Chemical Properties of Tetrachloroethylene (CAS 127-18-4)

InChI

InChI=1S/C2Cl4/c3-1(4)2(5)6

InChI Key

CYTYCFOTNPOANT-UHFFFAOYSA-N

Formula

C2Cl4

SMILES

ClC(Cl)=C(Cl)Cl

Molecular Weight¹

165.83

CAS

127-18-4

Other Names

• 1,1,2,2-Tetrachloroethene
• 1,1,2,2-Tetrachloroethylene
• Ankilostin
• Antisal 1
• Antisol 1
• C2Cl4
• Carbon bichloride
• Carbon dichloride
• Czterochloroetylen
• Didakene
• Dilatin PT
• Dow-per
• ENT 1,860
• Ethene, tetrachloro-
• Ethylene tetrachloride
• Ethylene, tetrachloro-
• F 1110
• Fedal-Un
• Freon 1110
• NCI-C04580
• Nema
• Nema, veterinary
• PERC
• PERK
• PerSec
• Perawin
• Perchloorethyleen, per
• Perchlor
• Perchloraethylen, per
• Perchlorethylene
• Perchlorethylene, per
• Perchloroethene
• Perclene
• Perclene D
• Perclene TG
• Percloroetilene
• Percosolve
• Perklone
• RCRA Waste Number U210
• Tetlen
• Tetracap
• Tetrachlooretheen
• Tetrachloraethen
• Tetrachlorethylene
• Tetracloroetene
• Tetraguer
• Tetraleno
• Tetralex
• Tetravec
• Tetroguer
• Tetropil
• UN 1897
• perchloroethylene
• tetrachloroethene

• 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).
• 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).
• 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).
• ¹: Molecular weight from the IUPAC atomic weights tables.

Physical Properties

Property	Value	Unit	Source
ΔcH°liquid	-830.00 ± 10.00	kJ/mol	NIST
μ	0.00	debye	KDB
η	[0.0008474; 0.0008900]	Pa×s
η	0.0008474	Pa×s	Densities and Viscosities of Binary Liquid Mixtures of Trichloroethylene and Tetrachloroethylene with Some Polar and Nonpolar Solvents
η	0.0008900	Pa×s	Studies on Transport and Thermodynamic Properties of Binary Mixtures of Hexan-1-ol with Halogenated Compounds at 293.15 K
EA	[0.50; 0.64]	eV
EA	0.64 ± 0.03	eV	NIST
EA	0.50	eV	NIST
ΔfG°	22.61	kJ/mol	KDB
ΔfH°gas	[-24.00; -12.14]	kJ/mol
ΔfH°gas	-12.14	kJ/mol	KDB
ΔfH°gas	-24.00 ± 4.00	kJ/mol	NIST
ΔfH°gas	-15.00	kJ/mol	NIST
ΔfH°liquid	[-64.00; -54.40]	kJ/mol
ΔfH°liquid	-64.00 ± 4.00	kJ/mol	NIST
ΔfH°liquid	-54.40	kJ/mol	NIST
ΔfusH°	15.31	kJ/mol	Joback Calculated Property
ΔvapH°	[39.70; 39.72]	kJ/mol
ΔvapH°	39.72	kJ/mol	NIST
ΔvapH°	39.72 ± 0.05	kJ/mol	NIST
ΔvapH°	39.70 ± 0.10	kJ/mol	NIST
ΔvapH°	39.70 ± 0.84	kJ/mol	NIST
IE	[9.32; 9.51]	eV
IE	9.33 ± 0.00	eV	NIST
IE	9.33 ± 0.00	eV	NIST
IE	9.51	eV	NIST
IE	9.34	eV	NIST
IE	9.32 ± 0.01	eV	NIST
IE	9.32	eV	NIST
IE	9.50	eV	NIST
log10WS	[-2.60; -2.54]
log10WS	-2.60		Aq. Solubility Prediction
log10WS	-2.54		Estimated Solubility
logPoct/wat	3.068		Crippen Calculated Property
McVol	83.700	ml/mol	McGowan Calculated Property
Pc	4760.00	kPa	KDB
Inp	[785.00; 832.30]
Inp	806.00		NIST
Inp	823.00		NIST
Inp	825.59		NIST
Inp	Outlier 832.30		NIST
Inp	803.00		NIST
Inp	799.00		NIST
Inp	801.00		NIST
Inp	809.00		NIST
Inp	814.00		NIST
Inp	804.00		NIST
Inp	806.00		NIST
Inp	825.00		NIST
Inp	814.00		NIST
Inp	801.00		NIST
Inp	815.45		NIST
Inp	817.10		NIST
Inp	815.90		NIST
Inp	794.80		NIST
Inp	809.30		NIST
Inp	804.00		NIST
Inp	815.00		NIST
Inp	796.00		NIST
Inp	801.00		NIST
Inp	806.00		NIST
Inp	814.00		NIST
Inp	807.00		NIST
Inp	796.52		NIST
Inp	819.00		NIST
Inp	823.00		NIST
Inp	794.00		NIST
Inp	808.00		NIST
Inp	814.00		NIST
Inp	808.00		NIST
Inp	815.00		NIST
Inp	806.00		NIST
Inp	794.51		NIST
Inp	794.00		NIST
Inp	803.00		NIST
Inp	806.00		NIST
Inp	811.00		NIST
Inp	802.00		NIST
Inp	793.00		NIST
Inp	793.00		NIST
Inp	811.00		NIST
Inp	797.00		NIST
Inp	816.00		NIST
Inp	785.00		NIST
Inp	800.00		NIST
Inp	789.00		NIST
Inp	797.00		NIST
Inp	789.00		NIST
Inp	796.00		NIST
Inp	814.00		NIST
Inp	794.00		NIST
Inp	793.00		NIST
Inp	785.00		NIST
Inp	796.00		NIST
I	[1012.00; 1059.96]
I	1044.00		NIST
I	1038.00		NIST
I	1050.23		NIST
I	Outlier 1059.96		NIST
I	1036.20		NIST
I	1030.00		NIST
I	1024.00		NIST
I	1022.00		NIST
I	1022.00		NIST
I	1021.00		NIST
I	1026.00		NIST
I	1045.00		NIST
I	1012.00		NIST
I	1012.00		NIST
I	1018.00		NIST
I	1024.00		NIST
I	1044.00		NIST
I	1030.00		NIST
I	1021.00		NIST
S°liquid	240.60	J/mol×K	NIST
Tboil	[392.70; 394.70]	K
Tboil	394.45	K	Excess volumes and speeds of sound of mixtures of 1,2-dibromoethane with chlorinated ethanes and ethenes at 303.15 K
Tboil	394.15	K	Excess molar enthalpies of dimethylsulfoxide with chloroethanes and chloroethenes at 298.15K
Tboil	394.15	K	Vapor-Liquid Equilibria and Excess Molar Enthalpies for N-Methyl-2-pyrrolidone with Chloroethanes and Chloroethenes
Tboil	394.15	K	Isobaric Vapor Liquid Equilibrium for Dimethylsulfoxide with Chloroethanes and Chloroethenes
Tboil	394.40	K	KDB
Tboil	394.45 ± 0.30	K	NIST
Tboil	394.20	K	NIST
Tboil	394.21 ± 0.30	K	NIST
Tboil	394.10	K	NIST
Tboil	394.50 ± 0.50	K	NIST
Tboil	394.23 ± 0.10	K	NIST
Tboil	394.18 ± 0.10	K	NIST
Tboil	Outlier 392.70 ± 3.00	K	NIST
Tboil	394.70 ± 1.50	K	NIST
Tboil	394.17 ± 0.07	K	NIST
Tboil	394.25 ± 0.50	K	NIST
Tboil	394.15 ± 0.30	K	NIST
Tboil	393.80 ± 0.30	K	NIST
Tboil	394.35 ± 0.30	K	NIST
Tboil	394.25 ± 0.30	K	NIST
Tc	[620.00; 620.20]	K
Tc	620.20	K	KDB
Tc	620.00	K	NIST
Tfus	[250.60; 251.00]	K
Tfus	250.80	K	KDB
Tfus	251.00	K	Aq. Solubility Prediction
Tfus	250.97 ± 0.05	K	NIST
Tfus	250.60 ± 0.60	K	NIST
Ttriple	[250.81; 250.81]	K
Ttriple	250.81 ± 0.02	K	NIST
Ttriple	250.81 ± 0.02	K	NIST

Cheméo can also estimate Critical Volume, Acentric Factor for this compound, but they fall outside the models' validated range, so they are not shown here. Open the prediction tool to compute them on demand.

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[100.88; 114.11]	J/mol×K	[399.00; 620.69]
Cp,gas	100.88	J/mol×K	399.00	Joback Calculated Property
Cp,gas	103.84	J/mol×K	435.95	Joback Calculated Property
Cp,gas	106.45	J/mol×K	472.90	Joback Calculated Property
Cp,gas	108.76	J/mol×K	509.84	Joback Calculated Property
Cp,gas	110.78	J/mol×K	546.79	Joback Calculated Property
Cp,gas	112.55	J/mol×K	583.74	Joback Calculated Property
Cp,gas	114.11	J/mol×K	620.69	Joback Calculated Property
Cp,liquid	[139.70; 158.50]	J/mol×K	[260.00; 300.00]
Cp,liquid	148.50	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	148.70	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	149.20	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	151.00	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	154.60	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	139.70	J/mol×K	298.00	NIST
Cp,liquid	146.90	J/mol×K	298.00	NIST
Cp,liquid	157.80	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	147.16	J/mol×K	298.15	NIST
Cp,liquid	157.90	J/mol×K	298.15	NIST
Cp,liquid	146.50	J/mol×K	298.15	NIST
Cp,liquid	158.50	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
ΔfusH	[0.82; 10.88]	kJ/mol	[210.00; 250.81]
ΔfusH	0.82	kJ/mol	210.00	NIST
ΔfusH	10.88	kJ/mol	250.80	NIST
ΔfusH	10.88	kJ/mol	250.80	NIST
ΔfusH	10.88	kJ/mol	250.81	NIST
ΔfusH	10.88	kJ/mol	250.81	NIST
ΔvapH	[34.68; 38.90]	kJ/mol	[340.00; 394.20]
ΔvapH	38.90	kJ/mol	340.00	NIST
ΔvapH	38.40	kJ/mol	350.00	NIST
ΔvapH	38.70	kJ/mol	351.50	NIST
ΔvapH	37.60	kJ/mol	353.00	NIST
ΔvapH	34.68	kJ/mol	394.10	NIST
ΔvapH	34.73	kJ/mol	394.20	KDB
Pvap	[1.02; 8.29]	kPa	[283.15; 323.15]
Pvap	1.02	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	1.02	kPa	283.15	Isothermal (vapour + liquid) equilibrium for binary mixtures of (tetrahydrofuran + 1,1,2,2-tetrachloroethane or tetrachloroethene) at nine temperatures
Pvap	1.02	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	1.40	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	1.40	kPa	288.15	Isothermal (vapour + liquid) equilibrium for binary mixtures of (tetrahydrofuran + 1,1,2,2-tetrachloroethane or tetrachloroethene) at nine temperatures
Pvap	1.40	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	1.86	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	1.86	kPa	293.15	Isothermal (vapour + liquid) equilibrium for binary mixtures of (tetrahydrofuran + 1,1,2,2-tetrachloroethane or tetrachloroethene) at nine temperatures
Pvap	1.86	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	2.46	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	2.46	kPa	298.15	Isothermal (vapour + liquid) equilibrium for binary mixtures of (tetrahydrofuran + 1,1,2,2-tetrachloroethane or tetrachloroethene) at nine temperatures
Pvap	2.46	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	3.21	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	3.21	kPa	303.15	Isothermal (vapour + liquid) equilibrium for binary mixtures of (tetrahydrofuran + 1,1,2,2-tetrachloroethane or tetrachloroethene) at nine temperatures
Pvap	3.21	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	4.12	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	4.12	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	4.12	kPa	308.15	Isothermal (vapour + liquid) equilibrium for binary mixtures of (tetrahydrofuran + 1,1,2,2-tetrachloroethane or tetrachloroethene) at nine temperatures
Pvap	5.25	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	5.25	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	5.25	kPa	313.15	Isothermal (vapour + liquid) equilibrium for binary mixtures of (tetrahydrofuran + 1,1,2,2-tetrachloroethane or tetrachloroethene) at nine temperatures
Pvap	6.62	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	6.62	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	6.62	kPa	318.15	Isothermal (vapour + liquid) equilibrium for binary mixtures of (tetrahydrofuran + 1,1,2,2-tetrachloroethane or tetrachloroethene) at nine temperatures
Pvap	8.29	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	8.29	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	8.29	kPa	323.15	Isothermal (vapour + liquid) equilibrium for binary mixtures of (tetrahydrofuran + 1,1,2,2-tetrachloroethane or tetrachloroethene) at nine temperatures
n0	[1.49780; 1.50580]		[293.15; 308.15]
n0	1.50500		293.15	Bubble points of some binary mixtures formed by o-cresol at 95.75 kPa
n0	1.50580		293.15	Excess Gibbs energies of selected binary mixtures formed by N,N-dimethyl formamide at 95.5 kPa
n0	1.50580		293.15	Vapor-Liquid Equilibria of Binary Mixtures Formed by Hexan-1-ol with Chloroethanes and Chloroethenes at 95.6 kPa
n0	1.50500		293.15	Activity coefficients and excess Gibbs free energy of some binary mixtures formed by p-cresol at 95.23 kPa
n0	1.50360		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	1.50320		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	1.50500		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	1.50360		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	1.50500		298.15	Bubble points of the binary mixtures formed by ethylbenzene with some chloroaliphatics and substituted benzenes at p = 94.7 kPa
n0	1.50050		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	1.50100		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	1.49780		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	1.49800		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	[1590.60; 1622.39]	kg/m3	[293.00; 313.15]
ρl	1620.00	kg/m3	293.00	KDB
ρl	1622.39	kg/m3	293.15	Thermophysical and sonochemical behaviour of binary mixtures of decan-1-ol with halohydrocarbons at (T = 293.15 and 313.15) K
ρl	1614.49	kg/m3	298.15	Excess molar volumes, viscosities, and speeds of sound of the ternary mixture {1-heptanol (1) + trichloroethylene (2) + methylcyclohexane (3)} at T = 298.15 K
ρl	1613.20	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	1614.80	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	1607.20	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	1597.90	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	1590.60	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	[3.90; 43.38]	J/mol×K	[210.00; 250.81]
ΔfusS	3.90	J/mol×K	210.00	NIST
ΔfusS	43.38	J/mol×K	250.80	NIST
ΔfusS	43.38	J/mol×K	250.81	NIST
ΔfusS	43.38	J/mol×K	250.81	NIST
csound,fluid	[1038.97; 1054.03]	m/s	[293.15; 298.15]
csound,fluid	1054.03	m/s	293.15	Densities, Excess Molar Volumes, Ultrasonic Speeds, and Isentropic Compressibilities of Hexan-1-ol with 1,2-Dichloroethane, 1,2-Dibromoethane, and 1,1,2,2-Tetrachloroethene at (293.15 and 298.15) K
csound,fluid	1038.97	m/s	298.15	Densities, Excess Molar Volumes, Ultrasonic Speeds, and Isentropic Compressibilities of Hexan-1-ol with 1,2-Dichloroethane, 1,2-Dibromoethane, and 1,1,2,2-Tetrachloroethene at (293.15 and 298.15) K
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	0.0007
Reference

Correlations

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 203.96]	kPa	[286.48; 421.37]	The Yaws Handbook of Vapor Pressure
Equation			ln(Pvp) = A + B/(T + C)
Coefficient A			1.42797e+01
Coefficient B			-3.36251e+03
Coefficient C			-4.61640e+01
Temperature range, min.			286.48
Temperature range, max.			421.37
Pvap	1.33	kPa	286.48	Calculated Property
Pvap	3.03	kPa	301.47	Calculated Property
Pvap	6.29	kPa	316.46	Calculated Property
Pvap	12.10	kPa	331.44	Calculated Property
Pvap	21.79	kPa	346.43	Calculated Property
Pvap	37.10	kPa	361.42	Calculated Property
Pvap	60.21	kPa	376.41	Calculated Property
Pvap	93.67	kPa	391.39	Calculated Property
Pvap	140.48	kPa	406.38	Calculated Property
Pvap	203.96	kPa	421.37	Calculated Property
Pvap	[0.11; 4603.17]	kPa	[250.80; 620.00]	KDB Vapor Pressure Data
Equation			ln(Pvp) = A + B/T + C*ln(T) + D*T^2
Coefficient A			6.04740e+01
Coefficient B			-6.53097e+03
Coefficient C			-6.66587e+00
Coefficient D			3.52238e-06
Temperature range, min.			250.80
Temperature range, max.			620.00
Pvap	0.11	kPa	250.80	Calculated Property
Pvap	1.75	kPa	291.82	Calculated Property
Pvap	12.55	kPa	332.84	Calculated Property
Pvap	55.13	kPa	373.87	Calculated Property
Pvap	173.62	kPa	414.89	Calculated Property
Pvap	432.94	kPa	455.91	Calculated Property
Pvap	912.80	kPa	496.93	Calculated Property
Pvap	1701.91	kPa	537.96	Calculated Property
Pvap	2896.38	kPa	578.98	Calculated Property
Pvap	4603.17	kPa	620.00	Calculated Property

Similar Compounds

Find more compounds similar to Tetrachloroethylene.

Mixtures

• Tetrachloroethylene + Tetrahydrofuran
• Tetrachloroethylene + Dimethyl Sulfoxide
• Phenol, 2-methyl- + Tetrachloroethylene
• Tetrachloroethylene + Benzene, ethyl-
• Tetrachloroethylene + Formamide, N,N-dimethyl-
• Tetrachloroethylene + Carbon Tetrachloride
• Benzene + Tetrachloroethylene
• Tetrachloroethylene + Acetamide, N-methyl-
• PHENOL, 4-METHYL- + Tetrachloroethylene
• Tetrachloroethylene + Cyclohexane, methyl-
• Tetrachloroethylene + 1-Decanol
• Tetrachloroethylene + Ethane, 1,2-dibromo-
• Tetrachloroethylene + 1-Hexanol
• Tetrachloroethylene + Water
• Tetrachloroethylene + Anisole
• Tetrachloroethylene + Benzyl nitrile
• Tetrachloroethylene + Heptane
• Benzene, nitro- + Tetrachloroethylene
• Tetrachloroethylene + Benzene, chloro-
• Tetrachloroethylene + Methyl Alcohol

Find more mixtures with Tetrachloroethylene.

Sources

• KDB Vapor Pressure Data
• Crippen Method
• Densities, Excess Molar Volumes, Ultrasonic Speeds, and Isentropic Compressibilities of Hexan-1-ol with 1,2-Dichloroethane, 1,2-Dibromoethane, and 1,1,2,2-Tetrachloroethene at (293.15 and 298.15) K
• 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
• Excess Gibbs energies of selected binary mixtures formed by N,N-dimethyl formamide at 95.5 kPa
• 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
• 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
• Excess molar volumes, viscosities, and speeds of sound of the ternary mixture {1-heptanol (1) + trichloroethylene (2) + methylcyclohexane (3)} at T = 298.15 K
• Activity coefficients and excess Gibbs free energy of some binary mixtures formed by p-cresol at 95.23 kPa
• Thermophysical and sonochemical behaviour of binary mixtures of decan-1-ol with halohydrocarbons at (T = 293.15 and 313.15) K
• Relation between characteristic molecular volume and hydrophobicity of nonpolar molecules
• 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
• 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 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 Henry's Law Constants Using Internal Standards with Benchmark Values
• 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
• Studies on Transport and Thermodynamic Properties of Binary Mixtures of Hexan-1-ol with Halogenated Compounds at 293.15 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
• 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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