Chemical Properties of Ethylene, 1,2-dichloro-, (E)- (CAS 156-60-5)

InChI

InChI=1S/C2H2Cl2/c3-1-2-4/h1-2H/b2-1+

InChI Key

KFUSEUYYWQURPO-OWOJBTEDSA-N

Formula

C2H2Cl2

SMILES

ClC=CCl

Molecular Weight¹

96.94

CAS

156-60-5

Other Names

• (E)-1,2-Dichloroethylene
• (E)-1,2-dichloroethene
• (E)-CHCl=CHCl
• 1,2-trans-Dichloroethene
• 1,2-trans-Dichloroethylene
• 1,trans-2-Dichloroethene
• Dichloroethylene, trans-
• Ethene, 1,2-dichloro-, (1E)-
• Ethylene, 1,2-dichloro-, trans-
• HCC 1130t
• NSC 60512
• R 1130t
• Rcra waste number U079
• ethene, 1,2-dichloro-, (E)-
• ethene, 1,2-dichloro-, trans-
• trans-1,2-dichloroethene
• trans-1,2-dichloroethylene
• trans-Acetylene dichloride
• trans-Di-1,2-Chloroethylene
• trans-Dichloroethylene

• 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).
• 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_vapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
• Δ_vapH : Enthalpy of vaporization at a given temperature (kJ/mol).
• IE : Ionization energy (eV).
• 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).
• ρ_l : Liquid Density (kg/m³).
• I_np : Non-polar retention indices.
• I_p : Polar retention indices.
• γ : Surface Tension (N/m).
• 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	[0.2131; 0.2320]
ω	0.2131		PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
ω	0.2320		KDB
ΔcH°liquid	-1095.80 ± 8.40	kJ/mol	NIST
μ	0.00	debye	KDB
ΔfG°	26.60	kJ/mol	KDB
ΔfH°gas	[-1.00; 4.19]	kJ/mol
ΔfH°gas	4.19	kJ/mol	KDB
ΔfH°gas	-1.00 ± 2.00	kJ/mol	NIST
ΔfH°gas	1.70	kJ/mol	NIST
ΔfH°liquid	[-30.00; -14.34]	kJ/mol
ΔfH°liquid	-30.00 ± 2.20	kJ/mol	NIST
ΔfH°liquid	-14.34	kJ/mol	NIST
ΔfusH°	9.53	kJ/mol	Joback Calculated Property
ΔvapH°	[29.47; 30.00]	kJ/mol
ΔvapH°	30.00 ± 1.00	kJ/mol	NIST
ΔvapH°	29.47	kJ/mol	NIST
ΔvapH°	30.00 ± 1.00	kJ/mol	NIST
IE	[9.60; 11.92]	eV
IE	9.64 ± 0.02	eV	NIST
IE	9.64	eV	NIST
IE	9.69	eV	NIST
IE	9.60	eV	NIST
IE	9.66 ± 0.03	eV	NIST
IE	9.64 ± 0.02	eV	NIST
IE	9.63	eV	NIST
IE	9.80	eV	NIST
IE	9.80	eV	NIST
IE	Outlier 11.92	eV	NIST
IE	9.72	eV	NIST
logPoct/wat	1.935		Crippen Calculated Property
McVol	59.220	ml/mol	McGowan Calculated Property
NFPA Fire	3		KDB
NFPA Health	2		KDB
NFPA Safety	2		KDB
Pc	[5510.00; 5520.00]	kPa
Pc	5520.00	kPa	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Pc	5510.00	kPa	KDB
Inp	[528.00; 596.00]
Inp	558.00		NIST
Inp	559.00		NIST
Inp	557.00		NIST
Inp	555.00		NIST
Inp	559.00		NIST
Inp	Outlier 528.00		NIST
Inp	551.00		NIST
Inp	551.00		NIST
Inp	Outlier 596.00		NIST
Inp	567.00		NIST
Inp	551.00		NIST
Inp	558.00		NIST
Ip	[863.21; 870.00]
Ip	867.61		NIST
Ip	866.47		NIST
Ip	863.21		NIST
Ip	870.00		NIST
Ip	870.00		NIST
Tboil	[320.45; 322.70]	K
Tboil	321.88	K	KDB
Tboil	320.70	K	NIST
Tboil	320.45 ± 0.25	K	NIST
Tboil	320.50 ± 0.40	K	NIST
Tboil	321.40 ± 0.60	K	NIST
Tboil	321.40 ± 0.70	K	NIST
Tboil	322.70 ± 2.00	K	NIST
Tc	[515.50; 517.00]	K
Tc	515.50	K	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 10 Compiled value
Tc	517.00	K	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Tc	516.50	K	KDB
Tfus	[223.00; 223.30]	K
Tfus	223.30	K	KDB
Tfus	223.00 ± 0.10	K	NIST
Vc	0.220	m3/kmol	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value

Cheméo can also estimate Log10 of Water solubility in mol/l for this compound, but it falls outside the models' validated range, so it is not shown here. Open the prediction tool to compute it on demand.

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[112.08; 115.07]	J/mol×K	[268.30; 309.14]
Cp,liquid	113.08	J/mol×K	268.30	Heat capacities of selected chlorohydrocarbons
Cp,liquid	112.74	J/mol×K	268.30	Heat capacities of selected chlorohydrocarbons
Cp,liquid	112.41	J/mol×K	268.30	Heat capacities of selected chlorohydrocarbons
Cp,liquid	112.08	J/mol×K	268.30	Heat capacities of selected chlorohydrocarbons
Cp,liquid	112.99	J/mol×K	278.51	Heat capacities of selected chlorohydrocarbons
Cp,liquid	112.83	J/mol×K	278.51	Heat capacities of selected chlorohydrocarbons
Cp,liquid	112.41	J/mol×K	278.51	Heat capacities of selected chlorohydrocarbons
Cp,liquid	112.08	J/mol×K	278.51	Heat capacities of selected chlorohydrocarbons
Cp,liquid	113.00	J/mol×K	288.00	NIST
Cp,liquid	112.91	J/mol×K	288.72	Heat capacities of selected chlorohydrocarbons
Cp,liquid	113.41	J/mol×K	288.72	Heat capacities of selected chlorohydrocarbons
Cp,liquid	112.58	J/mol×K	288.72	Heat capacities of selected chlorohydrocarbons
Cp,liquid	113.49	J/mol×K	288.72	Heat capacities of selected chlorohydrocarbons
Cp,liquid	114.24	J/mol×K	298.93	Heat capacities of selected chlorohydrocarbons
Cp,liquid	113.99	J/mol×K	298.93	Heat capacities of selected chlorohydrocarbons
Cp,liquid	113.82	J/mol×K	298.93	Heat capacities of selected chlorohydrocarbons
Cp,liquid	113.41	J/mol×K	298.93	Heat capacities of selected chlorohydrocarbons
Cp,liquid	115.07	J/mol×K	309.14	Heat capacities of selected chlorohydrocarbons
Cp,liquid	114.49	J/mol×K	309.14	Heat capacities of selected chlorohydrocarbons
Cp,liquid	114.16	J/mol×K	309.14	Heat capacities of selected chlorohydrocarbons
Cp,liquid	113.66	J/mol×K	309.14	Heat capacities of selected chlorohydrocarbons
ΔvapH	[29.00; 31.40]	kJ/mol	[293.00; 397.00]
ΔvapH	30.40	kJ/mol	293.00	NIST
ΔvapH	30.10	kJ/mol	296.00	NIST
ΔvapH	31.40	kJ/mol	296.50	NIST
ΔvapH	30.30	kJ/mol	321.50	KDB
ΔvapH	29.00	kJ/mol	397.00	NIST
Pvap	[53.33; 269.90]	kPa	[303.15; 353.15]
Pvap	53.33	kPa	303.15	Phase Equilibria on Four Binary Systems: 1,2-Dichloroethane + trans-1,2-Dichloroethylene, 1-Octene + 2-Methyl Thiophene, 2-Ethyl Thiophene + 2,2,4-Trimethylpentane, and Cyclopropanecarbonitrile + Water
Pvap	269.90	kPa	353.15	Phase Equilibria on Four Binary Systems: 1,2-Dichloroethane + trans-1,2-Dichloroethylene, 1-Octene + 2-Methyl Thiophene, 2-Ethyl Thiophene + 2,2,4-Trimethylpentane, and Cyclopropanecarbonitrile + Water
ρl	1255.00	kg/m3	293.00	KDB
γ	0.02	N/m	293.20	KDB

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[60.72; 108.47]	J/mol×K	[273.00; 1000.00]	Joback Predicted correlation
Equation			Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is Cp,gas in J/mol×K, T in K
Coefficient A			1.26700e+01
Coefficient B			2.27400e-01
Coefficient C			-2.09600e-04
Coefficient D			7.80000e-08
Coefficient E			0.00000e+00
Temperature range, min.			273.00
Temperature range, max.			1000.00
Cp,gas	60.72	J/mol×K	273.00	Calculated Property
Cp,gas	70.34	J/mol×K	353.78	Calculated Property
Cp,gas	78.31	J/mol×K	434.56	Calculated Property
Cp,gas	84.87	J/mol×K	515.33	Calculated Property
Cp,gas	90.27	J/mol×K	596.11	Calculated Property
Cp,gas	94.75	J/mol×K	676.89	Calculated Property
Cp,gas	98.57	J/mol×K	757.67	Calculated Property
Cp,gas	101.96	J/mol×K	838.44	Calculated Property
Cp,gas	105.18	J/mol×K	919.22	Calculated Property
Cp,gas	108.47	J/mol×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.0008453; 0.0002081]	Pa×s	[223.15; 361.43]	Joback Predicted correlation
Equation			Y = exp(A + B/T + C·ln(T) + D·T^E) Y is η in Pa×s, T in K
Coefficient A			-1.07399e+01
Coefficient B			8.17640e+02
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Comment			Liquid phase. Joback/Reid (1987), valid from Tf to 0.7·Tc.
Temperature range, min.			223.15
Temperature range, max.			361.43
η	0.0008453	Pa×s	223.15	Calculated Property
η	0.0006676	Pa×s	238.51	Calculated Property
η	0.0005425	Pa×s	253.88	Calculated Property
η	0.0004514	Pa×s	269.24	Calculated Property
η	0.0003832	Pa×s	284.61	Calculated Property
η	0.0003307	Pa×s	299.97	Calculated Property
η	0.0002896	Pa×s	315.34	Calculated Property
η	0.0002567	Pa×s	330.70	Calculated Property
η	0.0002301	Pa×s	346.07	Calculated Property
η	0.0002081	Pa×s	361.43	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[0.52; 6698.23]	kPa	[223.35; 516.50]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.50408e+01
Coefficient B			-3.02933e+03
Coefficient C			-3.03460e+01
Temperature range, min.			223.35
Temperature range, max.			516.50
Pvap	0.52	kPa	223.35	Calculated Property
Pvap	5.01	kPa	255.92	Calculated Property
Pvap	27.28	kPa	288.49	Calculated Property
Pvap	101.57	kPa	321.07	Calculated Property
Pvap	290.20	kPa	353.64	Calculated Property
Pvap	684.19	kPa	386.21	Calculated Property
Pvap	1396.96	kPa	418.78	Calculated Property
Pvap	2554.01	kPa	451.36	Calculated Property
Pvap	4281.80	kPa	483.93	Calculated Property
Pvap	6698.23	kPa	516.50	Calculated Property
Pvap	[0.62; 5421.34]	kPa	[223.35; 513.00]	KDB Vapor Pressure Data
Equation			ln(Y) = A + B/T + C·ln(T) + D·T² + E/T² Y is Pvap in kPa, T in K
Coefficient A			8.76830e+01
Coefficient B			-6.29447e+03
Coefficient C			-1.11957e+01
Coefficient D			1.15854e-05
Coefficient E			0.00000e+00
Temperature range, min.			223.35
Temperature range, max.			513.00
Pvap	0.62	kPa	223.35	Calculated Property
Pvap	5.73	kPa	255.53	Calculated Property
Pvap	29.23	kPa	287.72	Calculated Property
Pvap	101.06	kPa	319.90	Calculated Property
Pvap	268.16	kPa	352.08	Calculated Property
Pvap	592.41	kPa	384.27	Calculated Property
Pvap	1150.75	kPa	416.45	Calculated Property
Pvap	2041.81	kPa	448.63	Calculated Property
Pvap	3400.32	kPa	480.82	Calculated Property
Pvap	5421.34	kPa	513.00	Calculated Property
Pvap	[1.50; 303.73]	kPa	[234.96; 357.99]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.36823e+01
Coefficient B			-2.45075e+03
Coefficient C			-5.03440e+01
Reference			Ketelaar, van Velden, et al., 1947
Comment			Coefficents calculated by NIST from author's data.
Temperature range, min.			234.96
Temperature range, max.			357.99
Pvap	1.50	kPa	234.96	Calculated Property
Pvap	3.75	kPa	248.63	Calculated Property
Pvap	8.33	kPa	262.30	Calculated Property
Pvap	16.78	kPa	275.97	Calculated Property
Pvap	31.21	kPa	289.64	Calculated Property
Pvap	54.28	kPa	303.31	Calculated Property
Pvap	89.20	kPa	316.98	Calculated Property
Pvap	139.65	kPa	330.65	Calculated Property
Pvap	209.71	kPa	344.32	Calculated Property
Pvap	303.73	kPa	357.99	Calculated Property

Similar Compounds

Find more compounds similar to Ethylene, 1,2-dichloro-, (E)-.

Mixtures

• Ethylene, 1,2-dichloro-, (E)- + Water
• Ethylene, 1,2-dichloro-, (E)- + Ethane, 1,2-dichloro-

Sources

• KDB Vapor Pressure Data
• 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.
• Crippen Method
• Crippen Method
• Heat capacities of selected chlorohydrocarbons
• Measurement and Estimation of Henry's Law Constants of Chlorinated Ethylenes in Aqueous Surfactant Solutions
• Phase Equilibria on Four Binary Systems: 1,2-Dichloroethane + trans-1,2-Dichloroethylene, 1-Octene + 2-Methyl Thiophene, 2-Ethyl Thiophene + 2,2,4-Trimethylpentane, and Cyclopropanecarbonitrile + Water
• Determination of Henry's Law Constants Using Internal Standards with Benchmark Values
• Joback Method
• KDB
• McGowan Method
• NIST Webbook
• The Yaws Handbook of Vapor Pressure

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