Chemical Properties of 1-Hexanol (CAS 111-27-3)

InChI

InChI=1S/C6H14O/c1-2-3-4-5-6-7/h7H,2-6H2,1H3

InChI Key

ZSIAUFGUXNUGDI-UHFFFAOYSA-N

Formula

C6H14O

SMILES

CCCCCCO

Molecular Weight¹

102.17

CAS

111-27-3

Other Names

• 1-Hexyl alcohol
• 1-Hydroxyhexane
• Amylcarbinol
• Caproyl alcohol
• Epal 6
• Hexan-1-ol
• Hexanol
• Hexanol-(1)
• Hexyl alcohol
• NSC 9254
• Pentylcarbinol
• n-C6H13OH
• n-Hexan-1-ol
• n-Hexanol
• n-Hexyl alcohol

• ω : Acentric Factor.
• PAff : Proton affinity (kJ/mol).
• T_ig : Autoignition Temperature (K).
• 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).
• 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).
• 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).
• γ : Surface Tension (N/m).
• 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.
• 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	0.5600		KDB
PAff	799.00	kJ/mol	NIST
Tig	577.59	K	KDB
ΔcH°liquid	[-3984.37; -3978.10]	kJ/mol
ΔcH°liquid	-3984.37 ± 0.44	kJ/mol	NIST
ΔcH°liquid	-3982.60 ± 0.92	kJ/mol	NIST
ΔcH°liquid	-3978.10 ± 2.00	kJ/mol	NIST
ΔcH°liquid	-3978.10	kJ/mol	NIST
μ	1.80	debye	KDB
η	[0.0044395; 0.0052910]	Pa×s
η	0.0052910	Pa×s	Studies...
η	0.0044395	Pa×s	Volumet...
LFL	1.20	% in Air	KDB
UFL	7.70	% in Air	KDB
Tflash,cc	338.15	K	KDB
Tflash,oc	335.93	K	KDB
ΔfG°	-135.70	kJ/mol	KDB
ΔfH°gas	-317.80	kJ/mol	KDB
ΔfH°liquid	[-387.70; -377.50]	kJ/mol
ΔfH°liquid	-377.50 ± 0.44	kJ/mol	NIST
ΔfH°liquid	-379.40 ± 1.00	kJ/mol	NIST
ΔfH°liquid	-383.90 ± 2.00	kJ/mol	NIST
ΔfH°liquid	-387.70	kJ/mol	NIST
ΔfusH°	16.73	kJ/mol	Heat Ca...
ΔvapH°	[59.10; 69.20]	kJ/mol
ΔvapH°	61.61	kJ/mol	NIST
ΔvapH°	59.10	kJ/mol	NIST
ΔvapH°	59.90	kJ/mol	NIST
ΔvapH°	61.70 ± 0.30	kJ/mol	NIST
ΔvapH°	61.10	kJ/mol	NIST
ΔvapH°	62.10 ± 0.20	kJ/mol	NIST
ΔvapH°	61.50	kJ/mol	NIST
ΔvapH°	61.60	kJ/mol	NIST
ΔvapH°	61.85 ± 0.20	kJ/mol	NIST
ΔvapH°	60.80 ± 0.20	kJ/mol	NIST
ΔvapH°	61.60 ± 0.20	kJ/mol	NIST
ΔvapH°	61.60 ± 0.20	kJ/mol	NIST
ΔvapH°	62.80 ± 1.30	kJ/mol	NIST
ΔvapH°	Outlier 69.20	kJ/mol	NIST
IE	[9.89; 10.35]	eV
IE	9.89	eV	NIST
IE	10.35	eV	NIST
log10WS	[-1.24; -1.24]
log10WS	-1.24		Aq. Sol...
log10WS	-1.24		Estimat...
logPoct/wat	1.559		Crippen Calculated Property
McVol	101.270	ml/mol	McGowan Calculated Property
NFPA Fire	2		KDB
NFPA Health	1		KDB
Pc	[3413.00; 3420.00]	kPa
Pc	3417.00	kPa	KDB
Pc	3420.00 ± 20.00	kPa	NIST
Pc	3420.00 ± 50.00	kPa	NIST
Pc	3413.00 ± 6.00	kPa	NIST
Pc	3413.00 ± 20.00	kPa	NIST
ρc	[259.52; 267.70]	kg/m3
ρc	263.61 ± 2.04	kg/m3	NIST
ρc	267.70	kg/m3	NIST
ρc	259.52 ± 6.13	kg/m3	NIST
ρc	267.70 ± 3.07	kg/m3	NIST
Inp	[136.97; 896.80]
Inp	889.40		NIST
Inp	896.80		NIST
Inp	870.10		NIST
Inp	866.30		NIST
Inp	862.30		NIST
Inp	861.10		NIST
Inp	859.90		NIST
Inp	859.54		NIST
Inp	848.00		NIST
Inp	848.20		NIST
Inp	831.90		NIST
Inp	836.60		NIST
Inp	878.00		NIST
Inp	879.50		NIST
Inp	822.00		NIST
Inp	851.00		NIST
Inp	845.00		NIST
Inp	823.00		NIST
Inp	863.00		NIST
Inp	860.00		NIST
Inp	854.00		NIST
Inp	852.00		NIST
Inp	831.00		NIST
Inp	838.00		NIST
Inp	856.00		NIST
Inp	853.00		NIST
Inp	850.00		NIST
Inp	831.20		NIST
Inp	831.00		NIST
Inp	855.00		NIST
Inp	856.00		NIST
Inp	832.00		NIST
Inp	862.00		NIST
Inp	821.00		NIST
Inp	854.00		NIST
Inp	867.00		NIST
Inp	869.00		NIST
Inp	856.00		NIST
Inp	860.00		NIST
Inp	878.00		NIST
Inp	860.00		NIST
Inp	859.00		NIST
Inp	868.00		NIST
Inp	868.00		NIST
Inp	867.00		NIST
Inp	881.00		NIST
Inp	881.00		NIST
Inp	858.00		NIST
Inp	859.00		NIST
Inp	857.00		NIST
Inp	858.00		NIST
Inp	858.00		NIST
Inp	858.00		NIST
Inp	858.00		NIST
Inp	858.00		NIST
Inp	853.00		NIST
Inp	865.00		NIST
Inp	858.00		NIST
Inp	850.00		NIST
Inp	865.00		NIST
Inp	868.00		NIST
Inp	867.00		NIST
Inp	867.00		NIST
Inp	864.00		NIST
Inp	862.00		NIST
Inp	854.00		NIST
Inp	865.00		NIST
Inp	867.00		NIST
Inp	852.00		NIST
Inp	871.00		NIST
Inp	871.00		NIST
Inp	870.00		NIST
Inp	867.00		NIST
Inp	880.00		NIST
Inp	880.00		NIST
Inp	876.00		NIST
Inp	862.00		NIST
Inp	867.00		NIST
Inp	867.00		NIST
Inp	884.00		NIST
Inp	867.00		NIST
Inp	867.00		NIST
Inp	867.00		NIST
Inp	874.00		NIST
Inp	874.00		NIST
Inp	867.00		NIST
Inp	841.00		NIST
Inp	847.90		NIST
Inp	865.10		NIST
Inp	885.00		NIST
Inp	872.00		NIST
Inp	867.00		NIST
Inp	843.00		NIST
Inp	869.00		NIST
Inp	849.00		NIST
Inp	849.00		NIST
Inp	863.00		NIST
Inp	867.00		NIST
Inp	860.00		NIST
Inp	854.00		NIST
Inp	854.00		NIST
Inp	854.00		NIST
Inp	876.00		NIST
Inp	880.00		NIST
Inp	852.00		NIST
Inp	849.00		NIST
Inp	860.00		NIST
Inp	866.00		NIST
Inp	867.00		NIST
Inp	859.00		NIST
Inp	861.00		NIST
Inp	869.00		NIST
Inp	863.00		NIST
Inp	852.70		NIST
Inp	854.00		NIST
Inp	880.00		NIST
Inp	857.00		NIST
Inp	869.00		NIST
Inp	870.00		NIST
Inp	859.00		NIST
Inp	861.00		NIST
Inp	851.00		NIST
Inp	853.00		NIST
Inp	854.00		NIST
Inp	854.00		NIST
Inp	867.00		NIST
Inp	852.00		NIST
Inp	852.00		NIST
Inp	859.00		NIST
Inp	861.00		NIST
Inp	859.00		NIST
Inp	859.00		NIST
Inp	866.00		NIST
Inp	858.00		NIST
Inp	889.00		NIST
Inp	869.00		NIST
Inp	860.00		NIST
Inp	848.00		NIST
Inp	857.00		NIST
Inp	861.00		NIST
Inp	859.00		NIST
Inp	867.00		NIST
Inp	872.00		NIST
Inp	869.00		NIST
Inp	865.60		NIST
Inp	828.00		NIST
Inp	828.00		NIST
Inp	867.00		NIST
Inp	884.00		NIST
Inp	876.00		NIST
Inp	853.00		NIST
Inp	876.00		NIST
Inp	865.00		NIST
Inp	863.00		NIST
Inp	872.00		NIST
Inp	870.00		NIST
Inp	871.00		NIST
Inp	876.00		NIST
Inp	876.00		NIST
Inp	867.00		NIST
Inp	871.00		NIST
Inp	867.00		NIST
Inp	871.00		NIST
Inp	888.00		NIST
Inp	873.00		NIST
Inp	868.00		NIST
Inp	874.00		NIST
Inp	868.00		NIST
Inp	848.00		NIST
Inp	851.00		NIST
Inp	849.00		NIST
Inp	856.00		NIST
Inp	868.00		NIST
Inp	853.00		NIST
Inp	890.00		NIST
Inp	870.00		NIST
Inp	871.00		NIST
Inp	876.00		NIST
Inp	874.00		NIST
Inp	852.00		NIST
Inp	865.00		NIST
Inp	868.00		NIST
Inp	861.00		NIST
Inp	863.00		NIST
Inp	874.00		NIST
Inp	870.00		NIST
Inp	867.00		NIST
Inp	863.00		NIST
Inp	860.00		NIST
Inp	860.00		NIST
Inp	868.00		NIST
Inp	873.00		NIST
Inp	875.00		NIST
Inp	839.00		NIST
Inp	868.00		NIST
Inp	871.00		NIST
Inp	878.00		NIST
Inp	879.00		NIST
Inp	843.00		NIST
Inp	868.00		NIST
Inp	868.00		NIST
Inp	878.00		NIST
Inp	871.00		NIST
Inp	871.00		NIST
Inp	870.00		NIST
Inp	870.00		NIST
Inp	859.00		NIST
Inp	847.00		NIST
Inp	845.00		NIST
Inp	887.00		NIST
Inp	866.00		NIST
Inp	872.00		NIST
Inp	882.00		NIST
Inp	888.00		NIST
Inp	878.10		NIST
Inp	855.00		NIST
Inp	832.00		NIST
Inp	867.00		NIST
Inp	858.00		NIST
Inp	872.00		NIST
Inp	850.00		NIST
Inp	862.00		NIST
Inp	862.00		NIST
Inp	864.00		NIST
Inp	878.00		NIST
Inp	865.00		NIST
Inp	885.00		NIST
Inp	866.00		NIST
Inp	859.00		NIST
Inp	847.00		NIST
Inp	878.00		NIST
Inp	866.00		NIST
Inp	843.00		NIST
Inp	839.00		NIST
Inp	858.00		NIST
Inp	858.00		NIST
Inp	858.00		NIST
Inp	859.00		NIST
Inp	866.00		NIST
Inp	867.00		NIST
Inp	852.00		NIST
Inp	859.00		NIST
Inp	868.00		NIST
Inp	849.00		NIST
Inp	868.00		NIST
Inp	872.00		NIST
Inp	872.00		NIST
Inp	848.00		NIST
Inp	867.00		NIST
Inp	859.11		NIST
Inp	888.00		NIST
Inp	855.00		NIST
Inp	867.00		NIST
Inp	874.00		NIST
Inp	877.00		NIST
Inp	854.00		NIST
Inp	849.00		NIST
Inp	871.00		NIST
Inp	848.00		NIST
Inp	862.00		NIST
Inp	858.00		NIST
Inp	870.00		NIST
Inp	878.00		NIST
Inp	849.00		NIST
Inp	850.00		NIST
Inp	850.00		NIST
Inp	851.00		NIST
Inp	852.00		NIST
Inp	848.00		NIST
Inp	862.00		NIST
Inp	872.00		NIST
Inp	858.00		NIST
Inp	848.00		NIST
Inp	848.00		NIST
Inp	846.00		NIST
Inp	848.00		NIST
Inp	849.00		NIST
Inp	848.00		NIST
Inp	847.00		NIST
Inp	867.00		NIST
Inp	856.00		NIST
Inp	856.00		NIST
Inp	852.00		NIST
Inp	849.00		NIST
Inp	864.00		NIST
Inp	859.00		NIST
Inp	858.00		NIST
Inp	862.00		NIST
Inp	874.00		NIST
Inp	888.00		NIST
Inp	863.00		NIST
Inp	872.00		NIST
Inp	863.00		NIST
Inp	876.00		NIST
Inp	857.00		NIST
Inp	874.00		NIST
Inp	867.00		NIST
Inp	857.00		NIST
Inp	871.00		NIST
Inp	872.00		NIST
Inp	860.00		NIST
Inp	872.00		NIST
Inp	861.00		NIST
Inp	869.00		NIST
Inp	876.00		NIST
Inp	889.00		NIST
Inp	888.00		NIST
Inp	861.00		NIST
Inp	850.00		NIST
Inp	854.00		NIST
Inp	837.00		NIST
Inp	871.00		NIST
Inp	869.00		NIST
Inp	860.00		NIST
Inp	871.00		NIST
Inp	886.00		NIST
Inp	888.00		NIST
Inp	849.00		NIST
Inp	865.00		NIST
Inp	872.00		NIST
Inp	870.00		NIST
Inp	853.00		NIST
Inp	864.00		NIST
Inp	872.00		NIST
Inp	868.00		NIST
Inp	871.00		NIST
Inp	864.00		NIST
Inp	864.00		NIST
Inp	867.00		NIST
Inp	867.00		NIST
Inp	878.00		NIST
Inp	865.00		NIST
Inp	852.00		NIST
Inp	883.00		NIST
Inp	878.00		NIST
Inp	871.00		NIST
Inp	850.00		NIST
Inp	867.00		NIST
Inp	858.00		NIST
Inp	867.00		NIST
Inp	856.00		NIST
Inp	870.00		NIST
Inp	870.00		NIST
Inp	852.00		NIST
Inp	858.00		NIST
Inp	827.00		NIST
Inp	866.00		NIST
Inp	870.00		NIST
Inp	853.00		NIST
Inp	858.00		NIST
Inp	865.80		NIST
Inp	870.00		NIST
Inp	844.00		NIST
Inp	891.00		NIST
Inp	875.00		NIST
Inp	853.00		NIST
Inp	842.00		NIST
Inp	852.00		NIST
Inp	862.00		NIST
Inp	843.00		NIST
Inp	854.00		NIST
Inp	871.00		NIST
Inp	852.00		NIST
Inp	857.00		NIST
Inp	858.00		NIST
Inp	858.00		NIST
Inp	852.00		NIST
Inp	860.00		NIST
Inp	848.00		NIST
Inp	868.00		NIST
Inp	858.00		NIST
Inp	858.00		NIST
Inp	839.00		NIST
Inp	858.00		NIST
Inp	885.00		NIST
Inp	856.00		NIST
Inp	858.00		NIST
Inp	884.00		NIST
Inp	Outlier 136.97		NIST
Inp	853.00		NIST
Inp	874.00		NIST
Inp	863.00		NIST
Inp	860.00		NIST
Inp	839.00		NIST
Inp	843.00		NIST
Inp	871.00		NIST
Inp	845.00		NIST
Inp	888.00		NIST
Inp	858.00		NIST
Inp	864.00		NIST
Inp	859.00		NIST
Inp	866.00		NIST
Inp	849.00		NIST
Inp	867.00		NIST
Inp	848.00		NIST
Inp	847.00		NIST
Inp	850.00		NIST
Inp	852.00		NIST
Inp	880.00		NIST
Inp	865.10		NIST
Inp	869.00		NIST
Inp	852.70		NIST
Inp	870.00		NIST
Inp	854.00		NIST
Inp	857.00		NIST
Inp	Outlier 136.97		NIST
Inp	876.00		NIST
Inp	865.00		NIST
Inp	872.00		NIST
Inp	883.00		NIST
Inp	891.00		NIST
Inp	862.00		NIST
I	[1308.00; 1398.00]
I	1384.00		NIST
I	1384.00		NIST
I	1357.00		NIST
I	1332.00		NIST
I	1362.00		NIST
I	1378.00		NIST
I	1358.00		NIST
I	1348.00		NIST
I	1347.99		NIST
I	1346.20		NIST
I	1344.79		NIST
I	1348.98		NIST
I	Outlier 1315.00		NIST
I	1329.00		NIST
I	1326.00		NIST
I	1357.00		NIST
I	1350.00		NIST
I	Outlier 1321.00		NIST
I	1342.00		NIST
I	1355.00		NIST
I	1342.00		NIST
I	1350.00		NIST
I	1338.00		NIST
I	1347.00		NIST
I	1342.00		NIST
I	1339.00		NIST
I	Outlier 1316.00		NIST
I	Outlier 1316.00		NIST
I	1339.00		NIST
I	1357.00		NIST
I	1359.00		NIST
I	1359.00		NIST
I	1356.00		NIST
I	1359.00		NIST
I	1376.00		NIST
I	1356.00		NIST
I	Outlier 1308.00		NIST
I	1332.00		NIST
I	1339.00		NIST
I	1337.00		NIST
I	1362.00		NIST
I	1361.00		NIST
I	1361.00		NIST
I	1360.00		NIST
I	1360.00		NIST
I	1363.00		NIST
I	1363.00		NIST
I	1340.00		NIST
I	1351.00		NIST
I	1353.00		NIST
I	1356.00		NIST
I	1359.00		NIST
I	1360.00		NIST
I	1345.00		NIST
I	1363.00		NIST
I	1348.00		NIST
I	1343.00		NIST
I	1348.00		NIST
I	1339.00		NIST
I	1344.00		NIST
I	Outlier 1320.00		NIST
I	1353.00		NIST
I	1367.00		NIST
I	1363.00		NIST
I	1362.00		NIST
I	1356.00		NIST
I	1371.00		NIST
I	1371.00		NIST
I	1371.00		NIST
I	1344.00		NIST
I	1344.00		NIST
I	Outlier 1320.00		NIST
I	1344.00		NIST
I	1371.00		NIST
I	1338.00		NIST
I	1362.00		NIST
I	1335.00		NIST
I	1354.00		NIST
I	Outlier 1396.00		NIST
I	1343.00		NIST
I	1354.00		NIST
I	1358.00		NIST
I	1358.00		NIST
I	1358.00		NIST
I	1360.60		NIST
I	1343.00		NIST
I	1358.00		NIST
I	Outlier 1392.00		NIST
I	1356.00		NIST
I	1356.00		NIST
I	1353.00		NIST
I	1336.00		NIST
I	1355.00		NIST
I	1368.00		NIST
I	Outlier 1315.00		NIST
I	1351.00		NIST
I	1355.00		NIST
I	1351.00		NIST
I	1353.00		NIST
I	1356.00		NIST
I	1355.00		NIST
I	1333.00		NIST
I	1335.00		NIST
I	1349.00		NIST
I	1354.00		NIST
I	1367.00		NIST
I	1364.00		NIST
I	1348.00		NIST
I	1338.00		NIST
I	1345.00		NIST
I	1345.00		NIST
I	1361.00		NIST
I	1358.00		NIST
I	1325.00		NIST
I	1361.00		NIST
I	1353.00		NIST
I	1343.00		NIST
I	1353.00		NIST
I	1336.00		NIST
I	1348.00		NIST
I	1353.00		NIST
I	1353.00		NIST
I	1353.00		NIST
I	1357.00		NIST
I	1345.00		NIST
I	1337.00		NIST
I	1354.00		NIST
I	1356.00		NIST
I	1359.00		NIST
I	1343.00		NIST
I	Outlier 1318.00		NIST
I	Outlier 1314.00		NIST
I	1324.00		NIST
I	1362.00		NIST
I	1354.00		NIST
I	1359.00		NIST
I	1362.00		NIST
I	1360.00		NIST
I	1351.00		NIST
I	1372.00		NIST
I	1345.00		NIST
I	1370.00		NIST
I	1357.00		NIST
I	1356.00		NIST
I	1356.00		NIST
I	1361.00		NIST
I	1336.00		NIST
I	1342.00		NIST
I	1371.00		NIST
I	1356.00		NIST
I	1351.00		NIST
I	1344.00		NIST
I	1368.00		NIST
I	1359.00		NIST
I	1359.00		NIST
I	1386.00		NIST
I	1339.00		NIST
I	1336.00		NIST
I	1360.00		NIST
I	Outlier 1387.00		NIST
I	1357.00		NIST
I	1348.00		NIST
I	1345.00		NIST
I	1375.00		NIST
I	1357.00		NIST
I	1353.00		NIST
I	1356.00		NIST
I	1341.00		NIST
I	1363.00		NIST
I	1360.00		NIST
I	Outlier 1316.00		NIST
I	1357.00		NIST
I	1363.00		NIST
I	1363.00		NIST
I	1357.00		NIST
I	1348.00		NIST
I	1341.00		NIST
I	1341.00		NIST
I	1362.00		NIST
I	1350.00		NIST
I	1336.00		NIST
I	1352.00		NIST
I	Outlier 1321.00		NIST
I	1378.00		NIST
I	1367.00		NIST
I	1362.00		NIST
I	1346.00		NIST
I	Outlier 1311.00		NIST
I	1363.00		NIST
I	1341.00		NIST
I	1351.00		NIST
I	1353.00		NIST
I	1384.00		NIST
I	1379.00		NIST
I	Outlier 1398.00		NIST
I	1356.00		NIST
I	1356.00		NIST
I	1356.00		NIST
I	1362.00		NIST
I	1354.00		NIST
I	1349.00		NIST
I	1356.00		NIST
I	1358.00		NIST
I	1359.00		NIST
I	Outlier 1320.00		NIST
I	1357.00		NIST
I	1353.00		NIST
I	1350.00		NIST
I	1354.00		NIST
I	1354.00		NIST
I	Outlier 1392.00		NIST
I	1354.00		NIST
I	Outlier 1392.00		NIST
I	1386.00		NIST
I	1360.00		NIST
I	1350.00		NIST
I	1369.00		NIST
I	1374.00		NIST
I	1348.00		NIST
I	1348.00		NIST
I	1360.00		NIST
I	1360.00		NIST
I	1341.00		NIST
I	1352.00		NIST
I	1358.00		NIST
I	1341.00		NIST
I	Outlier 1316.00		NIST
I	1365.00		NIST
I	1359.00		NIST
I	1371.00		NIST
I	1325.00		NIST
I	1359.00		NIST
I	1357.00		NIST
I	1345.00		NIST
I	1366.00		NIST
I	1357.00		NIST
I	1360.00		NIST
I	Outlier 1320.00		NIST
I	1380.00		NIST
I	Outlier 1316.00		NIST
I	1353.00		NIST
I	1365.40		NIST
I	Outlier 1316.00		NIST
I	1352.00		NIST
I	1352.00		NIST
I	1349.00		NIST
I	1352.00		NIST
I	1366.00		NIST
I	1358.00		NIST
I	1361.00		NIST
I	Outlier 1321.00		NIST
I	1355.00		NIST
I	1371.00		NIST
I	1375.00		NIST
I	Outlier 1392.00		NIST
I	1361.00		NIST
I	1362.00		NIST
I	1354.00		NIST
I	1359.00		NIST
I	1361.00		NIST
I	1360.00		NIST
I	1366.00		NIST
I	1362.00		NIST
I	1360.00		NIST
I	1357.00		NIST
I	1340.00		NIST
I	1345.00		NIST
I	1366.00		NIST
I	1359.00		NIST
I	Outlier 1392.00		NIST
I	1366.00		NIST
I	1352.00		NIST
I	1336.00		NIST
I	Outlier 1392.00		NIST
I	1356.00		NIST
I	1345.00		NIST
I	Outlier 1392.00		NIST
I	1360.00		NIST
I	1354.00		NIST
I	1359.00		NIST
I	1331.00		NIST
I	1358.00		NIST
I	1356.00		NIST
I	Outlier 1392.00		NIST
I	1358.00		NIST
I	1346.00		NIST
I	1350.00		NIST
I	1362.00		NIST
I	1372.00		NIST
I	1360.00		NIST
I	1358.00		NIST
I	1356.00		NIST
I	1358.00		NIST
I	1360.00		NIST
I	1358.00		NIST
I	1368.00		NIST
I	1353.00		NIST
I	1343.00		NIST
I	1358.00		NIST
I	1362.00		NIST
I	Outlier 1316.00		NIST
I	1358.00		NIST
I	1373.00		NIST
I	1360.00		NIST
I	Outlier 1316.00		NIST
I	1360.00		NIST
I	1365.00		NIST
I	1363.00		NIST
I	1363.00		NIST
I	1348.00		NIST
I	1328.00		NIST
I	1354.00		NIST
I	1363.00		NIST
I	1363.00		NIST
I	1341.00		NIST
I	1336.00		NIST
I	1344.00		NIST
I	1365.00		NIST
I	Outlier 1316.00		NIST
I	1330.00		NIST
I	1347.00		NIST
I	1332.00		NIST
I	1332.00		NIST
I	1372.00		NIST
I	1354.00		NIST
I	1358.00		NIST
I	1360.00		NIST
I	1367.00		NIST
I	1352.00		NIST
I	Outlier 1316.00		NIST
I	1360.00		NIST
I	1351.00		NIST
I	1345.00		NIST
I	1339.00		NIST
I	1363.00		NIST
I	1371.00		NIST
I	Outlier 1396.00		NIST
I	1358.00		NIST
I	1356.00		NIST
I	1368.00		NIST
I	1353.00		NIST
I	1349.00		NIST
I	1338.00		NIST
I	1325.00		NIST
I	1336.00		NIST
I	1357.00		NIST
I	1359.00		NIST
I	1362.00		NIST
I	1355.00		NIST
I	1366.00		NIST
I	1352.00		NIST
I	Outlier 1392.00		NIST
I	1350.00		NIST
I	1365.00		NIST
I	1354.00		NIST
I	1344.00		NIST
I	1332.00		NIST
I	1375.00		NIST
I	1378.00		NIST
I	1379.00		NIST
I	1386.00		NIST
I	1348.00		NIST
I	1380.00		NIST
I	1384.00		NIST
I	1344.79		NIST
I	1342.00		NIST
S°gas	439.70 ± 2.10	J/mol×K	NIST
S°liquid	287.40	J/mol×K	NIST
Tboil	[409.15; 440.15]	K
Tboil	430.70	K	KDB
Tboil	430.75	K	Excess ...
Tboil	430.50	K	Phase e...
Tboil	430.11	K	Vapor-l...
Tboil	429.70	K	NIST
Tboil	431.20	K	NIST
Tboil	430.50	K	NIST
Tboil	430.00 ± 0.12	K	NIST
Tboil	430.50 ± 0.50	K	NIST
Tboil	430.40 ± 0.30	K	NIST
Tboil	430.25	K	NIST
Tboil	430.55 ± 0.50	K	NIST
Tboil	430.65 ± 0.70	K	NIST
Tboil	429.40 ± 0.70	K	NIST
Tboil	428.15 ± 1.00	K	NIST
Tboil	430.25	K	NIST
Tboil	428.15 ± 1.00	K	NIST
Tboil	427.65 ± 3.00	K	NIST
Tboil	430.15 ± 2.00	K	NIST
Tboil	429.65 ± 2.00	K	NIST
Tboil	431.15 ± 2.00	K	NIST
Tboil	426.65 ± 2.00	K	NIST
Tboil	430.55 ± 0.30	K	NIST
Tboil	426.90 ± 2.00	K	NIST
Tboil	430.45 ± 0.50	K	NIST
Tboil	428.65 ± 1.50	K	NIST
Tboil	430.27 ± 0.20	K	NIST
Tboil	429.65 ± 1.00	K	NIST
Tboil	430.95 ± 0.70	K	NIST
Tboil	429.65 ± 2.00	K	NIST
Tboil	425.65 ± 3.00	K	NIST
Tboil	429.75 ± 0.70	K	NIST
Tboil	430.15 ± 0.70	K	NIST
Tboil	428.90 ± 0.70	K	NIST
Tboil	429.90 ± 1.00	K	NIST
Tboil	428.65 ± 2.00	K	NIST
Tboil	430.65 ± 1.00	K	NIST
Tboil	431.05 ± 0.50	K	NIST
Tboil	428.65 ± 2.00	K	NIST
Tboil	428.45 ± 2.00	K	NIST
Tboil	429.60 ± 0.70	K	NIST
Tboil	430.55 ± 1.00	K	NIST
Tboil	430.62 ± 0.20	K	NIST
Tboil	428.85 ± 0.30	K	NIST
Tboil	Outlier 421.15 ± 2.00	K	NIST
Tboil	429.65 ± 0.50	K	NIST
Tboil	431.00 ± 0.30	K	NIST
Tboil	430.20 ± 0.50	K	NIST
Tboil	430.95 ± 0.50	K	NIST
Tboil	430.80 ± 0.30	K	NIST
Tboil	432.15 ± 2.00	K	NIST
Tboil	430.15 ± 0.70	K	NIST
Tboil	429.00 ± 0.40	K	NIST
Tboil	Outlier 440.15 ± 5.00	K	NIST
Tboil	431.15 ± 2.00	K	NIST
Tboil	Outlier 409.15 ± 3.00	K	NIST
Tboil	428.15 ± 2.00	K	NIST
Tboil	428.70 ± 0.70	K	NIST
Tboil	430.15 ± 3.00	K	NIST
Tboil	429.00 ± 3.00	K	NIST
Tboil	429.75 ± 1.00	K	NIST
Tboil	430.60 ± 1.00	K	NIST
Tboil	430.45 ± 2.00	K	NIST
Tboil	423.15 ± 4.00	K	NIST
Tc	610.30	K	KDB
Tfus	[224.75; 229.00]	K
Tfus	224.75	K	Aq. Sol...
Tfus	228.50	K	KDB
Tfus	229.00	K	Vapour ...
Ttriple	225.80 ± 0.30	K	NIST
Vc	[0.387; 0.387]	m3/kmol
Vc	0.387	m3/kmol	KDB
Vc	0.387	m3/kmol	NIST
Zc	0.2606010		KDB

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[207.67; 259.79]	J/mol×K	[428.86; 589.96]
Cp,gas	207.67	J/mol×K	428.86	Joback Calculated Property
Cp,gas	217.18	J/mol×K	455.71	Joback Calculated Property
Cp,gas	226.36	J/mol×K	482.56	Joback Calculated Property
Cp,gas	235.20	J/mol×K	509.41	Joback Calculated Property
Cp,gas	243.71	J/mol×K	536.26	Joback Calculated Property
Cp,gas	251.90	J/mol×K	563.11	Joback Calculated Property
Cp,gas	259.79	J/mol×K	589.96	Joback Calculated Property
Cp,liquid	[232.46; 249.15]	J/mol×K	[290.01; 303.74]
Cp,liquid	232.46	J/mol×K	290.01	NIST
Cp,liquid	236.50	J/mol×K	293.15	NIST
Cp,liquid	236.50	J/mol×K	293.15	NIST
Cp,liquid	244.80	J/mol×K	298.00	NIST
Cp,liquid	243.20	J/mol×K	298.15	NIST
Cp,liquid	239.68	J/mol×K	298.15	NIST
Cp,liquid	239.62	J/mol×K	298.15	NIST
Cp,liquid	240.57	J/mol×K	298.15	NIST
Cp,liquid	241.32	J/mol×K	298.15	NIST
Cp,liquid	240.65	J/mol×K	298.15	NIST
Cp,liquid	237.85	J/mol×K	298.15	NIST
Cp,liquid	241.32	J/mol×K	298.15	NIST
Cp,liquid	242.50	J/mol×K	298.15	NIST
Cp,liquid	249.15	J/mol×K	300.61	NIST
Cp,liquid	247.70	J/mol×K	303.74	NIST
η	[0.0014110; 0.0074590]	Pa×s	[283.15; 343.15]
η	0.0074590	Pa×s	283.15	Densiti...
η	0.0053350	Pa×s	293.15	Densiti...
η	0.0054120	Pa×s	293.15	A Study...
η	0.0046426	Pa×s	298.15	Densiti...
η	0.0045940	Pa×s	298.15	Acousti...
η	0.0046050	Pa×s	298.15	Densiti...
η	0.0045960	Pa×s	298.15	A Study...
η	0.0039985	Pa×s	303.15	Densiti...
η	0.0038290	Pa×s	303.15	Volumet...
η	0.0039640	Pa×s	303.15	A Study...
η	0.0039170	Pa×s	303.15	Densiti...
η	0.0039440	Pa×s	303.15	Densiti...
η	0.0037630	Pa×s	303.15	Densiti...
η	0.0038870	Pa×s	303.15	Acousti...
η	0.0038290	Pa×s	303.15	Thermod...
η	0.0033180	Pa×s	308.15	Density...
η	0.0034140	Pa×s	308.15	Densiti...
η	0.0033590	Pa×s	308.15	Acousti...
η	0.0034713	Pa×s	308.15	Densiti...
η	0.0029660	Pa×s	313.15	A Study...
η	0.0029600	Pa×s	313.15	Densiti...
η	0.0029140	Pa×s	313.15	Acousti...
η	0.0029370	Pa×s	313.15	Densiti...
η	0.0028790	Pa×s	313.15	Thermod...
η	0.0028790	Pa×s	313.15	Volumet...
η	0.0025180	Pa×s	318.15	Density...
η	0.0025810	Pa×s	318.15	Densiti...
η	0.0022510	Pa×s	323.15	Densiti...
η	0.0022760	Pa×s	323.15	Densiti...
η	0.0021720	Pa×s	323.15	Densiti...
η	0.0022150	Pa×s	323.15	Thermod...
η	0.0022150	Pa×s	323.15	Volumet...
η	0.0016540	Pa×s	333.15	Densiti...
η	0.0014110	Pa×s	343.15	Densiti...
ΔfusH	[15.38; 15.48]	kJ/mol	[225.80; 225.80]
ΔfusH	15.38	kJ/mol	225.80	NIST
ΔfusH	15.48	kJ/mol	225.80	NIST
ΔfusH	15.48	kJ/mol	225.80	NIST
ΔvapH	[44.50; 62.00]	kJ/mol	[295.50; 430.50]
ΔvapH	61.20	kJ/mol	295.50	NIST
ΔvapH	62.00	kJ/mol	296.50	NIST
ΔvapH	61.90 ± 0.20	kJ/mol	300.50	NIST
ΔvapH	57.70	kJ/mol	320.50	NIST
ΔvapH	58.50 ± 0.20	kJ/mol	328.00	NIST
ΔvapH	57.60 ± 0.20	kJ/mol	343.00	NIST
ΔvapH	56.00	kJ/mol	357.50	NIST
ΔvapH	55.20 ± 0.20	kJ/mol	358.00	NIST
ΔvapH	59.70	kJ/mol	364.00	NIST
ΔvapH	53.80 ± 0.20	kJ/mol	368.00	NIST
ΔvapH	57.90	kJ/mol	369.00	NIST
ΔvapH	58.50	kJ/mol	378.00	NIST
ΔvapH	57.90	kJ/mol	379.00	NIST
ΔvapH	51.40	kJ/mol	393.00	NIST
ΔvapH	47.90	kJ/mol	398.50	NIST
ΔvapH	48.53	kJ/mol	430.30	KDB
ΔvapH	44.50	kJ/mol	430.50	NIST
ν	[0.0000036; 0.0000047]	m2/s	[303.15; 313.15]
ν	0.0000047	m2/s	303.15	Densiti...
ν	0.0000036	m2/s	313.15	Densiti...
Pvap	[1.43e-04; 106.98]	kPa	[237.95; 432.32]
Pvap	1.43e-04	kPa	237.95	Vapor p...
Pvap	1.45e-04	kPa	238.00	Vapor p...
Pvap	1.43e-04	kPa	238.00	Vapor p...
Pvap	2.96e-04	kPa	243.20	Vapor p...
Pvap	2.96e-04	kPa	243.20	Vapor p...
Pvap	2.93e-04	kPa	243.25	Vapor p...
Pvap	5.64e-04	kPa	248.20	Vapor p...
Pvap	5.60e-04	kPa	248.20	Vapor p...
Pvap	5.69e-04	kPa	248.20	Vapor p...
Pvap	1.06e-03	kPa	253.15	Vapor p...
Pvap	1.05e-03	kPa	253.15	Vapor p...
Pvap	1.05e-03	kPa	253.15	Vapor p...
Pvap	1.92e-03	kPa	258.15	Vapor p...
Pvap	1.92e-03	kPa	258.15	Vapor p...
Pvap	1.92e-03	kPa	258.15	Vapor p...
Pvap	3.39e-03	kPa	263.15	Vapor p...
Pvap	3.38e-03	kPa	263.15	Vapor p...
Pvap	3.39e-03	kPa	263.15	Vapor p...
Pvap	4.68e-03	kPa	265.00	Measure...
Pvap	5.84e-03	kPa	268.15	Vapor p...
Pvap	5.84e-03	kPa	268.15	Vapor p...
Pvap	5.84e-03	kPa	268.15	Vapor p...
Pvap	6.64e-03	kPa	268.20	Measure...
Pvap	9.86e-03	kPa	273.15	Vapor p...
Pvap	9.87e-03	kPa	273.15	Vapor p...
Pvap	9.87e-03	kPa	273.15	Vapor p...
Pvap	0.01	kPa	273.40	Measure...
Pvap	0.01	kPa	273.65	Vapor p...
Pvap	0.01	kPa	273.65	Vapor p...
Pvap	0.01	kPa	273.65	Vapor p...
Pvap	0.02	kPa	278.15	Vapor p...
Pvap	0.02	kPa	278.15	Vapor p...
Pvap	0.02	kPa	278.15	Vapor p...
Pvap	0.02	kPa	278.20	Measure...
Pvap	0.03	kPa	283.15	Vapor p...
Pvap	0.03	kPa	283.15	Vapor p...
Pvap	0.03	kPa	283.15	Vapor p...
Pvap	0.03	kPa	283.20	Measure...
Pvap	0.05	kPa	288.10	Measure...
Pvap	0.04	kPa	288.15	Vapor p...
Pvap	0.04	kPa	288.15	Vapor p...
Pvap	0.04	kPa	288.15	Vapor p...
Pvap	0.07	kPa	293.15	Vapor p...
Pvap	0.07	kPa	293.15	Vapor p...
Pvap	0.07	kPa	293.15	Vapor p...
Pvap	0.07	kPa	293.20	Measure...
Pvap	0.07	kPa	293.30	Measure...
Pvap	0.10	kPa	298.15	Vapor p...
Pvap	0.10	kPa	298.15	Vapor p...
Pvap	0.12	kPa	298.15	Vapor P...
Pvap	0.10	kPa	298.15	Vapor p...
Pvap	0.12	kPa	298.20	Measure...
Pvap	0.11	kPa	298.30	Measure...
Pvap	0.17	kPa	303.15	Vapor P...
Pvap	0.15	kPa	303.15	Vapor p...
Pvap	0.15	kPa	303.15	Vapor p...
Pvap	0.15	kPa	303.15	Vapor p...
Pvap	0.17	kPa	303.20	Measure...
Pvap	0.17	kPa	303.20	Measure...
Pvap	0.17	kPa	303.30	Measure...
Pvap	0.25	kPa	308.15	Vapor P...
Pvap	0.22	kPa	308.15	Vapor p...
Pvap	0.22	kPa	308.15	Vapor p...
Pvap	0.22	kPa	308.15	Vapor p...
Pvap	0.25	kPa	308.20	Measure...
Pvap	0.25	kPa	308.30	Measure...
Pvap	0.30	kPa	310.40	Measure...
Pvap	0.36	kPa	313.10	Measure...
Pvap	0.36	kPa	313.15	Vapor P...
Pvap	0.37	kPa	313.20	Measure...
Pvap	0.52	kPa	318.15	Vapor P...
Pvap	0.53	kPa	318.20	Measure...
Pvap	0.53	kPa	318.20	Measure...
Pvap	0.73	kPa	323.15	Vapor P...
Pvap	0.71	kPa	323.20	Measure...
Pvap	0.75	kPa	323.20	Measure...
Pvap	1.03	kPa	328.10	Measure...
Pvap	1.01	kPa	328.15	Vapor P...
Pvap	1.01	kPa	328.20	Measure...
Pvap	1.43	kPa	333.10	Measure...
Pvap	1.40	kPa	333.15	Vapor P...
Pvap	1.46	kPa	333.20	Measure...
Pvap	1.90	kPa	338.15	Vapor P...
Pvap	1.98	kPa	338.20	Measure...
Pvap	2.54	kPa	343.15	Vapor P...
Pvap	2.64	kPa	343.20	Measure...
Pvap	2.04	kPa	343.46	Vapor-L...
Pvap	2.16	kPa	344.20	Vapor-L...
Pvap	2.23	kPa	344.60	Vapor-L...
Pvap	2.35	kPa	345.36	Vapor-L...
Pvap	2.47	kPa	346.17	Vapor-L...
Pvap	2.67	kPa	347.27	Vapor-L...
Pvap	2.79	kPa	348.10	Vapor-L...
Pvap	3.38	kPa	348.15	Vapor P...
Pvap	3.48	kPa	348.20	Measure...
Pvap	2.85	kPa	348.35	Vapor-L...
Pvap	3.04	kPa	349.38	Vapor-L...
Pvap	3.11	kPa	349.75	Vapor-L...
Pvap	3.32	kPa	350.75	Vapor-L...
Pvap	3.44	kPa	351.39	Vapor-L...
Pvap	3.64	kPa	352.20	Vapor-L...
Pvap	3.73	kPa	352.63	Vapor-L...
Pvap	3.83	kPa	353.00	Vapor-L...
Pvap	4.43	kPa	353.15	Vapor P...
Pvap	4.64	kPa	353.20	Measure...
Pvap	3.89	kPa	353.31	Vapor-L...
Pvap	3.96	kPa	353.82	Vapor-L...
Pvap	4.31	kPa	355.20	Vapor-L...
Pvap	4.79	kPa	357.01	Vapor-L...
Pvap	5.79	kPa	357.20	Measure...
Pvap	5.76	kPa	358.15	Vapor P...
Pvap	6.13	kPa	358.20	Measure...
Pvap	5.15	kPa	358.22	Vapor-L...
Pvap	5.51	kPa	359.43	Vapor-L...
Pvap	5.79	kPa	360.34	Vapor-L...
Pvap	6.04	kPa	361.12	Vapor-L...
Pvap	6.29	kPa	361.86	Vapor-L...
Pvap	7.41	kPa	363.15	Vapor P...
Pvap	7.87	kPa	363.20	Measure...
Pvap	6.99	kPa	363.85	Vapor-L...
Pvap	7.27	kPa	364.61	Vapor-L...
Pvap	7.64	kPa	365.58	Vapor-L...
Pvap	7.92	kPa	366.30	Vapor-L...
Pvap	8.32	kPa	366.67	Vapor p...
Pvap	8.40	kPa	367.44	Vapor-L...
Pvap	8.67	kPa	368.05	Vapor-L...
Pvap	9.44	kPa	368.15	Vapor P...
Pvap	9.08	kPa	368.99	Vapor-L...
Pvap	9.40	kPa	369.67	Vapor-L...
Pvap	9.67	kPa	370.24	Vapor-L...
Pvap	9.95	kPa	370.83	Vapor-L...
Pvap	10.27	kPa	371.45	Vapor-L...
Pvap	10.59	kPa	372.10	Vapor-L...
Pvap	11.06	kPa	372.64	Vapor p...
Pvap	11.05	kPa	373.00	Vapor-L...
Pvap	11.91	kPa	373.15	Vapor P...
Pvap	11.43	kPa	373.67	Vapor-L...
Pvap	11.73	kPa	374.19	Vapor-L...
Pvap	12.27	kPa	375.14	Vapor-L...
Pvap	12.73	kPa	375.93	Vapor-L...
Pvap	13.15	kPa	376.59	Vapor-L...
Pvap	13.53	kPa	377.22	Vapor-L...
Pvap	13.87	kPa	377.56	Vapor p...
Pvap	13.71	kPa	377.83	Vapor-L...
Pvap	13.85	kPa	378.01	Vapor-L...
Pvap	14.90	kPa	378.15	Vapor P...
Pvap	14.15	kPa	378.37	Vapor-L...
Pvap	14.40	kPa	378.72	Vapor-L...
Pvap	14.65	kPa	379.10	Vapor-L...
Pvap	14.91	kPa	379.46	Vapor-L...
Pvap	15.12	kPa	379.75	Vapor-L...
Pvap	15.37	kPa	380.06	Vapor-L...
Pvap	15.61	kPa	380.41	Vapor-L...
Pvap	15.95	kPa	380.87	Vapor-L...
Pvap	16.15	kPa	381.15	Vapor-L...
Pvap	16.37	kPa	381.45	Vapor-L...
Pvap	16.77	kPa	381.80	Vapor p...
Pvap	16.77	kPa	381.81	Vapor p...
Pvap	16.71	kPa	381.89	Vapor-L...
Pvap	16.97	kPa	382.25	Vapor-L...
Pvap	17.21	kPa	382.56	Vapor-L...
Pvap	17.44	kPa	382.85	Vapor-L...
Pvap	18.50	kPa	383.15	Vapor P...
Pvap	17.69	kPa	383.18	Vapor-L...
Pvap	17.84	kPa	383.34	Vapor-L...
Pvap	18.09	kPa	383.67	Vapor-L...
Pvap	18.43	kPa	384.08	Vapor-L...
Pvap	19.05	kPa	384.87	Vapor-L...
Pvap	19.47	kPa	385.37	Vapor-L...
Pvap	19.91	kPa	385.86	Vapor-L...
Pvap	20.26	kPa	386.17	Vapor p...
Pvap	20.31	kPa	386.31	Vapor-L...
Pvap	20.79	kPa	386.83	Vapor-L...
Pvap	21.15	kPa	387.23	Vapor-L...
Pvap	21.48	kPa	387.62	Vapor-L...
Pvap	21.91	kPa	388.10	Vapor-L...
Pvap	22.79	kPa	388.15	Vapor P...
Pvap	22.37	kPa	388.59	Vapor-L...
Pvap	22.79	kPa	389.05	Vapor-L...
Pvap	23.20	kPa	389.48	Vapor-L...
Pvap	23.60	kPa	389.89	Vapor-L...
Pvap	23.95	kPa	390.23	Vapor-L...
Pvap	24.36	kPa	390.65	Vapor-L...
Pvap	24.54	kPa	390.77	Vapor p...
Pvap	24.54	kPa	390.78	Vapor p...
Pvap	24.67	kPa	390.93	Vapor-L...
Pvap	25.00	kPa	391.07	Phase E...
Pvap	25.13	kPa	391.40	Vapor-L...
Pvap	25.51	kPa	391.75	Vapor-L...
Pvap	25.83	kPa	392.06	Vapor-L...
Pvap	26.31	kPa	392.51	Vapor-L...
Pvap	26.59	kPa	392.77	Vapor-L...
Pvap	27.00	kPa	393.14	Vapor-L...
Pvap	27.86	kPa	393.15	Vapor P...
Pvap	29.35	kPa	395.23	Vapor p...
Pvap	29.35	kPa	395.23	Vapor p...
Pvap	30.00	kPa	395.62	Phase E...
Pvap	33.84	kPa	398.15	Vapor P...
Pvap	34.77	kPa	399.57	Vapor p...
Pvap	35.00	kPa	399.65	Phase E...
Pvap	40.00	kPa	402.36	Low-Pre...
Pvap	40.85	kPa	403.15	Vapor P...
Pvap	40.00	kPa	403.15	Phase E...
Pvap	40.02	kPa	403.66	Low-Pre...
Pvap	40.70	kPa	403.73	Vapor p...
Pvap	45.00	kPa	406.36	Phase E...
Pvap	48.72	kPa	407.89	Low-Pre...
Pvap	47.57	kPa	407.98	Vapor p...
Pvap	49.02	kPa	408.15	Vapor P...
Pvap	50.00	kPa	409.25	Phase E...
Pvap	55.00	kPa	411.92	Phase E...
Pvap	58.50	kPa	413.15	Vapor P...
Pvap	58.84	kPa	413.31	Low-Pre...
Pvap	60.00	kPa	414.44	Phase E...
Pvap	60.20	kPa	414.61	Vapor p...
Pvap	65.00	kPa	416.75	Phase E...
Pvap	69.49	kPa	418.15	Vapor P...
Pvap	69.27	kPa	418.35	Low-Pre...
Pvap	70.00	kPa	418.98	Phase E...
Pvap	74.69	kPa	420.99	Vapor p...
Pvap	75.00	kPa	421.05	Phase E...
Pvap	77.40	kPa	421.90	Low-Pre...
Pvap	80.00	kPa	423.01	Phase E...
Pvap	82.16	kPa	423.15	Vapor P...
Pvap	85.00	kPa	424.87	Phase E...
Pvap	85.63	kPa	425.15	Low-Pre...
Pvap	90.00	kPa	426.69	Phase E...
Pvap	92.07	kPa	427.54	Low-Pre...
Pvap	93.19	kPa	427.85	Vapor p...
Pvap	93.26	kPa	427.90	Vapor p...
Pvap	99.78	kPa	429.19	Low-Pre...
Pvap	98.12	kPa	429.52	Vapor p...
Pvap	98.16	kPa	429.54	Vapor p...
Pvap	101.30	kPa	430.11	Vapor-l...
Pvap	105.46	kPa	431.85	Vapor p...
Pvap	106.75	kPa	432.25	Vapor p...
Pvap	106.98	kPa	432.32	Vapor p...
n0	[1.41270; 1.42070]		[293.10; 313.15]
n0	1.41800		293.10	Viscosi...
n0	1.41830		293.15	Densiti...
n0	1.41800		293.15	ERAS mo...
n0	1.41826		293.15	Excess ...
n0	1.41807		293.15	Densiti...
n0	1.41750		293.15	Measure...
n0	1.41826		293.15	Densiti...
n0	1.41780		293.15	Densiti...
n0	1.41780		293.15	Densiti...
n0	1.41810		293.20	Liquid-...
n0	1.42070		293.20	Vapor L...
n0	1.41650		298.15	Excess ...
n0	1.41600		298.15	Compara...
n0	1.41610		298.15	Densiti...
n0	1.41580		298.15	Liquid ...
n0	1.41738		298.15	Atmosph...
n0	1.41550		298.15	Ternary...
n0	1.41600		298.15	Liquid-...
n0	1.41620		298.15	Phase e...
n0	1.41590		298.15	Density...
n0	1.41660		298.15	Excess ...
n0	1.41570		298.15	Effect ...
n0	1.41570		298.15	Vapor-L...
n0	1.41550		298.20	Ternary...
n0	1.41570		303.15	Compara...
n0	1.41423		303.15	Densiti...
n0	1.41423		303.15	Densiti...
n0	1.41340		303.15	Measure...
n0	1.41410		308.15	Compara...
n0	1.41270		313.15	Compara...
ρl	[765.64; 827.82]	kg/m3	[283.15; 363.15]
ρl	826.03	kg/m3	283.15	Excess ...
ρl	825.94	kg/m3	283.15	Densiti...
ρl	827.82	kg/m3	283.15	Volumet...
ρl	824.25	kg/m3	288.15	Volumet...
ρl	822.42	kg/m3	288.15	Densiti...
ρl	822.00	kg/m3	288.15	Effect ...
ρl	822.26	kg/m3	288.15	Volumet...
ρl	822.26	kg/m3	288.15	Volumet...
ρl	819.00	kg/m3	293.00	KDB
ρl	818.70	kg/m3	293.15	Investi...
ρl	818.70	kg/m3	293.15	Volumet...
ρl	818.90	kg/m3	293.15	Density...
ρl	818.75	kg/m3	293.15	Volume ...
ρl	818.00	kg/m3	293.15	Densiti...
ρl	820.65	kg/m3	293.15	Volumet...
ρl	819.00	kg/m3	293.15	Effect ...
ρl	818.88	kg/m3	293.15	Densiti...
ρl	818.70	kg/m3	293.15	Correla...
ρl	818.69	kg/m3	293.15	Volumet...
ρl	815.16	kg/m3	298.10	Excess ...
ρl	815.34	kg/m3	298.15	Excess ...
ρl	815.02	kg/m3	298.15	Surface...
ρl	815.30	kg/m3	298.15	Bubble ...
ρl	815.21	kg/m3	298.15	Excess ...
ρl	815.10	kg/m3	298.15	Investi...
ρl	815.10	kg/m3	298.15	Correla...
ρl	814.94	kg/m3	298.15	Phase b...
ρl	815.32	kg/m3	298.15	Densiti...
ρl	815.50	kg/m3	298.15	Viscosi...
ρl	815.26	kg/m3	298.15	Studies...
ρl	814.94	kg/m3	298.15	Phase b...
ρl	815.19	kg/m3	298.15	Volume ...
ρl	815.30	kg/m3	298.15	Bubble ...
ρl	815.40	kg/m3	298.15	Excess ...
ρl	815.70	kg/m3	298.15	Thermod...
ρl	814.95	kg/m3	298.15	Densiti...
ρl	815.65	kg/m3	298.15	Thermod...
ρl	815.31	kg/m3	298.15	FT-IR s...
ρl	815.30	kg/m3	298.15	Density...
ρl	815.20	kg/m3	298.15	Excess ...
ρl	815.29	kg/m3	298.15	Densiti...
ρl	817.03	kg/m3	298.15	Volumet...
ρl	815.15	kg/m3	298.15	Speeds ...
ρl	815.00	kg/m3	298.15	Effect ...
ρl	815.90	kg/m3	298.15	Excess ...
ρl	815.11	kg/m3	298.15	Volumet...
ρl	814.90	kg/m3	298.15	Densiti...
ρl	815.20	kg/m3	298.15	Effect ...
ρl	815.12	kg/m3	298.15	Volumet...
ρl	815.88	kg/m3	298.20	Isother...
ρl	815.17	kg/m3	298.20	Liquid-...
ρl	811.60	kg/m3	303.15	Volume ...
ρl	811.51	kg/m3	303.15	Volumet...
ρl	811.52	kg/m3	303.15	Volumet...
ρl	811.74	kg/m3	303.15	Densiti...
ρl	811.50	kg/m3	303.15	Investi...
ρl	813.39	kg/m3	303.15	Volumet...
ρl	812.00	kg/m3	303.15	Effect ...
ρl	811.50	kg/m3	303.15	Correla...
ρl	811.39	kg/m3	303.15	Excess ...
ρl	811.70	kg/m3	303.15	FT-IR s...
ρl	811.70	kg/m3	303.15	Density...
ρl	811.30	kg/m3	303.15	Densiti...
ρl	808.40	kg/m3	308.15	Viscosi...
ρl	808.00	kg/m3	308.15	Effect ...
ρl	809.71	kg/m3	308.15	Volumet...
ρl	807.60	kg/m3	308.15	Densiti...
ρl	808.06	kg/m3	308.15	FT-IR s...
ρl	807.98	kg/m3	308.15	Volume ...
ρl	808.10	kg/m3	308.15	Density...
ρl	807.89	kg/m3	308.15	Volumet...
ρl	807.88	kg/m3	308.15	Volumet...
ρl	807.90	kg/m3	308.15	Correla...
ρl	808.13	kg/m3	308.15	Densiti...
ρl	807.90	kg/m3	308.15	Investi...
ρl	804.50	kg/m3	313.15	Densiti...
ρl	806.00	kg/m3	313.15	Volumet...
ρl	803.90	kg/m3	313.15	Densiti...
ρl	804.20	kg/m3	313.15	Investi...
ρl	804.50	kg/m3	313.15	Density...
ρl	804.23	kg/m3	313.15	Volumet...
ρl	804.46	kg/m3	313.15	Excess ...
ρl	804.20	kg/m3	313.15	Correla...
ρl	805.00	kg/m3	313.15	Effect ...
ρl	804.25	kg/m3	313.15	Volumet...
ρl	804.34	kg/m3	313.15	Volume ...
ρl	800.60	kg/m3	318.15	Investi...
ρl	802.27	kg/m3	318.15	Volumet...
ρl	800.80	kg/m3	318.15	Density...
ρl	800.56	kg/m3	318.15	Volumet...
ρl	800.60	kg/m3	318.15	Correla...
ρl	800.56	kg/m3	318.15	Volumet...
ρl	801.00	kg/m3	318.15	Viscosi...
ρl	800.66	kg/m3	318.15	Volume ...
ρl	800.10	kg/m3	318.15	Densiti...
ρl	800.60	kg/m3	318.15	Effect ...
ρl	800.83	kg/m3	318.15	Densiti...
ρl	796.20	kg/m3	323.15	Densiti...
ρl	796.80	kg/m3	323.15	Investi...
ρl	797.12	kg/m3	323.15	Densiti...
ρl	796.85	kg/m3	323.15	Volumet...
ρl	796.85	kg/m3	323.15	Volumet...
ρl	796.80	kg/m3	323.15	Correla...
ρl	797.10	kg/m3	323.15	Density...
ρl	798.49	kg/m3	323.15	Volumet...
ρl	798.00	kg/m3	323.15	Effect ...
ρl	793.37	kg/m3	328.15	Densiti...
ρl	793.20	kg/m3	328.15	Effect ...
ρl	793.40	kg/m3	328.15	Density...
ρl	794.67	kg/m3	328.15	Volumet...
ρl	793.50	kg/m3	328.15	Viscosi...
ρl	791.00	kg/m3	333.15	Effect ...
ρl	789.57	kg/m3	333.15	Densiti...
ρl	790.80	kg/m3	333.15	Volumet...
ρl	785.50	kg/m3	338.15	Effect ...
ρl	785.90	kg/m3	338.15	Viscosi...
ρl	785.72	kg/m3	338.15	Densiti...
ρl	783.00	kg/m3	343.15	Effect ...
ρl	781.83	kg/m3	343.15	Densiti...
ρl	777.86	kg/m3	348.15	Densiti...
ρl	773.86	kg/m3	353.15	Densiti...
ρl	769.78	kg/m3	358.15	Densiti...
ρl	765.64	kg/m3	363.15	Densiti...
ΔfusS	68.11	J/mol×K	225.80	NIST
csound,fluid	[1237.50; 1339.20]	m/s	[288.15; 318.15]
csound,fluid	1339.20	m/s	288.15	Ultraso...
csound,fluid	1320.38	m/s	293.15	Thermod...
csound,fluid	1320.11	m/s	293.15	Densiti...
csound,fluid	1321.20	m/s	293.15	Ultraso...
csound,fluid	1312.40	m/s	298.15	Ultraso...
csound,fluid	1306.90	m/s	298.15	Ultraso...
csound,fluid	1303.19	m/s	298.15	Densiti...
csound,fluid	1303.54	m/s	298.15	Thermod...
csound,fluid	1289.50	m/s	303.15	Ultraso...
csound,fluid	1286.68	m/s	303.15	Thermod...
csound,fluid	1275.70	m/s	308.15	Ultraso...
csound,fluid	1270.00	m/s	308.15	Thermod...
csound,fluid	1256.30	m/s	313.15	Ultraso...
csound,fluid	1253.54	m/s	313.15	Thermod...
csound,fluid	1237.50	m/s	318.15	Ultraso...
γ	[0.02; 0.03]	N/m	[288.15; 328.15]
γ	0.03	N/m	288.15	Density...
γ	0.03	N/m	288.15	Density...
γ	0.03	N/m	288.15	The add...
γ	0.03	N/m	288.15	Study o...
γ	0.03	N/m	293.15	Density...
γ	0.03	N/m	293.15	The add...
γ	0.03	N/m	298.15	Density...
γ	0.02	N/m	298.15	Study o...
γ	0.03	N/m	298.15	Density...
γ	0.03	N/m	298.15	Surface...
γ	0.03	N/m	298.15	The add...
γ	0.03	N/m	298.20	KDB
γ	0.02	N/m	303.15	Surface...
γ	0.03	N/m	303.15	The add...
γ	0.02	N/m	303.15	Density...
γ	0.02	N/m	308.15	Study o...
γ	0.02	N/m	308.15	Density...
γ	0.02	N/m	308.15	Surface...
γ	0.02	N/m	308.15	The add...
γ	0.02	N/m	308.15	Density...
γ	0.02	N/m	313.15	Surface...
γ	0.02	N/m	313.15	The add...
γ	0.02	N/m	318.15	The add...
γ	0.02	N/m	318.15	Study o...
γ	0.02	N/m	318.15	Surface...
γ	0.02	N/m	323.15	Surface...
γ	0.02	N/m	328.15	Study o...

Datasets

1. Mass density, kg/m3 (8)
2. Speed of sound, m/s (1)

Mass density, kg/m3

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
293.15	100.00	818.6
293.15	10000.00	824.8
293.15	20000.00	830.9
293.15	30000.00	836.4
293.15	40000.00	841.6
293.15	50000.00	846.5
293.15	60000.00	851.1
293.15	70000.00	855.5
293.15	80000.00	859.8
293.15	90000.00	863.7
293.15	100000.00	867.9
293.15	110000.00	871.5
293.15	120000.00	875.2
293.15	130000.00	878.7
293.15	140000.00	882.2
303.15	100.00	811.5
303.15	10000.00	818.2
303.15	20000.00	824.1
303.15	30000.00	830.0
303.15	40000.00	835.1
303.15	50000.00	840.5
303.15	60000.00	845.3
303.15	70000.00	849.8
303.15	80000.00	854.2
303.15	90000.00	858.4
303.15	100000.00	862.4
303.15	110000.00	866.3
303.15	120000.00	870.0
303.15	130000.00	873.6
303.15	140000.00	877.1
313.15	100.00	804.2
313.15	10000.00	811.1
313.15	20000.00	817.4
313.15	30000.00	823.5
313.15	40000.00	829.0
313.15	50000.00	834.4
313.15	60000.00	839.4
313.15	70000.00	844.3
313.15	80000.00	848.7
313.15	90000.00	853.1
313.15	100000.00	857.1
313.15	110000.00	861.2
313.15	120000.00	865.1
313.15	130000.00	868.7
313.15	140000.00	872.5
323.15	100.00	797.3
323.15	10000.00	804.5
323.15	20000.00	811.2
323.15	30000.00	817.4
323.15	40000.00	823.3
323.15	50000.00	828.7
323.15	60000.00	833.8
323.15	70000.00	838.5
323.15	80000.00	843.1
323.15	90000.00	847.6
323.15	100000.00	851.8
323.15	110000.00	856.0
323.15	120000.00	860.0
323.15	130000.00	863.7
323.15	140000.00	867.3
333.15	100.00	789.7
333.15	10000.00	797.2
333.15	20000.00	804.3
333.15	30000.00	810.8
333.15	40000.00	817.0
333.15	50000.00	822.7
333.15	60000.00	828.0
333.15	70000.00	832.8
333.15	80000.00	837.6
333.15	90000.00	842.5
333.15	100000.00	846.8
333.15	110000.00	850.8
333.15	120000.00	854.4
333.15	130000.00	858.5
333.15	140000.00	862.2
343.15	100.00	781.9
343.15	10000.00	790.2
343.15	20000.00	797.6
343.15	30000.00	804.4
343.15	40000.00	810.6
343.15	50000.00	816.4
343.15	60000.00	822.1
343.15	70000.00	827.3
343.15	80000.00	832.1
343.15	90000.00	836.9
343.15	100000.00	841.4
343.15	110000.00	845.7
343.15	120000.00	849.7
343.15	130000.00	853.6
343.15	140000.00	857.5
353.15	100.00	773.8
353.15	10000.00	782.3
353.15	20000.00	790.1
353.15	30000.00	797.3
353.15	40000.00	803.8
353.15	50000.00	810.0
353.15	60000.00	815.6
353.15	70000.00	821.0
353.15	80000.00	826.2
353.15	90000.00	831.1
353.15	100000.00	835.6
353.15	110000.00	840.0
353.15	120000.00	844.3
353.15	130000.00	848.4
353.15	140000.00	852.3
363.15	100.00	765.5
363.15	10000.00	774.9
363.15	20000.00	783.1
363.15	30000.00	790.6
363.15	40000.00	797.5
363.15	50000.00	803.8
363.15	60000.00	809.7
363.15	70000.00	815.4
363.15	80000.00	820.6
363.15	90000.00	825.6
363.15	100000.00	830.3
363.15	110000.00	834.8
363.15	120000.00	839.2
363.15	130000.00	843.3
363.15	140000.00	847.2
373.15	100.00	756.9
373.15	10000.00	766.6
373.15	20000.00	775.4
373.15	30000.00	783.4
373.15	40000.00	790.4
373.15	50000.00	796.9
373.15	60000.00	803.1
373.15	70000.00	808.9
373.15	80000.00	814.2
373.15	90000.00	819.5
373.15	100000.00	824.4
373.15	110000.00	829.2
373.15	120000.00	833.3
373.15	130000.00	837.7
373.15	140000.00	841.7
383.15	100.00	748.2
383.15	10000.00	759.1
383.15	20000.00	767.8
383.15	30000.00	776.5
383.15	40000.00	783.5
383.15	50000.00	790.4
383.15	60000.00	796.8
383.15	70000.00	802.6
383.15	80000.00	808.3
383.15	90000.00	813.7
383.15	100000.00	818.7
383.15	110000.00	823.4
383.15	120000.00	828.0
383.15	130000.00	832.3
383.15	140000.00	836.5
393.15	100.00	739.4
393.15	10000.00	750.8
393.15	20000.00	760.5
393.15	30000.00	768.8
393.15	40000.00	777.0
393.15	50000.00	783.7
393.15	60000.00	790.3
393.15	70000.00	796.5
393.15	80000.00	802.5
393.15	90000.00	807.8
393.15	100000.00	813.0
393.15	110000.00	818.1
393.15	120000.00	822.6
393.15	130000.00	827.2
393.15	140000.00	831.5
403.15	100.00	730.2
403.15	10000.00	741.8
403.15	20000.00	751.9
403.15	30000.00	761.1
403.15	40000.00	769.3
403.15	50000.00	776.9
403.15	60000.00	783.7
403.15	70000.00	790.1
403.15	80000.00	796.2
403.15	90000.00	801.8
403.15	100000.00	807.2
403.15	110000.00	812.3
403.15	120000.00	817.1
403.15	130000.00	821.8
403.15	140000.00	826.5
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
298.15	100.00	815.1
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
278.15	100.00	828.9
278.15	1000.00	829.5
278.15	5000.00	832.0
278.15	10000.00	835.0
278.15	15000.00	838.0
278.15	20000.00	840.8
278.15	25000.00	843.6
278.15	30000.00	846.3
278.15	35000.00	848.9
278.15	40000.00	851.4
278.15	45000.00	853.9
278.15	50000.00	856.3
278.15	55000.00	858.7
278.15	60000.00	860.9
288.15	100.00	822.1
288.15	1000.00	822.7
288.15	5000.00	825.3
288.15	10000.00	828.5
288.15	15000.00	831.6
288.15	20000.00	834.6
288.15	25000.00	837.4
288.15	30000.00	840.2
288.15	35000.00	842.9
288.15	40000.00	845.5
288.15	45000.00	848.0
288.15	50000.00	850.5
288.15	55000.00	853.0
288.15	60000.00	855.4
298.15	100.00	814.9
298.15	1000.00	815.6
298.15	5000.00	818.4
298.15	10000.00	821.7
298.15	15000.00	824.9
298.15	20000.00	828.0
298.15	25000.00	830.9
298.15	30000.00	833.8
298.15	35000.00	836.6
298.15	40000.00	839.4
298.15	45000.00	842.0
298.15	50000.00	844.6
298.15	55000.00	847.1
298.15	60000.00	849.6
308.15	100.00	807.8
308.15	1000.00	808.4
308.15	5000.00	811.4
308.15	10000.00	814.8
308.15	15000.00	818.2
308.15	20000.00	821.4
308.15	25000.00	824.5
308.15	30000.00	827.5
308.15	35000.00	830.3
308.15	40000.00	833.2
308.15	45000.00	835.9
308.15	50000.00	838.5
308.15	55000.00	841.1
308.15	60000.00	843.5
318.15	100.00	800.5
318.15	1000.00	801.2
318.15	5000.00	804.3
318.15	10000.00	807.9
318.15	15000.00	811.4
318.15	20000.00	814.7
318.15	25000.00	817.9
318.15	30000.00	821.0
318.15	35000.00	824.0
318.15	40000.00	826.9
318.15	45000.00	829.7
318.15	50000.00	832.4
318.15	55000.00	835.1
318.15	60000.00	837.7
328.15	100.00	793.0
328.15	1000.00	793.7
328.15	5000.00	797.0
328.15	10000.00	800.8
328.15	15000.00	804.4
328.15	20000.00	807.9
328.15	25000.00	811.2
328.15	30000.00	814.4
328.15	35000.00	817.6
328.15	40000.00	820.6
328.15	45000.00	823.5
328.15	50000.00	826.4
328.15	55000.00	829.1
328.15	60000.00	831.6
338.15	100.00	785.4
338.15	1000.00	786.2
338.15	5000.00	789.6
338.15	10000.00	793.6
338.15	15000.00	797.4
338.15	20000.00	801.0
338.15	25000.00	804.5
338.15	30000.00	807.9
338.15	35000.00	811.1
338.15	40000.00	814.2
338.15	45000.00	817.3
338.15	50000.00	820.2
338.15	55000.00	823.1
338.15	60000.00	825.7
348.15	100.00	777.6
348.15	1000.00	778.4
348.15	5000.00	782.0
348.15	10000.00	786.2
348.15	15000.00	790.2
348.15	20000.00	794.1
348.15	25000.00	797.6
348.15	30000.00	801.2
348.15	35000.00	804.6
348.15	40000.00	807.8
348.15	45000.00	811.0
348.15	50000.00	814.0
348.15	55000.00	817.0
348.15	60000.00	819.7
358.15	100.00	769.4
358.15	1000.00	770.0
358.15	5000.00	774.2
358.15	10000.00	778.6
358.15	15000.00	782.8
358.15	20000.00	786.9
358.15	25000.00	790.7
358.15	30000.00	794.3
358.15	35000.00	797.9
358.15	40000.00	801.3
358.15	45000.00	804.6
358.15	50000.00	807.7
358.15	55000.00	810.8
358.15	60000.00	813.5
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
278.15	100.00	828.9
278.15	1000.00	829.5
278.15	5000.00	832.0
278.15	10000.00	835.0
278.15	15000.00	838.0
278.15	20000.00	840.8
278.15	25000.00	843.6
278.15	30000.00	846.3
278.15	35000.00	848.9
278.15	40000.00	851.4
278.15	45000.00	853.9
278.15	50000.00	856.3
278.15	55000.00	858.7
278.15	60000.00	860.9
288.15	100.00	822.1
288.15	1000.00	822.7
288.15	5000.00	825.3
288.15	10000.00	828.5
288.15	15000.00	831.6
288.15	20000.00	834.6
288.15	25000.00	837.4
288.15	30000.00	840.2
288.15	35000.00	842.9
288.15	40000.00	845.5
288.15	45000.00	848.0
288.15	50000.00	850.5
288.15	55000.00	853.0
288.15	60000.00	855.4
298.15	100.00	814.9
298.15	1000.00	815.6
298.15	5000.00	818.4
298.15	10000.00	821.7
298.15	15000.00	824.9
298.15	20000.00	828.0
298.15	25000.00	830.9
298.15	30000.00	833.8
298.15	35000.00	836.6
298.15	40000.00	839.4
298.15	45000.00	842.0
298.15	50000.00	844.6
298.15	55000.00	847.1
298.15	60000.00	849.6
308.15	100.00	807.8
308.15	1000.00	808.4
308.15	5000.00	811.4
308.15	10000.00	814.8
308.15	15000.00	818.2
308.15	20000.00	821.4
308.15	25000.00	824.5
308.15	30000.00	827.5
308.15	35000.00	830.3
308.15	40000.00	833.2
308.15	45000.00	835.9
308.15	50000.00	838.5
308.15	55000.00	841.1
308.15	60000.00	843.5
318.15	100.00	800.5
318.15	1000.00	801.2
318.15	5000.00	804.3
318.15	10000.00	807.9
318.15	15000.00	811.4
318.15	20000.00	814.7
318.15	25000.00	817.9
318.15	30000.00	821.0
318.15	35000.00	824.0
318.15	40000.00	826.9
318.15	45000.00	829.7
318.15	50000.00	832.4
318.15	55000.00	835.1
318.15	60000.00	837.7
328.15	100.00	793.0
328.15	1000.00	793.7
328.15	5000.00	797.0
328.15	10000.00	800.8
328.15	15000.00	804.4
328.15	20000.00	807.9
328.15	25000.00	811.2
328.15	30000.00	814.4
328.15	35000.00	817.6
328.15	40000.00	820.6
328.15	45000.00	823.5
328.15	50000.00	826.4
328.15	55000.00	829.1
328.15	60000.00	831.6
338.15	100.00	785.4
338.15	1000.00	786.2
338.15	5000.00	789.6
338.15	10000.00	793.6
338.15	15000.00	797.4
338.15	20000.00	801.0
338.15	25000.00	804.5
338.15	30000.00	807.9
338.15	35000.00	811.1
338.15	40000.00	814.2
338.15	45000.00	817.3
338.15	50000.00	820.2
338.15	55000.00	823.1
338.15	60000.00	825.7
348.15	100.00	777.6
348.15	1000.00	778.4
348.15	5000.00	782.0
348.15	10000.00	786.2
348.15	15000.00	790.2
348.15	20000.00	794.1
348.15	25000.00	797.6
348.15	30000.00	801.2
348.15	35000.00	804.6
348.15	40000.00	807.8
348.15	45000.00	811.0
348.15	50000.00	814.0
348.15	55000.00	817.0
348.15	60000.00	819.7
358.15	100.00	769.4
358.15	1000.00	770.0
358.15	5000.00	774.2
358.15	10000.00	778.6
358.15	15000.00	782.8
358.15	20000.00	786.9
358.15	25000.00	790.7
358.15	30000.00	794.3
358.15	35000.00	797.9
358.15	40000.00	801.3
358.15	45000.00	804.6
358.15	50000.00	807.7
358.15	55000.00	810.8
358.15	60000.00	813.5
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
298.15	100.00	815.1
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
313.14	1034.00	804.9
313.14	2032.00	805.6
313.14	3046.00	806.3
313.14	4016.00	807.0
313.14	5013.00	807.7
313.14	6035.00	808.4
313.14	7010.00	809.1
313.14	8036.00	809.8
313.14	9015.00	810.5
313.14	10002.00	811.2
313.14	11020.00	811.8
313.14	12017.00	812.5
313.14	13002.00	813.2
313.14	14016.00	813.8
313.14	15016.00	814.5
313.14	16009.00	815.1
313.14	17010.00	815.8
313.14	18010.00	816.4
313.14	19012.00	817.1
313.14	20019.00	817.7
313.14	21006.00	818.3
313.14	22037.00	818.9
313.14	23037.00	819.6
313.14	24010.00	820.2
313.14	25023.00	820.8
323.12	1021.00	797.6
323.12	2009.00	798.4
323.12	3003.00	799.1
323.12	4014.00	799.8
323.12	5025.00	800.6
323.12	6021.00	801.3
323.12	7032.00	802.1
323.12	8016.00	802.8
323.12	9016.00	803.5
323.12	10019.00	804.2
323.12	11015.00	805.0
323.12	12012.00	805.7
323.12	13015.00	806.3
323.12	14006.00	807.0
323.12	15002.00	807.7
323.12	16013.00	808.4
323.12	17016.00	809.1
323.12	18018.00	809.7
323.12	19000.00	810.4
323.12	20003.00	811.0
323.12	21009.00	811.7
323.12	22000.00	812.3
323.12	23002.00	813.0
323.12	24021.00	813.6
323.12	25004.00	814.3
333.01	1023.00	790.2
333.01	2011.00	791.0
333.01	3042.00	791.8
333.01	4000.00	792.6
333.01	5014.00	793.3
333.01	6004.00	794.1
333.01	7021.00	794.9
333.01	8012.00	795.7
333.01	9002.00	796.4
333.01	10004.00	797.2
333.01	11026.00	797.9
333.01	12020.00	798.7
333.01	13018.00	799.4
333.01	14009.00	800.1
333.01	15019.00	800.8
333.01	16017.00	801.6
333.01	17006.00	802.3
333.01	18018.00	803.0
333.01	19013.00	803.7
333.01	20037.00	804.4
333.01	21029.00	805.0
333.01	22008.00	805.7
333.01	23026.00	806.4
333.01	24019.00	807.0
333.01	25025.00	807.7
342.96	1036.00	782.9
342.96	2011.00	783.7
342.96	3012.00	784.5
342.96	4015.00	785.4
342.96	5007.00	786.2
342.96	6013.00	787.0
342.96	7039.00	787.8
342.96	8023.00	788.6
342.96	9022.00	789.4
342.96	10035.00	790.2
342.96	11017.00	791.0
342.96	12016.00	791.7
342.96	13023.00	792.5
342.96	14003.00	793.2
342.96	15009.00	793.9
342.96	16014.00	794.7
342.96	17038.00	795.4
342.96	18023.00	796.1
342.96	19015.00	796.8
342.96	20015.00	797.5
342.96	21026.00	798.1
342.96	22003.00	798.8
342.96	23005.00	799.5
342.96	24003.00	800.1
342.96	25031.00	800.8
352.86	1020.00	775.0
352.86	2012.00	775.9
352.86	3028.00	776.9
352.86	4014.00	777.7
352.86	5010.00	778.6
352.86	6028.00	779.5
352.86	7039.00	780.4
352.86	8000.00	781.2
352.86	9030.00	782.1
352.86	10033.00	782.9
352.86	11014.00	783.7
352.86	12017.00	784.5
352.86	13014.00	785.3
352.86	14011.00	786.1
352.86	15010.00	786.9
352.86	16023.00	787.7
352.86	17018.00	788.5
352.86	18016.00	789.3
352.86	19014.00	790.0
352.86	20021.00	790.8
352.86	21017.00	791.5
352.86	22038.00	792.3
352.86	23016.00	793.0
352.86	24020.00	793.7
352.86	25048.00	794.5
362.80	1011.00	767.0
362.80	2009.00	768.0
362.80	3024.00	769.0
362.80	4006.00	769.9
362.80	5021.00	770.8
362.80	6035.00	771.8
362.80	7009.00	772.6
362.80	8023.00	773.6
362.80	9041.00	774.5
362.80	10000.00	775.3
362.80	11014.00	776.2
362.80	12026.00	777.1
362.80	13045.00	777.9
362.80	14030.00	778.8
362.80	15012.00	779.6
362.80	16031.00	780.4
362.80	17003.00	781.2
362.80	18020.00	782.0
362.80	19033.00	782.8
362.80	20004.00	783.6
362.80	21006.00	784.4
362.80	22032.00	785.2
362.80	22989.00	785.9
362.80	24055.00	786.7
362.80	25035.00	787.5
Reference

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
278.15	100.00	829.2
278.15	5000.00	832.2
278.15	10000.00	835.1
278.15	15000.00	837.8
278.15	20000.00	840.7
283.15	100.00	825.8
283.15	5000.00	828.7
283.15	10000.00	831.6
283.15	15000.00	834.5
283.15	20000.00	837.4
288.15	100.00	822.1
288.15	5000.00	825.2
288.15	10000.00	828.2
288.15	15000.00	831.3
288.15	20000.00	834.0
293.15	100.00	818.7
293.15	5000.00	821.9
293.15	10000.00	824.9
293.15	15000.00	827.9
293.15	20000.00	830.7
298.15	100.00	815.1
298.15	5000.00	818.3
298.15	10000.00	821.5
298.15	15000.00	824.6
298.15	20000.00	827.5
303.15	100.00	811.4
303.15	5000.00	814.8
303.15	10000.00	818.0
303.15	15000.00	821.1
303.15	20000.00	824.2
308.15	100.00	808.0
308.15	5000.00	811.3
308.15	10000.00	814.6
308.15	15000.00	817.8
308.15	20000.00	820.9
313.15	100.00	804.2
313.15	5000.00	807.6
313.15	10000.00	811.0
313.15	15000.00	814.3
313.15	20000.00	817.6
Reference

Fixed		Measured
Pressure, kPa - Liquid	Temperature, K - Liquid	Mass density, kg/m3 - Liquid
100.00	283.15	825.6
100.00	288.15	822.2
100.00	293.15	818.6
100.00	298.15	815.0
100.00	303.15	811.4
100.00	308.15	807.8
100.00	313.15	804.1
100.00	318.15	800.5
100.00	323.15	796.8
5000.00	283.15	828.7
5000.00	288.15	825.2
5000.00	293.15	821.7
5000.00	298.15	818.2
5000.00	303.15	814.7
5000.00	308.15	811.1
5000.00	313.15	807.6
5000.00	318.15	804.0
5000.00	323.15	800.4
10000.00	283.15	831.7
10000.00	288.15	828.2
10000.00	293.15	824.9
10000.00	298.15	821.4
10000.00	303.15	817.9
10000.00	308.15	814.5
10000.00	313.15	811.0
10000.00	318.15	807.5
10000.00	323.15	803.9
20000.00	283.15	837.3
20000.00	288.15	834.1
20000.00	293.15	830.8
20000.00	298.15	827.4
20000.00	303.15	824.1
20000.00	308.15	820.8
20000.00	313.15	817.4
20000.00	318.15	814.0
20000.00	323.15	810.7
30000.00	283.15	842.7
30000.00	288.15	839.5
30000.00	293.15	836.3
30000.00	298.15	833.1
30000.00	303.15	829.9
30000.00	308.15	826.7
30000.00	313.15	823.5
30000.00	318.15	820.1
30000.00	323.15	816.9
40000.00	283.15	847.8
40000.00	288.15	844.7
40000.00	293.15	841.6
40000.00	298.15	838.5
40000.00	303.15	835.4
40000.00	308.15	832.3
40000.00	313.15	829.1
40000.00	318.15	825.9
40000.00	323.15	822.8
50000.00	283.15	852.6
50000.00	288.15	849.6
50000.00	293.15	846.6
50000.00	298.15	843.5
50000.00	303.15	840.5
50000.00	308.15	837.5
50000.00	313.15	834.4
50000.00	318.15	831.4
50000.00	323.15	828.2
60000.00	283.15	857.2
60000.00	288.15	854.3
60000.00	293.15	851.4
60000.00	298.15	848.3
60000.00	303.15	845.4
60000.00	308.15	842.4
60000.00	313.15	839.4
60000.00	318.15	836.4
60000.00	323.15	833.4
Reference

Speed of sound, m/s

Fixed		Measured
Pressure, kPa - Liquid	Temperature, K - Liquid	Speed of sound, m/s - Liquid
101.00	292.91	1320.79
30390.00	292.92	1465.73
45590.00	292.92	1525.8
60790.00	292.91	1581.37
75990.00	292.92	1633.75
91180.00	292.91	1682.67
101320.00	292.91	1713.2
101.00	308.15	1269.05
15200.00	308.15	1349.81
30390.00	308.15	1419.69
45590.00	308.15	1482.88
60790.00	308.15	1540.4
75990.00	308.15	1594.13
91180.00	308.16	1643.48
101320.00	308.16	1675.87
101.00	298.18	1302.75
15200.00	298.19	1381.46
30390.00	298.19	1449.11
45590.00	298.19	1510.11
60790.00	298.19	1566.83
75990.00	298.19	1619.35
91180.00	298.19	1668.5
101320.00	298.19	1699.28
101.00	313.13	1252.38
15200.00	313.14	1334.05
30390.00	313.14	1404.76
45590.00	313.14	1469.3
60790.00	313.14	1527.64
75990.00	313.14	1581.73
91180.00	313.14	1632.08
101320.00	313.14	1664.3
101.00	318.22	1235.52
15200.00	318.22	1318.81
30390.00	318.21	1390.85
45590.00	318.21	1456.0
60790.00	318.21	1514.43
75990.00	318.21	1569.15
91180.00	318.21	1620.49
101320.00	318.21	1653.0
Reference

Correlations

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.64]	kPa	[328.27; 454.77]	The Yaw...
Equation			ln(Pvp) = A + B/(T + C)
Coefficient A			1.49468e+01
Coefficient B			-3.55660e+03
Coefficient C			-8.56520e+01
Temperature range, min.			328.27
Temperature range, max.			454.77
Pvap	1.33	kPa	328.27	Calculated Property
Pvap	2.98	kPa	342.33	Calculated Property
Pvap	6.11	kPa	356.38	Calculated Property
Pvap	11.68	kPa	370.44	Calculated Property
Pvap	21.02	kPa	384.49	Calculated Property
Pvap	35.88	kPa	398.55	Calculated Property
Pvap	58.48	kPa	412.60	Calculated Property
Pvap	91.57	kPa	426.66	Calculated Property
Pvap	138.38	kPa	440.71	Calculated Property
Pvap	202.64	kPa	454.77	Calculated Property
Pvap	[5.21e-05; 3364.66]	kPa	[228.55; 611.35]	KDB Vap...
Equation			ln(Pvp) = A + B/T + C*ln(T) + D*T^2
Coefficient A			1.08932e+02
Coefficient B			-1.08747e+04
Coefficient C			-1.31440e+01
Coefficient D			3.48998e-06
Temperature range, min.			228.55
Temperature range, max.			611.35
Pvap	5.21e-05	kPa	228.55	Calculated Property
Pvap	0.01	kPa	271.08	Calculated Property
Pvap	0.39	kPa	313.62	Calculated Property
Pvap	5.03	kPa	356.15	Calculated Property
Pvap	33.18	kPa	398.68	Calculated Property
Pvap	137.52	kPa	441.22	Calculated Property
Pvap	410.94	kPa	483.75	Calculated Property
Pvap	970.21	kPa	526.28	Calculated Property
Pvap	1926.83	kPa	568.82	Calculated Property
Pvap	3364.66	kPa	611.35	Calculated Property

Similar Compounds

Find more compounds similar to 1-Hexanol.

Mixtures

• Isopropyl Alcohol + 1-Hexanol
• Dimethyl Sulfoxide + 1-Hexanol
• Ethane, 1,2-dichloro- + 1-Hexanol
• Ethane, 1,2-dibromo- + 1-Hexanol
• Tetrachloroethylene + 1-Hexanol
• 1-Propanol, 2-methyl- + 1-Hexanol
• Isobutyl acetate + 1-Hexanol
• Isobutyl acetate + 1-Propanol, 2-methyl- + 1-Hexanol
• 1-Hexanol + Nonane
• 2-Butanone + Benzene, 1,3-dichloro- + 1-Hexanol
• 1-Octene + 1-Hexanol
• 2-Octanone + 1-Hexanol
• 2-Propanol, 1-propoxy- + 1-Hexanol
• Pentanoic acid, 4-oxo- + 1-Hexanol + Water
• 1-Hexanol + Simvastatin
• Cholesterol + 1-Hexanol
• Cholesterol + 1-Hexanol + Cyclohexane
• Acetonitrile + 1-Hexanol
• 2-Propenenitrile + 1-Hexanol
• Formamide, N,N-dimethyl- + 1-Hexanol

Find more mixtures with 1-Hexanol.

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
• Measurements of the Properties of Binary Mixtures of Dimethylsulphoxide (DMSO) with 1-Alkanols (C4, C6, C7) at 303.15K
• Densities, Excess Molar Volumes, Ultrasonic Speeds, and Isentropic Compressibilities of Hexan-1-ol with 1,2-Dichloroethane, 1,2-Dibromoethane, and 1,1,2,2-Tetrachloroethene at (293.15 and 298.15) K
• Liquid phase behavior of imidazolium-based ionic liquids with alcohols: effect of hydrogen bonding and non-polar interactions
• 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
• Density and surface tension variation with temperature for n-nonane + 1-hexanol
• Excess molar volumes of ternary mixtures of 1,3-dichlorobenzene and methyl ethyl ketone with 1-alkanols at 303.15K
• 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
• 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
• Limiting activity coefficients in binary mixtures of 1-alkanols and ethylbenzene
• Vapour liquid equilibria, azeotropic data, excess enthalpies, activity coefficients at infinite dilution and solid liquid equilibria for binary alcohol ketone systems
• Isobaric vapour liquid equilibria of binary 1-propoxy-2-propanol mixtures with water and alcohols at reduced pressure
• Phase equilibria of (water + levunilic acid + alcohol) ternary systems
• Solubility and limiting activity coefficient of simvastatin in different organic solvents
• Solubility of pyrene in simple and mixed solvent systems
• 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}
• Temperature dependence of the excess molar volume of 1-hexanol + 1-alkene systems in terms of an association and equation of state model
• Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 1
• Bubble point measurements of binary mixtures formed by 1-hexanol with selected nitro-compounds and substituted benzenes at 95.6 kPa
• Liquid-liquid phase equilibrium of (piperidinium-based ionic liquid + an alcohol) binary systems and modelling with NRHB and PCP-SAFT
• Liquid density of oxygenated additives to bio-fuels: 1-Hexanol at pressures up to 140 MPa and from 293.15 K to 403.15 K
• Solubility of triclosan and iodopropynyl butylcarbamate in pure alkanols at several temperatures
• Phase behaviour of ionic liquid 1-butyl-1-methylpyrrolidinium tris(pentafluoroethyl)trifluorophosphate with alcohols, water and aromatic hydrocarbons
• Liquid-liquid equilibrium data for systems containing of formic acid, water, and primary normal alcohols at T = 298.2 K
• Liquid-liquid equilibrium data for ternary systems of water + lactic acid + C4-C7 alcohols at 298.2 K and atmospheric pressure
• (p, VE, T) Measurements of mixtures (DBE + alcohol) at temperaturesfrom (293.15 to 353.15) K and at pressures up to 140 MPa
• Unusual behavior of the isotope effect on miscibility of 1-hexyl-3-methylimidazolium bis(trifluorosulfonyl)imide with 1-alkanols
• Liquid-liquid phase equilibria of ionic liquid solutions in the critical region: 1-Methyl-3-octylimidazolium tetrafluoroborate with1-pentanol or 1-hexanol
• Measurement and correlation of the solubility of N-(phosphonomethyl)iminodiacetic acid in different organic solvents
• Phase behaviour of tricyanomethanide-based ionic liquids with alcohols and hydrocarbons
• 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.
• Vapor pressures and thermophysical properties of selected hexenols and recommended vapor pressure for hexan-1-ol
• Isothermal vapor-liquid equilibria, excess molar volume and the deviation of refractive indices for binary mixtures of 1-butanol, 1- hexanol, 3-methyl-1-butanol and butyl acetate
• Solubility and dissolution characteristics of capecitabine in pure lower alcohols and water with methanol mixture solvents at atmospheric pressure and different temperatures
• Solubility determination and correlation of cyromazine in sixteen pure solvents and mixing properties of solutions
• The behavior of mercury in water, alcohols, monoethylene glycol and triethylene glycol II. Elemental mercury solubility in alcohols, ethers and acetone; gas plant mercury distribution; and speciation in monoethylene glycol solution
• Study of molecular interactions and preferential solvation in binary mixtures of cyclohexane and (C5-C10) 1-alkanol by Kirkwood-Buff integrals
• Phase equilibria for ternary liquid systems of (water + carboxylic acid or alcohol + 1-hexanol) at T = 293.15 K: modelling considerations
• 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
• Excess molar volumes of binary mixtures of 1,3-dimethylimidazolidin-2-one with an alkan-1-ol at the temperatures 283.15 K, 298.15 K, and 313.15 K
• Densities and derived thermodynamic properties of binary mixtures of diethylcarbonate, acetophenone, and 1-hexanol at T = (293.15 to 323.15) K for the liquid region and at ambient pressure
• Measurement and correlation of solubility of trans-resveratrol in 11 solvents at T = (278.2, 288.2, 298.2, 308.2, and 318.2) K
• Bubble point measurements of binary mixtures formed by ethyl benzene with selected compounds at 95.35 kPa
• Activity coefficients at infinite dilution of hydrocarbons, alkylbenzenes, and alcohols in the paramagnetic ionic liquid 1-butyl-3-methyl-imidazolium tetrachloridoferrate(III) using gas liquid chromatography
• Studies on thermodynamic properties of binary mixtures of hexan-1-ol with halogenated compounds at T = (308.15 and 313.15) K
• 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
• High-pressure phase equilibria in the (carbon dioxide + 1-hexanol) system
• Ultrasonic speeds and isentropic compressibilities of {difurylmethane + (C1 C6) n-alkanol} binary mixtures at T = 298.15 K
• Cloud point measurements of 1-butyl-2,3-dimethylimidazolium tetrafluoroborate with alcohols
• Thermophysical properties and phase equilibria study of the binary systems {N-hexylquinolinium bis(trifluoromethylsulfonyl)imide + aromatic hydrocarbons, or an alcohol}
• Compressed liquid density measurements for {methylbenzoate + (cyclohexane or 1-hexanol)} binary systems
• Volumetric and viscometric properties of binary mixtures of {methyl tert-butyl ether (MTBE) + alcohol} at several temperatures and p = 0.1 MPa: Experimental results and application of the ERAS model
• Volumetric properties and enthalpies of solution of alcohols CkH2k+1OH (k = 1, 2, 6) in 1-methyl-3-alkylimidazolium bis(trifluoromethylsulfonyl)imide {[C1CnIm][NTf2] n = 2, 4, 6, 8, 10} ionic liquids
• 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
• Comparative study of physico-chemical properties of binary mixtures of N,N-dimethylformamide with 1-alkanols at different temperatures
• Effect of temperature and composition on the density, viscosity, surface tension, and thermodynamic properties of binary mixtures of N-octylisoquinolinium bis{(trifluoromethyl)sulfonyl}imide with alcohols
• 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
• Viscosity and surface tension of binary systems of N,N-dimethylformamide with alkan-1-ols at different temperatures
• Solubility of salicylic acid in pure alcohols at different temperatures
• Density, speed of sound, heat capacity, and related properties of 1-hexanol and 2-ethyl-1-butanol as function of temperature and pressure
• 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
• Ternary liquid liquid equilibrium data for the (water + butyric acid + n-hexane or n-hexanol) systems at T = (298.2, 308.2, and 318.2) K
• On the solubility of nicotinic acid and isonicotinic acid in water and organic solvents
• Study of surface tension and surface properties of binary systems of DMSO with long chain alcohols at various temperatures
• Thermodynamic, transport and excess properties of 2-butoxy ethanol +1-alkanol (C6,C8,C10) at different temperatures
• FT-IR studies on excess thermodynamic properties of binary liquid mixtures o-chlorotoluene with 1-propanol, 1-butanol, 1-pentanol, 1-hexanol and 1-heptanol at different temperatures
• 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
• Application of the NRTL method to correlate solubility of diosgenin
• Solubility of climbazole in various alcohols at different temperatures
• Measurements and equation-of-state modelling of thermodynamic properties of binary mixtures of 1-butyl-1-methylpyrrolidinium tetracyanoborate ionic liquid with molecular compounds
• Volumetric and viscometric study with FT-IR analysis of binary systems with diethyl succinate and alcohols
• Solubility of commercial octacosanol in organic solvents and their correlation by thermodynamic models at different temperatures
• Physical properties of systems of interest to the edible oil industry: Viscosities and densities of model systems formed by (triacylglycerol + fatty acid + solvent)
• High pressure liquid densities and excess volumes of the (di-isopropyl ether + 1-hexanol) system
• Effect of temperature on intermolecular interactions between the organic solvents: Insights from density and excess volume
• Volumetric and transport properties of binary liquid mixtures with 1-ethyl-3-methylimidazolium ethyl sulfate as candidate solvents for regenerative flue gas desulfurization processes
• 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
• Vapor-liquid equilibrium data of binary mixtures of 1-hexanol, 1-heptanol, 1-nonanol and 1,3-propanediol at P = 101.3 kPa using differential scanning calorimetry (DSC)
• The additivity of surface and volumetric properties of alpha,omega-dihalogenoalkanes
• Excess volumes and partial molar volumes of binary liquid mixtures of furfural or 2-methylfuran with alcohols at 298.15 K
• Liquid-liquid equilibrium for (water + 5-hydroxymethylfurfural + 1-pentanol/1-hexanol/1-heptanol) systems at 298.15 K
• Solubility and mixing thermodynamic properties of levamisole hydrochloride in twelve pure solvents at various temperatures
• Excess molar enthalpies of methyl isobutyl ketone (MIBK) with alkan-1-ols (C1-C6) and their correlations at 298.15 K
• Thermophysical properties and thermodynamic phase behavior of ionic liquids
• ERAS modeling of the excess molar enthalpies of binary liquid mixtures of 1-pentanol and 1-hexanol with acetonitrile at atmospheric pressure and 288, 298, 313 and 323K
• Excess molar enthalpies and heat capacities of dimethyl sulfoxide + seven normal alkanols at 303.15K and atmospheric pressure
• Thermodynamic and spectral studies of molecular interactions in binary liquid mixtures of 1-butoxy-2- propanol with 1-alcohols
• 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
• Surface Tension of Binary Mixtures of 2,2,4-Trimethylpentane +1-Alkanols from 298.15 to 323.15 K
• Densities and Viscosities for Binary Liquid Mixtures of n-Undecane + 1-Propanol, + 1-Butanol, + 1-Pentanol, and + 1-Hexanol from 283.15 to 363.15 K at 0.1 MPa
• Determination and Correlation of Solubility of Phenylbutazone in Monosolvents and Binary Solvent Mixtures
• Solubilities of 4',5,7-Triacetoxyflavanone in Fourteen Organic Solvents at Different Temperatures
• Thermodynamic Functions for Solubility of 1-Hydroxybenzotriazole in Sixteen Solvents at Temperatures from (278.15 to 313.15) K and Mixing Property of Mixtures
• Solubility and Thermodynamic Behavior of Syringic Acid in Eight Pure and Water + Methanol Mixed Solvents
• Correlation Studies of Cyclohexanone/(C5-C10) Alkan-1-ol Binary Mixtures: PC-SAFT Model and Free Volume Theory
• Solubility Modeling and Solvent Effects of Allopurinol in 15 Neat Solvents
• 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
• 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
• Kirkwood-Buff Integrals, Excess Volume, and Preferential Solvation in Pentanoic Acid/(C5-C10) 1-Alkanol Binary Mixtures
• 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 Determination and Modeling of EGCG Peracetate in 12 Pure Solvents at Temperatures from 278.15 to 318.15 K
• Solubility Study and Mixing Property of 3,5-Dinitro-2-methylbenzoic Acid in 13 Pure Solvents from 288.15 to 333.15 K
• Thermodynamic Properties of 1-Hexyl-3-methylimidazolium Nitrate and 1-Alkanols Mixtures: PC-SAFT Model
• Liquid-Liquid Equilibria for Ternary Mixtures of Water + Ethanol with 1-Hexanol, Butyl Propionate, or Ethyl Caproate
• Excess Molar Enthalpies of Propyl Propanoate + 1-Hexanol + Benzene at the Temperatures of 25 :C and 35 :C
• Solubility of Benzimidazoles in Alcohols
• A Study on Properties Derived from Densities and Viscosities for the Ternary Systems (Methyl Pentanoate or Methyl Heptanoate) + n-Octane + 1-Hexanol and their Binary Subsystems at Various Temperatures.
• 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
• Measurement and Prediction of Thermochemical Properties. Improved Benson-Type Increments for the Estimation of Enthalpies of Vaporization and Standard Enthalpies of Formation of Aliphatic Alcohols
• Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
• Liquid-Liquid Equilibria for the Ternary Systems of (Water + Tetrahydrofuran + Polar Solvent) at 298.15 K
• Liquid-Liquid Equilibrium of MTBE + Ethanol + Water and MTBE + 1-Hexanol + Water over the Temperature Range of 288.15 to 308.15 K
• Solubility and Density of 2,6-Dimethylnaphthalene in C1-C7 1-Alkanols
• Thermodynamic Properties of Mixtures Containing Ionic Liquids. 5. Activity Coefficients at Infinite Dilution of Hydrocarbons, Alcohols, Esters, and Aldehydes in 1-Methyl-3-butyl-imidazolium Bis(trifluoromethyl-sulfonyl) Imide Using Gas-Liquid Chromatography
• Thermodynamic Properties of Mixtures Containing Ionic Liquids. 6. Activity Coefficients at Infinite Dilution of Hydrocarbons, Alcohols, Esters, and Aldehydes in 1-Methyl-3-octyl-imidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
• Phase Equlibria for Hexyl Acetate Reactive Distillation
• 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
• Thermodynamic Properties of Mixtures Containing Ionic Liquids. 9. Activity Coefficients at Infinite Dilution of Hydrocarbons, Alcohols, Esters, and Aldehydes in Trimethyl-butylammonium Bis(trifluoromethylsulfonyl) Imide Using Gas-Liquid Chromatography and Static Method
• Densities, Viscosities, and Ultrasonic Velocity Studies of Binary Mixtures of Chloroform with Pentan-1-ol, Hexan-1-ol, and Heptan-1-ol at (303.15 and 313.15) K
• Excess Molar Enthalpies of 1,2-Propanediol + Alkan-1-ols (C1-C6) and Their Correlations at 298.15 K and Ambient Pressure (81.5 kPa)
• Henry s Constants of 1-Alkanols and 2-Ketones in Salt Solutions
• Compressed Liquid Densities and Excess Molar Volumes of CO2 + Hexan-1-ol Mixtures from (313 to 363) K and Pressures up to 25 MPa
• Density and Surface Tension Variation with Temperature for Heptane + 1-Alkanol
• Effect of Pressure on the Static Relative Permittivities of Alkan-1-ols at 298.15 K
• Experimental Study of Thermodynamic Properties of Mixtures Containing Ionic Liquid 1-Ethyl-3-methylimidazolium Ethyl Sulfate Using Gas-Liquid Chromatography and Transpiration Method
• 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
• Excess Molar Enthalpies of Benzyl Alcohol + Alkanols (C1-C6) and Their Correlations at 298.15 K and Ambient Pressure
• Volumetric and Viscometric Behavior of the Binary System: (Hexan-1-ol + p-Xylene)
• Thermodynamic Parameters of Anionic Surfactant-Additive Systems at the Cloud Point
• Thermodynamics of Dissolution for Bis(triazine)-Bipyridine-Class Ligands in Different Diluents and Its Reflection on Extraction
• Density and Viscosity of the Binary Mixtures of Hexan-1-ol with Isomeric Xylenes at T = (308.15 and 318.15) K and Atmospheric Pressure
• Liquid-Liquid Phase Behavior of Solutions of 1-Hexyl-3-methylimidazolium Bis((trifluoromethyl)sulfonyl)amide (C6mimNTf2) in n-Alkyl Alcohols
• Solubilities of Phloretin in 12 Solvents at Different Temperatures
• Measurement and Study on the Liquid Liquid Equilibrium of Ionic Liquids with Aliphatic Alcohols
• Liquid Liquid Phase Equilibria of 1-Propanol + Water + n-Alcohol Ternary Systems at 298.15 K and Atmospheric Pressure
• Solubilities of Betulinic Acid in Thirteen Organic Solvents at Different Temperatures
• Liquid Liquid Phase Behavior of Solutions of 1-Butyl-3-methylimidazolium Bis((trifluoromethyl)sulfonyl)amide (C4mimNTf2) in n-Alkyl Alcohols
• Liquid Phase Behavior of 1-Butyl-1-methylpyrrolidinium Bis(trifluoromethylsulfonyl)imide with 1-Butanol or Hexan-1-ol: Measurements of Coexistence Curves, Density, and Interfacial Tension
• Vapor Liquid Equilibrium Data for Binary Systems of 1-Methyl-4-(1-methylethenyl)-cyclohexene + {Ethanol, Propan-1-ol, Propan-2-ol, Butan-1-ol, Pentan-1-ol, or Hexan-1-ol} at 40 kPa
• 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
• Determination and Correlation of Solubilities of Lauric Acid in Eight Alcohols
• Isobaric Vapor Liquid Equilibria of Binary Systems (Propyl Acetate + 2-Methylbutan-1-ol), (Propyl Acetate + Hexan-1-ol), and (Propyl Acetate + Heptan-1-ol) at 101.3 kPa
• Comparison Study on Temperature Dependence of the Interfacial Tension of n-Alkane Water and n-Alcohol Water Two Binary Systems
• Volumetric and Viscometric Study of Binary Systems of Ethyl Butyrate with Alcohols
• Densities and Viscosities of Binary Mixtures of 2,2,4-Trimethylpentane + 1-Propanol, + 1-Pentanol, + 1-Hexanol, and + 1-Heptanol from (298.15 to 323.15) K
• Density and Viscosity of Binary Liquid Mixtures of Ethanol + 1-Hexanol and Ethanol + 1-Heptanol from (293.15 to 328.15) K at 0.1 MPa
• 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, Viscosities, Speeds of Sound, and Refractive Indices for Binary Mixtures of Diethylcarbonate, Acetophenone, and 1-Hexanol at (293.15, 303.15, 313.15, and 323.15) K for the Liquid Region and at Ambient Pressure
• Solubilities of Betulin in Fourteen Organic Solvents at Different Temperatures
• Densities and Viscosities for Binary and Ternary Mixtures of 1, 4-Dioxane + 1-Hexanol + N,N-Dimethylaniline from T ) (283.15 to 343.15) K
• Densities and Excess Molar Volumes of N-Methylmorpholine + 1-Alkanol Systems at 298.15 K
• Liquid Liquid Equilibria for the Quaternary Systems of Water + N-Methyl-2-pyrrolidone + 1-Hexanol + NaCl, + KCl, or + KAc
• 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
• Setup and Validation of a PGT Measuring Device. Volumetric Behavior of the Mixture 1,8-Cineole + Ethanol
• Surface Properties of Binary Mixtures of Ethylene Glycol with a Series of Aliphatic Alcohols (1-Pentanol, 1-Hexanol, and 1-Heptanol)
• Measurement and Correlation of the Solubilities of m-Phthalic Acid in Monobasic Alcohols
• Phase Equilibria Study of the Binary Systems (N-Butyl-4-methylpyridinium Tosylate Ionic Liquid + Organic Solvent, or Water)
• Thermophysical Characterization of Liquids Using Precise Density and Isobaric Heat Capacity Measurements As a Function of Pressure
• Paramagnetic Ionic Liquid 1-Butyl-3-methylimidazolium Tetrabromidocobaltate(II): Activity Coefficients at Infinite Dilution of Organic Solutes and Crystal Structure
• Thermodynamic Properties of Micellization of Sodium Dodecylbenzene Sulfonate in the Aqueous-Rich Region of 1-Pentanol and 1-Hexanol
• Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
• Vapor-Liquid Equilibria of Binary Mixtures Formed by Hexan-1-ol with Chloroethanes and Chloroethenes at 95.6 kPa
• Thermodynamic Properties of the Binary Mixture of Hexan-1-ol with m-Xylene at T = (303.15, 313.15, and 323.15) K
• Studies on Transport and Thermodynamic Properties of Binary Mixtures of Hexan-1-ol with Halogenated Compounds at 293.15 K
• 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
• Measurement and Correlation of Solubilities of Decanedioic Acid in C4-C6 Alcohol Solvents
• Studies of Monohydric Alcohols in Aqueous Sodium Dodecyl Sulfate Solutions at T = (298.15 and 308.15) K
• Densities, Viscosities, and Volumetric Properties of Binary Mixtures of 1,2-Propanediol + 1-Heptanol or 1-Hexanol and 1,2-Ethanediol + 2-Butanol or 2-Propanol at T = (298.15, 303.15, and 308.15) K
• Joback Method
• KDB
• Aqueous Solubility Prediction Method
• Estimated Solubility Method
• McGowan Method
• NIST Webbook
• The Yaws Handbook of Vapor Pressure

Note: Cheméo is only indexing the data, follow the source links to retrieve the latest data. The source is also providing more information like the publication year, authors and more. Take the time to validate and double check the source of the data.
Outlier This icon means that the value is more than 2 standard deviations away from the property mean.