Chemical Properties of Propane, 1-chloro-2-methyl- (CAS 513-36-0)

InChI

InChI=1S/C4H9Cl/c1-4(2)3-5/h4H,3H2,1-2H3

InChI Key

QTBFPMKWQKYFLR-UHFFFAOYSA-N

Formula

C4H9Cl

SMILES

CC(C)CCl

Molecular Weight¹

92.57

CAS

513-36-0

Other Names

• 1-chloro-2-methylpropane
• iso-C4H9Cl
• isobutyl chloride

• ω : Acentric Factor.
• 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).
• 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_fusH° : Enthalpy of fusion 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).
• 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).
• P_c : Critical Pressure (kPa).
• P_vap : Vapor pressure (kPa).
• n₀ : Refractive Index.
• ρ_l : Liquid Density (kg/m³).
• I_np : Non-polar retention indices.
• T_boil : Normal Boiling Point Temperature (K).
• T_c : Critical Temperature (K).
• T_fus : Normal melting (fusion) point (K).
• V_c : Critical Volume (m³/kmol).
• ¹: Molecular weight from the IUPAC atomic weights tables.

Physical Properties

Property	Value	Unit	Source
ω	0.2473		Relay (1.0) Calculated Property
ΔcH°liquid	-2692.80 ± 8.40	kJ/mol	NIST
ΔfG°	-31.57	kJ/mol	Joback Calculated Property
ΔfH°gas	-179.79	kJ/mol	Relay (1.0) Calculated Property
ΔfusH°	6.79	kJ/mol	Joback Calculated Property
ΔvapH°	[31.67; 31.81]	kJ/mol
ΔvapH°	31.81	kJ/mol	NIST
ΔvapH°	31.70 ± 0.10	kJ/mol	NIST
ΔvapH°	31.67 ± 0.06	kJ/mol	NIST
IE	[10.50; 10.80]	eV
IE	10.73 ± 0.07	eV	NIST
IE	10.62	eV	NIST
IE	10.80	eV	NIST
IE	10.50 ± 0.10	eV	NIST
IE	10.66 ± 0.03	eV	NIST
log10WS	[-2.00; -2.00]
log10WS	-2.00		Aq. Solubility Prediction
log10WS	-2.00		Estimated Solubility
logPoct/wat	1.881		Crippen Calculated Property
McVol	79.460	ml/mol	McGowan Calculated Property
Pc	3759.17	kPa	Joback Calculated Property
Inp	[588.00; 623.00]
Inp	595.00		NIST
Inp	596.00		NIST
Inp	588.00		NIST
Inp	592.00		NIST
Inp	594.00		NIST
Inp	597.00		NIST
Inp	619.00		NIST
Inp	603.00		NIST
Inp	602.00		NIST
Inp	Outlier 623.00		NIST
Inp	604.00		NIST
Inp	604.00		NIST
Inp	604.00		NIST
Inp	604.00		NIST
Inp	605.00		NIST
Inp	Outlier 623.00		NIST
Inp	602.00		NIST
Tboil	[341.55; 342.35]	K
Tboil	342.05	K	Study of tetrahydropyran-chlorobutane VLE using the a o and o o approaches
Tboil	342.05	K	Vapor-Liquid Equilibrium and Volumetric Measurements for Binary Mixtures of 1,4-Dioxane with Isomeric Chlorobutanes
Tboil	342.20	K	NIST
Tboil	341.60	K	NIST
Tboil	342.35 ± 0.60	K	NIST
Tboil	341.65 ± 0.30	K	NIST
Tboil	341.55 ± 0.30	K	NIST
Tboil	342.00 ± 0.30	K	NIST
Tboil	342.00 ± 0.50	K	NIST
Tboil	342.00 ± 0.50	K	NIST
Tboil	342.00 ± 0.20	K	NIST
Tc	528.81	K	Relay (1.0) Calculated Property
Tfus	156.17	K	Relay (1.0) Calculated Property
Vc	0.290	m3/kmol	Relay (1.0) Calculated Property

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[134.00; 162.00]	J/mol×K	[290.00; 310.00]
Cp,liquid	134.00	J/mol×K	290.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	158.60	J/mol×K	298.00	NIST
Cp,liquid	145.00	J/mol×K	298.15	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	148.00	J/mol×K	300.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	162.00	J/mol×K	310.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
η	[0.0003664; 0.0005155]	Pa×s	[283.15; 313.15]
η	0.0005155	Pa×s	283.15	Viscosities of Binary Mixtures Containing Isomeric Chlorobutanes and Diisopropylether: Experimental and Predicted Values
η	0.0005155	Pa×s	283.15	Experimental and Predicted Viscosities of Binary Mixtures Containing Chlorinated and Oxygenated Compounds
η	0.0004833	Pa×s	288.15	Viscosities of Binary Mixtures Containing Isomeric Chlorobutanes and Diisopropylether: Experimental and Predicted Values
η	0.0004833	Pa×s	288.15	Experimental and Predicted Viscosities of Binary Mixtures Containing Chlorinated and Oxygenated Compounds
η	0.0004540	Pa×s	293.15	Experimental and Predicted Viscosities of Binary Mixtures Containing Chlorinated and Oxygenated Compounds
η	0.0004540	Pa×s	293.15	Viscosities of Binary Mixtures Containing Isomeric Chlorobutanes and Diisopropylether: Experimental and Predicted Values
η	0.0004296	Pa×s	298.15	Viscosities of Binary Mixtures Containing Isomeric Chlorobutanes and Diisopropylether: Experimental and Predicted Values
η	0.0004295	Pa×s	298.15	Densities and Viscosities of the Binary Mixtures of Tetrahydrofuran with Isomeric Chlorobutanes at 298.15 K and 313.15 K
η	0.0004296	Pa×s	298.15	Experimental and Predicted Viscosities of Binary Mixtures Containing Chlorinated and Oxygenated Compounds
η	0.0004112	Pa×s	303.15	Viscosities of Binary Mixtures Containing Isomeric Chlorobutanes and Diisopropylether: Experimental and Predicted Values
η	0.0004112	Pa×s	303.15	Experimental and Predicted Viscosities of Binary Mixtures Containing Chlorinated and Oxygenated Compounds
η	0.0003921	Pa×s	308.15	Experimental and Predicted Viscosities of Binary Mixtures Containing Chlorinated and Oxygenated Compounds
η	0.0003921	Pa×s	308.15	Viscosities of Binary Mixtures Containing Isomeric Chlorobutanes and Diisopropylether: Experimental and Predicted Values
η	0.0003726	Pa×s	313.15	Viscosities of Binary Mixtures Containing Isomeric Chlorobutanes and Diisopropylether: Experimental and Predicted Values
η	0.0003726	Pa×s	313.15	Experimental and Predicted Viscosities of Binary Mixtures Containing Chlorinated and Oxygenated Compounds
η	0.0003664	Pa×s	313.15	Densities and Viscosities of the Binary Mixtures of Tetrahydrofuran with Isomeric Chlorobutanes at 298.15 K and 313.15 K
ΔvapH	[29.22; 36.10]	kJ/mol	[280.50; 341.60]
ΔvapH	36.10	kJ/mol	280.50	NIST
ΔvapH	29.22	kJ/mol	341.60	NIST
ν	[0.0000004; 0.0000006]	m2/s	[283.15; 313.15]
ν	0.0000006	m2/s	283.15	Experimental and Predicted Kinematic Viscosities for Alkane + Chloroalkane Mixtures
ν	0.0000005	m2/s	298.15	Thermophysical Properties of Mixtures of Tetrahydropyran with Chlorobutanes
ν	0.0000005	m2/s	298.15	Viscosities of Binary Mixtures of Isomeric Butanols or Isomeric Chlorobutanes with 2-Methyltetrahydrofuran
ν	0.0000005	m2/s	298.15	Experimental and Predicted Kinematic Viscosities for Alkane + Chloroalkane Mixtures
ν	0.0000004	m2/s	313.15	Thermophysical Properties of Mixtures of Tetrahydropyran with Chlorobutanes
ν	0.0000004	m2/s	313.15	Viscosities of Binary Mixtures of Isomeric Butanols or Isomeric Chlorobutanes with 2-Methyltetrahydrofuran
ν	0.0000004	m2/s	313.15	Experimental and Predicted Kinematic Viscosities for Alkane + Chloroalkane Mixtures
Pvap	[13.00; 30.45]	kPa	[288.15; 308.15]
Pvap	13.00	kPa	288.15	Isothermal vapour-liquid equilibria and excess enthalpies for the binary mixtures containing an isomeric chlorobutane and diisopropyl ether
Pvap	13.00	kPa	288.15	Experimental and predicted vapour-liquid equilibrium of the binary mixtures n-heptane + chlorobutane isomers
Pvap	13.00	kPa	288.15	Experimental and predicted properties of the binary mixtures containing an isomeric chlorobutane and butyl ethyl ether
Pvap	13.00	kPa	288.15	Article Previous Article Next Article Articles ASAP Phase Equilibrium of Binary Mixtures of n-Hexane + Branched Chlorobutanes: Experimental Results and Group Contribution Predictions
Pvap	20.35	kPa	298.15	Isothermal vapour-liquid equilibria and excess enthalpies for the binary mixtures containing an isomeric chlorobutane and diisopropyl ether
Pvap	20.35	kPa	298.15	Experimental and predicted vapour-liquid equilibrium of the binary mixtures n-heptane + chlorobutane isomers
Pvap	20.35	kPa	298.15	Experimental and predicted properties of the binary mixtures containing an isomeric chlorobutane and butyl ethyl ether
Pvap	20.35	kPa	298.15	Article Previous Article Next Article Articles ASAP Phase Equilibrium of Binary Mixtures of n-Hexane + Branched Chlorobutanes: Experimental Results and Group Contribution Predictions
Pvap	30.45	kPa	308.15	Isothermal vapour-liquid equilibria and excess enthalpies for the binary mixtures containing an isomeric chlorobutane and diisopropyl ether
Pvap	30.45	kPa	308.15	Experimental and predicted vapour-liquid equilibrium of the binary mixtures n-heptane + chlorobutane isomers
Pvap	30.45	kPa	308.15	Experimental and predicted properties of the binary mixtures containing an isomeric chlorobutane and butyl ethyl ether
Pvap	30.45	kPa	308.15	Article Previous Article Next Article Articles ASAP Phase Equilibrium of Binary Mixtures of n-Hexane + Branched Chlorobutanes: Experimental Results and Group Contribution Predictions
n0	[1.38683; 1.40354]		[283.15; 313.15]
n0	1.40354		283.15	Volumetric, Acoustic, and Refractive Properties of Isomeric Chlorobutanes with Diisopropyl Ether
n0	1.40080		288.15	Volumetric, Acoustic, and Refractive Properties of Isomeric Chlorobutanes with Diisopropyl Ether
n0	1.39802		293.15	Volumetric, Acoustic, and Refractive Properties of Isomeric Chlorobutanes with Diisopropyl Ether
n0	1.39528		298.15	Volumetric and refractive properties of binary mixtures containing 1,4-dioxane and chloroalkanes
n0	1.39529		298.15	Volumetric, Acoustic, and Refractive Properties of Isomeric Chlorobutanes with Diisopropyl Ether
n0	1.39245		303.15	Volumetric, Acoustic, and Refractive Properties of Isomeric Chlorobutanes with Diisopropyl Ether
n0	1.38963		308.15	Volumetric, Acoustic, and Refractive Properties of Isomeric Chlorobutanes with Diisopropyl Ether
n0	1.38686		313.15	Volumetric and refractive properties of binary mixtures containing 1,4-dioxane and chloroalkanes
n0	1.38683		313.15	Volumetric, Acoustic, and Refractive Properties of Isomeric Chlorobutanes with Diisopropyl Ether
ρl	[870.89; 871.13]	kg/m3	[298.15; 298.15]
ρl	871.13	kg/m3	298.15	Surface Tension of Mixtures of Tetrahydrofuran or Tetrahydropyran with Isomeric Chlorobutanes
ρl	871.13	kg/m3	298.15	Surface study of mixtures containing cyclic ethers and isomeric chlorobutanes
ρl	870.89	kg/m3	298.15	Thermodynamic study of 2-methyl-tetrahydrofuran with isomeric chlorobutanes

Datasets

Mass density, kg/m3

Fixed		Measured
Pressure, kPa - Liquid	Temperature, K - Liquid	Mass density, kg/m3 - Liquid
100.00	283.15	888.74
100.00	288.15	883.47
100.00	293.15	877.41
100.00	298.15	871.72
100.00	303.15	865.91
100.00	308.15	860.63
100.00	313.15	854.27
100.00	318.15	848.89
100.00	323.15	842.52
100.00	328.15	837.0
2000.00	283.15	890.75
2000.00	288.15	885.59
2000.00	293.15	879.49
2000.00	298.15	873.82
2000.00	303.15	868.26
2000.00	308.15	863.03
2000.00	313.15	856.75
2000.00	318.15	851.46
2000.00	323.15	845.19
2000.00	328.15	839.85
5000.00	283.15	893.77
5000.00	288.15	888.71
5000.00	293.15	882.8
5000.00	298.15	877.2
5000.00	303.15	871.68
5000.00	308.15	866.72
5000.00	313.15	860.48
5000.00	318.15	855.36
5000.00	323.15	849.19
5000.00	328.15	844.08
7000.00	283.15	895.72
7000.00	288.15	890.75
7000.00	293.15	884.93
7000.00	298.15	879.37
7000.00	303.15	873.97
7000.00	308.15	869.17
7000.00	313.15	862.93
7000.00	318.15	857.9
7000.00	323.15	851.95
7000.00	328.15	846.74
10000.00	283.15	898.62
10000.00	288.15	893.72
10000.00	293.15	888.0
10000.00	298.15	882.59
10000.00	303.15	877.32
10000.00	308.15	872.31
10000.00	313.15	866.38
10000.00	318.15	861.51
10000.00	323.15	855.62
10000.00	328.15	850.7
20000.00	283.15	907.63
20000.00	288.15	903.03
20000.00	293.15	897.62
20000.00	298.15	892.47
20000.00	303.15	887.46
20000.00	308.15	882.89
20000.00	313.15	877.3
20000.00	318.15	872.7
20000.00	323.15	867.15
20000.00	328.15	862.58
30000.00	283.15	915.91
30000.00	288.15	911.59
30000.00	293.15	906.26
30000.00	298.15	901.48
30000.00	303.15	896.65
30000.00	308.15	892.36
30000.00	313.15	887.04
30000.00	318.15	882.71
30000.00	323.15	877.47
30000.00	328.15	873.25
40000.00	283.15	923.6
40000.00	288.15	919.26
40000.00	293.15	914.31
40000.00	298.15	909.72
40000.00	303.15	905.09
40000.00	308.15	901.1
40000.00	313.15	895.94
40000.00	318.15	891.92
40000.00	323.15	886.79
40000.00	328.15	882.68
50000.00	283.15	930.74
50000.00	288.15	926.55
50000.00	293.15	921.75
50000.00	298.15	917.36
50000.00	303.15	912.92
50000.00	308.15	909.05
50000.00	313.15	904.09
50000.00	318.15	900.17
50000.00	323.15	895.27
50000.00	328.15	889.88
60000.00	283.15	937.43
60000.00	288.15	933.39
60000.00	293.15	928.75
60000.00	298.15	924.47
60000.00	303.15	920.14
60000.00	308.15	916.5
60000.00	313.15	911.72
60000.00	318.15	907.95
60000.00	323.15	903.21
60000.00	328.15	899.53
65000.00	283.15	940.6
65000.00	288.15	936.76
65000.00	293.15	932.1
65000.00	298.15	927.91
65000.00	303.15	923.66
65000.00	308.15	920.02
65000.00	313.15	915.32
65000.00	318.15	911.65
65000.00	323.15	906.99
65000.00	328.15	903.34
Reference

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[103.43; 234.50]	J/mol×K	[273.00; 1000.00]	Joback Predicted correlation
Equation			Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is Cp,gas in J/mol×K, T in K
Coefficient A			1.04610e+01
Coefficient B			3.96540e-01
Coefficient C			-2.17400e-04
Coefficient D			4.49000e-08
Coefficient E			0.00000e+00
Temperature range, min.			273.00
Temperature range, max.			1000.00
Cp,gas	103.43	J/mol×K	273.00	Calculated Property
Cp,gas	125.53	J/mol×K	353.78	Calculated Property
Cp,gas	145.41	J/mol×K	434.56	Calculated Property
Cp,gas	163.22	J/mol×K	515.33	Calculated Property
Cp,gas	179.10	J/mol×K	596.11	Calculated Property
Cp,gas	193.19	J/mol×K	676.89	Calculated Property
Cp,gas	205.63	J/mol×K	757.67	Calculated Property
Cp,gas	216.57	J/mol×K	838.44	Calculated Property
Cp,gas	226.15	J/mol×K	919.22	Calculated Property
Cp,gas	234.50	J/mol×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.66]	kPa	[248.92; 365.29]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.41015e+01
Coefficient B			-2.81263e+03
Coefficient C			-4.53090e+01
Temperature range, min.			248.92
Temperature range, max.			365.29
Pvap	1.33	kPa	248.92	Calculated Property
Pvap	3.04	kPa	261.85	Calculated Property
Pvap	6.32	kPa	274.78	Calculated Property
Pvap	12.16	kPa	287.71	Calculated Property
Pvap	21.89	kPa	300.64	Calculated Property
Pvap	37.22	kPa	313.57	Calculated Property
Pvap	60.28	kPa	326.50	Calculated Property
Pvap	93.57	kPa	339.43	Calculated Property
Pvap	139.96	kPa	352.36	Calculated Property
Pvap	202.66	kPa	365.29	Calculated Property
Pvap	[0.13; 101.55]	kPa	[219.40; 342.10]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.39950e+01
Coefficient B			-2.77480e+03
Coefficient C			-4.61040e+01
Reference			Stull, 1947
Temperature range, min.			219.40
Temperature range, max.			342.10
Pvap	0.13	kPa	219.40	Calculated Property
Pvap	0.43	kPa	233.03	Calculated Property
Pvap	1.17	kPa	246.67	Calculated Property
Pvap	2.83	kPa	260.30	Calculated Property
Pvap	6.15	kPa	273.93	Calculated Property
Pvap	12.22	kPa	287.57	Calculated Property
Pvap	22.59	kPa	301.20	Calculated Property
Pvap	39.23	kPa	314.83	Calculated Property
Pvap	64.58	kPa	328.47	Calculated Property
Pvap	101.55	kPa	342.10	Calculated Property

Similar Compounds

Find more compounds similar to Propane, 1-chloro-2-methyl-.

Mixtures

• 1,3-Dioxolane + Propane, 1-chloro-2-methyl-
• Propane, 1-chloro-2-methyl- + 1,4-Dioxane
• Tetrahydropyran + Propane, 1-chloro-2-methyl-
• n-Hexane + Propane, 1-chloro-2-methyl-
• Propane, 1-chloro-2-methyl- + Heptane
• Butane, 1-ethoxy- + Propane, 1-chloro-2-methyl-
• Propane, 1-chloro-2-methyl- + Furan, tetrahydro-2-methyl-
• Diisopropyl ether + Propane, 1-chloro-2-methyl-
• Propane, 1-chloro-2-methyl- + Tetrahydrofuran
• Propane, 1-chloro-2-methyl- + Propane, 2-methoxy-2-methyl-
• Propane, 1-chloro-2-methyl- + Pentane, 3-methyl-
• Propane, 1-chloro-2-methyl- + Butane, 2,2-dimethyl-

Sources

• Cheméo Relay (1.0)
• Crippen Method
• Thermophysical Properties of Mixtures of Tetrahydropyran with Chlorobutanes
• Surface Tension of Mixtures of Tetrahydrofuran or Tetrahydropyran with Isomeric Chlorobutanes
• Viscosities of Binary Mixtures Containing Isomeric Chlorobutanes and Diisopropylether: Experimental and Predicted Values
• Experimental and Predicted Viscosities of Binary Mixtures Containing Chlorinated and Oxygenated Compounds
• Study of tetrahydropyran-chlorobutane VLE using the a o and o o approaches
• Isothermal vapour-liquid equilibria and excess enthalpies for the binary mixtures containing an isomeric chlorobutane and diisopropyl ether
• Experimental and predicted vapour-liquid equilibrium of the binary mixtures n-heptane + chlorobutane isomers
• Volumetric and refractive properties of binary mixtures containing 1,4-dioxane and chloroalkanes
• Surface study of mixtures containing cyclic ethers and isomeric chlorobutanes
• Volumetric and acoustic behaviour of systems containing n-hexane, or n-heptane and isomeric chlorobutanes
• Experimental and predicted properties of the binary mixtures containing an isomeric chlorobutane and butyl ethyl ether
• Refractive indices and static permittivities of systems containing n-hexane or n-heptane and isomeric chlorobutanes
• Thermodynamic study of 2-methyl-tetrahydrofuran with isomeric chlorobutanes
• Excess properties from p.rho.T data for n-heptane + isomeric chlorobutane mixtures
• Vapor-Liquid Equilibrium and Volumetric Measurements for Binary Mixtures of 1,4-Dioxane with Isomeric Chlorobutanes
• Viscosities of Binary Mixtures of Isomeric Butanols or Isomeric Chlorobutanes with 2-Methyltetrahydrofuran
• Densities and Viscosities of the Binary Mixtures of Tetrahydrofuran with Isomeric Chlorobutanes at 298.15 K and 313.15 K
• Volumetric, Acoustic, and Refractive Properties of Isomeric Chlorobutanes with Diisopropyl Ether
• Experimental and Predicted Kinematic Viscosities for Alkane + Chloroalkane Mixtures
• Volumetric Properties of Short-Chain Chloroalkanes
• Article Previous Article Next Article Articles ASAP Phase Equilibrium of Binary Mixtures of n-Hexane + Branched Chlorobutanes: Experimental Results and Group Contribution Predictions
• Joback Method
• Aqueous Solubility Prediction Method
• Estimated Solubility Method
• McGowan Method
• NIST Webbook
• The Yaws Handbook of Vapor Pressure
• Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD

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