Chemical Properties of Trichloroethylene (CAS 79-01-6)

InChI

InChI=1S/C2HCl3/c3-1-2(4)5/h1H

InChI Key

XSTXAVWGXDQKEL-UHFFFAOYSA-N

Formula

C2HCl3

SMILES

ClC=C(Cl)Cl

Molecular Weight¹

131.39

CAS

79-01-6

Other Names

• 1,1,2-Trichloroethene
• 1,1,2-trichloroethylene
• 1,1-Dichloro-2-chloroethylene
• 1,2,2-Trichloroethylene
• 1-Chloro-2,2-dichloroethylene
• Acetylene trichloride
• Algylen
• Anamenth
• Benzinol
• Blacosolv
• Blancosolv
• C2HCl3
• Cecolene
• Chlorilen
• Chlorylea
• Chlorylen
• Chorylen
• Circosolv
• Crawhaspol
• Densinfluat
• Distillex DS2
• Dow-tri
• Dukeron
• Ethene, 1,1,2-trichloro-
• Ethene, trichloro-
• Ethinyl trichloride
• Ethylene trichloride
• Ethylene, trichloro-
• Fleck-flip
• Flock FLIP
• Fluate
• Gemalgene
• Germalgene
• Lanadin
• Lethurin
• NCI-C04546
• Narcogen
• Narkogen
• Narkosoid
• Nialk
• Perm-A-chlor
• Perm-A-clor
• Petzinol
• Philex
• R 1120
• RCRA Waste number U228
• TCE
• Threthylen
• Threthylene
• Trethylene
• Tri
• Tri-Clene
• Tri-plus
• Tri-plus M
• Triad
• Trial
• Triasol
• Trichlooretheen
• Trichloorethyleen, tri
• Trichloraethen
• Trichloraethylen, tri
• Trichloran
• Trichloren
• Trichlorethene
• Trichlorethylene
• Trichlorethylene, tri
• Tricloretene
• Tricloroetilene
• Trielene
• Trielin
• Trielina
• Trieline
• Triklone
• Triklone N
• Trilen
• Trilene
• Triline
• Trimar
• Triol
• UN 1710
• Vestrol
• Vitran
• Westrosol
• trichloroethene

• 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).
• EA : Electron affinity (eV).
• 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 : Polar retention indices.
• Δ_fusS : Entropy of fusion 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).
• V_c : Critical Volume (m³/kmol).
• ¹: Molecular weight from the IUPAC atomic weights tables.

Physical Properties

Property	Value	Unit	Source
ω	0.2070		Relay (1.0) Calculated Property
ΔcH°liquid	[-956.50; -947.70]	kJ/mol
ΔcH°liquid	-947.70 ± 2.90	kJ/mol	NIST
ΔcH°liquid	-956.50 ± 8.40	kJ/mol	NIST
η	0.0005510	Pa×s	Densities and Viscosities of Binary Liquid Mixtures of Trichloroethylene and Tetrachloroethylene with Some Polar and Nonpolar Solvents
EA	[0.30; 0.40]	eV
EA	0.40 ± 0.22	eV	NIST
EA	0.30	eV	NIST
ΔfG°	1.84	kJ/mol	Joback Calculated Property
ΔfH°gas	[-19.10; -5.90]	kJ/mol
ΔfH°gas	-18.00 ± 2.00	kJ/mol	NIST
ΔfH°gas	-19.10 ± 3.00	kJ/mol	NIST
ΔfH°gas	-5.90	kJ/mol	NIST
ΔfH°liquid	[-53.10; -41.00]	kJ/mol
ΔfH°liquid	-52.00 ± 3.00	kJ/mol	NIST
ΔfH°liquid	-53.10 ± 3.00	kJ/mol	NIST
ΔfH°liquid	-41.00	kJ/mol	NIST
ΔfusH°	12.42	kJ/mol	Joback Calculated Property
ΔvapH°	[33.97; 34.70]	kJ/mol
ΔvapH°	34.62	kJ/mol	NIST
ΔvapH°	34.57 ± 0.09	kJ/mol	NIST
ΔvapH°	33.97 ± 0.13	kJ/mol	NIST
ΔvapH°	34.50 ± 0.10	kJ/mol	NIST
ΔvapH°	34.70 ± 0.42	kJ/mol	NIST
IE	[9.45; 9.68]	eV
IE	9.46 ± 0.02	eV	NIST
IE	9.68	eV	NIST
IE	9.48	eV	NIST
IE	9.45 ± 0.01	eV	NIST
IE	9.45	eV	NIST
IE	9.47 ± 0.01	eV	NIST
IE	9.60	eV	NIST
log10WS	[-1.96; -1.95]
log10WS	-1.95		Aq. Solubility Prediction
log10WS	-1.96		Estimated Solubility
logPoct/wat	2.502		Crippen Calculated Property
McVol	71.460	ml/mol	McGowan Calculated Property
Pc	4665.71	kPa	Joback Calculated Property
Inp	[672.00; 722.00]
Inp	694.00		NIST
Inp	691.00		NIST
Inp	688.00		NIST
Inp	675.00		NIST
Inp	696.00		NIST
Inp	702.00		NIST
Inp	691.00		NIST
Inp	686.00		NIST
Inp	710.00		NIST
Inp	698.00		NIST
Inp	690.00		NIST
Inp	693.00		NIST
Inp	703.00		NIST
Inp	702.10		NIST
Inp	683.00		NIST
Inp	702.00		NIST
Inp	687.00		NIST
Inp	691.00		NIST
Inp	690.00		NIST
Inp	701.00		NIST
Inp	680.00		NIST
Inp	680.00		NIST
Inp	691.00		NIST
Inp	Outlier 722.00		NIST
Inp	686.00		NIST
Inp	690.00		NIST
Inp	702.00		NIST
Inp	693.00		NIST
Inp	694.00		NIST
Inp	691.00		NIST
Inp	701.00		NIST
Inp	681.00		NIST
Inp	681.00		NIST
Inp	691.00		NIST
Inp	710.00		NIST
Inp	700.00		NIST
Inp	686.00		NIST
Inp	689.00		NIST
Inp	672.00		NIST
Inp	686.00		NIST
Inp	673.00		NIST
Inp	680.00		NIST
Inp	689.00		NIST
Inp	710.00		NIST
Inp	683.00		NIST
Inp	691.00		NIST
Inp	702.00		NIST
Inp	681.00		NIST
Inp	686.00		NIST
Inp	680.00		NIST
I	[964.00; 1028.00]
I	1008.00		NIST
I	1019.00		NIST
I	1010.00		NIST
I	1010.70		NIST
I	1012.45		NIST
I	1007.14		NIST
I	999.00		NIST
I	993.00		NIST
I	1010.00		NIST
I	1010.00		NIST
I	1010.00		NIST
I	993.00		NIST
I	984.00		NIST
I	970.00		NIST
I	993.00		NIST
I	1028.00		NIST
I	999.00		NIST
I	1028.00		NIST
I	Outlier 964.00		NIST
I	993.00		NIST
I	1008.00		NIST
I	1007.14		NIST
I	1010.00		NIST
I	970.00		NIST
I	Outlier 964.00		NIST
Tboil	[360.00; 360.55]	K
Tboil	360.40	K	Excess volumes and speeds of sound of mixtures of 1,2-dibromoethane with chlorinated ethanes and ethenes at 303.15 K
Tboil	360.25	K	Excess molar enthalpies of dimethylsulfoxide with chloroethanes and chloroethenes at 298.15K
Tboil	360.25	K	Vapor-Liquid Equilibria and Excess Molar Enthalpies for N-Methyl-2-pyrrolidone with Chloroethanes and Chloroethenes
Tboil	360.25	K	Isobaric Vapor Liquid Equilibrium for Dimethylsulfoxide with Chloroethanes and Chloroethenes
Tboil	360.40 ± 0.30	K	NIST
Tboil	Outlier 360.55 ± 0.40	K	NIST
Tboil	360.20 ± 0.40	K	NIST
Tboil	360.20	K	NIST
Tboil	360.00 ± 0.40	K	NIST
Tboil	360.22 ± 0.30	K	NIST
Tboil	360.40	K	NIST
Tboil	360.05 ± 0.20	K	NIST
Tboil	360.40 ± 0.70	K	NIST
Tboil	360.05 ± 0.30	K	NIST
Tboil	360.10 ± 0.50	K	NIST
Tboil	360.10 ± 0.50	K	NIST
Tboil	360.25 ± 0.30	K	NIST
Tc	571.00	K	NIST
Tfus	[188.25; 188.50]	K
Tfus	188.25	K	Aq. Solubility Prediction
Tfus	188.50 ± 0.20	K	NIST
Tfus	188.35 ± 0.30	K	NIST
Vc	0.254	m3/kmol	Relay (1.0) Calculated Property

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[84.33; 100.24]	J/mol×K	[361.49; 569.29]
Cp,gas	84.33	J/mol×K	361.49	Joback Calculated Property
Cp,gas	87.67	J/mol×K	396.12	Joback Calculated Property
Cp,gas	90.70	J/mol×K	430.76	Joback Calculated Property
Cp,gas	93.46	J/mol×K	465.39	Joback Calculated Property
Cp,gas	95.95	J/mol×K	500.02	Joback Calculated Property
Cp,gas	98.20	J/mol×K	534.65	Joback Calculated Property
Cp,gas	100.24	J/mol×K	569.29	Joback Calculated Property
Cp,liquid	[120.10; 131.12]	J/mol×K	[260.64; 329.56]
Cp,liquid	126.71	J/mol×K	260.64	Heat capacities of selected chlorohydrocarbons
Cp,liquid	126.63	J/mol×K	260.64	Heat capacities of selected chlorohydrocarbons
Cp,liquid	126.63	J/mol×K	260.64	Heat capacities of selected chlorohydrocarbons
Cp,liquid	126.63	J/mol×K	260.64	Heat capacities of selected chlorohydrocarbons
Cp,liquid	126.71	J/mol×K	265.75	Heat capacities of selected chlorohydrocarbons
Cp,liquid	126.80	J/mol×K	265.75	Heat capacities of selected chlorohydrocarbons
Cp,liquid	126.71	J/mol×K	265.75	Heat capacities of selected chlorohydrocarbons
Cp,liquid	126.96	J/mol×K	265.75	Heat capacities of selected chlorohydrocarbons
Cp,liquid	126.71	J/mol×K	270.85	Heat capacities of selected chlorohydrocarbons
Cp,liquid	126.96	J/mol×K	270.85	Heat capacities of selected chlorohydrocarbons
Cp,liquid	126.63	J/mol×K	270.85	Heat capacities of selected chlorohydrocarbons
Cp,liquid	127.04	J/mol×K	270.85	Heat capacities of selected chlorohydrocarbons
Cp,liquid	127.13	J/mol×K	275.96	Heat capacities of selected chlorohydrocarbons
Cp,liquid	127.04	J/mol×K	275.96	Heat capacities of selected chlorohydrocarbons
Cp,liquid	126.96	J/mol×K	275.96	Heat capacities of selected chlorohydrocarbons
Cp,liquid	127.38	J/mol×K	275.96	Heat capacities of selected chlorohydrocarbons
Cp,liquid	127.38	J/mol×K	281.06	Heat capacities of selected chlorohydrocarbons
Cp,liquid	127.38	J/mol×K	281.06	Heat capacities of selected chlorohydrocarbons
Cp,liquid	127.46	J/mol×K	281.06	Heat capacities of selected chlorohydrocarbons
Cp,liquid	127.79	J/mol×K	281.06	Heat capacities of selected chlorohydrocarbons
Cp,liquid	127.96	J/mol×K	286.17	Heat capacities of selected chlorohydrocarbons
Cp,liquid	127.96	J/mol×K	286.17	Heat capacities of selected chlorohydrocarbons
Cp,liquid	127.88	J/mol×K	286.17	Heat capacities of selected chlorohydrocarbons
Cp,liquid	128.38	J/mol×K	286.17	Heat capacities of selected chlorohydrocarbons
Cp,liquid	121.00	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	128.21	J/mol×K	291.27	Heat capacities of selected chlorohydrocarbons
Cp,liquid	128.46	J/mol×K	291.27	Heat capacities of selected chlorohydrocarbons
Cp,liquid	128.38	J/mol×K	291.27	Heat capacities of selected chlorohydrocarbons
Cp,liquid	128.29	J/mol×K	291.27	Heat capacities of selected chlorohydrocarbons
Cp,liquid	128.54	J/mol×K	296.38	Heat capacities of selected chlorohydrocarbons
Cp,liquid	128.38	J/mol×K	296.38	Heat capacities of selected chlorohydrocarbons
Cp,liquid	128.46	J/mol×K	296.38	Heat capacities of selected chlorohydrocarbons
Cp,liquid	128.96	J/mol×K	296.38	Heat capacities of selected chlorohydrocarbons
Cp,liquid	124.70	J/mol×K	298.00	NIST
Cp,liquid	120.10	J/mol×K	298.00	NIST
Cp,liquid	124.00	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	125.00	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	128.79	J/mol×K	301.48	Heat capacities of selected chlorohydrocarbons
Cp,liquid	129.04	J/mol×K	301.48	Heat capacities of selected chlorohydrocarbons
Cp,liquid	128.96	J/mol×K	301.48	Heat capacities of selected chlorohydrocarbons
Cp,liquid	128.54	J/mol×K	301.48	Heat capacities of selected chlorohydrocarbons
Cp,liquid	129.21	J/mol×K	309.14	Heat capacities of selected chlorohydrocarbons
Cp,liquid	130.29	J/mol×K	309.14	Heat capacities of selected chlorohydrocarbons
Cp,liquid	129.04	J/mol×K	309.14	Heat capacities of selected chlorohydrocarbons
Cp,liquid	131.12	J/mol×K	319.35	Heat capacities of selected chlorohydrocarbons
Cp,liquid	130.29	J/mol×K	319.35	Heat capacities of selected chlorohydrocarbons
Cp,liquid	130.29	J/mol×K	319.35	Heat capacities of selected chlorohydrocarbons
Cp,liquid	130.95	J/mol×K	329.56	Heat capacities of selected chlorohydrocarbons
Cp,liquid	131.12	J/mol×K	329.56	Heat capacities of selected chlorohydrocarbons
ΔfusH	[8.45; 8.45]	kJ/mol	[188.50; 188.50]
ΔfusH	8.45	kJ/mol	188.50	NIST
ΔfusH	8.45	kJ/mol	188.50	NIST
ΔfusH	8.45	kJ/mol	188.50	NIST
ΔvapH	[31.40; 36.20]	kJ/mol	[324.50; 360.40]
ΔvapH	36.20	kJ/mol	324.50	NIST
ΔvapH	34.20	kJ/mol	328.50	NIST
ΔvapH	35.60	kJ/mol	329.00	NIST
ΔvapH	34.60	kJ/mol	354.00	NIST
ΔvapH	32.13	kJ/mol	360.19	NIST
ΔvapH	31.40	kJ/mol	360.40	NIST
n0	[1.46900; 1.47820]		[293.15; 308.15]
n0	1.47820		293.15	Bubble points of some binary mixtures formed by o-cresol at 95.75 kPa
n0	1.47820		293.15	Excess Gibbs energies of selected binary mixtures formed by N,N-dimethyl formamide at 95.5 kPa
n0	1.47520		298.15	Density, Viscosity, Refractive Index, and Speed of Sound in the Binary Mixtures of Tri-n-butylamine + Triethylamine, + Tetrahydrofuran, + Tetradecane, + Tetrachloroethylene, + Pyridine, or + Trichloroethylene at (298.15, 303.15, and 308.15) K
n0	1.47820		298.15	Activity coefficients and excess Gibbs free energy of some binary mixtures formed by p-cresol at 95.23 kPa
n0	1.47820		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	1.47500		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	1.47820		298.15	Bubble points of the binary mixtures formed by ethylbenzene with some chloroaliphatics and substituted benzenes at p = 94.7 kPa
n0	1.47600		298.15	Density, Viscosity, Refractive Index, and Speed of Sound for Binary Mixtures of 1,4-Dioxane with Different Organic Liquids at (298.15, 303.15, and 308.15) K
n0	1.47500		298.15	Densities, Excess Molar Volumes, Viscosity, and Refractive Indices of Binary Mixtures of Ethanoic Acid and Trichloroethylene with Dimethylbenzenes at Different Temperatures
n0	1.47220		303.15	Density, Viscosity, Refractive Index, and Speed of Sound in the Binary Mixtures of Tri-n-butylamine + Triethylamine, + Tetrahydrofuran, + Tetradecane, + Tetrachloroethylene, + Pyridine, or + Trichloroethylene at (298.15, 303.15, and 308.15) K
n0	1.47290		303.15	Density, Viscosity, Refractive Index, and Speed of Sound for Binary Mixtures of 1,4-Dioxane with Different Organic Liquids at (298.15, 303.15, and 308.15) K
n0	1.47500		303.15	Vapor-Liquid Equilibria of Binary Mixtures Formed by Hexan-1-ol with Chloroethanes and Chloroethenes at 95.6 kPa
n0	1.46900		308.15	Density, Viscosity, Refractive Index, and Speed of Sound in the Binary Mixtures of Tri-n-butylamine + Triethylamine, + Tetrahydrofuran, + Tetradecane, + Tetrachloroethylene, + Pyridine, or + Trichloroethylene at (298.15, 303.15, and 308.15) K
n0	1.46980		308.15	Density, Viscosity, Refractive Index, and Speed of Sound for Binary Mixtures of 1,4-Dioxane with Different Organic Liquids at (298.15, 303.15, and 308.15) K
ρl	[1430.40; 1455.90]	kg/m3	[298.15; 313.15]
ρl	1455.65	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	1455.90	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	1450.90	kg/m3	303.15	Excess Volumes and Excess Isentropic Compressibilities of Binary Liquid Mixtures of Trichloroethylene with Esters at 303.15 K
ρl	1447.50	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	1437.80	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	1430.40	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
ΔfusS	44.80	J/mol×K	188.50	NIST

Datasets

Viscosity, Pa*s

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Viscosity, Pa*s - Liquid
308.15	101.00	0.0005
Reference

Correlations

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.63]	kPa	[267.49; 383.80]	The Yaws Handbook of Vapor Pressure
Equation			ln(Pvp) = A + B/(T + C)
Coefficient A			1.38164e+01
Coefficient B			-2.66405e+03
Coefficient C			-7.05700e+01
Temperature range, min.			267.49
Temperature range, max.			383.80
Pvap	1.33	kPa	267.49	Calculated Property
Pvap	3.07	kPa	280.41	Calculated Property
Pvap	6.41	kPa	293.34	Calculated Property
Pvap	12.35	kPa	306.26	Calculated Property
Pvap	22.22	kPa	319.18	Calculated Property
Pvap	37.72	kPa	332.11	Calculated Property
Pvap	60.94	kPa	345.03	Calculated Property
Pvap	94.30	kPa	357.95	Calculated Property
Pvap	140.52	kPa	370.88	Calculated Property
Pvap	202.63	kPa	383.80	Calculated Property
Pvap	[2.02e-03; 4903.43]	kPa	[188.40; 571.00]	KDB Vapor Pressure Data
Equation			ln(Pvp) = A + B/T + C*ln(T) + D*T^2
Coefficient A			3.98315e+01
Coefficient B			-5.14297e+03
Coefficient C			-3.58643e+00
Coefficient D			1.34232e-06
Temperature range, min.			188.40
Temperature range, max.			571.00
Pvap	2.02e-03	kPa	188.40	Calculated Property
Pvap	0.15	kPa	230.91	Calculated Property
Pvap	2.71	kPa	273.42	Calculated Property
Pvap	21.01	kPa	315.93	Calculated Property
Pvap	95.71	kPa	358.44	Calculated Property
Pvap	306.11	kPa	400.96	Calculated Property
Pvap	765.33	kPa	443.47	Calculated Property
Pvap	1602.81	kPa	485.98	Calculated Property
Pvap	2945.14	kPa	528.49	Calculated Property
Pvap	4903.43	kPa	571.00	Calculated Property

Similar Compounds

Find more compounds similar to Trichloroethylene.

Mixtures

• Trichloroethylene + Water
• Trichloroethylene + Phenol, 2-methyl-
• Trichloroethylene + Benzene, ethyl-
• Trichloroethylene + Formamide, N,N-dimethyl-
• Trichloroethylene + Acetamide, N-methyl-
• Trichloroethylene + PHENOL, 4-METHYL-
• Trichloroethylene + Dimethyl Sulfoxide
• Trichloroethylene + Tetradecanoic acid
• Trichloroethylene + n-Hexadecanoic acid
• Trichloroethylene + n-Decanoic acid
• Trichloroethylene + Dodecanoic acid
• Trichloroethylene + Octadecanoic acid
• Oleic Acid + Trichloroethylene
• Trichloroethylene + Ethane, 1,2-dibromo-
• Trichloroethylene + Ethyl Acetate
• Trichloroethylene + Acetic acid, propyl ester
• Trichloroethylene + Acetic acid, butyl ester
• Trichloroethylene + Benzyl nitrile
• Trichloroethylene + Ethanol + n-Hexadecanoic acid
• Trichloroethylene + 2-Propanol + n-Hexadecanoic acid

Find more mixtures with Trichloroethylene.

Sources

• KDB Vapor Pressure Data
• Cheméo Relay (1.0)
• Crippen Method
• Excess Volumes and Excess Isentropic Compressibilities of Binary Liquid Mixtures of Trichloroethylene with Esters at 303.15 K
• Bubble points of some binary mixtures formed by o-cresol at 95.75 kPa
• Excess Gibbs energies of selected binary mixtures formed by N,N-dimethyl formamide at 95.5 kPa
• Determination of vapour-liquid and vapour-liquid-liquid equilibrium of the chloroform-water and trichloroethylene-water binary mixtures
• Heat capacities of selected chlorohydrocarbons
• Using binary mixtures of dicationic ionic liquids for determination ofactivity coefficients at infinite dilution by gas-liquid chromatography
• Excess volumes and speeds of sound of mixtures of 1,2-dibromoethane with chlorinated ethanes and ethenes at 303.15 K
• Bubble points of the binary mixtures formed by ethylbenzene with some chloroaliphatics and substituted benzenes at p = 94.7 kPa
• 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
• Activity coefficient at infinite dilution measurements for organic solutes (polar and non-polar) in fatty compounds: Saturated fatty acids
• Activity coefficient at infinite dilution measurements for organic solutes (polar and non-polar) in fatty compounds Part II: C18 fatty acids
• Excess molar enthalpies of dimethylsulfoxide with chloroethanes and chloroethenes at 298.15K
• Dilute Vapor Absorption: A New Accurate Technique for Measurement of the Limiting Activity Coefficient of Water in Hydrophobic Solvents of Lower Volatility
• Vapor-Liquid Equilibria and Excess Molar Enthalpies for N-Methyl-2-pyrrolidone with Chloroethanes and Chloroethenes
• Measurement and Estimation of Henry's Law Constants of Chlorinated Ethylenes in Aqueous Surfactant Solutions
• 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 in the Binary Mixtures of Tri-n-butylamine + Triethylamine, + Tetrahydrofuran, + Tetradecane, + Tetrachloroethylene, + Pyridine, or + Trichloroethylene at (298.15, 303.15, and 308.15) K
• Densities and Viscosities of Binary Liquid Mixtures of Trichloroethylene and Tetrachloroethylene with Some Polar and Nonpolar Solvents
• Density, Viscosity, Refractive Index, and Speed of Sound for Binary Mixtures of 1,4-Dioxane with Different Organic Liquids at (298.15, 303.15, and 308.15) K
• Liquid-Liquid Equilibria for the Ternary Systems of (Water + Tetrahydrofuran + Polar Solvent) at 298.15 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
• Activity Coefficients at Infinite Dilution in 1-Alkyl-3-methylimidazolium Tetrafluoroborate Ionic Liquids
• Activity Coefficients at Infinite Dilution in Methylimidazolium Nitrate Ionic Liquids
• Densities, Excess Molar Volumes, Viscosity, and Refractive Indices of Binary Mixtures of Ethanoic Acid and Trichloroethylene with Dimethylbenzenes at Different Temperatures
• Determination of Henry's Law Constants Using Internal Standards with Benchmark Values
• Isobaric Vapor Liquid Equilibrium for Dimethylsulfoxide with Chloroethanes and Chloroethenes
• Henry s Law Constants for Fragrance and Organic Solvent Compounds in Aqueous Industrial Surfactants
• Solubilities of Stearic Acid in Organic Solvents and in Azeotropic Solvent Mixtures
• Solubilities of Palmitic Acid in Pure Solvents and Its Mixtures
• Solubilities of Lauric Acid in n-Hexane, Acetone, Propanol, 2-Propanol, 1-Bromopropane, and Trichloroethylene from (279.0 to 315.3) K
• Vapor-Liquid Equilibria of Binary Mixtures Formed by Hexan-1-ol with Chloroethanes and Chloroethenes at 95.6 kPa
• 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
• 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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