Chemical Properties of Ethane, 1,1,2,2-tetrachloro- (CAS 79-34-5)

InChI

InChI=1S/C2H2Cl4/c3-1(4)2(5)6/h1-2H

InChI Key

QPFMBZIOSGYJDE-UHFFFAOYSA-N

Formula

C2H2Cl4

SMILES

ClC(Cl)C(Cl)Cl

Molecular Weight¹

167.85

CAS

79-34-5

Other Names

• (CHCl2)2
• 1,1,2,2-Czterochloroetan
• 1,1,2,2-Tetrachloorethaan
• 1,1,2,2-Tetrachloraethan
• 1,1,2,2-Tetrachlorethane
• 1,1,2,2-Tetracloroetano
• 1,1,2,2-tetrachloroethane
• 1,1-Dichloro-2,2-dichloroethane
• Acetosol
• Bonoform
• Cellon
• Freon 130
• NCI-C03554
• NSC 60912
• R-130
• Rcra waste number U209
• S-Tetrachloroethane
• Tetrachlorethane
• Tetrachloroethane
• Tetrachlorure d'acetylene
• UN 1702
• Westron
• acetylene tetrachloride
• sym-tetrachloroethane

• 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).
• μ : Dipole Moment (debye).
• η : Dynamic viscosity (Pa×s).
• Δ_fG° : Standard Gibbs free energy of formation (kJ/mol).
• Δ_fH°_gas : Enthalpy of formation at standard conditions (kJ/mol).
• Δ_fH°_liquid : Liquid phase enthalpy of formation at standard conditions (kJ/mol).
• Δ_fusH° : Enthalpy of fusion at standard conditions (kJ/mol).
• Δ_fusH : Enthalpy of fusion at a given temperature (kJ/mol).
• Δ_vapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
• Δ_vapH : Enthalpy of vaporization at a given temperature (kJ/mol).
• IE : Ionization energy (eV).
• log₁₀WS : Log10 of Water solubility in mol/l.
• logP_oct/wat : Octanol/Water partition coefficient.
• McVol : McGowan's characteristic volume (ml/mol).
• 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.
• I_p : Polar retention indices.
• Δ_fusS : Entropy of fusion at a given temperature (J/mol×K).
• S°_liquid : Liquid phase molar entropy at standard conditions (J/mol×K).
• c_sound,fluid : Speed of sound in fluid (m/s).
• γ : Surface Tension (N/m).
• T_boil : Normal Boiling Point Temperature (K).
• T_c : Critical Temperature (K).
• T_fus : Normal melting (fusion) point (K).
• T_triple : Triple Point Temperature (K).
• V_c : Critical Volume (m³/kmol).
• ¹: Molecular weight from the IUPAC atomic weights tables.

Physical Properties

Property	Value	Unit	Source
ω	0.3180		PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
ΔcH°liquid	-972.80 ± 8.40	kJ/mol	NIST
μ	1.50	debye	KDB
ΔfG°	-85.83	kJ/mol	KDB
ΔfH°gas	[-156.70; -152.80]	kJ/mol
ΔfH°gas	-152.80	kJ/mol	KDB
ΔfH°gas	-156.70 ± 3.50	kJ/mol	NIST
ΔfH°gas	-155.60 ± 8.40	kJ/mol	NIST
ΔfH°liquid	[-202.40; -195.40]	kJ/mol
ΔfH°liquid	-202.40 ± 3.50	kJ/mol	NIST
ΔfH°liquid	-195.40 ± 8.40	kJ/mol	NIST
ΔfusH°	10.68	kJ/mol	Joback Calculated Property
ΔvapH°	[45.20; 45.80]	kJ/mol
ΔvapH°	45.72	kJ/mol	NIST
ΔvapH°	45.73 ± 0.09	kJ/mol	NIST
ΔvapH°	45.78 ± 0.16	kJ/mol	NIST
ΔvapH°	45.80 ± 0.20	kJ/mol	NIST
ΔvapH°	45.20 ± 1.30	kJ/mol	NIST
IE	[11.10; 11.62]	eV
IE	11.62	eV	NIST
IE	11.10 ± 0.05	eV	NIST
log10WS	[-1.74; -1.74]
log10WS	-1.74		Aq. Solubility Prediction
log10WS	-1.74		Estimated Solubility
logPoct/wat	2.594		Crippen Calculated Property
McVol	88.000	ml/mol	McGowan Calculated Property
Pc	[5127.05; 5840.00]	kPa
Pc	5127.05	kPa	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Pc	5840.00	kPa	KDB
Inp	[865.00; 922.10]
Inp	888.00		NIST
Inp	895.00		NIST
Inp	882.00		NIST
Inp	865.00		NIST
Inp	900.00		NIST
Inp	916.00		NIST
Inp	884.00		NIST
Inp	877.00		NIST
Inp	916.00		NIST
Inp	Outlier 922.10		NIST
Inp	888.40		NIST
Inp	876.00		NIST
Inp	882.00		NIST
Inp	886.00		NIST
Inp	895.00		NIST
Inp	892.00		NIST
Inp	920.00		NIST
Inp	892.00		NIST
Inp	905.00		NIST
Inp	876.00		NIST
Inp	876.00		NIST
Inp	876.00		NIST
Inp	888.00		NIST
Inp	910.00		NIST
Inp	884.00		NIST
Inp	895.00		NIST
Inp	876.00		NIST
Ip	[1475.00; 1555.00]
Ip	1513.66		NIST
Ip	1515.59		NIST
Ip	1511.30		NIST
Ip	1516.00		NIST
Ip	Outlier 1555.00		NIST
Ip	1516.00		NIST
Ip	1475.00		NIST
Ip	1475.00		NIST
Ip	1500.00		NIST
Ip	1516.00		NIST
S°liquid	[244.30; 247.00]	J/mol×K
S°liquid	244.30	J/mol×K	NIST
S°liquid	247.00	J/mol×K	NIST
Tboil	[418.00; 419.65]	K
Tboil	419.25	K	Excess volumes and speeds of sound of mixtures of 1,2-dibromoethane with chlorinated ethanes and ethenes at 303.15 K
Tboil	Outlier 418.35	K	Excess molar enthalpies of dimethylsulfoxide with chloroethanes and chloroethenes at 298.15K
Tboil	419.35	K	Vapor-Liquid Equilibria and Excess Molar Enthalpies for N-Methyl-2-pyrrolidone with Chloroethanes and Chloroethenes
Tboil	Outlier 418.35	K	Isobaric Vapor Liquid Equilibrium for Dimethylsulfoxide with Chloroethanes and Chloroethenes
Tboil	419.60	K	KDB
Tboil	419.25 ± 0.30	K	NIST
Tboil	419.40	K	NIST
Tboil	419.26 ± 0.30	K	NIST
Tboil	419.05 ± 0.30	K	NIST
Tboil	419.40	K	NIST
Tboil	419.35 ± 0.25	K	NIST
Tboil	419.15 ± 2.00	K	NIST
Tboil	Outlier 418.00 ± 2.00	K	NIST
Tboil	419.40 ± 0.30	K	NIST
Tboil	419.40 ± 0.70	K	NIST
Tboil	419.00 ± 2.00	K	NIST
Tboil	419.15 ± 1.50	K	NIST
Tboil	419.35 ± 0.30	K	NIST
Tboil	419.15 ± 1.50	K	NIST
Tboil	419.40 ± 0.50	K	NIST
Tboil	419.50 ± 0.50	K	NIST
Tboil	419.40 ± 0.50	K	NIST
Tboil	419.50 ± 0.50	K	NIST
Tboil	419.50 ± 0.50	K	NIST
Tboil	419.65 ± 0.50	K	NIST
Tc	[644.50; 661.15]	K
Tc	650.00	K	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Tc	661.15	K	KDB
Tc	644.50	K	NIST
Tfus	[229.30; 229.75]	K
Tfus	229.75	K	Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
Tfus	229.30	K	KDB
Tfus	229.70	K	Aq. Solubility Prediction
Tfus	229.70 ± 0.60	K	NIST
Ttriple	[230.30; 230.80]	K
Ttriple	230.80 ± 0.20	K	NIST
Ttriple	230.30 ± 0.20	K	NIST
Ttriple	230.80 ± 0.20	K	NIST
Ttriple	230.30 ± 0.20	K	NIST
Vc	0.314	m3/kmol	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[164.00; 173.00]	J/mol×K	[240.00; 350.00]
Cp,liquid	164.00	J/mol×K	240.00	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	164.00	J/mol×K	250.00	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	164.00	J/mol×K	260.00	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	165.00	J/mol×K	270.00	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	165.00	J/mol×K	273.15	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	165.00	J/mol×K	280.00	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	166.00	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	165.30	J/mol×K	298.00	NIST
Cp,liquid	168.00	J/mol×K	298.15	NIST
Cp,liquid	166.00	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	165.40	J/mol×K	298.15	NIST
Cp,liquid	165.40	J/mol×K	298.15	NIST
Cp,liquid	167.00	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	168.00	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
Cp,liquid	169.00	J/mol×K	320.00	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	170.00	J/mol×K	330.00	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	172.00	J/mol×K	340.00	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	173.00	J/mol×K	350.00	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
ΔfusH	[0.36; 9.52]	kJ/mol	[204.80; 230.80]
ΔfusH	0.36	kJ/mol	204.80	NIST
ΔfusH	0.54	kJ/mol	207.30	NIST
ΔfusH	9.52	kJ/mol	230.30	NIST
ΔfusH	9.17	kJ/mol	230.80	NIST
ΔfusH	9.17	kJ/mol	230.80	NIST
ΔvapH	[37.64; 47.70]	kJ/mol	[350.50; 419.40]
ΔvapH	47.70	kJ/mol	350.50	NIST
ΔvapH	45.70	kJ/mol	361.50	NIST
ΔvapH	42.50	kJ/mol	380.50	NIST
ΔvapH	40.80	kJ/mol	395.00	NIST
ΔvapH	41.90	kJ/mol	396.00	NIST
ΔvapH	40.10	kJ/mol	397.50	NIST
ΔvapH	40.40	kJ/mol	398.00	NIST
ΔvapH	39.00	kJ/mol	415.00	NIST
ΔvapH	41.49	kJ/mol	419.20	KDB
ΔvapH	37.64	kJ/mol	419.40	NIST
Pvap	[0.26; 95.50]	kPa	[283.15; 417.25]
Pvap	0.26	kPa	283.15	Total vapour pressure and excess Gibbs energy for binary mixtures of 1,1,2,2-tetrachloroethane or tetrachloroethene with tetrachloromethane at nine temperatures
Pvap	0.26	kPa	283.15	Isothermal (vapour + liquid) equilibrium for binary mixtures of (tetrahydrofuran + 1,1,2,2-tetrachloroethane or tetrachloroethene) at nine temperatures
Pvap	0.26	kPa	283.15	Total vapour pressure and excess Gibbs energy for binary mixtures of 1,1,2,2-tetrachlorethane or tetrachloroethene with benzene at nine temperatures
Pvap	0.37	kPa	288.15	Total vapour pressure and excess Gibbs energy for binary mixtures of 1,1,2,2-tetrachlorethane or tetrachloroethene with benzene at nine temperatures
Pvap	0.37	kPa	288.15	Total vapour pressure and excess Gibbs energy for binary mixtures of 1,1,2,2-tetrachloroethane or tetrachloroethene with tetrachloromethane at nine temperatures
Pvap	0.37	kPa	288.15	Isothermal (vapour + liquid) equilibrium for binary mixtures of (tetrahydrofuran + 1,1,2,2-tetrachloroethane or tetrachloroethene) at nine temperatures
Pvap	0.52	kPa	293.15	Total vapour pressure and excess Gibbs energy for binary mixtures of 1,1,2,2-tetrachlorethane or tetrachloroethene with benzene at nine temperatures
Pvap	0.52	kPa	293.15	Total vapour pressure and excess Gibbs energy for binary mixtures of 1,1,2,2-tetrachloroethane or tetrachloroethene with tetrachloromethane at nine temperatures
Pvap	0.52	kPa	293.15	Isothermal (vapour + liquid) equilibrium for binary mixtures of (tetrahydrofuran + 1,1,2,2-tetrachloroethane or tetrachloroethene) at nine temperatures
Pvap	0.71	kPa	298.15	Total vapour pressure and excess Gibbs energy for binary mixtures of 1,1,2,2-tetrachlorethane or tetrachloroethene with benzene at nine temperatures
Pvap	0.71	kPa	298.15	Isothermal (vapour + liquid) equilibrium for binary mixtures of (tetrahydrofuran + 1,1,2,2-tetrachloroethane or tetrachloroethene) at nine temperatures
Pvap	0.71	kPa	298.15	Total vapour pressure and excess Gibbs energy for binary mixtures of 1,1,2,2-tetrachloroethane or tetrachloroethene with tetrachloromethane at nine temperatures
Pvap	0.98	kPa	303.15	Isothermal (vapour + liquid) equilibrium for binary mixtures of (tetrahydrofuran + 1,1,2,2-tetrachloroethane or tetrachloroethene) at nine temperatures
Pvap	0.98	kPa	303.15	Total vapour pressure and excess Gibbs energy for binary mixtures of 1,1,2,2-tetrachloroethane or tetrachloroethene with tetrachloromethane at nine temperatures
Pvap	0.98	kPa	303.15	Total vapour pressure and excess Gibbs energy for binary mixtures of 1,1,2,2-tetrachlorethane or tetrachloroethene with benzene at nine temperatures
Pvap	1.29	kPa	308.15	Total vapour pressure and excess Gibbs energy for binary mixtures of 1,1,2,2-tetrachloroethane or tetrachloroethene with tetrachloromethane at nine temperatures
Pvap	1.29	kPa	308.15	Total vapour pressure and excess Gibbs energy for binary mixtures of 1,1,2,2-tetrachlorethane or tetrachloroethene with benzene at nine temperatures
Pvap	1.29	kPa	308.15	Isothermal (vapour + liquid) equilibrium for binary mixtures of (tetrahydrofuran + 1,1,2,2-tetrachloroethane or tetrachloroethene) at nine temperatures
Pvap	1.70	kPa	313.15	Total vapour pressure and excess Gibbs energy for binary mixtures of 1,1,2,2-tetrachloroethane or tetrachloroethene with tetrachloromethane at nine temperatures
Pvap	1.70	kPa	313.15	Total vapour pressure and excess Gibbs energy for binary mixtures of 1,1,2,2-tetrachlorethane or tetrachloroethene with benzene at nine temperatures
Pvap	1.70	kPa	313.15	Isothermal (vapour + liquid) equilibrium for binary mixtures of (tetrahydrofuran + 1,1,2,2-tetrachloroethane or tetrachloroethene) at nine temperatures
Pvap	2.24	kPa	318.15	Total vapour pressure and excess Gibbs energy for binary mixtures of 1,1,2,2-tetrachloroethane or tetrachloroethene with tetrachloromethane at nine temperatures
Pvap	2.24	kPa	318.15	Total vapour pressure and excess Gibbs energy for binary mixtures of 1,1,2,2-tetrachlorethane or tetrachloroethene with benzene at nine temperatures
Pvap	2.24	kPa	318.15	Isothermal (vapour + liquid) equilibrium for binary mixtures of (tetrahydrofuran + 1,1,2,2-tetrachloroethane or tetrachloroethene) at nine temperatures
Pvap	2.86	kPa	323.15	Total vapour pressure and excess Gibbs energy for binary mixtures of 1,1,2,2-tetrachloroethane or tetrachloroethene with tetrachloromethane at nine temperatures
Pvap	2.86	kPa	323.15	Total vapour pressure and excess Gibbs energy for binary mixtures of 1,1,2,2-tetrachlorethane or tetrachloroethene with benzene at nine temperatures
Pvap	2.86	kPa	323.15	Isothermal (vapour + liquid) equilibrium for binary mixtures of (tetrahydrofuran + 1,1,2,2-tetrachloroethane or tetrachloroethene) at nine temperatures
Pvap	95.50	kPa	417.25	Vapor-liquid equilibrium and excess Gibbs energies of some binary mixtures of acrylonitrile at 95.5 kPa
n0	[1.48650; 1.49400]		[293.15; 308.15]
n0	1.49400		293.15	Activity coefficients and excess Gibbs free energy of some binary mixtures formed by p-cresol at 95.23 kPa
n0	1.49400		293.15	Excess Gibbs energies of selected binary mixtures formed by N,N-dimethyl formamide at 95.5 kPa
n0	1.49387		293.15	Densities, excess molar volumes, and refractive indices of 1,1,2,2-tetrachloroethane and 1-alkanols binary mixtures
n0	1.49400		293.15	Vapor-Liquid Equilibria of Binary Mixtures Formed by Hexan-1-ol with Chloroethanes and Chloroethenes at 95.6 kPa
n0	1.49400		293.15	Bubble points of the binary mixtures formed by ethylbenzene with some chloroaliphatics and substituted benzenes at p = 94.7 kPa
n0	1.49400		293.15	Bubble points of some binary mixtures formed by o-cresol at 95.75 kPa
n0	1.49400		298.15	Bubble Temperature Measurements on the Binary Mixtures of n-Heptane or Nitrobenzene or Chlorobenzene with Some Chloroethanes and Chloroethylenes at (94.6 to 95.8) kPa
n0	1.49140		298.15	Bubble Temperature Measurements on Binary Mixtures Formed by Cyclohexane at 94.7 kPa
n0	1.49200		298.15	Isothermal (vapour + liquid) equilibria for the binary (cyclopentanone or cyclohexanone with 1,1,2,2-tetrachloroethane) systems at temperatures of (343.15, 353.15, and 363.15) K
n0	1.49140		298.15	Bubble-Temperature Measurements on Some Binary Mixtures Formed by Tetrahydrofuran or Amyl Alcohol with Hydrocarbons, Chlorohydrocarbons, or Butanols at (94.6 or 95.8) kPa
n0	1.49220		298.15	Density, Viscosity, Refractive Index, and Speed of Sound for Binary Mixtures of Anisole with 2-Chloroethanol, 1,4-Dioxane, Tetrachloroethylene, Tetrachloroethane, DMF, DMSO, and Diethyl Oxalate at (298.15, 303.15, and 308.15) K
n0	1.48810		303.15	Densities, speeds of sound, isentropic compressibilities, refractive indexes, and viscosities of tetrahydrofuran with haloalkane or alkyl ethanoate at T = 303.15 K
n0	1.48940		303.15	Density, Viscosity, Refractive Index, and Speed of Sound for Binary Mixtures of Anisole with 2-Chloroethanol, 1,4-Dioxane, Tetrachloroethylene, Tetrachloroethane, DMF, DMSO, and Diethyl Oxalate at (298.15, 303.15, and 308.15) K
n0	1.48887		303.15	Densities, excess molar volumes, and refractive indices of 1,1,2,2-tetrachloroethane and 1-alkanols binary mixtures
n0	1.48650		308.15	Density, Viscosity, Refractive Index, and Speed of Sound for Binary Mixtures of Anisole with 2-Chloroethanol, 1,4-Dioxane, Tetrachloroethylene, Tetrachloroethane, DMF, DMSO, and Diethyl Oxalate at (298.15, 303.15, and 308.15) K
ρl	[1556.07; 1604.78]	kg/m3	[288.15; 318.15]
ρl	1602.77	kg/m3	288.15	Densities and Excess Molar Volumes of the Ternary System (1,4-Dioxane + 2-Propanol + 1,1,2,2-Tetrachloroethane) at T = 288.15-318.15 K and at Atmospheric Pressure: Experimental Measurements and Prigogine-Flory-Patterson Modeling
ρl	1604.78	kg/m3	288.15	Densities and Excess Molar Volumes of the Binary Mixtures of Cyclopentanone with Chloroalkanes at T = (288.15, 298.15, 308.15, and 318.15) K
ρl	1601.45	kg/m3	288.15	Volumetric properties of binary liquid mixtures of ketones with chloroalkanes at different temperatures and atmospheric pressure
ρl	1604.75	kg/m3	288.15	Densities and Excess Molar Volumes of the Binary Mixtures of Cyclohexanone with Chloroalkanes at Temperatures between (288.15 and 318.15) K
ρl	1600.00	kg/m3	293.00	KDB
ρl	1593.65	kg/m3	293.15	Volumetric properties of binary liquid mixtures of ketones with chloroalkanes at different temperatures and atmospheric pressure
ρl	1594.57	kg/m3	293.20	Isobaric vapour liquid equilibria for binary mixtures of 1,2-dibromoethane with 1,2-dichloroethane, trichloromethane, and 1,1,2,2-tetrachloroethane at atmospheric pressure
ρl	1586.80	kg/m3	298.15	Excess Molar Volumes and Sound Speed in (Phenylacetonitrile + 1,2-Dichloroethane), (Phenylacetonitrile + 1,1,2-Trichloroethane), (Phenylacetonitrile + 1,1,2,2-Tetrachloroethane), (Phenylacetonitrile + Trichloroethene), and (Phenylacetonitrile + Tetrachloroethene) at Temperatures of (303.15, 308.15, and 313.15) K
ρl	1589.18	kg/m3	298.15	Densities and Excess Molar Volumes of the Binary Mixtures of Cyclohexanone with Chloroalkanes at Temperatures between (288.15 and 318.15) K
ρl	1586.22	kg/m3	298.15	Thermodynamic study of 1,1,2,2-tetrachloroethane + hydrocarbon mixtures I. Excess and solvation enthalpies
ρl	1587.20	kg/m3	298.15	Densities and Excess Molar Volumes of the Ternary System (1,4-Dioxane + 2-Propanol + 1,1,2,2-Tetrachloroethane) at T = 288.15-318.15 K and at Atmospheric Pressure: Experimental Measurements and Prigogine-Flory-Patterson Modeling
ρl	1589.19	kg/m3	298.15	Densities and Excess Molar Volumes of the Binary Mixtures of Cyclopentanone with Chloroalkanes at T = (288.15, 298.15, 308.15, and 318.15) K
ρl	1587.60	kg/m3	298.15	Volumetric and optical properties for some (2-butanone + chloroalkane) binary mixtures at T = 298.15 K
ρl	1586.65	kg/m3	298.15	Studies of Viscosities and Excess Molar Volumes of the Binary Mixtures of 1-Heptanol + 1,2-Dichloroethane, + 1,1,1-Trichloroethane, + 1,1,2,2-Tetrachloroethane, + Trichloroethylene and Tetrachloroethylene at (293.15, 298.15, and 303.15) K for the Liquid Region and at Ambient Pressure
ρl	1588.23	kg/m3	298.15	Volumetric Study for the Binary Nitromethane with Chloroalkane Mixtures at Temperatures in the Range (298.15 to 318.15) K
ρl	1585.87	kg/m3	298.15	Volumetric properties of binary liquid mixtures of ketones with chloroalkanes at different temperatures and atmospheric pressure
ρl	1578.07	kg/m3	303.15	Volumetric properties of binary liquid mixtures of ketones with chloroalkanes at different temperatures and atmospheric pressure
ρl	1579.60	kg/m3	303.15	Excess Molar Volumes and Sound Speed in (Phenylacetonitrile + 1,2-Dichloroethane), (Phenylacetonitrile + 1,1,2-Trichloroethane), (Phenylacetonitrile + 1,1,2,2-Tetrachloroethane), (Phenylacetonitrile + Trichloroethene), and (Phenylacetonitrile + Tetrachloroethene) at Temperatures of (303.15, 308.15, and 313.15) K
ρl	1573.57	kg/m3	308.15	Densities and Excess Molar Volumes of the Binary Mixtures of Cyclohexanone with Chloroalkanes at Temperatures between (288.15 and 318.15) K
ρl	1572.66	kg/m3	308.15	Volumetric Study for the Binary Nitromethane with Chloroalkane Mixtures at Temperatures in the Range (298.15 to 318.15) K
ρl	1570.27	kg/m3	308.15	Volumetric properties of binary liquid mixtures of ketones with chloroalkanes at different temperatures and atmospheric pressure
ρl	1570.60	kg/m3	308.15	Excess Molar Volumes and Sound Speed in (Phenylacetonitrile + 1,2-Dichloroethane), (Phenylacetonitrile + 1,1,2-Trichloroethane), (Phenylacetonitrile + 1,1,2,2-Tetrachloroethane), (Phenylacetonitrile + Trichloroethene), and (Phenylacetonitrile + Tetrachloroethene) at Temperatures of (303.15, 308.15, and 313.15) K
ρl	1571.63	kg/m3	308.15	Densities and Excess Molar Volumes of the Ternary System (1,4-Dioxane + 2-Propanol + 1,1,2,2-Tetrachloroethane) at T = 288.15-318.15 K and at Atmospheric Pressure: Experimental Measurements and Prigogine-Flory-Patterson Modeling
ρl	1573.59	kg/m3	308.15	Densities and Excess Molar Volumes of the Binary Mixtures of Cyclopentanone with Chloroalkanes at T = (288.15, 298.15, 308.15, and 318.15) K
ρl	1563.70	kg/m3	313.15	Excess Molar Volumes and Sound Speed in (Phenylacetonitrile + 1,2-Dichloroethane), (Phenylacetonitrile + 1,1,2-Trichloroethane), (Phenylacetonitrile + 1,1,2,2-Tetrachloroethane), (Phenylacetonitrile + Trichloroethene), and (Phenylacetonitrile + Tetrachloroethene) at Temperatures of (303.15, 308.15, and 313.15) K
ρl	1562.45	kg/m3	313.15	Volumetric properties of binary liquid mixtures of ketones with chloroalkanes at different temperatures and atmospheric pressure
ρl	1557.04	kg/m3	318.15	Volumetric Study for the Binary Nitromethane with Chloroalkane Mixtures at Temperatures in the Range (298.15 to 318.15) K
ρl	1557.94	kg/m3	318.15	Densities and Excess Molar Volumes of the Binary Mixtures of Cyclohexanone with Chloroalkanes at Temperatures between (288.15 and 318.15) K
ρl	1556.07	kg/m3	318.15	Densities and Excess Molar Volumes of the Ternary System (1,4-Dioxane + 2-Propanol + 1,1,2,2-Tetrachloroethane) at T = 288.15-318.15 K and at Atmospheric Pressure: Experimental Measurements and Prigogine-Flory-Patterson Modeling
ρl	1557.95	kg/m3	318.15	Densities and Excess Molar Volumes of the Binary Mixtures of Cyclopentanone with Chloroalkanes at T = (288.15, 298.15, 308.15, and 318.15) K
ΔfusS	[1.74; 41.50]	J/mol×K	[204.80; 230.80]
ΔfusS	1.74	J/mol×K	204.80	NIST
ΔfusS	2.62	J/mol×K	207.30	NIST
ΔfusS	41.50	J/mol×K	230.30	NIST
ΔfusS	39.74	J/mol×K	230.80	NIST
csound,fluid	[1087.00; 1150.61]	m/s	[298.15; 318.15]
csound,fluid	1150.61	m/s	298.15	Speeds of sound, isentropic compressibilities and refractive indices for some binary mixtures of nitromethane with chloroalkane at temperatures from 298.15 to 318.15 K. Comparison with theories
csound,fluid	1118.66	m/s	308.15	Speeds of sound, isentropic compressibilities and refractive indices for some binary mixtures of nitromethane with chloroalkane at temperatures from 298.15 to 318.15 K. Comparison with theories
csound,fluid	1087.00	m/s	318.15	Speeds of sound, isentropic compressibilities and refractive indices for some binary mixtures of nitromethane with chloroalkane at temperatures from 298.15 to 318.15 K. Comparison with theories
γ	0.03	N/m	293.20	KDB

Datasets

Viscosity, Pa*s

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Viscosity, Pa*s - Liquid
308.15	101.00	0.0013
Reference

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[100.90; 156.67]	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			4.92700e+01
Coefficient B			2.32800e-01
Coefficient C			-1.73000e-04
Coefficient D			4.76000e-08
Coefficient E			0.00000e+00
Temperature range, min.			273.00
Temperature range, max.			1000.00
Cp,gas	100.90	J/mol×K	273.00	Calculated Property
Cp,gas	112.08	J/mol×K	353.78	Calculated Property
Cp,gas	121.67	J/mol×K	434.56	Calculated Property
Cp,gas	129.81	J/mol×K	515.33	Calculated Property
Cp,gas	136.65	J/mol×K	596.11	Calculated Property
Cp,gas	142.35	J/mol×K	676.89	Calculated Property
Cp,gas	147.05	J/mol×K	757.67	Calculated Property
Cp,gas	150.90	J/mol×K	838.44	Calculated Property
Cp,gas	154.06	J/mol×K	919.22	Calculated Property
Cp,gas	156.67	J/mol×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.0041910; 0.0002745]	Pa×s	[229.61; 456.32]	Joback Predicted correlation
Equation			Y = exp(A + B/T + C·ln(T) + D·T^E) Y is η in Pa×s, T in K
Coefficient A			-1.09609e+01
Coefficient B			1.25968e+03
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Comment			Liquid phase. Joback/Reid (1987), valid from Tf to 0.7·Tc.
Temperature range, min.			229.61
Temperature range, max.			456.32
η	0.0041910	Pa×s	229.61	Calculated Property
η	0.0024366	Pa×s	254.80	Calculated Property
η	0.0015618	Pa×s	279.99	Calculated Property
η	0.0010773	Pa×s	305.18	Calculated Property
η	0.0007864	Pa×s	330.37	Calculated Property
η	0.0006003	Pa×s	355.56	Calculated Property
η	0.0004749	Pa×s	380.75	Calculated Property
η	0.0003867	Pa×s	405.94	Calculated Property
η	0.0003226	Pa×s	431.13	Calculated Property
η	0.0002745	Pa×s	456.32	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.65]	kPa	[309.36; 447.30]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.38082e+01
Coefficient B			-3.15431e+03
Coefficient C			-7.60640e+01
Temperature range, min.			309.36
Temperature range, max.			447.30
Pvap	1.33	kPa	309.36	Calculated Property
Pvap	3.07	kPa	324.69	Calculated Property
Pvap	6.41	kPa	340.01	Calculated Property
Pvap	12.35	kPa	355.34	Calculated Property
Pvap	22.23	kPa	370.67	Calculated Property
Pvap	37.74	kPa	385.99	Calculated Property
Pvap	60.97	kPa	401.32	Calculated Property
Pvap	94.32	kPa	416.65	Calculated Property
Pvap	140.55	kPa	431.97	Calculated Property
Pvap	202.65	kPa	447.30	Calculated Property
Pvap	[1.26e-03; 5791.60]	kPa	[229.35; 661.00]	KDB Vapor Pressure Data
Equation			ln(Y) = A + B/T + C·ln(T) + D·T² + E/T² Y is Pvap in kPa, T in K
Coefficient A			1.48935e+02
Coefficient B			-1.09840e+04
Coefficient C			-1.99490e+01
Coefficient D			1.34830e-05
Coefficient E			0.00000e+00
Temperature range, min.			229.35
Temperature range, max.			661.00
Pvap	1.26e-03	kPa	229.35	Calculated Property
Pvap	0.16	kPa	277.31	Calculated Property
Pvap	3.30	kPa	325.27	Calculated Property
Pvap	25.56	kPa	373.23	Calculated Property
Pvap	109.33	kPa	421.19	Calculated Property
Pvap	325.30	kPa	469.16	Calculated Property
Pvap	774.51	kPa	517.12	Calculated Property
Pvap	1612.42	kPa	565.08	Calculated Property
Pvap	3111.67	kPa	613.04	Calculated Property
Pvap	5791.60	kPa	661.00	Calculated Property
Pvap	[0.53; 60.80]	kPa	[298.00; 403.00]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.20094e+01
Coefficient B			-2.20957e+03
Coefficient C			-1.23372e+02
Reference			Matthews, Sumner, et al., 1950, 2
Comment			Coefficents calculated by NIST from author's data.
Temperature range, min.			298.00
Temperature range, max.			403.00
Pvap	0.53	kPa	298.00	Calculated Property
Pvap	1.16	kPa	309.67	Calculated Property
Pvap	2.33	kPa	321.33	Calculated Property
Pvap	4.34	kPa	333.00	Calculated Property
Pvap	7.57	kPa	344.67	Calculated Property
Pvap	12.49	kPa	356.33	Calculated Property
Pvap	19.63	kPa	368.00	Calculated Property
Pvap	29.61	kPa	379.67	Calculated Property
Pvap	43.10	kPa	391.33	Calculated Property
Pvap	60.80	kPa	403.00	Calculated Property
Pvap	[0.53; 60.80]	kPa	[298.00; 403.00]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.20094e+01
Coefficient B			-2.20957e+03
Coefficient C			-1.23372e+02
Reference			Matthews, Sumner, et al., 1950
Comment			Coefficents calculated by NIST from author's data.
Temperature range, min.			298.00
Temperature range, max.			403.00
Pvap	0.53	kPa	298.00	Calculated Property
Pvap	1.16	kPa	309.67	Calculated Property
Pvap	2.33	kPa	321.33	Calculated Property
Pvap	4.34	kPa	333.00	Calculated Property
Pvap	7.57	kPa	344.67	Calculated Property
Pvap	12.49	kPa	356.33	Calculated Property
Pvap	19.63	kPa	368.00	Calculated Property
Pvap	29.61	kPa	379.67	Calculated Property
Pvap	43.10	kPa	391.33	Calculated Property
Pvap	60.80	kPa	403.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
γ	[0.05; 0.02]	N/m	[202.95; 403.65]	Jasper (1972), surface tension of pure liquid compounds Compiled value
Equation			Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is γ in N/m, T in K
Coefficient A			7.33854e-02
Coefficient B			-1.26800e-04
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Temperature range, min.			202.95
Temperature range, max.			403.65
γ	0.05	N/m	202.95	Calculated Property
γ	0.04	N/m	225.25	Calculated Property
γ	0.04	N/m	247.55	Calculated Property
γ	0.04	N/m	269.85	Calculated Property
γ	0.04	N/m	292.15	Calculated Property
γ	0.03	N/m	314.45	Calculated Property
γ	0.03	N/m	336.75	Calculated Property
γ	0.03	N/m	359.05	Calculated Property
γ	0.03	N/m	381.35	Calculated Property
γ	0.02	N/m	403.65	Calculated Property

Similar Compounds

Find more compounds similar to Ethane, 1,1,2,2-tetrachloro-.

Mixtures

• Methane, nitro- + Ethane, 1,1,2,2-tetrachloro-
• Tetrahydrofuran + Ethane, 1,1,2,2-tetrachloro-
• Phenol, 2-methyl- + Ethane, 1,1,2,2-tetrachloro-
• Benzene, ethyl- + Ethane, 1,1,2,2-tetrachloro-
• Formamide, N,N-dimethyl- + Ethane, 1,1,2,2-tetrachloro-
• 2-Butanone + Ethane, 1,1,2,2-tetrachloro-
• 2-Heptanone + Ethane, 1,1,2,2-tetrachloro-
• Cyclohexanone + Ethane, 1,1,2,2-tetrachloro-
• Carbon Tetrachloride + Ethane, 1,1,2,2-tetrachloro-
• 1-Hexanol + Ethane, 1,1,2,2-tetrachloro-
• Benzene + Ethane, 1,1,2,2-tetrachloro-
• Acetamide, N-methyl- + Ethane, 1,1,2,2-tetrachloro-
• PHENOL, 4-METHYL- + Ethane, 1,1,2,2-tetrachloro-
• Ethane, 1,2-dibromo- + Ethane, 1,1,2,2-tetrachloro-
• 2-Propenenitrile + Ethane, 1,1,2,2-tetrachloro-
• Cyclopentanone + Ethane, 1,1,2,2-tetrachloro-
• Toluene + Ethane, 1,1,2,2-tetrachloro-
• Benzene, propyl- + Ethane, 1,1,2,2-tetrachloro-
• Benzene, (1-methylethyl)- + Ethane, 1,1,2,2-tetrachloro-
• Benzene, n-butyl- + Ethane, 1,1,2,2-tetrachloro-

Find more mixtures with Ethane, 1,1,2,2-tetrachloro-.

Sources

• KDB Vapor Pressure Data
• Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) ChEDL chemicals 1.5.2, from Bradley, J.-C.; Williams, A.; Lang, A. Jean-Claude Bradley Open Melting Point Dataset. Figshare, 2014 (CC0).
• Jasper (1972), surface tension of pure liquid compounds ChEDL chemicals 1.5.2, from Jasper, J. J. The Surface Tension of Pure Liquid Compounds. J. Phys. Chem. Ref. Data 1972, 1, 841-1010 (as transcribed in Lange's Handbook).
• PSRK revision IV (2005), critical constants and acentric factors of 1000 components ChEDL chemicals 1.5.2, from Horstmann, S.; Jabłoniec, A.; Krafczyk, J.; Fischer, K.; Gmehling, J. PSRK Group Contribution Equation of State: Comprehensive Revision and Extension IV, Including Critical Constants and α-Function Parameters for 1000 Components. Fluid Phase Equilib. 2005, 227, 157-164.
• Crippen Method
• Total vapour pressure and excess Gibbs energy for binary mixtures of 1,1,2,2-tetrachlorethane or tetrachloroethene with benzene at nine temperatures
• Total vapour pressure and excess Gibbs energy for binary mixtures of 1,1,2,2-tetrachloroethane or tetrachloroethene with tetrachloromethane at nine temperatures
• Bubble points of some binary mixtures formed by o-cresol at 95.75 kPa
• Isobaric vapour liquid equilibria for binary mixtures of 1,2-dibromoethane with 1,2-dichloroethane, trichloromethane, and 1,1,2,2-tetrachloroethane at atmospheric pressure
• Excess Gibbs energies of selected binary mixtures formed by N,N-dimethyl formamide at 95.5 kPa
• Thermodynamic study of 1,1,2,2-tetrachloroethane + hydrocarbon mixtures I. Excess and solvation enthalpies
• Vapor-liquid equilibrium and excess Gibbs energies of some binary mixtures of acrylonitrile at 95.5 kPa
• Speeds of sound, isentropic compressibilities and refractive indices for some binary mixtures of nitromethane with chloroalkane at temperatures from 298.15 to 318.15 K. Comparison with theories
• Excess volumes and speeds of sound of mixtures of 1,2-dibromoethane with chlorinated ethanes and ethenes at 303.15 K
• Isothermal (vapour + liquid) equilibrium for binary mixtures of (tetrahydrofuran + 1,1,2,2-tetrachloroethane or tetrachloroethene) at nine temperatures
• Densities, excess molar volumes, and refractive indices of 1,1,2,2-tetrachloroethane and 1-alkanols binary mixtures
• Bubble points of the binary mixtures formed by ethylbenzene with some chloroaliphatics and substituted benzenes at p = 94.7 kPa
• Isothermal (vapour + liquid) equilibria for the binary (cyclopentanone or cyclohexanone with 1,1,2,2-tetrachloroethane) systems at temperatures of (343.15, 353.15, and 363.15) K
• Densities and viscosities of binary liquid mixtures of N-methylacetamide with some chloroethanes and chloroethenes at T = 308.15 K
• Activity coefficients and excess Gibbs free energy of some binary mixtures formed by p-cresol at 95.23 kPa
• Studies on thermodynamic properties of binary mixtures of hexan-1-ol with halogenated compounds at T = (308.15 and 313.15) K
• Volumetric and optical properties for some (2-butanone + chloroalkane) binary mixtures at T = 298.15 K
• Solubility determination and thermodynamic modeling of 3-methyl-4- nitrobenzoic acid in twelve organic solvents from T = (283.15-318.15) K and mixing properties of solutions
• Densities, speeds of sound, isentropic compressibilities, refractive indexes, and viscosities of tetrahydrofuran with haloalkane or alkyl ethanoate at T = 303.15 K
• Excess molar enthalpies of dimethylsulfoxide with chloroethanes and chloroethenes at 298.15K
• Volumetric properties of binary liquid mixtures of ketones with chloroalkanes at different temperatures and atmospheric pressure
• Densities and Excess Molar Volumes of the Ternary System (1,4-Dioxane + 2-Propanol + 1,1,2,2-Tetrachloroethane) at T = 288.15-318.15 K and at Atmospheric Pressure: Experimental Measurements and Prigogine-Flory-Patterson Modeling
• Vapor-Liquid Equilibria and Excess Molar Enthalpies for N-Methyl-2-pyrrolidone with Chloroethanes and Chloroethenes
• Bubble Temperature Measurements on Binary Mixtures Formed by Cyclohexane at 94.7 kPa
• Bubble Temperature Measurements on the Binary Mixtures of n-Heptane or Nitrobenzene or Chlorobenzene with Some Chloroethanes and Chloroethylenes at (94.6 to 95.8) kPa
• Bubble-Temperature Measurements on Some Binary Mixtures Formed by Tetrahydrofuran or Amyl Alcohol with Hydrocarbons, Chlorohydrocarbons, or Butanols at (94.6 or 95.8) kPa
• Density, Viscosity, Refractive Index, and Speed of Sound for Binary Mixtures of Anisole with 2-Chloroethanol, 1,4-Dioxane, Tetrachloroethylene, Tetrachloroethane, DMF, DMSO, and Diethyl Oxalate at (298.15, 303.15, and 308.15) K
• Studies of Viscosities and Excess Molar Volumes of the Binary Mixtures of 1-Heptanol + 1,2-Dichloroethane, + 1,1,1-Trichloroethane, + 1,1,2,2-Tetrachloroethane, + Trichloroethylene and Tetrachloroethylene at (293.15, 298.15, and 303.15) K for the Liquid Region and at Ambient Pressure
• Determination of Partitioning Coefficients of Numerous Organic Solutes between a Long-Chain Aliphatic Alcohol and the Gas Phase as a Function of Temperature
• Determination of Henry's Law Constants Using Internal Standards with Benchmark Values
• Volumetric Study for the Binary Nitromethane with Chloroalkane Mixtures at Temperatures in the Range (298.15 to 318.15) K
• Isobaric Vapor Liquid Equilibrium for Dimethylsulfoxide with Chloroethanes and Chloroethenes
• Vapor-Liquid Equilibria of Binary Mixtures Formed by Hexan-1-ol with Chloroethanes and Chloroethenes at 95.6 kPa
• Densities and Excess Molar Volumes of the Binary Mixtures of Cyclohexanone with Chloroalkanes at Temperatures between (288.15 and 318.15) K
• Excess Molar Volumes and Sound Speed in (Phenylacetonitrile + 1,2-Dichloroethane), (Phenylacetonitrile + 1,1,2-Trichloroethane), (Phenylacetonitrile + 1,1,2,2-Tetrachloroethane), (Phenylacetonitrile + Trichloroethene), and (Phenylacetonitrile + Tetrachloroethene) at Temperatures of (303.15, 308.15, and 313.15) K
• Densities and Excess Molar Volumes of the Binary Mixtures of Cyclopentanone with Chloroalkanes at T = (288.15, 298.15, 308.15, and 318.15) K
• Joback Method
• KDB
• 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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