Chemical Properties of Ethane, 1,1,2-trichloro- (CAS 79-00-5)

InChI

InChI=1S/C2H3Cl3/c3-1-2(4)5/h2H,1H2

InChI Key

UBOXGVDOUJQMTN-UHFFFAOYSA-N

Formula

C2H3Cl3

SMILES

ClCC(Cl)Cl

Molecular Weight¹

133.40

CAS

79-00-5

Other Names

• 1,1,2-Trichlorethane
• 1,1,2-trichloroethane
• 1,2,2-trichloroethane
• CHCl2CH2Cl
• Ethane trichloride
• NCI-C04579
• NSC 405074
• R-140
• Rcra waste number U227
• Rcra waste number U359
• Trichloroethane
• Trojchloroetan(1,1,2)
• Vinyl trichloride
• freon 140
• vinyltrichloride
• «beta»-T
• «beta»-Trichloroethane

• 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).
• C_p,solid : Solid phase heat capacity (J/mol×K).
• μ : Dipole Moment (debye).
• η : Dynamic viscosity (Pa×s).
• Δ_fG° : Standard Gibbs free energy of formation (kJ/mol).
• Δ_fH°_gas : Enthalpy of formation at standard conditions (kJ/mol).
• Δ_fH°_liquid : Liquid phase enthalpy of formation at standard conditions (kJ/mol).
• Δ_fusH° : Enthalpy of fusion at standard conditions (kJ/mol).
• Δ_fusH : Enthalpy of fusion at a given temperature (kJ/mol).
• Δ_vapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
• Δ_vapH : Enthalpy of vaporization at a given temperature (kJ/mol).
• IE : Ionization energy (eV).
• log₁₀WS : Log10 of Water solubility in mol/l.
• logP_oct/wat : Octanol/Water partition coefficient.
• McVol : McGowan's characteristic volume (ml/mol).
• P_c : Critical Pressure (kPa).
• P_triple : Triple Point Pressure (kPa).
• P_vap : Vapor pressure (kPa).
• 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).
• γ : Surface Tension (N/m).
• T_boil : Normal Boiling Point Temperature (K).
• T_c : Critical Temperature (K).
• λ_gas : Gas thermal conductivity (W/m×K).
• λ_liquid : Liquid thermal conductivity (W/m×K).
• T_fus : Normal melting (fusion) point (K).
• T_triple : Triple Point Temperature (K).
• U_Qi : UNIQUAC Qi Parameter.
• U_Ri : UNIQUAC Ri Parameter.
• V_c : Critical Volume (m³/kmol).
• Z_c : Critical Compressibility.
• Z_ra : Rackett Parameter.
• ¹: Molecular weight from the IUPAC atomic weights tables.

Physical Properties

Property	Value	Unit	Source
ω	[0.2454; 0.2591]
ω	0.2454		PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
ω	0.2591		ChemSep v8.3 pure component data Compiled value
ΔcH°liquid	-1098.10 ± 4.40	kJ/mol	NIST
μ	[1.25; 1.25]	debye
μ	1.25	debye	ChemSep v8.3 pure component data Compiled value
μ	1.25	debye	KDB
ΔfG°	[-80.97; -77.54]	kJ/mol
ΔfG°	-80.97	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfG°	-77.54	kJ/mol	KDB
ΔfH°gas	[-148.20; -138.60]	kJ/mol
ΔfH°gas	-142.00	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfH°gas	-138.60	kJ/mol	KDB
ΔfH°gas	-148.00 ± 4.00	kJ/mol	NIST
ΔfH°gas	-148.20 ± 4.40	kJ/mol	NIST
ΔfH°liquid	[-188.50; -188.00]	kJ/mol
ΔfH°liquid	-188.00 ± 4.00	kJ/mol	NIST
ΔfH°liquid	-188.50 ± 4.40	kJ/mol	NIST
ΔfusH°	10.00	kJ/mol	Joback Calculated Property
ΔvapH°	[40.10; 40.30]	kJ/mol
ΔvapH°	40.28	kJ/mol	NIST
ΔvapH°	40.10 ± 0.60	kJ/mol	NIST
ΔvapH°	40.30 ± 0.07	kJ/mol	NIST
ΔvapH°	40.20 ± 0.10	kJ/mol	NIST
ΔvapH°	40.28 ± 0.06	kJ/mol	NIST
ΔvapH°	40.30 ± 0.10	kJ/mol	NIST
IE	[11.00; 11.48]	eV
IE	11.00	eV	NIST
IE	11.48	eV	NIST
log10WS	[-1.48; -1.48]
log10WS	-1.48		Aq. Solubility Prediction
log10WS	-1.48		Estimated Solubility
logPoct/wat	2.029		Crippen Calculated Property
McVol	75.760	ml/mol	McGowan Calculated Property
Pc	[4154.32; 5140.00]	kPa
Pc	4154.32	kPa	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Pc	4480.00	kPa	ChemSep v8.3 pure component data Compiled value
Pc	5140.00	kPa	KDB
Ptriple	0.04	kPa	ChemSep v8.3 pure component data Compiled value
Inp	[713.00; 772.00]
Inp	742.80		NIST
Inp	743.10		NIST
Inp	748.10		NIST
Inp	745.10		NIST
Inp	741.40		NIST
Inp	738.70		NIST
Inp	735.00		NIST
Inp	744.00		NIST
Inp	729.00		NIST
Inp	Outlier 713.00		NIST
Inp	769.00		NIST
Inp	739.00		NIST
Inp	Outlier 772.00		NIST
Inp	747.50		NIST
Inp	748.00		NIST
Inp	747.00		NIST
Inp	748.00		NIST
Inp	752.00		NIST
Inp	748.00		NIST
Inp	752.00		NIST
Inp	752.00		NIST
Inp	727.00		NIST
Inp	Outlier 772.00		NIST
Inp	748.00		NIST
Inp	739.00		NIST
Ip	[1226.00; 1282.00]
Ip	1226.00		NIST
Ip	1282.00		NIST
Ip	1267.00		NIST
Ip	1269.00		NIST
Ip	1236.00		NIST
Ip	1236.00		NIST
Ip	1267.00		NIST
Ip	1240.00		NIST
Ip	1226.00		NIST
Tboil	[377.15; 387.25]	K
Tboil	387.00	K	ChemSep v8.3 pure component data Compiled value
Tboil	386.60	K	KDB
Tboil	385.70	K	NIST
Tboil	387.00	K	NIST
Tboil	386.85 ± 0.20	K	NIST
Tboil	386.90	K	NIST
Tboil	386.95	K	NIST
Tboil	386.78 ± 0.20	K	NIST
Tboil	387.20 ± 0.30	K	NIST
Tboil	386.15 ± 1.00	K	NIST
Tboil	386.75 ± 0.40	K	NIST
Tboil	387.25 ± 0.50	K	NIST
Tboil	386.82 ± 0.07	K	NIST
Tboil	Outlier 377.15 ± 2.00	K	NIST
Tboil	386.65 ± 0.50	K	NIST
Tboil	387.15 ± 1.50	K	NIST
Tc	[602.00; 606.00]	K
Tc	602.00	K	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Tc	602.00	K	ChemSep v8.3 pure component data Compiled value
Tc	606.00	K	KDB
Tc	602.00	K	NIST
Tfus	[235.80; 237.90]	K
Tfus	236.55	K	Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
Tfus	236.50	K	ChemSep v8.3 pure component data Compiled value
Tfus	235.80	K	KDB
Tfus	236.95	K	Aq. Solubility Prediction
Tfus	Outlier 237.90 ± 0.20	K	NIST
Tfus	236.55	K	NIST
Tfus	236.60 ± 0.02	K	NIST
Tfus	236.50 ± 0.20	K	NIST
Tfus	236.58 ± 0.05	K	NIST
Ttriple	[236.50; 237.10]	K
Ttriple	236.50	K	ChemSep v8.3 pure component data Compiled value
Ttriple	237.10 ± 0.20	K	NIST
Ttriple	237.10 ± 0.20	K	NIST
UQi	2.95		ChemSep v8.3 pure component data Compiled value
URi	3.53		ChemSep v8.3 pure component data Compiled value
Vc	[0.281; 0.294]	m3/kmol
Vc	0.294	m3/kmol	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Vc	0.281	m3/kmol	ChemSep v8.3 pure component data Compiled value
Zc	0.2520000		ChemSep v8.3 pure component data Compiled value
Zra	0.27		ChemSep v8.3 pure component data Compiled value

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[142.00; 144.00]	J/mol×K	[240.00; 250.00]
Cp,liquid	142.00	J/mol×K	240.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid	144.00	J/mol×K	250.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,solid	143.10	J/mol×K	251.70	NIST
ΔfusH	[10.88; 11.38]	kJ/mol	[237.10; 237.90]
ΔfusH	11.38	kJ/mol	237.10	NIST
ΔfusH	11.38	kJ/mol	237.10	NIST
ΔfusH	11.38	kJ/mol	237.10	NIST
ΔfusH	11.38	kJ/mol	237.10	NIST
ΔfusH	10.88	kJ/mol	237.90	NIST
ΔfusH	10.90	kJ/mol	237.90	NIST
ΔvapH	[33.30; 38.60]	kJ/mol	[330.33; 386.90]
ΔvapH	38.29 ± 0.63	kJ/mol	330.33	NIST
ΔvapH	38.60	kJ/mol	350.00	NIST
ΔvapH	38.30	kJ/mol	354.50	NIST
ΔvapH	38.20	kJ/mol	365.00	NIST
ΔvapH	33.30	kJ/mol	386.60	KDB
ΔvapH	34.82	kJ/mol	386.90	NIST
ρl	[1409.60; 1441.00]	kg/m3	[293.00; 313.15]
ρl	1441.00	kg/m3	293.00	KDB
ρl	1425.00	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	1416.10	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	1409.60	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	[45.70; 48.00]	J/mol×K	[237.10; 237.90]
ΔfusS	48.00	J/mol×K	237.10	NIST
ΔfusS	48.00	J/mol×K	237.10	NIST
ΔfusS	45.70	J/mol×K	237.90	NIST
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	0.0009
Reference

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[75.52; 164.42]	J/mol×K	[236.50; 1500.00]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A + exp(B/T + C + D·T + E·T²) Y is Cp,gas in J/mol×K, T in K
Coefficient A			5.65060e+01
Coefficient B			-5.35360e+02
Coefficient C			5.25824e+00
Coefficient D			-2.19580e-04
Coefficient E			4.86050e-08
Temperature range, min.			236.50
Temperature range, max.			1500.00
Cp,gas	75.52	J/mol×K	236.50	Calculated Property
Cp,gas	99.54	J/mol×K	376.89	Calculated Property
Cp,gas	118.23	J/mol×K	517.28	Calculated Property
Cp,gas	131.76	J/mol×K	657.67	Calculated Property
Cp,gas	141.55	J/mol×K	798.06	Calculated Property
Cp,gas	148.76	J/mol×K	938.44	Calculated Property
Cp,gas	154.18	J/mol×K	1078.83	Calculated Property
Cp,gas	158.37	J/mol×K	1219.22	Calculated Property
Cp,gas	161.70	J/mol×K	1359.61	Calculated Property
Cp,gas	164.42	J/mol×K	1500.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[141.10; 151.13]	J/mol×K	[236.50; 300.00]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A + exp(B/T + C + D·T + E·T²) Y is Cp,liquid in J/mol×K, T in K
Coefficient A			1.21000e+02
Coefficient B			4.33160e+02
Coefficient C			-4.68426e+00
Coefficient D			3.44230e-02
Coefficient E			-4.09010e-05
Temperature range, min.			236.50
Temperature range, max.			300.00
Cp,liquid	141.10	J/mol×K	236.50	Calculated Property
Cp,liquid	142.16	J/mol×K	243.56	Calculated Property
Cp,liquid	143.25	J/mol×K	250.61	Calculated Property
Cp,liquid	144.36	J/mol×K	257.67	Calculated Property
Cp,liquid	145.49	J/mol×K	264.72	Calculated Property
Cp,liquid	146.63	J/mol×K	271.78	Calculated Property
Cp,liquid	147.78	J/mol×K	278.83	Calculated Property
Cp,liquid	148.91	J/mol×K	285.89	Calculated Property
Cp,liquid	150.03	J/mol×K	292.94	Calculated Property
Cp,liquid	151.13	J/mol×K	300.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.0029614; 0.0002007]	Pa×s	[236.50; 452.00]	ChemSep v8.3 pure component data Compiled value
Equation			Y = exp(A + B/T + C·ln(T) + D·T^E) Y is η in Pa×s, T in K
Coefficient A			-2.62180e+01
Coefficient B			1.57130e+03
Coefficient C			2.59920e+00
Coefficient D			-8.13780e-06
Coefficient E			2.00000e+00
Temperature range, min.			236.50
Temperature range, max.			452.00
η	0.0029614	Pa×s	236.50	Calculated Property
η	0.0018751	Pa×s	260.44	Calculated Property
η	0.0012753	Pa×s	284.39	Calculated Property
η	0.0009127	Pa×s	308.33	Calculated Property
η	0.0006778	Pa×s	332.28	Calculated Property
η	0.0005168	Pa×s	356.22	Calculated Property
η	0.0004016	Pa×s	380.17	Calculated Property
η	0.0003162	Pa×s	404.11	Calculated Property
η	0.0002512	Pa×s	428.06	Calculated Property
η	0.0002007	Pa×s	452.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ΔvapH	[41.56; 0.00]	kJ/mol	[236.50; 602.00]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A·(1 − Tr)^(B + C·Tr + D·Tr² + E·Tr³), Tr = T/Tc Y is ΔvapH in kJ/mol, T in K
Coefficient A			5.05030e+01
Coefficient B			6.40210e-01
Coefficient C			-1.13820e+00
Coefficient D			1.53790e+00
Coefficient E			-6.60310e-01
Critical temperature, Tc (K)			6.02000e+02
Temperature range, min.			236.50
Temperature range, max.			602.00
ΔvapH	41.56	kJ/mol	236.50	Calculated Property
ΔvapH	40.01	kJ/mol	277.11	Calculated Property
ΔvapH	38.24	kJ/mol	317.72	Calculated Property
ΔvapH	36.19	kJ/mol	358.33	Calculated Property
ΔvapH	33.81	kJ/mol	398.94	Calculated Property
ΔvapH	31.02	kJ/mol	439.56	Calculated Property
ΔvapH	27.71	kJ/mol	480.17	Calculated Property
ΔvapH	23.64	kJ/mol	520.78	Calculated Property
ΔvapH	18.09	kJ/mol	561.39	Calculated Property
ΔvapH	0.00	kJ/mol	602.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 203.99]	kPa	[282.31; 412.98]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.44525e+01
Coefficient B			-3.36081e+03
Coefficient C			-4.50510e+01
Temperature range, min.			282.31
Temperature range, max.			412.98
Pvap	1.33	kPa	282.31	Calculated Property
Pvap	3.02	kPa	296.83	Calculated Property
Pvap	6.25	kPa	311.35	Calculated Property
Pvap	11.99	kPa	325.87	Calculated Property
Pvap	21.60	kPa	340.39	Calculated Property
Pvap	36.82	kPa	354.90	Calculated Property
Pvap	59.83	kPa	369.42	Calculated Property
Pvap	93.26	kPa	383.94	Calculated Property
Pvap	140.16	kPa	398.46	Calculated Property
Pvap	203.99	kPa	412.98	Calculated Property
Pvap	[0.05; 4390.35]	kPa	[236.50; 602.00]	ChemSep v8.3 pure component data Compiled value
Equation			Y = exp(A + B/T + C·ln(T) + D·T^E) Y is Pvap in kPa, T in K
Coefficient A			5.91432e+01
Coefficient B			-6.42816e+03
Coefficient C			-6.44717e+00
Coefficient D			3.27127e-06
Coefficient E			2.00000e+00
Temperature range, min.			236.50
Temperature range, max.			602.00
Pvap	0.05	kPa	236.50	Calculated Property
Pvap	0.94	kPa	277.11	Calculated Property
Pvap	8.15	kPa	317.72	Calculated Property
Pvap	40.67	kPa	358.33	Calculated Property
Pvap	139.76	kPa	398.94	Calculated Property
Pvap	370.57	kPa	439.56	Calculated Property
Pvap	815.97	kPa	480.17	Calculated Property
Pvap	1568.50	kPa	520.78	Calculated Property
Pvap	2725.61	kPa	561.39	Calculated Property
Pvap	4390.35	kPa	602.00	Calculated Property
Pvap	[0.05; 4668.14]	kPa	[236.50; 602.00]	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			6.69520e+01
Coefficient B			-6.70908e+03
Coefficient C			-7.67345e+00
Coefficient D			4.83782e-06
Coefficient E			0.00000e+00
Temperature range, min.			236.50
Temperature range, max.			602.00
Pvap	0.05	kPa	236.50	Calculated Property
Pvap	0.96	kPa	277.11	Calculated Property
Pvap	8.30	kPa	317.72	Calculated Property
Pvap	41.22	kPa	358.33	Calculated Property
Pvap	141.17	kPa	398.94	Calculated Property
Pvap	374.11	kPa	439.56	Calculated Property
Pvap	827.23	kPa	480.17	Calculated Property
Pvap	1605.71	kPa	520.78	Calculated Property
Pvap	2834.66	kPa	561.39	Calculated Property
Pvap	4668.14	kPa	602.00	Calculated Property
Pvap	[10.12; 101.31]	kPa	[323.12; 386.82]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.39761e+01
Coefficient B			-3.01707e+03
Coefficient C			-6.44100e+01
Reference			Dreisbach and Shrader, 1949
Comment			Coefficents calculated by NIST from author's data.
Temperature range, min.			323.12
Temperature range, max.			386.82
Pvap	10.12	kPa	323.12	Calculated Property
Pvap	13.80	kPa	330.20	Calculated Property
Pvap	18.52	kPa	337.28	Calculated Property
Pvap	24.50	kPa	344.35	Calculated Property
Pvap	31.96	kPa	351.43	Calculated Property
Pvap	41.16	kPa	358.51	Calculated Property
Pvap	52.38	kPa	365.59	Calculated Property
Pvap	65.92	kPa	372.66	Calculated Property
Pvap	82.12	kPa	379.74	Calculated Property
Pvap	101.31	kPa	386.82	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ρl	[1531.32; 474.37]	kg/m3	[236.50; 602.00]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A / B^(1 + (1 − T/C)^D) Y is ρl in kg/m3, T in K
Coefficient A			1.20798e+02
Coefficient B			2.54650e-01
Coefficient C			6.02000e+02
Coefficient D			3.09870e-01
Temperature range, min.			236.50
Temperature range, max.			602.00
ρl	1531.32	kg/m3	236.50	Calculated Property
ρl	1468.33	kg/m3	277.11	Calculated Property
ρl	1402.60	kg/m3	317.72	Calculated Property
ρl	1333.44	kg/m3	358.33	Calculated Property
ρl	1259.85	kg/m3	398.94	Calculated Property
ρl	1180.26	kg/m3	439.56	Calculated Property
ρl	1091.98	kg/m3	480.17	Calculated Property
ρl	989.61	kg/m3	520.78	Calculated Property
ρl	858.49	kg/m3	561.39	Calculated Property
ρl	474.37	kg/m3	602.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
γ	[0.04; 0.02]	N/m	[236.15; 387.15]	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			7.43026e-02
Coefficient B			-1.35100e-04
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Temperature range, min.			236.15
Temperature range, max.			387.15
γ	0.04	N/m	236.15	Calculated Property
γ	0.04	N/m	252.93	Calculated Property
γ	0.04	N/m	269.71	Calculated Property
γ	0.04	N/m	286.48	Calculated Property
γ	0.03	N/m	303.26	Calculated Property
γ	0.03	N/m	320.04	Calculated Property
γ	0.03	N/m	336.82	Calculated Property
γ	0.03	N/m	353.59	Calculated Property
γ	0.02	N/m	370.37	Calculated Property
γ	0.02	N/m	387.15	Calculated Property
γ	[0.04; 1.01e-06]	N/m	[236.50; 599.81]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A + exp(B/T + C + D·T + E·T²) Y is γ in N/m, T in K
Coefficient A			-1.08700e-02
Coefficient B			1.26610e+02
Coefficient C			-3.79290e+00
Coefficient D			3.26850e-03
Coefficient E			-8.06160e-06
Comment			Range stopped where the equation turns negative; ChemSep gives it to 602 K.
Temperature range, min.			236.50
Temperature range, max.			599.81
γ	0.04	N/m	236.50	Calculated Property
γ	0.04	N/m	276.87	Calculated Property
γ	0.03	N/m	317.23	Calculated Property
γ	0.03	N/m	357.60	Calculated Property
γ	0.02	N/m	397.97	Calculated Property
γ	0.02	N/m	438.34	Calculated Property
γ	0.01	N/m	478.70	Calculated Property
γ	0.01	N/m	519.07	Calculated Property
γ	0.00	N/m	559.44	Calculated Property
γ	1.01e-06	N/m	599.81	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λgas	[0.00; 0.06]	W/m×K	[236.50; 1000.00]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A·T^B / (1 + C/T + D/T²) Y is λgas in W/m×K, T in K
Coefficient A			9.54550e-05
Coefficient B			1.04270e+00
Coefficient C			1.25830e+03
Coefficient D			-2.96020e+03
Temperature range, min.			236.50
Temperature range, max.			1000.00
λgas	0.00	W/m×K	236.50	Calculated Property
λgas	0.01	W/m×K	321.33	Calculated Property
λgas	0.01	W/m×K	406.17	Calculated Property
λgas	0.02	W/m×K	491.00	Calculated Property
λgas	0.02	W/m×K	575.83	Calculated Property
λgas	0.03	W/m×K	660.67	Calculated Property
λgas	0.04	W/m×K	745.50	Calculated Property
λgas	0.04	W/m×K	830.33	Calculated Property
λgas	0.05	W/m×K	915.17	Calculated Property
λgas	0.06	W/m×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λliquid	[0.15; 0.09]	W/m×K	[236.50; 482.00]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A + exp(B/T + C + D·T + E·T²) Y is λliquid in W/m×K, T in K
Coefficient A			-2.72580e-02
Coefficient B			-7.87240e+01
Coefficient C			-7.39410e-01
Coefficient D			-3.04010e-03
Coefficient E			8.85650e-07
Temperature range, min.			236.50
Temperature range, max.			482.00
λliquid	0.15	W/m×K	236.50	Calculated Property
λliquid	0.14	W/m×K	263.78	Calculated Property
λliquid	0.13	W/m×K	291.06	Calculated Property
λliquid	0.13	W/m×K	318.33	Calculated Property
λliquid	0.12	W/m×K	345.61	Calculated Property
λliquid	0.11	W/m×K	372.89	Calculated Property
λliquid	0.11	W/m×K	400.17	Calculated Property
λliquid	0.10	W/m×K	427.44	Calculated Property
λliquid	0.09	W/m×K	454.72	Calculated Property
λliquid	0.09	W/m×K	482.00	Calculated Property

Similar Compounds

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

Mixtures

• Ethane, 1,1,2-trichloro- + Acetamide, N-methyl-
• Ethane, 1,1,2-trichloro- + Water
• Ethane, 1,1,2-trichloro- + Benzyl nitrile

Sources

• KDB Vapor Pressure Data
• Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) ChEDL chemicals 1.5.2, from Bradley, J.-C.; Williams, A.; Lang, A. Jean-Claude Bradley Open Melting Point Dataset. Figshare, 2014 (CC0).
• Jasper (1972), surface tension of pure liquid compounds ChEDL chemicals 1.5.2, from Jasper, J. J. The Surface Tension of Pure Liquid Compounds. J. Phys. Chem. Ref. Data 1972, 1, 841-1010 (as transcribed in Lange's Handbook).
• PSRK revision IV (2005), critical constants and acentric factors of 1000 components ChEDL chemicals 1.5.2, from Horstmann, S.; Jabłoniec, A.; Krafczyk, J.; Fischer, K.; Gmehling, J. PSRK Group Contribution Equation of State: Comprehensive Revision and Extension IV, Including Critical Constants and α-Function Parameters for 1000 Components. Fluid Phase Equilib. 2005, 227, 157-164.
• ChemSep v8.3 pure component data Converted from ChemSep v8.3 pure component data, H. Kooijman and R. Taylor (2021, 2022), Artistic License 2.0; see how the values differ.
• Crippen Method
• Densities and viscosities of binary liquid mixtures of N-methylacetamide with some chloroethanes and chloroethenes at T = 308.15 K
• Determination of Henry's Law Constants Using Internal Standards with Benchmark Values
• 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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