Chemical Properties of Ethane, 1,1,1-trichloro- (CAS 71-55-6)

InChI

InChI=1S/C2H3Cl3/c1-2(3,4)5/h1H3

InChI Key

UOCLXMDMGBRAIB-UHFFFAOYSA-N

Formula

C2H3Cl3

SMILES

CC(Cl)(Cl)Cl

Molecular Weight¹

133.40

CAS

71-55-6

Other Names

• 1,1,1-TCE
• 1,1,1-Trichloraethan
• 1,1,1-Trichlorethane
• 1,1,1-Trichloroethane [R140a]
• 1,1,1-Tricloroetano
• 1,1,1-trichloroethane
• ALPHA-TRICHLOROETHANE
• Aerothene TT
• CF 2
• CH3CCl3
• Chloroetene
• Chloroethene
• Chloroethene NU
• Chloroform, methyl-
• Chlorothane NU
• Chlorothene
• Chlorothene NU
• Chlorothene SM
• Chlorothene VG
• Chlorten
• Cleanite
• Distillex DS1
• Ethana
• Ethana NU
• F 140a
• Freon 140a
• Genklene LB
• HCC 140a
• ICI-CF 2
• Inhibisol
• Methyltrichloromethane
• NCI-C04626
• R-140a
• REFRIGERANT-140A
• Rcra waste number U226
• Solvent 111
• Solvethane
• Tafclean
• Three One A
• Three One S
• Tri-ethane
• Trichloro-1,1,1-ethane
• Trichloroethane
• Trichloromethylmethane
• UN 2831
• chlorotene
• methylchloroform
• «alpha»-T
• «alpha»-Trichloroethane

• ω : Acentric Factor.
• 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).
• C_p,solid : Solid phase heat capacity (J/mol×K).
• μ : Dipole Moment (debye).
• η : Dynamic viscosity (Pa×s).
• ε_r : Dielectric Constant (Relative permittivity).
• 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).
• NFPA Fire : NFPA Fire Rating.
• NFPA Health : NFPA Health Rating.
• NFPA Safety : NFPA Safety Rating.
• 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).
• Δ_vapS : Entropy of vaporization at a given temperature (J/mol×K).
• T_boil : Normal Boiling Point Temperature (K).
• T_c : Critical Temperature (K).
• T_fus : Normal melting (fusion) point (K).
• T_triple : Triple Point Temperature (K).
• V_c : Critical Volume (m³/kmol).
• ¹: Molecular weight from the IUPAC atomic weights tables.

Physical Properties

Property	Value	Unit	Source
ω	[0.2160; 0.2170]
ω	0.2160		PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
ω	0.2170		KDB
Tig	810.15	K	NCMS SOLV-DB
ΔcH°liquid	[-1112.10; -1108.00]	kJ/mol
ΔcH°liquid	-1108.00 ± 0.79	kJ/mol	NIST
ΔcH°liquid	-1112.10 ± 1.30	kJ/mol	NIST
μ	1.70	debye	KDB
εr	7.25		NCMS SOLV-DB
ΔfG°	-66.99	kJ/mol	Joback Calculated Property
ΔfH°gas	[-145.00; -142.30]	kJ/mol
ΔfH°gas	-145.00 ± 2.00	kJ/mol	NIST
ΔfH°gas	-144.40 ± 1.60	kJ/mol	NIST
ΔfH°gas	-142.30 ± 1.40	kJ/mol	NIST
ΔfH°liquid	[-178.60; -174.00]	kJ/mol
ΔfH°liquid	-177.00 ± 2.00	kJ/mol	NIST
ΔfH°liquid	-174.00	kJ/mol	NIST
ΔfH°liquid	-178.60 ± 0.84	kJ/mol	NIST
ΔfH°liquid	-174.80 ± 1.40	kJ/mol	NIST
ΔfusH°	6.11	kJ/mol	Joback Calculated Property
ΔvapH°	[32.38; 32.62]	kJ/mol
ΔvapH°	32.38	kJ/mol	NCMS SOLV-DB
ΔvapH°	32.62	kJ/mol	NIST
ΔvapH°	32.59 ± 0.07	kJ/mol	NIST
ΔvapH°	32.50 ± 0.10	kJ/mol	NIST
ΔvapH°	32.47 ± 0.06	kJ/mol	NIST
ΔvapH°	32.50 ± 0.10	kJ/mol	NIST
ΔvapH°	32.47 ± 0.08	kJ/mol	NIST
IE	[11.00; 11.25]	eV
IE	11.00	eV	NIST
IE	11.25	eV	NIST
log10WS	[-2.04; -2.00]
log10WS	-2.04		Aq. Solubility Prediction
log10WS	-2.00		Estimated Solubility
logPoct/wat	2.490		NCMS SOLV-DB
McVol	75.760	ml/mol	McGowan Calculated Property
NFPA Fire	[%!d(float64=1); %!d(float64=1)]
NFPA Fire	1		KDB
NFPA Fire	1		NCMS SOLV-DB
NFPA Health	[%!d(float64=2); %!d(float64=3)]
NFPA Health	2		KDB
NFPA Health	3		NCMS SOLV-DB
NFPA Safety	[%!d(float64=1); %!d(float64=2)]
NFPA Safety	2		KDB
NFPA Safety	1		NCMS SOLV-DB
Pc	[4300.00; 4301.25]	kPa
Pc	4300.00	kPa	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 10 Compiled value
Pc	4301.25	kPa	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Pc	4300.00	kPa	KDB
Inp	[621.00; 660.00]
Inp	637.00		NIST
Inp	639.00		NIST
Inp	637.00		NIST
Inp	646.00		NIST
Inp	651.00		NIST
Inp	640.00		NIST
Inp	650.00		NIST
Inp	621.00		NIST
Inp	637.00		NIST
Inp	642.40		NIST
Inp	623.50		NIST
Inp	645.10		NIST
Inp	628.00		NIST
Inp	645.00		NIST
Inp	Outlier 660.00		NIST
Inp	628.60		NIST
Inp	641.00		NIST
Inp	634.00		NIST
Inp	634.00		NIST
Inp	628.00		NIST
Inp	636.00		NIST
Inp	625.98		NIST
Inp	636.00		NIST
Inp	639.00		NIST
Inp	639.00		NIST
Inp	650.00		NIST
Inp	626.00		NIST
Inp	626.00		NIST
Inp	639.00		NIST
Inp	634.00		NIST
Inp	621.00		NIST
Inp	629.00		NIST
Inp	632.00		NIST
Inp	650.00		NIST
Inp	634.00		NIST
Inp	630.00		NIST
Inp	636.00		NIST
Inp	650.00		NIST
Inp	621.00		NIST
Inp	630.00		NIST
Inp	637.00		NIST
Ip	[885.00; 909.11]
Ip	898.00		NIST
Ip	898.00		NIST
Ip	904.35		NIST
Ip	909.11		NIST
Ip	897.56		NIST
Ip	891.00		NIST
Ip	885.00		NIST
Ip	908.00		NIST
Ip	900.00		NIST
Ip	900.00		NIST
Ip	886.00		NIST
Ip	898.00		NIST
Ip	891.00		NIST
S°liquid	[226.70; 227.48]	J/mol×K
S°liquid	226.70	J/mol×K	NIST
S°liquid	227.48	J/mol×K	NIST
Tboil	[347.00; 386.80]	K
Tboil	347.00	K	Excess volumes and speeds of sound of mixtures of 1,2-dibromoethane with chlorinated ethanes and ethenes at 303.15 K
Tboil	347.35	K	Excess molar enthalpies of dimethylsulfoxide with chloroethanes and chloroethenes at 298.15K
Tboil	347.35	K	Vapor-Liquid Equilibria and Excess Molar Enthalpies for N-Methyl-2-pyrrolidone with Chloroethanes and Chloroethenes
Tboil	347.35	K	Isobaric Vapor Liquid Equilibrium for Dimethylsulfoxide with Chloroethanes and Chloroethenes
Tboil	347.24	K	KDB
Tboil	347.23	K	NCMS SOLV-DB
Tboil	347.00 ± 0.30	K	NIST
Tboil	347.30	K	NIST
Tboil	347.00 ± 0.30	K	NIST
Tboil	347.20 ± 0.30	K	NIST
Tboil	347.20	K	NIST
Tboil	347.35 ± 0.30	K	NIST
Tboil	347.20 ± 0.15	K	NIST
Tboil	347.20 ± 0.20	K	NIST
Tboil	347.30 ± 0.30	K	NIST
Tboil	347.21 ± 0.15	K	NIST
Tboil	347.15 ± 0.50	K	NIST
Tboil	347.05 ± 0.30	K	NIST
Tboil	347.20 ± 0.30	K	NIST
Tboil	347.90 ± 0.50	K	NIST
Tboil	Outlier 386.80 ± 0.50	K	NIST
Tc	[545.00; 550.00]	K
Tc	550.00	K	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 10 Compiled value
Tc	545.00	K	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Tc	545.00	K	KDB
Tc	548.40	K	NIST
Tfus	[231.90; 244.95]	K
Tfus	242.74	K	Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
Tfus	242.70	K	KDB
Tfus	242.01	K	Aq. Solubility Prediction
Tfus	242.75	K	NCMS SOLV-DB
Tfus	240.90 ± 0.20	K	NIST
Tfus	Outlier 231.90 ± 1.20	K	NIST
Tfus	239.20 ± 1.00	K	NIST
Tfus	241.15 ± 1.00	K	NIST
Tfus	242.70 ± 0.02	K	NIST
Tfus	240.95 ± 0.20	K	NIST
Tfus	244.95 ± 0.40	K	NIST
Tfus	240.50 ± 0.30	K	NIST
Tfus	240.80 ± 0.50	K	NIST
Ttriple	[240.10; 243.13]	K
Ttriple	243.13	K	KDB
Ttriple	243.13 ± 0.02	K	NIST
Ttriple	240.10 ± 0.20	K	NIST
Ttriple	240.20 ± 0.20	K	NIST
Ttriple	243.13 ± 0.02	K	NIST
Ttriple	240.10 ± 0.20	K	NIST
Ttriple	240.20 ± 0.20	K	NIST
Vc	0.268	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	[138.90; 145.50]	J/mol×K	[250.00; 310.00]
Cp,liquid	140.10	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	138.90	J/mol×K	257.29	NIST
Cp,liquid	141.00	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	141.90	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	142.10	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	142.80	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	143.70	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	144.40	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	144.40	J/mol×K	298.15	NIST
Cp,liquid	144.31	J/mol×K	299.59	NIST
Cp,liquid	144.60	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	145.50	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,solid	123.00	J/mol×K	225.00	NIST
η	0.0007950	Pa×s	298.15	NCMS SOLV-DB
ΔfusH	[0.21; 7.49]	kJ/mol	[205.00; 243.10]
ΔfusH	0.21	kJ/mol	205.00	NIST
ΔfusH	7.45	kJ/mol	223.60	NIST
ΔfusH	7.47	kJ/mol	224.20	NIST
ΔfusH	7.49	kJ/mol	224.80	NIST
ΔfusH	1.88	kJ/mol	240.10	NIST
ΔfusH	1.88	kJ/mol	240.10	NIST
ΔfusH	1.88	kJ/mol	240.10	NIST
ΔfusH	1.88	kJ/mol	240.20	NIST
ΔfusH	2.35	kJ/mol	243.10	NIST
ΔvapH	[29.40; 37.60]	kJ/mol	[247.00; 512.00]
ΔvapH	37.60	kJ/mol	247.00	NIST
ΔvapH	33.40	kJ/mol	279.00	NIST
ΔvapH	33.40	kJ/mol	279.00	NIST
ΔvapH	33.40 ± 0.10	kJ/mol	284.00	NIST
ΔvapH	33.40 ± 0.10	kJ/mol	284.00	NIST
ΔvapH	33.31	kJ/mol	286.53	NIST
ΔvapH	33.31	kJ/mol	286.53	NIST
ΔvapH	32.30	kJ/mol	333.50	NIST
ΔvapH	32.40	kJ/mol	344.00	NIST
ΔvapH	29.86	kJ/mol	347.20	NIST
ΔvapH	30.50	kJ/mol	378.50	NIST
ΔvapH	29.40	kJ/mol	443.00	NIST
ΔvapH	29.50	kJ/mol	512.00	NIST
Pvap	[16.53; 37.61]	kPa	[298.15; 318.15]
Pvap	16.64	kPa	298.15	(Vapour + liquid) equilibria and excess Gibbs free energies of (cyclohexanone + 1- chlorobutane and + 1,1,1-trichloroethane) binary mixtures at temperatures from (298.15 to 318.15) K
Pvap	16.53	kPa	298.15	NCMS SOLV-DB
Pvap	25.85	kPa	308.15	(Vapour + liquid) equilibria and excess Gibbs free energies of (cyclohexanone + 1- chlorobutane and + 1,1,1-trichloroethane) binary mixtures at temperatures from (298.15 to 318.15) K
Pvap	37.61	kPa	318.15	(Vapour + liquid) equilibria and excess Gibbs free energies of (cyclohexanone + 1- chlorobutane and + 1,1,1-trichloroethane) binary mixtures at temperatures from (298.15 to 318.15) K
n0	[1.43500; 1.43790]		[293.15; 298.15]
n0	1.43790		293.15	Bubble points of the binary mixtures formed by ethylbenzene with some chloroaliphatics and substituted benzenes at p = 94.7 kPa
n0	1.43540		298.15	Isothermal (vapour + liquid) equilibria in the binary mixtures (1,2-dichloroethane and 1,1,1-trichloroethane with cyclopentanone) within the temperature range (298.15 to 313.15) K
n0	1.43590		298.15	Bubble Temperature Measurements on Binary Mixtures Formed by Cyclohexane at 94.7 kPa
n0	1.43600		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	1.43590		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	1.43500		298.15	NCMS SOLV-DB
ρl	[1294.47; 1346.17]	kg/m3	[288.15; 318.15]
ρl	1344.95	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	1346.17	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	1339.00	kg/m3	298.00	KDB
ρl	1328.27	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	1331.30	kg/m3	298.15	Volumetric and optical properties for some (2-butanone + chloroalkane) binary mixtures at T = 298.15 K
ρl	1328.24	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	1329.49	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	1329.55	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	1311.45	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	1311.45	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	1312.65	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	1294.47	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	1294.47	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	1295.66	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	[1.02; 33.31]	J/mol×K	[205.00; 243.10]
ΔfusS	1.02	J/mol×K	205.00	NIST
ΔfusS	33.31	J/mol×K	223.60	NIST
ΔfusS	33.30	J/mol×K	224.20	NIST
ΔfusS	33.30	J/mol×K	224.80	NIST
ΔfusS	7.84	J/mol×K	240.10	NIST
ΔfusS	7.80	J/mol×K	240.20	NIST
ΔfusS	9.67	J/mol×K	243.10	NIST
csound,fluid	[894.71; 962.94]	m/s	[298.15; 318.15]
csound,fluid	962.94	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	928.68	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	894.71	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	298.15	NCMS SOLV-DB
ΔvapS	[116.26; 116.26]	J/mol×K	[286.53; 286.53]
ΔvapS	116.26	J/mol×K	286.53	NIST
ΔvapS	116.26	J/mol×K	286.53	NIST

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[86.66; 148.79]	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			1.52700e+01
Coefficient B			3.40020e-01
Coefficient C			-3.18000e-04
Coefficient D			1.11500e-07
Coefficient E			0.00000e+00
Temperature range, min.			273.00
Temperature range, max.			1000.00
Cp,gas	86.66	J/mol×K	273.00	Calculated Property
Cp,gas	100.70	J/mol×K	353.78	Calculated Property
Cp,gas	112.13	J/mol×K	434.56	Calculated Property
Cp,gas	121.30	J/mol×K	515.33	Calculated Property
Cp,gas	128.58	J/mol×K	596.11	Calculated Property
Cp,gas	134.31	J/mol×K	676.89	Calculated Property
Cp,gas	138.84	J/mol×K	757.67	Calculated Property
Cp,gas	142.53	J/mol×K	838.44	Calculated Property
Cp,gas	145.73	J/mol×K	919.22	Calculated Property
Cp,gas	148.79	J/mol×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[0.71; 4303.56]	kPa	[243.10; 545.00]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.41227e+01
Coefficient B			-2.88621e+03
Coefficient C			-4.35260e+01
Temperature range, min.			243.10
Temperature range, max.			545.00
Pvap	0.71	kPa	243.10	Calculated Property
Pvap	5.71	kPa	276.64	Calculated Property
Pvap	27.09	kPa	310.19	Calculated Property
Pvap	90.79	kPa	343.73	Calculated Property
Pvap	238.62	kPa	377.28	Calculated Property
Pvap	525.66	kPa	410.82	Calculated Property
Pvap	1014.61	kPa	444.37	Calculated Property
Pvap	1769.21	kPa	477.91	Calculated Property
Pvap	2848.66	kPa	511.46	Calculated Property
Pvap	4303.56	kPa	545.00	Calculated Property
Pvap	[0.72; 4295.56]	kPa	[242.75; 545.00]	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			8.02341e+01
Coefficient B			-6.44789e+03
Coefficient C			-9.92362e+00
Coefficient D			8.37906e-06
Coefficient E			0.00000e+00
Temperature range, min.			242.75
Temperature range, max.			545.00
Pvap	0.72	kPa	242.75	Calculated Property
Pvap	5.77	kPa	276.33	Calculated Property
Pvap	27.35	kPa	309.92	Calculated Property
Pvap	90.54	kPa	343.50	Calculated Property
Pvap	233.85	kPa	377.08	Calculated Property
Pvap	506.76	kPa	410.67	Calculated Property
Pvap	968.24	kPa	444.25	Calculated Property
Pvap	1688.95	kPa	477.83	Calculated Property
Pvap	2758.14	kPa	511.42	Calculated Property
Pvap	4295.56	kPa	545.00	Calculated Property
Pvap	[3.84; 12.16]	kPa	[267.79; 290.07]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.81583e+01
Coefficient B			-5.08913e+03
Coefficient C			3.49020e+01
Reference			Rubin, Levedahl, et al., 1944, 2
Comment			Coefficents calculated by NIST from author's data.
Temperature range, min.			267.79
Temperature range, max.			290.07
Pvap	3.84	kPa	267.79	Calculated Property
Pvap	4.40	kPa	270.27	Calculated Property
Pvap	5.03	kPa	272.74	Calculated Property
Pvap	5.74	kPa	275.22	Calculated Property
Pvap	6.54	kPa	277.69	Calculated Property
Pvap	7.43	kPa	280.17	Calculated Property
Pvap	8.43	kPa	282.64	Calculated Property
Pvap	9.54	kPa	285.12	Calculated Property
Pvap	10.78	kPa	287.59	Calculated Property
Pvap	12.16	kPa	290.07	Calculated Property
Pvap	[3.84; 12.16]	kPa	[267.79; 290.07]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.81583e+01
Coefficient B			-5.08913e+03
Coefficient C			3.49020e+01
Reference			Rubin, Levedahl, et al., 1944
Comment			Coefficents calculated by NIST from author's data.
Temperature range, min.			267.79
Temperature range, max.			290.07
Pvap	3.84	kPa	267.79	Calculated Property
Pvap	4.40	kPa	270.27	Calculated Property
Pvap	5.03	kPa	272.74	Calculated Property
Pvap	5.74	kPa	275.22	Calculated Property
Pvap	6.54	kPa	277.69	Calculated Property
Pvap	7.43	kPa	280.17	Calculated Property
Pvap	8.43	kPa	282.64	Calculated Property
Pvap	9.54	kPa	285.12	Calculated Property
Pvap	10.78	kPa	287.59	Calculated Property
Pvap	12.16	kPa	290.07	Calculated Property

Property	Value	Unit	Temperature (K)	Source
γ	[0.03; 0.02]	N/m	[242.75; 347.15]	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			6.22052e-02
Coefficient B			-1.24200e-04
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Temperature range, min.			242.75
Temperature range, max.			347.15
γ	0.03	N/m	242.75	Calculated Property
γ	0.03	N/m	254.35	Calculated Property
γ	0.03	N/m	265.95	Calculated Property
γ	0.03	N/m	277.55	Calculated Property
γ	0.03	N/m	289.15	Calculated Property
γ	0.02	N/m	300.75	Calculated Property
γ	0.02	N/m	312.35	Calculated Property
γ	0.02	N/m	323.95	Calculated Property
γ	0.02	N/m	335.55	Calculated Property
γ	0.02	N/m	347.15	Calculated Property

Similar Compounds

Find more compounds similar to Ethane, 1,1,1-trichloro-.

Mixtures

• Ethane, 1,1,1-trichloro- + Methane, nitro-
• Ethane, 1,1,1-trichloro- + Benzene, ethyl-
• 2-Butanone + Ethane, 1,1,1-trichloro-
• Ethane, 1,1,1-trichloro- + Cyclopentanone
• Ethane, 1,1,1-trichloro- + Dimethyl Sulfoxide
• Ethane, 1,1,1-trichloro- + Cyclohexanone
• Ethane, 1,1,1-trichloro- + Ethane, 1,2-dibromo-
• Ethane, 1,1,1-trichloro- + Water
• Ethane, 1,1,1-trichloro- + Heptane
• Benzene, nitro- + Ethane, 1,1,1-trichloro-
• Ethane, 1,1,1-trichloro- + Benzene, chloro-
• Ethane, 1,1,1-trichloro- + Cyclohexane
• Ethane, 1,1,1-trichloro- + 2-Pyrrolidinone, 1-methyl-
• Ethane, 1,1,1-trichloro- + Tetrahydrofuran
• Ethane, 1,1,1-trichloro- + 1-Butanol, 2-methyl-
• Ethane, 1,1,1-trichloro- + 1-Heptanol

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).
• IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 10 ChEDL chemicals 1.5.2, from Marsh, K. N.; Abramson, A.; Ambrose, D.; Morton, D. W.; Nikitin, E.; Tsonopoulos, C.; Young, C. L. Vapor-Liquid Critical Properties of Elements and Compounds. 10. Organic Compounds Containing Halogens. J. Chem. Eng. Data 2007, 52, 1509-1538.
• 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.
• 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) equilibria in the binary mixtures (1,2-dichloroethane and 1,1,1-trichloroethane with cyclopentanone) within the temperature range (298.15 to 313.15) K
• Bubble points of the binary mixtures formed by ethylbenzene with some chloroaliphatics and substituted benzenes at p = 94.7 kPa
• (Vapour + liquid) equilibria and excess Gibbs free energies of (cyclohexanone + 1- chlorobutane and + 1,1,1-trichloroethane) binary mixtures at temperatures from (298.15 to 318.15) K
• Volumetric and optical properties for some (2-butanone + chloroalkane) binary mixtures at T = 298.15 K
• Excess molar enthalpies of dimethylsulfoxide with chloroethanes and chloroethenes at 298.15K
• 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
• 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 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
• Densities and Excess Molar Volumes of the Binary Mixtures of Cyclohexanone with Chloroalkanes at Temperatures between (288.15 and 318.15) 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
• NCMS SOLV-DB
• 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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