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

• 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).
• EA : Electron affinity (eV).
• 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).
• 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	0.2420		PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
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
εr	2.28		NCMS SOLV-DB
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°	[39.62; 39.72]	kJ/mol
ΔvapH°	39.62	kJ/mol	NCMS SOLV-DB
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	3.400		NCMS SOLV-DB
McVol	83.700	ml/mol	McGowan Calculated Property
NFPA Fire	0		NCMS SOLV-DB
NFPA Health	2		NCMS SOLV-DB
NFPA Safety	0		NCMS SOLV-DB
Pc	[4458.30; 4760.00]	kPa
Pc	4458.30	kPa	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
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
Ip	[1012.00; 1059.96]
Ip	1044.00		NIST
Ip	1038.00		NIST
Ip	1050.23		NIST
Ip	Outlier 1059.96		NIST
Ip	1036.20		NIST
Ip	1030.00		NIST
Ip	1024.00		NIST
Ip	1022.00		NIST
Ip	1022.00		NIST
Ip	1021.00		NIST
Ip	1026.00		NIST
Ip	1045.00		NIST
Ip	1012.00		NIST
Ip	1012.00		NIST
Ip	1018.00		NIST
Ip	1024.00		NIST
Ip	1044.00		NIST
Ip	1030.00		NIST
Ip	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	394.22	K	NCMS SOLV-DB
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	[611.00; 620.20]	K
Tc	611.00	K	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 10 Compiled value
Tc	620.00	K	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Tc	620.20	K	KDB
Tc	620.00	K	NIST
Tfus	[250.60; 251.00]	K
Tfus	251.00	K	Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
Tfus	250.80	K	KDB
Tfus	251.00	K	Aq. Solubility Prediction
Tfus	250.80	K	NCMS SOLV-DB
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
Vc	0.290	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	[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
η	0.0007980	Pa×s	298.15	NCMS SOLV-DB
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	Total vapour pressure and excess Gibbs energy for binary mixtures of 1,1,2,2-tetrachlorethane or tetrachloroethene with benzene at nine temperatures
Pvap	1.02	kPa	283.15	Isothermal (vapour + liquid) equilibrium for binary mixtures of (tetrahydrofuran + 1,1,2,2-tetrachloroethane or tetrachloroethene) at nine temperatures
Pvap	1.40	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	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	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-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	2.47	kPa	298.15	NCMS SOLV-DB
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	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	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	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	Isothermal (vapour + liquid) equilibrium for binary mixtures of (tetrahydrofuran + 1,1,2,2-tetrachloroethane or tetrachloroethene) 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	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	1.50300		298.15	NCMS SOLV-DB
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; 0.03]	N/m	[293.20; 298.15]
γ	0.03	N/m	293.20	KDB
γ	0.03	N/m	298.15	NCMS SOLV-DB

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
Cp,gas	[95.51; 127.03]	J/mol×K	[298.00; 1100.00]	NIST
Equation			Y = A + B·t + C·t² + D·t³ + E/t², t = T/1000 Y is Cp,gas in J/mol×K, T in K
Coefficient A			7.27623e+01
Coefficient B			1.30955e+02
Coefficient C			-1.11930e+02
Coefficient D			3.46977e+01
Coefficient E			-6.44470e-01
Reference			Chase, 1998
Comment			F=-41.18395, G=393.4684, H=-12.42602; Data last reviewed in September, 1967
Temperature range, min.			298.00
Temperature range, max.			1100.00
Cp,gas	95.51	J/mol×K	298.00	Calculated Property
Cp,gas	104.40	J/mol×K	387.11	Calculated Property
Cp,gas	110.65	J/mol×K	476.22	Calculated Property
Cp,gas	115.28	J/mol×K	565.33	Calculated Property
Cp,gas	118.75	J/mol×K	654.44	Calculated Property
Cp,gas	121.35	J/mol×K	743.56	Calculated Property
Cp,gas	123.30	J/mol×K	832.67	Calculated Property
Cp,gas	124.79	J/mol×K	921.78	Calculated Property
Cp,gas	125.97	J/mol×K	1010.89	Calculated Property
Cp,gas	127.03	J/mol×K	1100.00	Calculated Property
Cp,gas	[126.98; 132.90]	J/mol×K	[1100.00; 6000.00]	NIST
Equation			Y = A + B·t + C·t² + D·t³ + E/t², t = T/1000 Y is Cp,gas in J/mol×K, T in K
Coefficient A			1.31629e+02
Coefficient B			8.25549e-01
Coefficient C			-1.79961e-01
Coefficient D			1.37800e-02
Coefficient E			-6.48579e+00
Reference			Chase, 1998
Comment			F=-69.40294, G=476.3651, H=-12.42602; Data last reviewed in September, 1967
Temperature range, min.			1100.00
Temperature range, max.			6000.00
Cp,gas	126.98	J/mol×K	1100.00	Calculated Property
Cp,gas	130.16	J/mol×K	1644.44	Calculated Property
Cp,gas	131.36	J/mol×K	2188.89	Calculated Property
Cp,gas	131.95	J/mol×K	2733.33	Calculated Property
Cp,gas	132.28	J/mol×K	3277.78	Calculated Property
Cp,gas	132.48	J/mol×K	3822.22	Calculated Property
Cp,gas	132.61	J/mol×K	4366.67	Calculated Property
Cp,gas	132.71	J/mol×K	4911.11	Calculated Property
Cp,gas	132.80	J/mol×K	5455.56	Calculated Property
Cp,gas	132.90	J/mol×K	6000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 203.96]	kPa	[286.48; 421.37]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
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(Y) = A + B/T + C·ln(T) + D·T² + E/T² Y is Pvap in kPa, T in K
Coefficient A			6.04740e+01
Coefficient B			-6.53097e+03
Coefficient C			-6.66587e+00
Coefficient D			3.52238e-06
Coefficient E			0.00000e+00
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
Pvap	[2.88; 68.61]	kPa	[301.03; 380.84]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.42313e+01
Coefficient B			-3.31761e+03
Coefficient C			-4.91710e+01
Reference			Polak, Murakami, et al., 1970
Comment			Coefficents calculated by NIST from author's data.
Temperature range, min.			301.03
Temperature range, max.			380.84
Pvap	2.88	kPa	301.03	Calculated Property
Pvap	4.51	kPa	309.90	Calculated Property
Pvap	6.86	kPa	318.77	Calculated Property
Pvap	10.15	kPa	327.63	Calculated Property
Pvap	14.66	kPa	336.50	Calculated Property
Pvap	20.71	kPa	345.37	Calculated Property
Pvap	28.68	kPa	354.24	Calculated Property
Pvap	38.99	kPa	363.10	Calculated Property
Pvap	52.13	kPa	371.97	Calculated Property
Pvap	68.61	kPa	380.84	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
• 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.
• 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.
• 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
• 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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