47.80; 70.40]	kJ/mol	[267.00; 515.00]
ΔvapH	64.00 ± 1.00	kJ/mol	267.00	NIST
ΔvapH	64.00	kJ/mol	274.50	NIST
ΔvapH	69.60	kJ/mol	301.50	NIST
ΔvapH	68.70	kJ/mol	318.00	NIST
ΔvapH	70.40	kJ/mol	323.00	NIST
ΔvapH	67.30	kJ/mol	364.00	NIST
ΔvapH	61.60	kJ/mol	396.00	NIST
ΔvapH	67.50	kJ/mol	405.50	NIST
ΔvapH	65.00	kJ/mol	410.00	NIST
ΔvapH	56.60	kJ/mol	438.00	NIST
ΔvapH	52.50	kJ/mol	452.00	NIST
ΔvapH	50.63	kJ/mol	468.30	KDB
ΔvapH	47.80	kJ/mol	515.00	NIST
Pvap	[1.00e-03; 101.40]	kPa	[288.15; 468.47]
Pvap	1.00e-03	kPa	288.15	Vapor L...
Pvap	3.00e-03	kPa	293.15	Isother...
Pvap	3.00e-03	kPa	293.15	Vapor L...
Pvap	0.01	kPa	298.15	Vapor P...
Pvap	7.00e-03	kPa	298.15	Isother...
Pvap	7.00e-03	kPa	298.15	Vapor L...
Pvap	0.01	kPa	303.15	Isother...
Pvap	0.01	kPa	303.15	Vapor L...
Pvap	0.02	kPa	303.15	Vapor P...
Pvap	0.03	kPa	308.15	Vapor P...
Pvap	0.02	kPa	308.15	Vapor L...
Pvap	0.02	kPa	308.15	Isother...
Pvap	0.03	kPa	313.15	Vapor L...
Pvap	0.04	kPa	313.15	Vapor P...
Pvap	0.03	kPa	313.15	Isother...
Pvap	0.05	kPa	318.15	Vapor L...
Pvap	0.06	kPa	318.15	Vapor P...
Pvap	0.05	kPa	318.15	Isother...
Pvap	0.06	kPa	319.82	Thermog...
Pvap	0.08	kPa	323.15	Isother...
Pvap	0.08	kPa	323.15	Vapor L...
Pvap	0.09	kPa	323.15	Vapor P...
Pvap	0.09	kPa	324.46	Thermog...
Pvap	0.14	kPa	328.15	Vapor P...
Pvap	0.20	kPa	333.15	Vapor P...
Pvap	0.22	kPa	333.69	Vapor p...
Pvap	0.21	kPa	333.93	Thermog...
Pvap	0.22	kPa	333.97	Vapor p...
Pvap	0.24	kPa	334.46	Vapor p...
Pvap	0.29	kPa	338.15	Vapor P...
Pvap	0.20	kPa	338.55	Vapor p...
Pvap	0.39	kPa	341.76	Vapor p...
Pvap	0.39	kPa	342.10	Vapor p...
Pvap	0.41	kPa	343.15	Vapor P...
Pvap	0.38	kPa	343.23	Thermog...
Pvap	0.37	kPa	343.33	Vapor p...
Pvap	0.40	kPa	343.39	Thermog...
Pvap	0.39	kPa	344.50	Vapor p...
Pvap	0.54	kPa	348.15	Thermog...
Pvap	0.57	kPa	348.15	Vapor P...
Pvap	0.57	kPa	348.20	Vapor p...
Pvap	0.59	kPa	348.72	Vapor p...
Pvap	0.60	kPa	349.10	Vapor p...
Pvap	0.59	kPa	349.38	Vapor p...
Pvap	0.75	kPa	352.09	Vapor p...
Pvap	0.80	kPa	352.98	Vapor p...
Pvap	0.79	kPa	353.15	Vapor P...
Pvap	0.81	kPa	353.96	Vapor p...
Pvap	0.85	kPa	354.85	Vapor P...
Pvap	0.79	kPa	354.96	Vapor p...
Pvap	1.07	kPa	357.90	Vapor p...
Pvap	1.06	kPa	357.94	Vapor p...
Pvap	1.06	kPa	357.99	Vapor p...
Pvap	1.07	kPa	358.15	Vapor P...
Pvap	1.07	kPa	358.15	Vapor P...
Pvap	1.07	kPa	358.41	Vapor p...
Pvap	1.36	kPa	362.32	Thermog...
Pvap	1.43	kPa	362.88	Vapor p...
Pvap	1.45	kPa	363.15	Vapor P...
Pvap	1.45	kPa	363.30	Vapor p...
Pvap	1.46	kPa	363.51	Vapor p...
Pvap	1.51	kPa	363.55	Vapor P...
Pvap	1.47	kPa	364.35	Vapor p...
Pvap	1.93	kPa	368.15	Vapor P...
Pvap	2.01	kPa	368.25	Vapor P...
Pvap	2.10	kPa	369.69	Vapor p...
Pvap	2.09	kPa	369.76	Vapor p...
Pvap	2.13	kPa	369.90	Vapor p...
Pvap	2.13	kPa	370.00	Vapor p...
Pvap	2.54	kPa	373.15	Vapor P...
Pvap	2.99	kPa	376.05	Vapor P...
Pvap	3.32	kPa	378.15	Vapor P...
Pvap	3.44	kPa	379.04	Vapor p...
Pvap	3.49	kPa	379.35	Vapor p...
Pvap	3.49	kPa	379.45	Vapor p...
Pvap	3.49	kPa	379.49	Vapor p...
Pvap	4.01	kPa	381.75	Vapor P...
Pvap	4.29	kPa	383.15	Vapor P...
Pvap	5.01	kPa	386.05	Vapor P...
Pvap	5.17	kPa	387.20	Vapor p...
Pvap	5.16	kPa	387.28	Vapor p...
Pvap	5.18	kPa	387.87	Vapor p...
Pvap	5.17	kPa	387.92	Vapor p...
Pvap	5.48	kPa	388.15	Vapor P...
Pvap	6.01	kPa	389.95	Vapor P...
Pvap	6.14	kPa	390.95	Thermog...
Pvap	7.01	kPa	393.15	Vapor P...
Pvap	6.94	kPa	393.15	Vapor P...
Pvap	8.02	kPa	396.05	Vapor P...
Pvap	8.36	kPa	397.32	Vapor p...
Pvap	8.71	kPa	398.15	Vapor P...
Pvap	9.02	kPa	398.55	Vapor P...
Pvap	9.99	kPa	400.95	Vapor P...
Pvap	10.83	kPa	403.15	Vapor P...
Pvap	11.10	kPa	403.71	Vapor p...
Pvap	13.57	kPa	407.24	Vapor p...
Pvap	13.36	kPa	408.15	Vapor P...
Pvap	13.58	kPa	408.44	Vapor p...
Pvap	13.55	kPa	408.90	Vapor p...
Pvap	13.95	kPa	409.14	Vapor p...
Pvap	13.55	kPa	409.30	Vapor p...
Pvap	14.97	kPa	410.15	Vapor P...
Pvap	16.36	kPa	413.15	Vapor P...
Pvap	16.83	kPa	413.79	Vapor p...
Pvap	19.91	kPa	417.35	Vapor P...
Pvap	20.50	kPa	417.83	Isobari...
Pvap	19.88	kPa	418.15	Vapor P...
Pvap	20.33	kPa	418.61	Vapor p...
Pvap	20.33	kPa	418.62	Vapor p...
Pvap	20.33	kPa	418.63	Vapor p...
Pvap	23.99	kPa	423.15	Vapor P...
Pvap	24.62	kPa	423.70	Vapor p...
Pvap	28.76	kPa	428.15	Vapor P...
Pvap	30.40	kPa	428.60	Isobari...
Pvap	29.45	kPa	428.65	Vapor p...
Pvap	34.27	kPa	433.15	Vapor P...
Pvap	34.89	kPa	433.49	Vapor p...
Pvap	40.47	kPa	435.48	Vapor p...
Pvap	40.00	kPa	436.67	Low-Pre...
Pvap	41.50	kPa	437.35	Isobari...
Pvap	40.08	kPa	437.67	Low-Pre...
Pvap	40.83	kPa	438.12	Vapor p...
Pvap	40.83	kPa	438.14	Vapor p...
Pvap	40.61	kPa	438.15	Vapor P...
Pvap	40.53	kPa	438.31	Vapor p...
Pvap	40.53	kPa	438.58	Vapor p...
Pvap	40.53	kPa	438.80	Vapor p...
Pvap	47.73	kPa	442.88	Vapor p...
Pvap	47.88	kPa	443.15	Vapor P...
Pvap	48.62	kPa	443.61	Low-Pre...
Pvap	50.50	kPa	443.90	Isobari...
Pvap	52.15	kPa	445.86	Low-Pre...
Pvap	56.17	kPa	448.15	Vapor P...
Pvap	60.70	kPa	449.55	Isobari...
Pvap	60.37	kPa	450.34	Vapor p...
Pvap	60.03	kPa	450.45	Low-Pre...
Pvap	65.45	kPa	453.15	Vapor P...
Pvap	67.60	kPa	454.35	Low-Pre...
Pvap	71.00	kPa	454.52	Isobari...
Pvap	74.25	kPa	457.08	Low-Pre...
Pvap	74.88	kPa	457.52	Vapor p...
Pvap	75.95	kPa	458.15	Vapor P...
Pvap	81.00	kPa	459.23	Isobari...
Pvap	81.52	kPa	460.31	Low-Pre...
Pvap	87.73	kPa	463.15	Vapor P...
Pvap	91.10	kPa	463.21	Isobari...
Pvap	89.16	kPa	463.50	Low-Pre...
Pvap	93.42	kPa	465.25	Vapor p...
Pvap	93.54	kPa	465.29	Vapor p...
Pvap	100.30	kPa	466.61	Isobari...
Pvap	97.64	kPa	466.80	Low-Pre...
Pvap	101.40	kPa	468.15	Vapor p...
Pvap	101.40	kPa	468.47	Vapor p...
n0	[1.41800; 1.42980]		[293.15; 318.20]
n0	1.42958		293.15	Densiti...
n0	1.42930		293.15	Experim...
n0	1.42958		293.15	Excess ...
n0	1.42941		293.15	Densiti...
n0	1.42980		293.15	Densiti...
n0	1.42910		293.15	Experim...
n0	1.42900		293.15	Effect ...
n0	1.42695		298.15	Liquid ...
n0	1.42884		298.15	Atmosph...
n0	1.42800		298.15	Densiti...
n0	1.42750		298.15	Effect ...
n0	1.42740		298.15	Density...
n0	1.42760		298.20	A therm...
n0	1.42700		298.20	Tie-lin...
n0	1.42700		298.20	Ternary...
n0	1.42760		298.20	Solubil...
n0	1.42562		303.15	Densiti...
n0	1.42563		303.15	Densiti...
n0	1.42280		308.20	A therm...
n0	1.41850		318.20	A therm...
n0	1.41800		318.20	A therm...
ρl	[774.43; 832.13]	kg/m3	[283.15; 363.15]
ρl	832.11	kg/m3	283.15	Densiti...
ρl	832.13	kg/m3	283.15	Volumet...
ρl	832.07	kg/m3	283.15	Densiti...
ρl	832.06	kg/m3	283.15	Excess ...
ρl	828.71	kg/m3	288.15	Volumet...
ρl	828.66	kg/m3	288.15	Densiti...
ρl	826.00	kg/m3	293.00	KDB
ρl	824.90	kg/m3	293.15	Investi...
ρl	825.13	kg/m3	293.15	Densiti...
ρl	824.90	kg/m3	293.15	Correla...
ρl	825.10	kg/m3	293.15	A therm...
ρl	825.09	kg/m3	293.15	Volume ...
ρl	824.60	kg/m3	293.15	Densiti...
ρl	831.00	kg/m3	293.15	Interfa...
ρl	825.24	kg/m3	293.15	Densiti...
ρl	825.27	kg/m3	293.15	Volumet...
ρl	825.57	kg/m3	293.15	Isobari...
ρl	825.05	kg/m3	293.15	Speeds ...
ρl	825.95	kg/m3	293.20	Modelin...
ρl	823.60	kg/m3	293.20	Ternary...
ρl	821.64	kg/m3	298.15	Speeds ...
ρl	821.65	kg/m3	298.15	Densiti...
ρl	821.40	kg/m3	298.15	Investi...
ρl	821.72	kg/m3	298.15	Excess ...
ρl	821.40	kg/m3	298.15	Correla...
ρl	822.11	kg/m3	298.15	Partial...
ρl	821.67	kg/m3	298.15	Excess ...
ρl	821.79	kg/m3	298.15	Studies...
ρl	821.22	kg/m3	298.15	Physico...
ρl	821.70	kg/m3	298.15	Viscosi...
ρl	821.65	kg/m3	298.15	Volume ...
ρl	821.80	kg/m3	298.15	Densiti...
ρl	821.60	kg/m3	298.15	Determi...
ρl	823.27	kg/m3	298.15	Phase b...
ρl	822.47	kg/m3	298.15	Excess ...
ρl	821.88	kg/m3	298.15	Thermod...
ρl	821.74	kg/m3	298.15	Volumet...
ρl	821.60	kg/m3	298.15	Thermod...
ρl	820.70	kg/m3	298.15	Densiti...
ρl	822.21	kg/m3	298.15	Experim...
ρl	821.63	kg/m3	298.15	Densiti...
ρl	821.90	kg/m3	298.15	Isobari...
ρl	821.84	kg/m3	298.15	Densiti...
ρl	821.81	kg/m3	298.15	Volumet...
ρl	822.28	kg/m3	298.15	Thermod...
ρl	821.72	kg/m3	298.15	Speeds ...
ρl	821.72	kg/m3	298.15	Thermod...
ρl	821.87	kg/m3	298.15	Effect ...
ρl	821.70	kg/m3	298.15	A therm...
ρl	822.99	kg/m3	298.15	The phy...
ρl	823.27	kg/m3	298.15	Phase b...
ρl	821.70	kg/m3	298.20	Physica...
ρl	818.35	kg/m3	303.15	Densiti...
ρl	818.26	kg/m3	303.15	Volumet...
ρl	817.90	kg/m3	303.15	Correla...
ρl	818.24	kg/m3	303.15	Excess ...
ρl	817.52	kg/m3	303.15	Volumet...
ρl	817.90	kg/m3	303.15	Investi...
ρl	818.27	kg/m3	303.15	Effect ...
ρl	818.18	kg/m3	303.15	Volume ...
ρl	818.14	kg/m3	303.15	Densiti...
ρl	817.20	kg/m3	303.15	Densiti...
ρl	818.79	kg/m3	303.15	Thermod...
ρl	818.30	kg/m3	303.15	A therm...
ρl	818.08	kg/m3	303.15	Isobari...
ρl	818.33	kg/m3	303.15	Volumet...
ρl	818.30	kg/m3	303.15	Effect ...
ρl	818.17	kg/m3	303.15	Speeds ...
ρl	814.67	kg/m3	308.15	Speeds ...
ρl	814.60	kg/m3	308.15	Viscosi...
ρl	814.31	kg/m3	308.15	Isobari...
ρl	814.76	kg/m3	308.15	Volumet...
ρl	815.27	kg/m3	308.15	Thermod...
ρl	813.80	kg/m3	308.15	Densiti...
ρl	814.68	kg/m3	308.15	Effect ...
ρl	814.40	kg/m3	308.15	Correla...
ρl	814.84	kg/m3	308.15	Volumet...
ρl	814.80	kg/m3	308.15	A therm...
ρl	814.69	kg/m3	308.15	Volume ...
ρl	814.87	kg/m3	308.15	Densiti...
ρl	814.40	kg/m3	308.15	Investi...
ρl	811.17	kg/m3	313.15	Speeds ...
ρl	811.31	kg/m3	313.15	Volumet...
ρl	811.24	kg/m3	313.15	Volumet...
ρl	810.90	kg/m3	313.15	Correla...
ρl	811.38	kg/m3	313.15	Densiti...
ρl	811.40	kg/m3	313.15	A therm...
ρl	810.60	kg/m3	313.15	Densiti...
ρl	811.04	kg/m3	313.15	Effect ...
ρl	811.21	kg/m3	313.15	Excess ...
ρl	811.15	kg/m3	313.15	Densiti...
ρl	810.90	kg/m3	313.15	Investi...
ρl	811.73	kg/m3	313.15	Thermod...
ρl	811.09	kg/m3	313.15	Isobari...
ρl	811.20	kg/m3	313.15	Effect ...
ρl	811.17	kg/m3	313.15	Volume ...
ρl	807.65	kg/m3	318.15	Speeds ...
ρl	807.69	kg/m3	318.15	Volumet...
ρl	807.70	kg/m3	318.15	Isobari...
ρl	807.50	kg/m3	318.15	Viscosi...
ρl	807.85	kg/m3	318.15	Densiti...
ρl	807.63	kg/m3	318.15	Volume ...
ρl	807.30	kg/m3	318.15	Correla...
ρl	807.30	kg/m3	318.15	Investi...
ρl	806.90	kg/m3	318.15	Densiti...
ρl	807.76	kg/m3	318.15	Volumet...
ρl	808.17	kg/m3	318.15	Thermod...
ρl	804.19	kg/m3	323.15	Volumet...
ρl	804.12	kg/m3	323.15	Volumet...
ρl	803.70	kg/m3	323.15	Correla...
ρl	803.70	kg/m3	323.15	Investi...
ρl	804.05	kg/m3	323.15	Isobari...
ρl	803.90	kg/m3	323.15	Densiti...
ρl	804.29	kg/m3	323.15	Densiti...
ρl	804.20	kg/m3	323.15	Effect ...
ρl	804.58	kg/m3	323.15	Thermod...
ρl	800.58	kg/m3	328.15	Volumet...
ρl	800.40	kg/m3	328.15	Viscosi...
ρl	800.70	kg/m3	328.15	Densiti...
ρl	796.93	kg/m3	333.15	Volumet...
ρl	796.90	kg/m3	333.15	Effect ...
ρl	796.88	kg/m3	333.15	Isobari...
ρl	797.08	kg/m3	333.15	Densiti...
ρl	793.10	kg/m3	338.15	Viscosi...
ρl	793.41	kg/m3	338.15	Densiti...
ρl	789.70	kg/m3	343.15	Densiti...
ρl	785.95	kg/m3	348.15	Densiti...
ρl	782.16	kg/m3	353.15	Densiti...
ρl	778.31	kg/m3	358.15	Densiti...
ρl	774.43	kg/m3	363.15	Densiti...
csound,fluid	[1282.90; 1390.20]	m/s	[288.15; 318.15]
csound,fluid	1390.20	m/s	288.15	Ultraso...
csound,fluid	1371.50	m/s	293.15	Ultraso...
csound,fluid	1364.08	m/s	293.15	Thermod...
csound,fluid	1347.40	m/s	298.15	Micella...
csound,fluid	1352.40	m/s	298.15	Ultraso...
csound,fluid	1347.32	m/s	298.15	Thermod...
csound,fluid	1333.10	m/s	303.15	Ultraso...
csound,fluid	1330.99	m/s	303.15	Thermod...
csound,fluid	1330.58	m/s	303.15	Micella...
csound,fluid	1315.70	m/s	308.15	Ultraso...
csound,fluid	1314.28	m/s	308.15	Thermod...
csound,fluid	1313.92	m/s	308.15	Micella...
csound,fluid	1298.90	m/s	313.15	Ultraso...
csound,fluid	1297.72	m/s	313.15	Thermod...
csound,fluid	1282.90	m/s	318.15	Ultraso...
γ	[0.03; 0.03]	N/m	[288.15; 308.15]
γ	0.03	N/m	288.15	Density...
γ	0.03	N/m	293.15	Density...
γ	0.03	N/m	293.20	KDB
γ	0.03	N/m	298.15	Density...
γ	0.03	N/m	303.15	Density...
γ	0.03	N/m	308.15	Density...

Pressure Dependent Properties

Property	Value	Unit	Pressure (kPa)	Source
Tboilr	371.20	K	2.50	NIST

Datasets

1. Mass density, kg/m3 (5)
2. Thermal conductivity, W/m/K (1)

Mass density, kg/m3

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
298.15	100.00	821.4
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
278.15	100.00	835.2
278.15	1000.00	835.7
278.15	5000.00	838.0
278.15	10000.00	841.0
278.15	15000.00	843.7
278.15	20000.00	846.4
278.15	25000.00	849.0
278.15	30000.00	851.5
278.15	35000.00	854.0
278.15	40000.00	856.4
278.15	45000.00	858.8
278.15	50000.00	861.1
278.15	55000.00	863.4
278.15	60000.00	865.5
288.15	100.00	828.4
288.15	1000.00	829.0
288.15	5000.00	831.5
288.15	10000.00	834.4
288.15	15000.00	837.3
288.15	20000.00	840.1
288.15	25000.00	842.8
288.15	30000.00	845.5
288.15	35000.00	848.0
288.15	40000.00	850.5
288.15	45000.00	852.9
288.15	50000.00	855.3
288.15	55000.00	857.6
288.15	60000.00	859.8
298.15	100.00	821.4
298.15	1000.00	822.0
298.15	5000.00	824.6
298.15	10000.00	827.7
298.15	15000.00	830.7
298.15	20000.00	833.6
298.15	25000.00	836.4
298.15	30000.00	839.1
298.15	35000.00	841.8
298.15	40000.00	844.4
298.15	45000.00	846.9
298.15	50000.00	849.4
298.15	55000.00	851.7
298.15	60000.00	853.9
308.15	100.00	814.5
308.15	1000.00	815.1
308.15	5000.00	817.8
308.15	10000.00	821.1
308.15	15000.00	824.2
308.15	20000.00	827.2
308.15	25000.00	830.1
308.15	30000.00	833.0
308.15	35000.00	835.7
308.15	40000.00	838.4
308.15	45000.00	841.0
308.15	50000.00	843.5
308.15	55000.00	846.0
308.15	60000.00	848.2
318.15	100.00	807.5
318.15	1000.00	808.1
318.15	5000.00	811.0
318.15	10000.00	814.4
318.15	15000.00	817.7
318.15	20000.00	820.8
318.15	25000.00	823.8
318.15	30000.00	826.8
318.15	35000.00	829.6
318.15	40000.00	832.4
318.15	45000.00	835.1
318.15	50000.00	837.7
318.15	55000.00	840.3
318.15	60000.00	842.6
328.15	100.00	800.4
328.15	1000.00	801.1
328.15	5000.00	804.1
328.15	10000.00	807.7
328.15	15000.00	811.1
328.15	20000.00	814.4
328.15	25000.00	817.5
328.15	30000.00	820.5
328.15	35000.00	823.5
328.15	40000.00	826.4
328.15	45000.00	829.1
328.15	50000.00	831.9
328.15	55000.00	834.5
328.15	60000.00	836.9
338.15	100.00	793.2
338.15	1000.00	793.9
338.15	5000.00	796.9
338.15	10000.00	800.8
338.15	15000.00	804.4
338.15	20000.00	807.8
338.15	25000.00	811.1
338.15	30000.00	814.2
338.15	35000.00	817.3
338.15	40000.00	820.3
338.15	45000.00	823.1
338.15	50000.00	825.9
338.15	55000.00	828.7
338.15	60000.00	831.2
348.15	100.00	785.6
348.15	1000.00	786.4
348.15	5000.00	789.8
348.15	10000.00	793.6
348.15	15000.00	797.4
348.15	20000.00	801.0
348.15	25000.00	804.5
348.15	30000.00	807.8
348.15	35000.00	810.9
348.15	40000.00	814.0
348.15	45000.00	817.0
348.15	50000.00	819.9
348.15	55000.00	822.7
348.15	60000.00	825.5
358.15	100.00	778.0
358.15	1000.00	778.8
358.15	5000.00	782.3
358.15	10000.00	786.4
358.15	15000.00	790.4
358.15	20000.00	794.1
358.15	25000.00	797.7
358.15	30000.00	801.1
358.15	35000.00	804.5
358.15	40000.00	807.7
358.15	45000.00	810.8
358.15	50000.00	813.6
358.15	55000.00	816.7
358.15	60000.00	819.6
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
298.15	2000.00	823.6
298.15	4010.00	824.8
298.15	6000.00	826.0
298.15	8000.00	827.2
298.15	10000.00	828.4
298.15	13010.00	830.1
298.15	16010.00	831.8
298.15	18990.00	833.4
298.15	22010.00	835.0
298.15	25010.00	836.6
298.15	28010.00	838.3
298.15	30010.00	839.3
303.15	1990.00	819.4
303.15	3990.00	820.6
303.15	5980.00	821.9
303.16	7980.00	823.1
303.15	10010.00	824.4
303.16	13000.00	826.2
303.15	16020.00	827.9
303.15	19030.00	829.7
303.16	22010.00	831.3
303.15	25000.00	833.0
303.16	28000.00	834.6
303.15	29980.00	835.6
313.15	1970.00	812.3
313.15	4000.00	813.6
313.15	6010.00	815.0
313.15	8000.00	816.3
313.15	10010.00	817.5
313.15	13030.00	819.4
313.15	15980.00	821.2
313.15	18990.00	823.0
313.15	21990.00	824.8
313.15	25000.00	826.5
313.15	27980.00	828.2
313.15	29990.00	829.3
323.15	2010.00	805.6
323.15	4010.00	807.0
323.15	6010.00	808.4
323.15	8000.00	809.7
323.15	10010.00	811.1
323.15	13020.00	813.0
323.15	16020.00	814.9
323.15	19010.00	816.8
323.15	22000.00	818.6
323.15	25010.00	820.4
323.15	28010.00	822.1
323.15	30020.00	823.3
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
298.15	100.00	821.4
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
313.14	1004.00	811.26
313.14	2019.00	811.95
313.14	3000.00	812.59
313.14	4020.00	813.22
313.14	4995.00	813.89
313.14	6000.00	814.53
313.14	7007.00	815.21
313.14	8012.00	815.83
313.14	8994.00	816.51
313.14	10014.00	817.19
313.14	11007.00	817.79
313.14	12000.00	818.42
313.14	12997.00	819.05
313.14	14001.00	819.67
313.14	14997.00	820.27
313.14	16002.00	820.89
313.14	17001.00	821.48
313.14	17997.00	822.1
313.14	19004.00	822.69
313.14	20007.00	823.28
313.14	21004.00	823.86
323.09	1007.00	804.26
323.09	2016.00	804.97
323.09	3019.00	805.7
323.09	4025.00	806.4
323.09	5012.00	807.07
323.09	6093.00	807.82
323.09	7143.00	808.56
323.09	8009.00	809.12
323.09	8989.00	809.77
323.09	10014.00	810.47
323.09	11031.00	811.14
323.09	12010.00	811.82
323.09	13005.00	812.44
323.09	14003.00	813.11
323.09	15012.00	813.76
323.09	16009.00	814.4
323.09	17005.00	815.04
323.09	18013.00	815.66
323.09	19003.00	816.26
323.09	20025.00	816.9
323.09	21081.00	817.56
323.09	22009.00	818.09
333.05	1038.00	797.31
333.05	2029.00	798.03
333.05	2999.00	798.76
333.05	4033.00	799.51
333.05	5020.00	800.25
333.05	6014.00	800.97
333.05	7029.00	801.69
333.05	8011.00	802.44
333.05	9005.00	803.11
333.05	10022.00	803.83
333.05	11011.00	804.55
333.05	12021.00	805.23
333.05	13022.00	805.92
333.05	14031.00	806.61
333.05	15010.00	807.28
333.05	16023.00	807.92
333.05	17012.00	808.59
333.05	18035.00	809.23
333.05	19009.00	809.87
333.05	20002.00	810.51
333.05	21011.00	811.15
333.05	22019.00	811.82
343.03	1049.00	790.6
343.03	2003.00	791.16
343.03	2981.00	791.93
343.03	4017.00	792.68
343.03	5000.00	793.37
343.03	6005.00	794.05
343.03	7018.00	794.88
343.03	8104.00	795.68
343.03	9014.00	796.44
343.03	10022.00	797.1
343.03	11028.00	797.87
343.03	11997.00	798.58
343.03	13030.00	799.3
343.03	14005.00	800.0
343.03	15002.00	800.66
343.03	16032.00	801.38
343.03	17016.00	801.99
343.03	18012.00	802.68
343.03	19005.00	803.29
343.03	20018.00	803.98
343.03	21014.00	804.61
343.03	22004.00	805.23
352.89	1023.00	782.71
352.89	2011.00	783.55
352.89	3032.00	784.42
352.89	4022.00	785.42
352.89	5005.00	786.18
352.89	6026.00	787.13
352.89	7003.00	787.9
352.89	8016.00	788.71
352.89	9007.00	789.47
352.89	10003.00	790.22
352.89	11022.00	791.0
352.89	12170.00	791.78
352.89	13015.00	792.51
352.89	14018.00	793.24
352.89	15009.00	794.0
352.89	16023.00	794.74
352.89	17010.00	795.48
352.89	18002.00	796.16
352.89	19029.00	796.9
352.89	20046.00	797.63
352.89	21023.00	798.3
362.77	1051.00	775.67
362.77	2025.00	776.41
362.77	3016.00	777.19
362.77	4009.00	778.05
362.77	4974.00	778.77
362.77	6005.00	779.51
362.77	7006.00	780.3
362.77	8011.00	780.95
362.77	9008.00	781.79
362.77	10034.00	782.62
362.77	11013.00	783.32
362.77	11987.00	784.03
362.77	13015.00	784.77
362.77	14006.00	785.51
362.77	14997.00	786.3
362.77	16001.00	787.03
362.77	17013.00	787.79
362.77	17997.00	788.55
362.77	19000.00	789.33
362.77	20023.00	790.04
362.77	21004.00	790.83
Reference

Thermal conductivity, W/m/K

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Thermal conductivity, W/m/K - Liquid
274.92	100.00	0.1580
274.85	5000.00	0.1598
274.82	10000.00	0.1611
274.77	20000.00	0.1639
274.63	30000.00	0.1669
294.93	100.00	0.1545
294.62	5000.00	0.1560
294.61	10100.00	0.1576
294.59	20100.00	0.1606
294.58	30000.00	0.1634
314.41	100.00	0.1511
314.95	5000.00	0.1530
314.91	10000.00	0.1545
314.86	20000.00	0.1578
314.86	30000.00	0.1609
334.98	100.00	0.1471
334.92	5000.00	0.1490
334.90	10000.00	0.1509
334.84	20000.00	0.1544
334.83	30000.00	0.1576
354.98	100.00	0.1427
354.41	5000.00	0.1445
354.36	10000.00	0.1466
354.50	20000.00	0.1505
354.35	30000.00	0.1539
374.96	100.00	0.1380
374.43	5100.00	0.1400
374.41	10000.00	0.1421
374.81	20000.00	0.1464
374.84	30000.00	0.1503
394.88	300.00	0.1325
395.13	5000.00	0.1349
395.05	10000.00	0.1377
394.82	20000.00	0.1420
394.85	30000.00	0.1461
Reference

Correlations

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.64]	kPa	[358.71; 495.05]	The Yaw...
Equation			ln(Pvp) = A + B/(T + C)
Coefficient A			1.45038e+01
Coefficient B			-3.54647e+03
Coefficient C			-1.09245e+02
Temperature range, min.			358.71
Temperature range, max.			495.05
Pvap	1.33	kPa	358.71	Calculated Property
Pvap	3.01	kPa	373.86	Calculated Property
Pvap	6.22	kPa	389.01	Calculated Property
Pvap	11.92	kPa	404.16	Calculated Property
Pvap	21.45	kPa	419.31	Calculated Property
Pvap	36.55	kPa	434.45	Calculated Property
Pvap	59.38	kPa	449.60	Calculated Property
Pvap	92.58	kPa	464.75	Calculated Property
Pvap	139.18	kPa	479.90	Calculated Property
Pvap	202.64	kPa	495.05	Calculated Property
Pvap	[7.80e-05; 2692.59]	kPa	[257.65; 652.50]	KDB Vap...
Equation			ln(Pvp) = A + B/T + C*ln(T) + D*T^2
Coefficient A			2.04801e+02
Coefficient B			-1.63274e+04
Coefficient C			-2.73260e+01
Coefficient D			1.22481e-05
Temperature range, min.			257.65
Temperature range, max.			652.50
Pvap	7.80e-05	kPa	257.65	Calculated Property
Pvap	0.01	kPa	301.52	Calculated Property
Pvap	0.49	kPa	345.39	Calculated Property
Pvap	5.66	kPa	389.27	Calculated Property
Pvap	33.30	kPa	433.14	Calculated Property
Pvap	124.61	kPa	477.01	Calculated Property
Pvap	343.81	kPa	520.88	Calculated Property
Pvap	771.79	kPa	564.76	Calculated Property
Pvap	1508.48	kPa	608.63	Calculated Property
Pvap	2692.59	kPa	652.50	Calculated Property

Similar Compounds

Find more compounds similar to 1-Octanol.

Mixtures

• Isopropyl Alcohol + 1-Octanol
• 1-Octene + 1-Octanol
• 1-Octanol + Simvastatin
• 1-Octanol + Cholesterol
• 1-Octanol + Cholesterol + Cyclohexane
• Tributyl phosphate + 1-Octanol
• 1-Octanol + 1-Decanol
• Benzo[b]thiophene + 1-Octanol
• 1-Octanol + Tridodecylamine
• Butanoic acid + 1-Octanol + Water
• 1-Octanol + Water
• 1-Octanol + Perphenazine
• Indomethacin + 1-Octanol
• Aspirin + 1-Octanol
• Acetaminophen + 1-Octanol
• 1-Octanol + Cyclohexane
• Butane, 1-chloro- + 1-Octanol
• Ethane, 1,1,2,2-tetrabromo- + 1-Octanol
• 1-Octanol + Ethane, 1,1,2,2-tetrachloro-
• 1-Octanol + Propanoic acid + Water

Find more mixtures with 1-Octanol.

Sources

• KDB Pure (Korean Thermophysical Properties Databank)
• KDB Vapor Pressure Data
• Crippen Method
• Speeds of Sound and Isentropic Compressibilities in Binary Mixtures of 2-Propanol with Several 1-Alkanols at 298.15K
• Excess Volumes, Densities, Speeds of Sound, and Viscosities for the Binary Systems of 1-Octanol with Hexadecane and Squalane at (298.15, 303.15 and 308.15) K
• Liquid phase behavior of imidazolium-based ionic liquids with alcohols: effect of hydrogen bonding and non-polar interactions
• Liquid-liquid equilibria for ternary systems of (water + carboxylic acid + 1-octanol) at 293.15 K: modeling phase equilibria using a solvatochromic approach
• Excess molar enthalpies for mixtures of carbon dioxide + a modifier (5 mol% methanol or 1-octanol) and hexane at 308.15K and 12.40MPa
• Phase behaviour of I-hexyloxymethyl-3-methyl-imidazolium and 1,3-dihexyloxymethyl-imidazolium based ionic liquids with alcohols, water, ketones and hydrocarbons: The effect of cation and anion on solubility
• Solubility of naproxen in several organic solvents at different temperatures
• 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
• Excess molar enthalpy of 1-alkanol + 1-octene mixtures at 298.15K Experimental results and theoretical description by means of the ERAS and TB models
• Measurement and prediction of pyrene solubility in pure, binary, ternary and quaternary solvent systems
• Solubility and limiting activity coefficient of simvastatin in different organic solvents
• Benchmarks for the fifth industrial fluid properties simulation challenge
• Experimental solid-liquid phase equilibria of {cholesterol + binary solvent mixture: 1-Alcohol (C4-C10) + cyclohexane}
• (Solid + liquid) and (liquid + liquid) phase equilibria study and correlation of the binary systems {N-butyl-3-methylpyridinium tosylate + water, or + an alcohol, or + a hydrocarbon}
• SLE and LLE for tri-butylphosphate or tri-octylamine contained systems; extractive solvents of Molybdenum
• Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 1
• The solid-liquid phase diagrams of binary mixtures of even saturated fatty alcohols
• Liquid-liquid phase equilibrium of (piperidinium-based ionic liquid + an alcohol) binary systems and modelling with NRHB and PCP-SAFT
• Isobaric vapor-liquid equilibrium for binary systems containing benzothiophene
• Liquid phase equilibria of the system (water + phosphoric acid + 1-octanol) at T = (298.2, 308.2, and 318.2) K
• Solid-liquid equilibrium, excess molar volume, and deviations in the molar refractivity for the binary and ternary mixtures of Alamine 304-1 with 1-octanol, 2-octanol, and 1-decanol
• Phase behaviour of ionic liquid 1-butyl-1-methylpyrrolidinium tris(pentafluoroethyl)trifluorophosphate with alcohols, water and aromatic hydrocarbons
• Solubility and tie line data for the aqueous solutions of butyric acid with 1-octanol and 2-ethyl-1-hexanol at various temperatures
• Towards automated characterisation of liquid-liquid equilibria
• Unusual behavior of the isotope effect on miscibility of 1-hexyl-3-methylimidazolium bis(trifluorosulfonyl)imide with 1-alkanols
• Ternary phase diagrams for aqueous mixtures of butyric acid with several solvents: experimental and correlated data
• Modeling extraction equilibria of butyric acid distributed between water and tri-n-butyl amine/diluent or tri-n-butyl phosphate/diluent system: Extension of the LSER approach
• Phase behaviour of tricyanomethanide-based ionic liquids with alcohols and hydrocarbons
• The role of organic diluents in the aspects of equilibrium, kinetics and thermodynamic model for silver ion extraction using an extractant D2EHPA
• Solubility of pharmaceuticals in water and alcohols
• Atmospheric densities and interfacial tensions for 1- alkanol (1-butanol to 1-octanol) + water and ether (MTBE, ETBE, DIPE, TAME and THP) + water demixed mixtures.
• Phase equilibrium for ternary liquid systems of water + di-(2- ethylhexyl)phosphoric acid + organic diluents: Thermodynamic study
• Determination and prediction of solubilities of active pharmaceutical ingredients in selected organic solvents
• Study of phase equilibria and the physicochemical properties of selected pharmaceuticals
• An experimental investigation on the solubility of methane in 1-octanol and n-dodecane at ambient temperatures
• Enhanced partition model of 4-nitrophenol in water - octanol system. Effects of association/dissociation processes
• Equilibrium data and GC-PC SAFT predictions for furanic extraction
• Effect of polarity and temperature on the binary interaction between D2EHPA extractant and organic solvents (kerosene, n-heptane, chlorobenzene and 1-octanol): Experimental and thermodynamics
• Solubility and dissolution characteristics of capecitabine in pure lower alcohols and water with methanol mixture solvents at atmospheric pressure and different temperatures
• Study of the physicochemical properties of protein kinase CK2 inhibitors -TBBt, TBBi and 2-Me-TBBi
• Study of molecular interactions and preferential solvation in binary mixtures of cyclohexane and (C5-C10) 1-alkanol by Kirkwood-Buff integrals
• Isothermal (vapour + liquid) equilibrium at several temperatures of (1-chlorobutane + 1-octanol, or 1-decanol)
• Excess molar volumes and viscosities of (1,1,2,2-tetrabromoethane + 1-alkanols) at T = (293.15 and 303.15) K
• Densities, excess molar volumes, and refractive indices of 1,1,2,2-tetrachloroethane and 1-alkanols binary mixtures
• (Liquid + liquid) phase equilibria of 1-alkyl-3-methylimidazolium methylsulfate with alcohols, or ethers, or ketones
• Densities, excess molar volumes, and refractive indices of 1,1,2,2-tetrabromoethane and 1-alkanols binary mixtures
• (Liquid + liquid) equilibria of (water + propionic acid + alcohol) ternary systems
• Excess molar volumes of binary mixtures of 1,3-dimethylimidazolidin-2-one with an alkan-1-ol at the temperatures 283.15 K, 298.15 K, and 313.15 K
• Phase equilibria of didecyldimethylammonium nitrate ionic liquid with water and organic solvents
• Experimental study and ERAS modeling of the excess molar enthalpy of (acetonitrile + 1-heptanol or 1-octanol) mixtures at (298.15, 313.15, and 323.15) K and atmospheric pressure
• Study of molecular interactions in binary liquid mixtures of 1-octanol with n-hexane, n-octane, and n-decane using volumetric, viscometric, and acoustic properties
• Evaluation of (vapor + liquid) equilibria for the binary systems (1-octanol + cyclohexane) and (1-octanol + n-hexane), at low alcohol compositions
• (Liquid + liquid) equilibria of (water + lactic acid + alcohol) ternary systems
• Molar excess enthalpies at T = 298.15 K for (1-alkanol + dibutylether) systems
• Volumetric, acoustic, and viscometric studies of molecular interactions in binary mixtures of diethylene glycol monomethyl ether with 1-alkanols at temperatures from (293.15 to 308.15) K
• Partial molar volumes of some drug and pro-drug substances in 1-octanol at T = 298.15 K
• Solubility and pKa of select pharmaceuticals in water, ethanol, and 1-octanol
• Thermodynamic aspects of solubility, solvation and partitioning processes of some sulfonamides
• Thermophysical properties and phase equilibria study of the binary systems {N-hexylquinolinium bis(trifluoromethylsulfonyl)imide + aromatic hydrocarbons, or an alcohol}
• Excess molar enthalpies of binary systems containing 2-octanone, hexanoic acid, or octanoic acid at T = 298.15 K
• PrhoT measurements and derived properties of liquid 1-alkanols
• Ternary equilibrium data of mixtures consisting of 2-butanol, water, and heavy alcohols at T = 298.2 K
• Studies of thermophysical properties of binary liquid mixtures of amine and alcohols at various temperatures
• Partition coefficient n-octanol/water of propranolol and atenolol at different temperatures: Experimental and theoretical studies
• A thermodynamic study of solute solvent interactions through dielectric properties of the mixtures consisting of 1,4-butanediol, 1-octanol, and 1,4-dioxane at different temperatures
• Solubility of ionic liquids in water and octan-1-ol and octan-1-ol/water, or 2-phenylethanol/water partition coefficients
• Tie-line data for the aqueous solutions of phenol with organic solvents at T = 298.2 K
• Physico-chemical properties of binary mixtures of N,N-dimethylformamide with 1-octanol, 1-nonanol and 1-decanol at different temperatures
• Ultrasonic study of molecular interactions in binary mixtures of methyl acrylate with 1-alkanols (C4 to C10) at temperatures from (288.15 to 318.15) K
• Volume effects for binary mixtures of propane-1,2-diol with methanol, propan-1-ol, hexan-1-ol, octan-1-ol, or nonan-1-ol at temperatures (293.15 to 318.15) K
• Thermodynamic, transport and excess properties of 2-butoxy ethanol +1-alkanol (C6,C8,C10) at different temperatures
• Thermodynamic aspects of solubility and partitioning processes of some sulfonamides in the solvents modeling biological media
• Volumetric and compressibility studies on tri-n-butyl phosphate (TBP)-phase modifier (1-octanol, 1-decanol and isodecanol) interactions from T = (298.15 to 323.15) K
• Densities, speeds of sound and viscosities of binary mixtures of tetrahydrofuran with 1-hexanol, 1-octanol and 1-decanol at T = (298.15 to 313.15) K
• Effect of temperature and chain length on the viscosity and surface tension of binary systems of N,N-dimethylformamide with 1-octanol, 1-nonanol and 1-decanol
• The physicochemical properties and solubility of pharmaceuticals - Methyl xanthines
• Measurements and equation-of-state modelling of thermodynamic properties of binary mixtures of 1-butyl-1-methylpyrrolidinium tetracyanoborate ionic liquid with molecular compounds
• Thermodynamics of mixing for binary mixtures of 1-octanol and 1-decanol with n-dodecane and ternary mixture of (TBP + 1-octanol + dodecane) at T = (298.15 to 323.15) K
• Solution thermodynamics of pyrazinamide, isoniazid, and p-aminobenzoic acid in buffers and octanol
• Impact of structural modification of 1,2,4-thiadiazole derivatives on thermodynamics of solubility and solvation processes in 1-octanol and n-hexane
• Experimental solubility for betulin and estrone in various solvents within the temperature range T = (293.2 to 328.2) K
• Experimental solubility of diosgenin and estriol in various solvents between T = (293.2-328.2) K
• Studies on the importance of chain length of alkanols on the thermodynamic and transport properties of liquid mixtures at various temperatures
• Physico-chemical characterization antituberculosis thioacetazone: Vapor pressure, solubility and lipophilicity
• FT-IR studies and excess thermodynamic properties of binary liquid mixtures 2-(2-butoxyethoxy) ethanol with 1-hexanol, 1-octanol and 1-decanol at different temperatures
• A thermodynamic study of sublimation, dissolution and distribution processes of anti-inflammatory drug Clonixin
• Solubility and vapor pressure data of bioactive 6-(acetylamino)-N-(5-ethyl-1,3,4-thiadiazol-2-yl) hexanamide
• Thermodynamic study of aceclofenac solubility, distribution and sublimation
• Thermophysical properties and thermodynamic phase behavior of ionic liquids
• Excess molar enthalpies and heat capacities of dimethyl sulfoxide + seven normal alkanols at 303.15K and atmospheric pressure
• Volumetric and transport properties of ternary mixtures containing 1-alkanol + ethyl ethanoate + cyclohexane at 303.15 K: Experimental data, correlation and prediction by ERAS model
• Measurement and Correlation for Solubility of Dexibuprofen in Different Solvents from (263.15 to 293.15) K
• Vapor pressure of 1-octanol below 5 kPa using DSC
• Effect of chain length of alcohol on thermodynamic properties of their binary mixtures with benzylalcohol
• Thermogravimetric measurement of evaporation: Data analysis based on the Stefan tube
• Thermodynamics of mixtures containing amines. XVI. CE pm of 1-butanol, 1-octanol or 1-decanol + benzylamine systems at (298.15, 308.15, 318.15 and 333.15) K
• The solubility of ethionamide and structural analogues in buffer solutions, octanol and hexane at several temperatures
• Isobaric phase equilibrium of morpholine + 1-decanol, volumetric properties and molar refractivity from 293.15 to 333.15 K of morpholine + 1-decanol and 1-octanol + toluene system with applications of Prigogine-Flory-Patterson theory
• On the photothermal characterization of liquid thermoelectrics. New methodology based on coupled pyroelectric-Seebeck effects, together with frequency and thickness scanning procedures
• Physico-chemical study of bioactive N-(5-ethyl-1,3,4-thiadiazole-2-yl)-4-nitrobenzamide: Sublimation, solubility and distribution
• Experimental solubility of clotrimazole and some thermodynamic aspects of dissolution in different solvents
• Thermodynamic and spectral studies of molecular interactions in binary liquid mixtures of 1-butoxy-2- propanol with 1-alcohols
• Solubility and distribution of salinazid and vanillin isoniazid in the solvents modeling biological media
• Densities, Viscosities, and Refractive Indices of Dimethyl Carbonate + 1-Hexanol/1-Octanol Binary Mixtures at Different Temperatures
• Thermodynamics of 1,3-dimethylurea in eight alcohols
• Ternary and Quaternary Liquid-Liquid Equilibria for Systems of Methyl Butyl Ketone + Water + Hydroquinone + Phenol at 313.2 K and Atmospheric Pressure
• Equilibrium Study on the Extraction of Levulinic Acid from Aqueous Solution with Aliquat 336 Dissolved in Different Diluents: Solvent s Polarity Effect and Column Design
• Sulfasalazine: Dissolution and Distribution in Pharmaceutically Relevant Mediums
• Densities and Viscosities for Binary Liquid Mixtures of n-Undecane + 1-Heptanol, 1-Octanol, 1-Nonanol, and 1-Decanol from 283.15 to 363.15 K at 0.1 MPa
• Measurement and Modeling of Solubility of para-tert-Butylbenzoic Acid in Pure and Mixed Organic Solvents at Different Temperatures
• L(+)-tartaric Acid Separations Using Aliquat 336 in n-Heptane, Kerosene, and 1-Octanol at 300 +- 1 K
• Extraction of Citric Acid and Maleic Acid from Their Aqueous Solutions Using a Phosphorus-Bonded Extractant, Tri-n-octylphosphineoxide, and a Secondary Amine, Dioctylamine
• Vapor Pressure and Isobaric Vapor-Liquid Equilibrium for Binary Systems of Furfural, 2-Acetylfuran, and 5-Methylfurfural at 3.60 and 5.18 kPa
• Thermodynamic Aspects of Solubility and Solvation of Bioactive Bicyclic Derivatives in Organic Solvents
• High-Pressure Phase Equilibria of Carbon Dioxide + 1-Octanol Binary System
• Physical Behavior of the Phases from the Liquid-Liquid Equilibrium of Citrus Essential Oils Systems at 298.2 K
• Determination of Solubility and Thermodynamic Properties of Benzophenone in Different Pure Solvents
• Correlation Studies of Cyclohexanone/(C5-C10) Alkan-1-ol Binary Mixtures: PC-SAFT Model and Free Volume Theory
• Experiment and Computation of Solubility and Dissolution Properties for Enalapril Maleate and Its Intermediate in Pure Solvents
• Liquid-Liquid Equilibrium for Ternary Systems of Water + 2,2,3,3-Tetrafluoro-1-propanol + Anisole/1-Octanol at 298.2, 308.2, and 318.2 K
• Investigation of Molecular Interactions in Binary Mixtures of n-Butyl Acetate and (C6 - C10) 1-Alkanol: PC-SAFT Model
• Low-Pressure VLE Measurements and Thermodynamic Modeling, with PSRK and NRTL, of Binary 1-Alcohol + n-Alkane Systems
• Viscosity and Density of n-Alcohols at Temperatures between (298.15 and 323.15) K and Pressures up to 30 MPa
• Experimental Study on Reactive Extraction of Malonic Acid with Validation by Fourier Transform Infrared Spectroscopy
• Viscosities and Densities of Fatty Alcohol Mixtures from 298.15 to 338.15 K: Estimation by Kay's Rule and Prediction by the UNIFAC-VISCO and GC-UNIMOD Group Contribution Methods
• Thermodynamic Modeling of Triglycerides using PC-SAFT
• Solubility Determination and Thermodynamic Modeling of Buprofezin in Different Solvents and Mixing Properties of Solutions
• Kirkwood-Buff Integrals, Excess Volume, and Preferential Solvation in Pentanoic Acid/(C5-C10) 1-Alkanol Binary Mixtures
• Thermodynamic Studies of Solubility for Naphthalene in 12 Solvents from 279 to 330 K
• Parametric Analysis of Mandelic Acid Separation from Aqueous Solutions by Using Secondary Amine Mixture (Amberlite LA-2) in Various Diluents
• Reactive Extraction of Gallic Acid Using Tributyl Phosphate in Different Classes of Diluents
• Solubility of d-Tryptophan and l-Tyrosine in Several Organic Solvents: Determination and Solvent Effect
• Solubility Measurement and Phase Equilibrium Modeling of 2-Aminobenzamide in 15 Pure Solvents
• Solid-Liquid Equilibrium Solubility, Thermodynamic Properties, and Molecular Simulation of Phenylphosphonic Acid in 15 Pure Solvents at Different Temperatures
• Solubility and Thermodynamic Modeling of Sulfanilamide in 12 Mono Solvents and 4 Binary Solvent Mixtures from 278.15 to 318.15 K
• Thermodynamic Properties of 1-Hexyl-3-methylimidazolium Nitrate and 1-Alkanols Mixtures: PC-SAFT Model
• Liquid-Liquid Equilibria for the Ternary and Quaternary Systems of Water + Trimethylolpropane + (2-Ethylhexan-1-ol/Octan-1-ol) + Formaldehyde at 298.15 K
• Measurements of the Thermal Conductivity of n-Octane, Isooctane, 1-Octene, and 1-Octanol in the Temperature Range from 253 to 393 K at Pressures up to 30 MPa
• Solubility measurement and thermodynamic model correlation of sancycline in twelve pure solvents
• Excess molar volumes and enthalpies of mixing for the ternary system (butyl butyrate + 1-octanol + dodecane) at the temperature 308.15 K.
• Vapor Liquid Equilibrium between (278.15 and 323.15) K and Excess Functions at T ) 298.15 K for 1-Bromobutane with 1-Octanol or 1-Decanol
• Experimental Solid + Liquid Equilibria and Excess Molar Volume of Alkanol + Octylamine Mixtures. Analysis in Terms of ERAS, DISQUAC, and Modified UNIFAC
• Density, Surface Tension, and Refractive Index of Octane + 1-Alkanol Mixtures at T ) 298.15 K.
• Heat Capacities and Derived Thermodynamic Functions of 1-Hexanol, 1-Heptanol, 1-Octanol, and 1-Decanol between 5 K and 390 K
• Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
• Pressure-Volume-Temperature Properties for 1-Octanol + Acetophenone, Poly(Propylene Glycol) + 1-Octanol + Acetophenone, and Poly(Ethylene Glycol) + Poly(Ethylene Glycol Methyl Ether) + Anisole
• Measurement of Density and Viscosity of Binary 1-Alkanol Systems (C8-C11) at 101 kPa and Temperatures from (283.15 to 313.15) K
• Experimental (Solid + Liquid) and (Liquid + Liquid) Equilibria and Excess Molar Volume of Alkanol + Acetonitrile, Propanenitrile, and Butanenitrile Mixtures
• Solubility of Berberine Chloride in Various Solvents
• Density and Surface Tension Variation with Temperature for Heptane + 1-Alkanol
• Densities, Viscosities, and Ultrasonic Velocity Studies of Binary Mixtures of Chloroform with Octan-1-ol and Decan-1-ol at (303.15 and 313.15) K
• Effect of Pressure on the Static Relative Permittivities of Alkan-1-ols at 298.15 K
• Densities, Viscosities, and Speed of Sound Studies of Binary Mixtures of Methylbenzene with Heptan-1-ol, Octan-1-ol, and Decan-1-ol at (303.15 and 313.15) K
• Fluid-Phase Behavior of {1-Hexyl-3-methylimidazolium Bis(trifluoromethylsulfonyl) Imide, [C6mim][NTf2], + C2-C8 n-Alcohol} Mixtures: Liquid-Liquid Equilibrium and Excess Volumes
• Acoustical and Excess Properties of {Chlorobenzene + 1-Hexanol, or 1-Heptanol, or 1-Octanol, or 1-Nonanol, or 1-Decanol} at (298.15, 303.15, 308.15, and 313.15) K
• Viscosities and Interfacial Properties of I-Methyl-3-butylimidazolium Hexafluorophosphate and 1-Isobutenyl-3-methylimidazolium Tetrafluoroborate Ionic Liquids
• Speeds of Sound, Densities, Isobaric Thermal Expansion, Compressibilities, and Internal Pressures of Heptan-1-ol, Octan-1-ol, Nonan-1-ol, and Decan-1-ol at Temperatures from (293 to 318) K and Pressures up to 100 MPa
• Determination and Correlation for Solubilities of Ofloxacin, Norfloxacin, Lomefloxacin, Ciprofloxacin, Pefloxacin, and Pipemidic Acid in 1-Octanol from (293.15 to 333.15) K
• Density, Viscosity, and Speed of Sound of (1-Octanol + 2-Methoxyethanol), (1-Octanol + N,N-Dimethylacetamide), and (1-Octanol + Acetophenone) at Temperatures of (298.15, 308.15, and 318.15) K
• Thermodynamics of Dissolution for Bis(triazine)-Bipyridine-Class Ligands in Different Diluents and Its Reflection on Extraction
• Volumetric Properties, Viscosities, and Isobaric Heat Capacities of Imidazolium Octanoate Protic Ionic Liquid in Molecular Solvents
• Measurements, Correlations, and Mod. UNIFAC (Do) Prediction of (Solid-Liquid) Phase Equilibria Diagrams in Binary Systems (Aliphatic Ketone + an Alcohol)
• Liquid-Liquid Phase Behavior of Solutions of 1-Hexyl-3-methylimidazolium Bis((trifluoromethyl)sulfonyl)amide (C6mimNTf2) in n-Alkyl Alcohols
• Measurement and Study on the Liquid Liquid Equilibrium of Ionic Liquids with Aliphatic Alcohols
• Densities and Viscosities of Four Binary Diethyl Carbonate + 1-Alcohol Systems from (288.15 to 313.15) K
• Micellar Properties and Related Thermodynamic Parameters of Aqueous Anionic Surfactants in the Presence of Monohydric Alcohols
• Liquid Liquid Phase Equilibria of 1-Propanol + Water + n-Alcohol Ternary Systems at 298.15 K and Atmospheric Pressure
• Liquid Liquid Phase Behavior of Solutions of 1-Butyl-3-methylimidazolium Bis((trifluoromethyl)sulfonyl)amide (C4mimNTf2) in n-Alkyl Alcohols
• Solubility of Water in Octan-1-ol from (275 to 369) K
• Densities and Viscosities of Three Binary Monoglyme + 1-Alcohol Systems from (283.15 to 313.15) K
• Chemical Equilibrium of the Liquid-Phase Dehydration of 1-Octanol to 1-(Octyloxy)octane
• Liquid Liquid Phase Behavior of Solutions of 1,3-Dimethylimidazolium- and 1-Methyl-3-propylimidazolium Bis((trifluoromethyl)sulphonyl)amide (C1,3mimNTf2) in n-Alkyl Alcohols
• Experimental Study of Chemical Equilibria in the Liquid-Phase Reaction between 1-Octanol and Ethanol to 1-Ethoxyoctane
• Solubility and Transfer Processes of Some Hydrazones in Biologically Relevant Solvents
• Density and Viscosity of the Binary Systems Ethanol + Butan-1-ol, + Pentan-1-ol, + Heptan-1-ol, + Octan-1-ol, Nonan-1-ol, + Decan-1-ol at 0.1 MPa and Temperatures from 283.15 K to 313.15 K
• Solubility Determination and Correlation of (2R,3S,4S,5S)-6-(Hydroxymethyl)-tetrahydro-2H-pyran-2,3,4, 5-tetraol in Fatty Alcohol
• Solubility and Solution Thermodynamics of Novel Bicyclic Derivatives of 1,3-Selenazine in Biological Relevant Solvents
• Comparison Study on Temperature Dependence of the Interfacial Tension of n-Alkane Water and n-Alcohol Water Two Binary Systems
• Impact of Sulfonamide Structure on Solubility and Transfer Processes in Biologically Relevant Solvents
• Deduction of Physicochemical Properties from Solubilities: 2,4-Dihydroxybenzophenone, Biotin, and Caprolactam as Examples
• Liquid Liquid Equilibrium for Ternary Systems Containing Water, Oleic Acid, and Alcohols at 313.15 K. Effect of Alcohol Chain Length
• Densities, Isothermal Compressibilities, and Isobaric Thermal Expansivities of Hexan-2-ol, Octan-1-ol, and Decan-1-ol from (313 to 363) K and Pressures up to 22 MPa
• Liquid Phase Behavior of Ionic Liquids with Water and 1-Octanol and Modeling of 1-Octanol/Water Partition Coefficients
• Densities and Excess Molar Volumes of N-Methylmorpholine + 1-Alkanol Systems at 298.15 K
• Densities, Excess Molar Volumes, and Isobaric Thermal Expansibilities for 1,2-Ethanediol + 1-Butanol, or 1-Hexanol, or 1-Octanol in the Temperature Range from (293.15 to 313.15) K
• Thermophysical Properties of an Insensitive Munitions Compound, 2,4-Dinitroanisole
• Solubilities of Benzoic Acid, p-Methylbenzoic Acid, m-Methylbenzoic Acid, o-Methylbenzoic Acid, p-Hydroxybenzoic Acid, and o-Nitrobenzoic Acid in 1-Octanol
• Solubility of 1-Alkyl-3-ethylimidazolium-Based Ionic Liquids in Water and 1-Octanol
• Solubility of Rifapentine in the Binary System of Acetic Acid and n-Octanol Solvent Mixtures
• Solubility of the Antimicrobial Agent Triclosan in Organic Solvents of Different Hydrogen Bonding Capabilities at Several Temperatures
• Phase Equilibria Study of the Binary Systems (N-Butyl-4-methylpyridinium Tosylate Ionic Liquid + Organic Solvent, or Water)
• Solubilities of Sulfamethazine, Sulfadimethoxine, Sulfamethoxydiazine, Sulfamonomethoxine, Sulfamethoxazole, and Sulfaquinoxaline in 1-Octanol from (298.15 to 333.15) K
• Comparison of the Efficiencies of Amine Extractants on Lactic Acid with Different Organic Solvents
• Interfacial Properties, Densities, and Contact Angles of Task Specific Ionic Liquids
• Volumetric and Viscometric Properties of Binary Liquid Mixtures of Ethylene Glycol Monomethyl Ether + 1-Hexanol, 1-Octanol, and 1-Decanol at Temperatures of T = (293.15, 298.15, 303.15, and 308.15) K
• Solid-Liquid Equilibria, Excess Molar Volumes, and Molar Refractivity Deviations for Extractive Solvents of Molybdenum
• Henry s Law Constants of Organic Compounds in Water and n-Octane at T = 293.2 K
• Liquid-Liquid Phase Behavior of Solutions of 1-Octyl- and 1-Decyl-3-methylimidazolium Bis(trifluoromethylsulfonyl)imide (C8,10mimNTf2) in n-Alkyl Alcohols
• Density and Viscosity of Binary Mixtures of {1-Butyl-3-methylimidazolium Thiocyanate + 1-Heptanol, 1-Octanol, 1-Nonanol, or 1-Decanol}
• Joback Method
• KDB
• Aqueous Solubility Prediction Method
• Estimated Solubility Method
• McGowan Method
• NIST Webbook
• The Yaws Handbook of Vapor Pressure

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