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

Physical Properties

Property	Value	Unit	Source
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	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
I	[863.21; 870.00]
I	867.61		NIST
I	866.47		NIST
I	863.21		NIST
I	870.00		NIST
I	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	516.50	K	KDB
Tfus	[223.00; 223.30]	K
Tfus	223.30	K	KDB
Tfus	223.00 ± 0.10	K	NIST

Cheméo can also estimate Critical Volume, Log10 of Water solubility in mol/l 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	[67.02; 84.99]	J/mol×K	[324.18; 517.06]
Cp,gas	67.02	J/mol×K	324.18	Joback Calculated Property
Cp,gas	70.61	J/mol×K	356.33	Joback Calculated Property
Cp,gas	73.95	J/mol×K	388.47	Joback Calculated Property
Cp,gas	77.04	J/mol×K	420.62	Joback Calculated Property
Cp,gas	79.90	J/mol×K	452.76	Joback Calculated Property
Cp,gas	82.55	J/mol×K	484.91	Joback Calculated Property
Cp,gas	84.99	J/mol×K	517.06	Joback Calculated Property
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
η	[0.0002698; 0.0028927]	Pa×s	[167.06; 324.18]
η	0.0028927	Pa×s	167.06	Joback Calculated Property
η	0.0014903	Pa×s	193.25	Joback Calculated Property
η	0.0008995	Pa×s	219.43	Joback Calculated Property
η	0.0006046	Pa×s	245.62	Joback Calculated Property
η	0.0004387	Pa×s	271.81	Joback Calculated Property
η	0.0003368	Pa×s	297.99	Joback Calculated Property
η	0.0002698	Pa×s	324.18	Joback Calculated Property
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
Pvap	[0.52; 6698.23]	kPa	[223.35; 516.50]	The Yaws Handbook of Vapor Pressure
Equation			ln(Pvp) = A + B/(T + C)
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(Pvp) = A + B/T + C*ln(T) + D*T^2
Coefficient A			8.76830e+01
Coefficient B			-6.29447e+03
Coefficient C			-1.11957e+01
Coefficient D			1.15854e-05
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

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
• 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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