Chemical Properties of Ethane, 1,2-dichloro- (CAS 107-06-2)

InChI

InChI=1S/C2H4Cl2/c3-1-2-4/h1-2H2

InChI Key

WSLDOOZREJYCGB-UHFFFAOYSA-N

Formula

C2H4Cl2

SMILES

ClCCCl

Molecular Weight¹

98.96

CAS

107-06-2

Other Names

• 1,2-Bichloroethane
• 1,2-DCE
• 1,2-Dichloorethaan
• 1,2-Dichlor-aethan
• 1,2-Dichlorethane
• 1,2-Dicloroetano
• 1,2-dichloroethane
• 1,2-dichloroethane (ethylene dichloride)
• 1,2-ethylene dichloride
• ALPHA,BETA-DICHLOROETHANE
• Aethylenchlorid
• Bichlorure D'ethylene
• Borer sol
• Brocide
• CH2ClCH2Cl
• Chlorure D'ethylene
• Cloruro di ethene
• DCE
• Destruxol borer-sol
• Di-chlor-mulsion
• Dichloremulsion
• Dichloro-1,2-ethane
• Dutch liquid
• Dutch oil
• EDC
• EDC (halocarbon)
• ENT 1,656
• Ethane dichloride
• Ethyleendichloride
• Ethylene chloride
• Ethylene dichloride
• Freon 150
• Glycol dichloride
• HCC 150
• NCI-C00511
• R-150
• Rcra waste number U077
• UN 1184
• s-Dichloroethane
• sym-Dichloroethane
• «alpha»,«beta»-Dichloroethane

• 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_sat : Molar heat capacity at saturation pressure (J/mol×K).
• μ : Dipole Moment (debye).
• η : Dynamic viscosity (Pa×s).
• Δ_fG° : Standard Gibbs free energy of formation (kJ/mol).
• R_g : Radius of Gyration.
• 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).
• n₀ : Refractive Index.
• ρ_c : Critical density (kg/m³).
• 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_boil(P) : Boiling point at given pressure (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.

Contents

1. Physical Properties
2. Temperature Dependent Properties
3. Pressure Dependent Properties
4. Datasets
5. Correlations
6. Similar Compounds
7. Mixtures
8. Sources

Physical Properties

Property	Value	Unit	Source
ω	[0.2780; 0.2860]
ω	0.2860		PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
ω	0.2860		ChemSep v8.3 pure component data Compiled value
ω	0.2780		KDB
ΔcH°liquid	[-1246.40; -1236.40]	kJ/mol
ΔcH°liquid	-1236.40	kJ/mol	NIST
ΔcH°liquid	-1246.40 ± 8.40	kJ/mol	NIST
μ	[1.44; 1.80]	debye
μ	1.44	debye	ChemSep v8.3 pure component data Compiled value
μ	1.80	debye	KDB
η	0.0008270	Pa×s	Studies on Transport and Thermodynamic Properties of Binary Mixtures of Hexan-1-ol with Halogenated Compounds at 293.15 K
ΔfG°	[-73.94; -73.90]	kJ/mol
ΔfG°	-73.94	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfG°	-73.90	kJ/mol	KDB
Rg	2.8510		KDB
ΔfH°gas	[-132.00; -125.40]	kJ/mol
ΔfH°gas	-130.09 ± 0.59	kJ/mol	Active Thermochemical Tables 1.112, gas-phase enthalpies of formation Compiled value
ΔfH°gas	-129.79	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfH°gas	-129.80	kJ/mol	KDB
ΔfH°gas	-132.00 ± 3.50	kJ/mol	NIST
ΔfH°gas	-125.40 ± 1.00	kJ/mol	NIST
ΔfH°gas	-129.00	kJ/mol	NIST
ΔfH°liquid	[-169.70; -167.20]	kJ/mol
ΔfH°liquid	-167.20 ± 3.50	kJ/mol	NIST
ΔfH°liquid	-169.70	kJ/mol	NIST
ΔfusH°	9.33	kJ/mol	Joback Calculated Property
ΔvapH°	[34.40; 35.40]	kJ/mol
ΔvapH°	35.22	kJ/mol	NIST
ΔvapH°	35.20 ± 0.40	kJ/mol	NIST
ΔvapH°	35.21 ± 0.05	kJ/mol	NIST
ΔvapH°	Outlier 34.40	kJ/mol	NIST
ΔvapH°	35.10 ± 0.10	kJ/mol	NIST
ΔvapH°	35.20 ± 0.10	kJ/mol	NIST
ΔvapH°	35.15 ± 0.01	kJ/mol	NIST
ΔvapH°	35.40 ± 0.08	kJ/mol	NIST
IE	[11.04; 11.40]	eV
IE	11.07 ± 0.04	eV	NIST
IE	11.05	eV	NIST
IE	11.04	eV	NIST
IE	11.12 ± 0.05	eV	NIST
IE	11.40 ± 0.10	eV	NIST
IE	11.22 ± 0.02	eV	NIST
IE	11.39 ± 0.03	eV	NIST
log10WS	[-1.07; -1.06]
log10WS	-1.07		Aq. Solubility Prediction
log10WS	-1.06		Estimated Solubility
logPoct/wat	1.464		Crippen Calculated Property
McVol	63.520	ml/mol	McGowan Calculated Property
Pc	[5370.23; 5400.00]	kPa
Pc	5380.00	kPa	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 10 Compiled value
Pc	5370.23	kPa	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Pc	5400.00	kPa	ChemSep v8.3 pure component data Compiled value
Pc	5400.00	kPa	KDB
Pc	5380.00 ± 50.00	kPa	NIST
Ptriple	0.24	kPa	ChemSep v8.3 pure component data Compiled value
ρc	440.37 ± 14.84	kg/m3	NIST
Inp	[586.00; 673.00]
Inp	645.40		NIST
Inp	648.20		NIST
Inp	656.20		NIST
Inp	654.00		NIST
Inp	650.10		NIST
Inp	647.70		NIST
Inp	644.80		NIST
Inp	632.00		NIST
Inp	630.00		NIST
Inp	632.00		NIST
Inp	638.00		NIST
Inp	641.00		NIST
Inp	633.00		NIST
Inp	645.00		NIST
Inp	640.00		NIST
Inp	629.00		NIST
Inp	641.00		NIST
Inp	620.00		NIST
Inp	641.00		NIST
Inp	643.00		NIST
Inp	648.00		NIST
Inp	660.00		NIST
Inp	628.60		NIST
Inp	606.00		NIST
Inp	607.00		NIST
Inp	610.00		NIST
Inp	632.00		NIST
Inp	Outlier 586.00		NIST
Inp	Outlier 595.00		NIST
Inp	621.00		NIST
Inp	627.00		NIST
Inp	632.00		NIST
Inp	632.00		NIST
Inp	632.00		NIST
Inp	633.00		NIST
Inp	630.00		NIST
Inp	632.00		NIST
Inp	632.00		NIST
Inp	Outlier 673.00		NIST
Inp	630.00		NIST
Inp	631.00		NIST
Inp	649.00		NIST
Inp	632.00		NIST
Inp	631.00		NIST
Inp	623.00		NIST
Inp	649.30		NIST
Inp	635.50		NIST
Inp	606.00		NIST
Inp	Outlier 595.00		NIST
Inp	620.00		NIST
Inp	628.60		NIST
Inp	632.00		NIST
Inp	649.00		NIST
Inp	635.50		NIST
Ip	[1045.00; 1093.00]
Ip	1088.00		NIST
Ip	1085.00		NIST
Ip	1090.00		NIST
Ip	1080.00		NIST
Ip	1084.20		NIST
Ip	1084.96		NIST
Ip	1077.64		NIST
Ip	1076.00		NIST
Ip	1072.00		NIST
Ip	1093.00		NIST
Ip	1088.00		NIST
Ip	1088.00		NIST
Ip	1065.00		NIST
Ip	1065.00		NIST
Ip	1045.00		NIST
Ip	1051.00		NIST
Ip	1045.00		NIST
S°liquid	208.53	J/mol×K	NIST
Tboil	[334.70; 361.15]	K
Tboil	356.70	K	Excess volumes and speeds of sound of mixtures of 1,2-dibromoethane with chlorinated ethanes and ethenes at 303.15 K
Tboil	356.95	K	Excess molar enthalpies of dimethylsulfoxide with chloroethanes and chloroethenes at 298.15K
Tboil	356.59	K	Isobaric Vapor-Liquid Equilibrium for the Binary Systems of 1,2-Dichloroethane + sec-Butyl Acetate, n-Propyl Acetate, and tert-Butyl Acetate at 101.3 kPa
Tboil	356.95	K	Vapor-Liquid Equilibria and Excess Molar Enthalpies for N-Methyl-2-pyrrolidone with Chloroethanes and Chloroethenes
Tboil	356.95	K	Isobaric Vapor Liquid Equilibrium for Dimethylsulfoxide with Chloroethanes and Chloroethenes
Tboil	356.66	K	ChemSep v8.3 pure component data Compiled value
Tboil	356.60	K	KDB
Tboil	356.70 ± 0.30	K	NIST
Tboil	357.20 ± 0.40	K	NIST
Tboil	356.65 ± 0.20	K	NIST
Tboil	356.70	K	NIST
Tboil	356.50 ± 0.30	K	NIST
Tboil	356.55 ± 0.40	K	NIST
Tboil	356.63 ± 0.20	K	NIST
Tboil	356.60	K	NIST
Tboil	356.75 ± 0.30	K	NIST
Tboil	356.65 ± 0.20	K	NIST
Tboil	356.65 ± 0.20	K	NIST
Tboil	356.62 ± 0.30	K	NIST
Tboil	355.85 ± 0.50	K	NIST
Tboil	356.70 ± 0.30	K	NIST
Tboil	356.65	K	NIST
Tboil	356.70 ± 0.30	K	NIST
Tboil	356.85 ± 0.50	K	NIST
Tboil	356.71 ± 0.25	K	NIST
Tboil	357.15 ± 1.50	K	NIST
Tboil	356.80 ± 0.40	K	NIST
Tboil	356.40 ± 0.80	K	NIST
Tboil	356.15 ± 1.50	K	NIST
Tboil	357.65 ± 2.00	K	NIST
Tboil	356.65 ± 0.40	K	NIST
Tboil	356.53 ± 0.07	K	NIST
Tboil	356.53 ± 0.35	K	NIST
Tboil	356.65 ± 0.40	K	NIST
Tboil	357.00 ± 1.50	K	NIST
Tboil	356.85 ± 0.40	K	NIST
Tboil	357.00 ± 0.50	K	NIST
Tboil	356.62 ± 0.15	K	NIST
Tboil	356.62 ± 0.15	K	NIST
Tboil	356.63 ± 0.15	K	NIST
Tboil	356.10 ± 0.30	K	NIST
Tboil	356.80 ± 0.50	K	NIST
Tboil	356.15 ± 0.50	K	NIST
Tboil	356.75 ± 0.30	K	NIST
Tboil	356.65 ± 0.50	K	NIST
Tboil	356.85 ± 0.30	K	NIST
Tboil	356.90 ± 0.30	K	NIST
Tboil	356.65 ± 0.20	K	NIST
Tboil	356.90 ± 0.50	K	NIST
Tboil	356.90 ± 0.50	K	NIST
Tboil	356.82 ± 0.20	K	NIST
Tboil	356.65 ± 0.50	K	NIST
Tboil	357.40 ± 0.50	K	NIST
Tboil	356.25 ± 0.50	K	NIST
Tboil	356.85 ± 0.20	K	NIST
Tboil	356.13 ± 0.30	K	NIST
Tboil	Outlier 334.70 ± 1.00	K	NIST
Tboil	361.15 ± 4.00	K	NIST
Tboil	356.50 ± 1.50	K	NIST
Tboil	357.90 ± 1.50	K	NIST
Tc	[561.00; 563.15]	K
Tc	561.50	K	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 10 Compiled value
Tc	561.00	K	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Tc	561.00	K	ChemSep v8.3 pure component data Compiled value
Tc	561.00	K	KDB
Tc	561.60 ± 0.40	K	NIST
Tc	561.20	K	NIST
Tc	Outlier 563.15 ± 3.00	K	NIST
Tfus	[176.35; 241.15]	K
Tfus	237.65	K	Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
Tfus	237.49	K	ChemSep v8.3 pure component data Compiled value
Tfus	237.60	K	KDB
Tfus	237.65	K	Aq. Solubility Prediction
Tfus	241.15 ± 1.00	K	NIST
Tfus	237.45	K	NIST
Tfus	237.50 ± 0.02	K	NIST
Tfus	237.85 ± 0.40	K	NIST
Tfus	237.28 ± 0.05	K	NIST
Tfus	237.70 ± 0.20	K	NIST
Tfus	Outlier 176.35 ± 0.40	K	NIST
Tfus	237.65 ± 0.30	K	NIST
Tfus	237.85 ± 0.30	K	NIST
Tfus	237.88 ± 0.20	K	NIST
Ttriple	[237.20; 237.60]	K
Ttriple	237.49	K	ChemSep v8.3 pure component data Compiled value
Ttriple	237.60 ± 0.30	K	NIST
Ttriple	237.20 ± 0.02	K	NIST
Ttriple	237.20 ± 0.02	K	NIST
UQi	2.52		ChemSep v8.3 pure component data Compiled value
URi	2.88		ChemSep v8.3 pure component data Compiled value
Vc	[0.220; 0.225]	m3/kmol
Vc	0.225	m3/kmol	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 10 Compiled value
Vc	0.220	m3/kmol	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Vc	0.220	m3/kmol	ChemSep v8.3 pure component data Compiled value
Vc	0.225	m3/kmol	KDB
Zc	[0.2550000; 0.2604810]
Zc	0.2590000		IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 10 Compiled value
Zc	0.2550000		ChemSep v8.3 pure component data Compiled value
Zc	0.2604810		KDB
Zra	0.27		KDB

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[122.20; 131.00]	J/mol×K	[293.00; 300.00]
Cp,liquid	124.30	J/mol×K	293.00	NIST
Cp,liquid	129.20	J/mol×K	293.00	NIST
Cp,liquid	129.70	J/mol×K	298.00	NIST
Cp,liquid	122.20	J/mol×K	298.00	NIST
Cp,liquid	123.00	J/mol×K	298.00	NIST
Cp,liquid	128.99	J/mol×K	298.15	NIST
Cp,liquid	128.60	J/mol×K	298.15	NIST
Cp,liquid	128.81	J/mol×K	298.15	NIST
Cp,liquid	129.40	J/mol×K	298.15	NIST
Cp,liquid	129.00	J/mol×K	298.15	NIST
Cp,liquid	128.90	J/mol×K	298.15	NIST
Cp,liquid	129.54	J/mol×K	298.15	NIST
Cp,liquid	128.99	J/mol×K	298.15	NIST
Cp,liquid	131.00	J/mol×K	300.00	NIST
Csat	[128.02; 134.46]	J/mol×K	[284.16; 353.14]
Csat	128.02	J/mol×K	284.16	Heat Capacities of alpha,omega-Dichloroalkanes at Temperatures from 284.15 K to 353.15 K and a Group Additivity Analysis
Csat	128.21	J/mol×K	286.66	Heat Capacities of alpha,omega-Dichloroalkanes at Temperatures from 284.15 K to 353.15 K and a Group Additivity Analysis
Csat	128.39	J/mol×K	289.15	Heat Capacities of alpha,omega-Dichloroalkanes at Temperatures from 284.15 K to 353.15 K and a Group Additivity Analysis
Csat	128.58	J/mol×K	291.66	Heat Capacities of alpha,omega-Dichloroalkanes at Temperatures from 284.15 K to 353.15 K and a Group Additivity Analysis
Csat	128.75	J/mol×K	294.15	Heat Capacities of alpha,omega-Dichloroalkanes at Temperatures from 284.15 K to 353.15 K and a Group Additivity Analysis
Csat	128.94	J/mol×K	296.65	Heat Capacities of alpha,omega-Dichloroalkanes at Temperatures from 284.15 K to 353.15 K and a Group Additivity Analysis
Csat	129.06	J/mol×K	298.15	Heat Capacities of alpha,omega-Dichloroalkanes at Temperatures from 284.15 K to 353.15 K and a Group Additivity Analysis
Csat	129.11	J/mol×K	299.16	Heat Capacities of alpha,omega-Dichloroalkanes at Temperatures from 284.15 K to 353.15 K and a Group Additivity Analysis
Csat	129.39	J/mol×K	301.65	Heat Capacities of alpha,omega-Dichloroalkanes at Temperatures from 284.15 K to 353.15 K and a Group Additivity Analysis
Csat	129.47	J/mol×K	304.16	Heat Capacities of alpha,omega-Dichloroalkanes at Temperatures from 284.15 K to 353.15 K and a Group Additivity Analysis
Csat	129.86	J/mol×K	308.56	Heat Capacities of alpha,omega-Dichloroalkanes at Temperatures from 284.15 K to 353.15 K and a Group Additivity Analysis
Csat	129.86	J/mol×K	309.15	Heat Capacities of alpha,omega-Dichloroalkanes at Temperatures from 284.15 K to 353.15 K and a Group Additivity Analysis
Csat	130.16	J/mol×K	311.66	Heat Capacities of alpha,omega-Dichloroalkanes at Temperatures from 284.15 K to 353.15 K and a Group Additivity Analysis
Csat	130.40	J/mol×K	314.15	Heat Capacities of alpha,omega-Dichloroalkanes at Temperatures from 284.15 K to 353.15 K and a Group Additivity Analysis
Csat	130.55	J/mol×K	316.65	Heat Capacities of alpha,omega-Dichloroalkanes at Temperatures from 284.15 K to 353.15 K and a Group Additivity Analysis
Csat	130.88	J/mol×K	319.16	Heat Capacities of alpha,omega-Dichloroalkanes at Temperatures from 284.15 K to 353.15 K and a Group Additivity Analysis
Csat	131.09	J/mol×K	321.65	Heat Capacities of alpha,omega-Dichloroalkanes at Temperatures from 284.15 K to 353.15 K and a Group Additivity Analysis
Csat	131.20	J/mol×K	324.16	Heat Capacities of alpha,omega-Dichloroalkanes at Temperatures from 284.15 K to 353.15 K and a Group Additivity Analysis
Csat	131.56	J/mol×K	326.65	Heat Capacities of alpha,omega-Dichloroalkanes at Temperatures from 284.15 K to 353.15 K and a Group Additivity Analysis
Csat	131.87	J/mol×K	329.15	Heat Capacities of alpha,omega-Dichloroalkanes at Temperatures from 284.15 K to 353.15 K and a Group Additivity Analysis
Csat	132.06	J/mol×K	331.66	Heat Capacities of alpha,omega-Dichloroalkanes at Temperatures from 284.15 K to 353.15 K and a Group Additivity Analysis
Csat	132.24	J/mol×K	334.15	Heat Capacities of alpha,omega-Dichloroalkanes at Temperatures from 284.15 K to 353.15 K and a Group Additivity Analysis
Csat	132.59	J/mol×K	336.66	Heat Capacities of alpha,omega-Dichloroalkanes at Temperatures from 284.15 K to 353.15 K and a Group Additivity Analysis
Csat	132.82	J/mol×K	339.16	Heat Capacities of alpha,omega-Dichloroalkanes at Temperatures from 284.15 K to 353.15 K and a Group Additivity Analysis
Csat	132.96	J/mol×K	341.65	Heat Capacities of alpha,omega-Dichloroalkanes at Temperatures from 284.15 K to 353.15 K and a Group Additivity Analysis
Csat	133.32	J/mol×K	344.16	Heat Capacities of alpha,omega-Dichloroalkanes at Temperatures from 284.15 K to 353.15 K and a Group Additivity Analysis
Csat	133.59	J/mol×K	346.65	Heat Capacities of alpha,omega-Dichloroalkanes at Temperatures from 284.15 K to 353.15 K and a Group Additivity Analysis
Csat	133.83	J/mol×K	349.15	Heat Capacities of alpha,omega-Dichloroalkanes at Temperatures from 284.15 K to 353.15 K and a Group Additivity Analysis
Csat	134.22	J/mol×K	351.66	Heat Capacities of alpha,omega-Dichloroalkanes at Temperatures from 284.15 K to 353.15 K and a Group Additivity Analysis
Csat	134.46	J/mol×K	353.14	Heat Capacities of alpha,omega-Dichloroalkanes at Temperatures from 284.15 K to 353.15 K and a Group Additivity Analysis
η	[0.0006269; 0.0008700]	Pa×s	[288.15; 313.15]
η	0.0008700	Pa×s	288.15	Densities and Viscosities of (1-Propanol + 1,2-Dichloroethane), (1-Propanol + Benzaldehyde), (Benzaldehyde + 1,2-Dichloroethane), and (1-Propanol + 1,2-Dichloroethane + Benzaldehyde) Mixtures from T = 288.15 K to 313.15 K
η	0.0008112	Pa×s	293.15	Densities and Viscosities of (1-Propanol + 1,2-Dichloroethane), (1-Propanol + Benzaldehyde), (Benzaldehyde + 1,2-Dichloroethane), and (1-Propanol + 1,2-Dichloroethane + Benzaldehyde) Mixtures from T = 288.15 K to 313.15 K
η	0.0007902	Pa×s	298.15	Thermophysical properties of the binary mixtures of 1,2-Dichloroethane with Chlorobenzene and Bromobenzene from 298.15 to 313.15 K
η	0.0007597	Pa×s	298.15	Densities and Viscosities of (1-Propanol + 1,2-Dichloroethane), (1-Propanol + Benzaldehyde), (Benzaldehyde + 1,2-Dichloroethane), and (1-Propanol + 1,2-Dichloroethane + Benzaldehyde) Mixtures from T = 288.15 K to 313.15 K
η	0.0007291	Pa×s	303.15	Thermophysical properties of the binary mixtures of 1,2-Dichloroethane with Chlorobenzene and Bromobenzene from 298.15 to 313.15 K
η	0.0007112	Pa×s	303.15	Densities and Viscosities of (1-Propanol + 1,2-Dichloroethane), (1-Propanol + Benzaldehyde), (Benzaldehyde + 1,2-Dichloroethane), and (1-Propanol + 1,2-Dichloroethane + Benzaldehyde) Mixtures from T = 288.15 K to 313.15 K
η	0.0006739	Pa×s	308.15	Thermophysical properties of the binary mixtures of 1,2-Dichloroethane with Chlorobenzene and Bromobenzene from 298.15 to 313.15 K
η	0.0006747	Pa×s	308.15	Densities and Viscosities of (1-Propanol + 1,2-Dichloroethane), (1-Propanol + Benzaldehyde), (Benzaldehyde + 1,2-Dichloroethane), and (1-Propanol + 1,2-Dichloroethane + Benzaldehyde) Mixtures from T = 288.15 K to 313.15 K
η	0.0006441	Pa×s	313.15	Thermophysical properties of the binary mixtures of 1,2-Dichloroethane with Chlorobenzene and Bromobenzene from 298.15 to 313.15 K
η	0.0006269	Pa×s	313.15	Densities and Viscosities of (1-Propanol + 1,2-Dichloroethane), (1-Propanol + Benzaldehyde), (Benzaldehyde + 1,2-Dichloroethane), and (1-Propanol + 1,2-Dichloroethane + Benzaldehyde) Mixtures from T = 288.15 K to 313.15 K
ΔfusH	[2.85; 8.84]	kJ/mol	[175.00; 237.60]
ΔfusH	2.85	kJ/mol	175.00	NIST
ΔfusH	8.84	kJ/mol	237.20	NIST
ΔfusH	8.83	kJ/mol	237.20	NIST
ΔfusH	8.83	kJ/mol	237.20	NIST
ΔfusH	8.84	kJ/mol	237.20	NIST
ΔfusH	8.75	kJ/mol	237.60	NIST
ΔvapH	[31.10; 40.80]	kJ/mol	[273.00; 542.00]
ΔvapH	33.91	kJ/mol	273.00	NIST
ΔvapH	37.50	kJ/mol	307.50	NIST
ΔvapH	34.80	kJ/mol	326.50	NIST
ΔvapH	34.70	kJ/mol	329.00	NIST
ΔvapH	34.80	kJ/mol	356.50	NIST
ΔvapH	31.98	kJ/mol	356.60	NIST
ΔvapH	32.01	kJ/mol	357.10	KDB
ΔvapH	31.10	kJ/mol	446.00	NIST
ΔvapH	31.10	kJ/mol	457.00	NIST
ΔvapH	40.80	kJ/mol	542.00	NIST
Pvap	[5.37; 101.30]	kPa	[284.86; 356.59]
Pvap	5.38	kPa	284.86	Isothermal vapour liquid equilibria of binary systems of 1,2-dichloroethane with ethers
Pvap	5.37	kPa	284.87	Isothermal vapour liquid equilibria of binary systems of 1,2-dichloroethane with ethers
Pvap	8.96	kPa	294.83	Isothermal vapour liquid equilibria of binary systems of 1,2-dichloroethane with ethers
Pvap	8.95	kPa	294.84	Isothermal vapour liquid equilibria of binary systems of 1,2-dichloroethane with ethers
Pvap	20.75	kPa	298.15	Excess molar enthalpies and (vapour + liquid) equilibria for mixtures containing N,N-dialkylamides and a,x-dichloroalkanes
Pvap	13.28	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	14.33	kPa	304.82	Isothermal vapour liquid equilibria of binary systems of 1,2-dichloroethane with ethers
Pvap	14.32	kPa	304.82	Isothermal vapour liquid equilibria of binary systems of 1,2-dichloroethane with ethers
Pvap	21.05	kPa	313.15	Isothermal Vapor-Liquid Equilibria of ethyl acetate + dibromomethane, or + bromochloromethane or + 1,2-dichloroethane or +1-bromo-2-chloroethane at T = 313.15 K
Pvap	20.75	kPa	313.15	Excess enthalpies and isothermal (vapour + liquid) equilibria of (1-methyl-2-pyrrolidone + 1-chloroalkane or +,?-dichloroalkane) mixtures
Pvap	22.18	kPa	314.81	Isothermal vapour liquid equilibria of binary systems of 1,2-dichloroethane with ethers
Pvap	22.18	kPa	314.83	Isothermal vapour liquid equilibria of binary systems of 1,2-dichloroethane with ethers
Pvap	33.28	kPa	324.82	Isothermal vapour liquid equilibria of binary systems of 1,2-dichloroethane with ethers
Pvap	33.27	kPa	324.83	Isothermal vapour liquid equilibria of binary systems of 1,2-dichloroethane with ethers
Pvap	48.45	kPa	334.79	Isothermal vapour liquid equilibria of binary systems of 1,2-dichloroethane with ethers
Pvap	48.46	kPa	334.82	Isothermal vapour liquid equilibria of binary systems of 1,2-dichloroethane with ethers
Pvap	67.97	kPa	344.81	Isothermal vapour liquid equilibria of binary systems of 1,2-dichloroethane with ethers
Pvap	67.97	kPa	344.81	Isothermal vapour liquid equilibria of binary systems of 1,2-dichloroethane with ethers
Pvap	67.98	kPa	344.82	Isothermal vapour liquid equilibria of binary systems of 1,2-dichloroethane with ethers
Pvap	67.98	kPa	344.82	Isothermal vapour liquid equilibria of binary systems of 1,2-dichloroethane with ethers
Pvap	90.90	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
Pvap	94.94	kPa	354.89	Isothermal vapour liquid equilibria of binary systems of 1,2-dichloroethane with ethers
Pvap	94.94	kPa	354.89	Isothermal vapour liquid equilibria of binary systems of 1,2-dichloroethane with ethers
Pvap	94.95	kPa	354.89	Isothermal vapour liquid equilibria of binary systems of 1,2-dichloroethane with ethers
Pvap	94.95	kPa	354.89	Isothermal vapour liquid equilibria of binary systems of 1,2-dichloroethane with ethers
Pvap	95.50	kPa	355.15	Vapor-liquid equilibrium and excess Gibbs energies of some binary mixtures of acrylonitrile at 95.5 kPa
Pvap	101.30	kPa	356.59	Isobaric Vapor-Liquid Equilibrium for the Binary Systems of 1,2-Dichloroethane + sec-Butyl Acetate, n-Propyl Acetate, and tert-Butyl Acetate at 101.3 kPa
n0	[1.41960; 1.44480]		[293.15; 298.15]
n0	1.41960		293.15	Bubble points of some binary mixtures formed by o-cresol at 95.75 kPa
n0	1.44480		293.15	Excess Gibbs energies of selected binary mixtures formed by N,N-dimethyl formamide at 95.5 kPa
n0	1.41960		293.15	Bubble points of the binary mixtures formed by ethylbenzene with some chloroaliphatics and substituted benzenes at p = 94.7 kPa
n0	1.44450		293.15	Isobaric (vapour + liquid) equilibria data for the binary systems {1,2-dichloroethane (1) + toluene (2)} and {1,2-dichloroethane (1) + acetic acid (2)} at atmospheric pressure
n0	1.41960		293.15	Activity coefficients and excess Gibbs free energy of some binary mixtures formed by p-cresol at 95.23 kPa
n0	1.41960		293.15	Vapor-Liquid Equilibria of Binary Mixtures Formed by Hexan-1-ol with Chloroethanes and Chloroethenes at 95.6 kPa
n0	1.44210		298.15	Vapour pressure and excess Gibbs energy of binary 1,2-dichloroethane + cyclohexanone, chloroform + cyclopentanone and chloroform + cyclohexanone mixtures at temperatures from 298.15 to 318.15 K
n0	1.44200		298.15	Thermodynamic study of (alkyl esters + a,x-alkyl dihalides) I: HE and V E for 25 binary mixtures {xCu-1H2u-1CO2C2H5 + (1-x)a,x-ClCH2(CH2)v-2CH2Cl}, where u = 1 to 5, a = 1 and v = x = 2 to 6
n0	1.44210		298.15	Isothermal (vapour + liquid) equilibria in the binary mixtures (1,2-dichloroethane and 1,1,1-trichloroethane with cyclopentanone) within the temperature range (298.15 to 313.15) K
n0	1.44210		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	1.44210		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
ρl	[1193.61; 1267.39]	kg/m3	[283.15; 333.15]
ρl	1267.39	kg/m3	283.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	1265.95	kg/m3	284.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	1264.50	kg/m3	285.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	1263.05	kg/m3	286.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	1261.60	kg/m3	287.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	1259.99	kg/m3	288.15	Volumetric properties of binary liquid mixtures of ketones with chloroalkanes at different temperatures and atmospheric pressure
ρl	1260.01	kg/m3	288.15	Densities and Excess Molar Volumes of the Binary Mixtures of Cyclohexanone with Chloroalkanes at Temperatures between (288.15 and 318.15) K
ρl	1260.33	kg/m3	288.15	Densities and Excess Molar Volumes of the Binary Mixtures of Cyclopentanone with Chloroalkanes at T = (288.15, 298.15, 308.15, and 318.15) K
ρl	1260.15	kg/m3	288.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	1259.99	kg/m3	288.15	Volumetric properties of binary liquid mixtures of alcohols with 1,2-dichloroethane at different temperatures and atmospheric pressure
ρl	1260.35	kg/m3	288.15	Densities and Excess Molar Volumes for the Binary and Ternary Systems of (1,4-Dioxane, 1-Propanol or 2-Propanol, and 1,2-Dichloroethane) at T = (288.15 to 318.15) K. Experimental Measurements and Prigogine-Flory-Patterson Modeling
ρl	1250.00	kg/m3	289.00	KDB
ρl	1258.70	kg/m3	289.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	1257.25	kg/m3	290.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	1255.80	kg/m3	291.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	1254.35	kg/m3	292.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	1253.00	kg/m3	293.15	Influence of chlorine atom on interactions between halo-hydrocarbons and 1-nonanol: Density and speed of sound measurements
ρl	1252.77	kg/m3	293.15	Volumetric properties of binary liquid mixtures of alcohols with 1,2-dichloroethane at different temperatures and atmospheric pressure
ρl	1252.89	kg/m3	293.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	1252.82	kg/m3	293.15	Theoretical and experimental study on volumetric and electromagnetic properties of binary systems consisting of 1,2-dichloroethane with benzene and its derivatives at T = (293.15 to 333.15) K
ρl	1252.74	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	1252.77	kg/m3	293.15	Volumetric properties of binary liquid mixtures of ketones with chloroalkanes at different temperatures and atmospheric pressure
ρl	1252.15	kg/m3	293.20	Isobaric vapour liquid equilibria for binary mixtures of 1,2-dibromoethane with 1,2-dichloroethane, trichloromethane, and 1,1,2,2-tetrachloroethane at atmospheric pressure
ρl	1251.44	kg/m3	294.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	1249.98	kg/m3	295.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	1248.52	kg/m3	296.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	1247.07	kg/m3	297.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	1245.48	kg/m3	298.15	Densities and Excess Molar Volumes of the Binary Mixtures of Cyclohexanone with Chloroalkanes at Temperatures between (288.15 and 318.15) K
ρl	1246.34	kg/m3	298.15	(Vapor + liquid) equilibria for the binary mixtures (1-propanol + dibromomethane, or + bromochloromethane, or + 1,2-dichloroethane or +1-bromo-2-chloroethane) at T = 313.15 K.
ρl	1245.75	kg/m3	298.15	Densities and Excess Molar Volumes for the Binary and Ternary Systems of (1,4-Dioxane, 1-Propanol or 2-Propanol, and 1,2-Dichloroethane) at T = (288.15 to 318.15) K. Experimental Measurements and Prigogine-Flory-Patterson Modeling
ρl	1245.61	kg/m3	298.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	1246.37	kg/m3	298.15	Hydrogen bond interactions in the blends of 1,4-dioxane with some 1, 2- disubstituted ethanes at T = (298.15, 308.15 and 318.15) K
ρl	1245.76	kg/m3	298.15	Densities and Excess Molar Volumes for the Binary and Ternary Systems of (1,4-Dioxane, 1-Propanol or 2-Propanol, and 1,2-Dichloroethane) at T = (288.15 to 318.15) K. Experimental Measurements and Prigogine-Flory-Patterson Modeling
ρl	1245.64	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	1245.49	kg/m3	298.15	Volumetric properties of binary liquid mixtures of ketones with chloroalkanes at different temperatures and atmospheric pressure
ρl	1245.80	kg/m3	298.15	Densities and Excess Molar Volumes of the Binary Mixtures of Cyclopentanone with Chloroalkanes at T = (288.15, 298.15, 308.15, and 318.15) K
ρl	1245.68	kg/m3	298.15	Isothermal Vapor-Liquid Equilibria and Excess Gibbs Energies for Binary Mixtures of Cyclic Ethers with 1,2-Dichloroethane
ρl	1245.59	kg/m3	298.15	Volumetric Study for the Binary Nitromethane with Chloroalkane Mixtures at Temperatures in the Range (298.15 to 318.15) K
ρl	1246.70	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	1245.49	kg/m3	298.15	Volumetric properties of binary liquid mixtures of alcohols with 1,2-dichloroethane at different temperatures and atmospheric pressure
ρl	1246.00	kg/m3	298.15	Influence of chlorine atom on interactions between halo-hydrocarbons and 1-nonanol: Density and speed of sound measurements
ρl	1244.15	kg/m3	299.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	1242.69	kg/m3	300.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	1241.22	kg/m3	301.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	1239.76	kg/m3	302.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	1238.70	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	1238.18	kg/m3	303.15	Volumetric properties of binary liquid mixtures of ketones with chloroalkanes at different temperatures and atmospheric pressure
ρl	1238.27	kg/m3	303.15	Theoretical and experimental study on volumetric and electromagnetic properties of binary systems consisting of 1,2-dichloroethane with benzene and its derivatives at T = (293.15 to 333.15) K
ρl	1238.00	kg/m3	303.15	Influence of chlorine atom on interactions between halo-hydrocarbons and 1-nonanol: Density and speed of sound measurements
ρl	1238.18	kg/m3	303.15	Volumetric properties of binary liquid mixtures of alcohols with 1,2-dichloroethane at different temperatures and atmospheric pressure
ρl	1238.29	kg/m3	303.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	1236.83	kg/m3	304.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	1235.36	kg/m3	305.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	1233.89	kg/m3	306.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	1232.42	kg/m3	307.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	1230.84	kg/m3	308.15	Volumetric properties of binary liquid mixtures of ketones with chloroalkanes at different temperatures and atmospheric pressure
ρl	1231.21	kg/m3	308.15	Hydrogen bond interactions in the blends of 1,4-dioxane with some 1, 2- disubstituted ethanes at T = (298.15, 308.15 and 318.15) K
ρl	1231.16	kg/m3	308.15	Densities and Excess Molar Volumes for the Binary and Ternary Systems of (1,4-Dioxane, 1-Propanol or 2-Propanol, and 1,2-Dichloroethane) at T = (288.15 to 318.15) K. Experimental Measurements and Prigogine-Flory-Patterson Modeling
ρl	1230.96	kg/m3	308.15	Volumetric Study for the Binary Nitromethane with Chloroalkane Mixtures at Temperatures in the Range (298.15 to 318.15) K
ρl	1230.95	kg/m3	308.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	1230.84	kg/m3	308.15	Volumetric properties of binary liquid mixtures of alcohols with 1,2-dichloroethane at different temperatures and atmospheric pressure
ρl	1231.00	kg/m3	308.15	Influence of chlorine atom on interactions between halo-hydrocarbons and 1-nonanol: Density and speed of sound measurements
ρl	1230.83	kg/m3	308.15	Densities and Excess Molar Volumes of the Binary Mixtures of Cyclohexanone with Chloroalkanes at Temperatures between (288.15 and 318.15) K
ρl	1230.50	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	1231.15	kg/m3	308.15	Densities and Excess Molar Volumes of the Binary Mixtures of Cyclopentanone with Chloroalkanes at T = (288.15, 298.15, 308.15, and 318.15) K
ρl	1229.47	kg/m3	309.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	1228.00	kg/m3	310.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	1226.53	kg/m3	311.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	1225.05	kg/m3	312.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	1223.53	kg/m3	313.15	Theoretical and experimental study on volumetric and electromagnetic properties of binary systems consisting of 1,2-dichloroethane with benzene and its derivatives at T = (293.15 to 333.15) K
ρl	1223.70	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
ρl	1223.57	kg/m3	313.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	1223.46	kg/m3	313.15	Volumetric properties of binary liquid mixtures of alcohols with 1,2-dichloroethane at different temperatures and atmospheric pressure
ρl	1223.46	kg/m3	313.15	Volumetric properties of binary liquid mixtures of ketones with chloroalkanes at different temperatures and atmospheric pressure
ρl	1222.09	kg/m3	314.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	1220.61	kg/m3	315.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	1219.13	kg/m3	316.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	1217.64	kg/m3	317.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	1216.16	kg/m3	318.15	Volumetric Study for the Binary Nitromethane with Chloroalkane Mixtures at Temperatures in the Range (298.15 to 318.15) K
ρl	1216.56	kg/m3	318.15	Densities and Excess Molar Volumes for the Binary and Ternary Systems of (1,4-Dioxane, 1-Propanol or 2-Propanol, and 1,2-Dichloroethane) at T = (288.15 to 318.15) K. Experimental Measurements and Prigogine-Flory-Patterson Modeling
ρl	1216.35	kg/m3	318.15	Densities and Excess Molar Volumes of the Binary Mixtures of Cyclopentanone with Chloroalkanes at T = (288.15, 298.15, 308.15, and 318.15) K
ρl	1214.55	kg/m3	318.15	Hydrogen bond interactions in the blends of 1,4-dioxane with some 1, 2- disubstituted ethanes at T = (298.15, 308.15 and 318.15) K
ρl	1216.16	kg/m3	318.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	1216.04	kg/m3	318.15	Densities and Excess Molar Volumes of the Binary Mixtures of Cyclohexanone with Chloroalkanes at Temperatures between (288.15 and 318.15) K
ρl	1214.67	kg/m3	319.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	1213.18	kg/m3	320.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	1211.69	kg/m3	321.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	1210.20	kg/m3	322.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	1208.70	kg/m3	323.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	1208.61	kg/m3	323.15	Theoretical and experimental study on volumetric and electromagnetic properties of binary systems consisting of 1,2-dichloroethane with benzene and its derivatives at T = (293.15 to 333.15) K
ρl	1207.21	kg/m3	324.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	1205.71	kg/m3	325.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	1204.21	kg/m3	326.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	1202.71	kg/m3	327.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	1201.21	kg/m3	328.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	1199.70	kg/m3	329.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	1198.19	kg/m3	330.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	1196.69	kg/m3	331.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	1195.18	kg/m3	332.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	1193.66	kg/m3	333.15	Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
ρl	1193.61	kg/m3	333.15	Theoretical and experimental study on volumetric and electromagnetic properties of binary systems consisting of 1,2-dichloroethane with benzene and its derivatives at T = (293.15 to 333.15) K
ΔfusS	[16.20; 37.25]	J/mol×K	[175.00; 237.20]
ΔfusS	36.80	J/mol×K	175.00	NIST
ΔfusS	37.25	J/mol×K	237.20	NIST
ΔfusS	16.20	J/mol×K	237.20	NIST
ΔfusS	37.25	J/mol×K	237.20	NIST
csound,fluid	[1117.75; 1212.92]	m/s	[293.15; 318.15]
csound,fluid	1212.92	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	1193.60	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
csound,fluid	1194.44	m/s	298.15	Speeds of sound, isentropic compressibilities and refractive indices for some binary mixtures of nitromethane with chloroalkane at temperatures from 298.15 to 318.15 K. Comparison with theories
csound,fluid	1156.06	m/s	308.15	Speeds of sound, isentropic compressibilities and refractive indices for some binary mixtures of nitromethane with chloroalkane at temperatures from 298.15 to 318.15 K. Comparison with theories
csound,fluid	1117.75	m/s	318.15	Speeds of sound, isentropic compressibilities and refractive indices for some binary mixtures of nitromethane with chloroalkane at temperatures from 298.15 to 318.15 K. Comparison with theories
γ	[0.03; 0.03]	N/m	[293.15; 313.15]
γ	0.03	N/m	293.15	The additivity of surface and volumetric properties of alpha,omega-dihalogenoalkanes
γ	0.03	N/m	293.20	KDB
γ	0.03	N/m	298.15	The additivity of surface and volumetric properties of alpha,omega-dihalogenoalkanes
γ	0.03	N/m	303.15	The additivity of surface and volumetric properties of alpha,omega-dihalogenoalkanes
γ	0.03	N/m	308.15	The additivity of surface and volumetric properties of alpha,omega-dihalogenoalkanes
γ	0.03	N/m	313.15	The additivity of surface and volumetric properties of alpha,omega-dihalogenoalkanes

Pressure Dependent Properties

Property	Value	Unit	Pressure (kPa)	Source
Tboil(P)	[340.45; 357.25]	K	[60.01; 101.35]
Tboil(P)	340.45	K	60.01	Isobaric Vapor Liquid Equilibrium Data for the 1,2-Dichloroethane-1-Butanol System
Tboil(P)	343.85	K	66.68	Isobaric Vapor Liquid Equilibrium Data for the 1,2-Dichloroethane-1-Butanol System
Tboil(P)	346.55	K	73.35	Isobaric Vapor Liquid Equilibrium Data for the 1,2-Dichloroethane-1-Butanol System
Tboil(P)	349.45	K	80.02	Isobaric Vapor Liquid Equilibrium Data for the 1,2-Dichloroethane-1-Butanol System
Tboil(P)	352.05	K	86.69	Isobaric Vapor Liquid Equilibrium Data for the 1,2-Dichloroethane-1-Butanol System
Tboil(P)	357.25	K	101.35	Isobaric Vapor Liquid Equilibrium Data for the 1,2-Dichloroethane-1-Butanol System

Datasets

1. Viscosity, Pa*s (1)
2. Mass density, kg/m3 (1)

Viscosity, Pa*s

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Viscosity, Pa*s - Liquid
308.15	101.00	0.0006
Reference

Mass density, kg/m3

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
288.15	100.00	1259.9
288.15	500.00	1260.3
288.15	1000.00	1260.8
288.15	1500.00	1261.2
288.15	2000.00	1261.6
288.15	2500.00	1262.2
288.15	3100.00	1262.7
288.15	3600.00	1263.2
288.15	4100.00	1263.6
288.15	4600.00	1264.0
288.15	5100.00	1264.5
288.15	5600.00	1264.9
288.15	6100.00	1265.4
288.15	6600.00	1265.8
288.15	7100.00	1266.2
288.15	7600.00	1266.7
288.15	8100.00	1267.2
288.15	8600.00	1267.6
288.15	9200.00	1268.2
288.15	9600.00	1268.6
288.15	10100.00	1269.0
288.15	10600.00	1269.4
288.15	11100.00	1269.8
288.15	11600.00	1270.3
288.15	12100.00	1270.7
288.15	12600.00	1271.0
288.15	13100.00	1271.5
288.15	13600.00	1271.9
288.15	14100.00	1272.4
288.15	14700.00	1272.9
288.15	15200.00	1273.3
288.15	15700.00	1273.7
288.15	16300.00	1274.2
288.15	16800.00	1274.6
288.15	17200.00	1275.0
288.15	17700.00	1275.4
288.15	18200.00	1275.8
288.15	18600.00	1276.2
288.15	19000.00	1276.5
288.15	19400.00	1276.9
288.15	20000.00	1277.3
298.15	100.00	1245.5
298.15	500.00	1246.1
298.15	1000.00	1246.4
298.15	1500.00	1246.9
298.15	2000.00	1247.4
298.15	2500.00	1247.8
298.15	3100.00	1248.5
298.15	3600.00	1248.9
298.15	4100.00	1249.4
298.15	4600.00	1249.9
298.15	5100.00	1250.4
298.15	5600.00	1250.9
298.15	6100.00	1251.4
298.15	6600.00	1251.9
298.15	7100.00	1252.3
298.15	7600.00	1252.9
298.15	8100.00	1253.2
298.15	8600.00	1253.8
298.15	9200.00	1254.4
298.15	9600.00	1254.9
298.15	10000.00	1255.1
298.15	10600.00	1255.9
298.15	11100.00	1256.4
298.15	11600.00	1256.7
298.15	12100.00	1257.3
298.15	12600.00	1257.6
298.15	13100.00	1258.0
298.15	13600.00	1258.5
298.15	14200.00	1259.0
298.15	14700.00	1259.4
298.15	15200.00	1260.0
298.15	15700.00	1260.5
298.15	16200.00	1260.8
298.15	16700.00	1261.4
298.15	17300.00	1261.9
298.15	17800.00	1262.4
298.15	18300.00	1262.8
298.15	18800.00	1263.3
298.15	19200.00	1263.7
298.15	19700.00	1264.1
298.15	20200.00	1264.5
308.15	100.00	1231.0
308.15	500.00	1231.4
308.15	1000.00	1232.0
308.15	1500.00	1232.5
308.15	2000.00	1233.0
308.15	2500.00	1233.5
308.15	3100.00	1234.2
308.15	3600.00	1234.7
308.15	4100.00	1235.2
308.15	4600.00	1235.7
308.15	5100.00	1236.2
308.15	5600.00	1236.9
308.15	6100.00	1237.3
308.15	6600.00	1237.9
308.15	7100.00	1238.4
308.15	7600.00	1238.6
308.15	8100.00	1239.3
308.15	8600.00	1239.8
308.15	9200.00	1240.4
308.15	9600.00	1240.9
308.15	10100.00	1241.3
308.15	10600.00	1241.8
308.15	11100.00	1242.3
308.15	11600.00	1242.8
308.15	12100.00	1243.4
308.15	12600.00	1243.8
308.15	13100.00	1244.2
308.15	13600.00	1244.7
308.15	14200.00	1245.3
308.15	14700.00	1245.8
308.15	15200.00	1246.4
308.15	15700.00	1246.8
308.15	16200.00	1247.2
308.15	16700.00	1247.7
308.15	17200.00	1248.2
308.15	17800.00	1248.7
308.15	18300.00	1249.2
308.15	18800.00	1249.6
308.15	19200.00	1250.1
308.15	19700.00	1250.6
308.15	20200.00	1251.0
318.15	100.00	1216.4
318.15	500.00	1216.7
318.15	1000.00	1217.4
318.15	1500.00	1218.0
318.15	2000.00	1218.5
318.15	2500.00	1219.1
318.15	3100.00	1219.8
318.15	3600.00	1220.3
318.15	4100.00	1220.9
318.15	4600.00	1221.4
318.15	5100.00	1222.0
318.15	5600.00	1222.6
318.15	6100.00	1223.1
318.15	6600.00	1223.6
318.15	7100.00	1224.1
318.15	7600.00	1224.7
318.15	8100.00	1225.2
318.15	8600.00	1225.8
318.15	9200.00	1226.3
318.15	9600.00	1226.9
318.15	10100.00	1227.5
318.15	10600.00	1227.9
318.15	11100.00	1228.4
318.15	11600.00	1229.0
318.15	12100.00	1229.5
318.15	12500.00	1230.0
318.15	13100.00	1230.6
318.15	13600.00	1231.0
318.15	14200.00	1231.6
318.15	14700.00	1232.1
318.15	15200.00	1232.7
318.15	15600.00	1233.1
318.15	16300.00	1233.8
318.15	16800.00	1234.2
318.15	17300.00	1234.8
318.15	17800.00	1235.2
318.15	18200.00	1235.5
318.15	18900.00	1236.2
318.15	19200.00	1236.5
318.15	19700.00	1237.1
318.15	20200.00	1237.5
Reference

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[66.85; 157.64]	J/mol×K	[200.00; 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			6.20730e+01
Coefficient B			-7.58840e+02
Coefficient C			5.43724e+00
Coefficient D			-4.19600e-04
Coefficient E			1.14600e-07
Temperature range, min.			200.00
Temperature range, max.			1500.00
Cp,gas	66.85	J/mol×K	200.00	Calculated Property
Cp,gas	84.34	J/mol×K	344.44	Calculated Property
Cp,gas	102.82	J/mol×K	488.89	Calculated Property
Cp,gas	117.73	J/mol×K	633.33	Calculated Property
Cp,gas	129.06	J/mol×K	777.78	Calculated Property
Cp,gas	137.63	J/mol×K	922.22	Calculated Property
Cp,gas	144.23	J/mol×K	1066.67	Calculated Property
Cp,gas	149.48	J/mol×K	1211.11	Calculated Property
Cp,gas	153.84	J/mol×K	1355.56	Calculated Property
Cp,gas	157.64	J/mol×K	1500.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[124.44; 211.24]	J/mol×K	[237.49; 522.04]	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			9.27570e+01
Coefficient B			2.24150e+02
Coefficient C			1.61454e+00
Coefficient D			2.56560e-03
Coefficient E			5.10600e-06
Temperature range, min.			237.49
Temperature range, max.			522.04
Cp,liquid	124.44	J/mol×K	237.49	Calculated Property
Cp,liquid	126.13	J/mol×K	269.11	Calculated Property
Cp,liquid	129.11	J/mol×K	300.72	Calculated Property
Cp,liquid	133.43	J/mol×K	332.34	Calculated Property
Cp,liquid	139.31	J/mol×K	363.96	Calculated Property
Cp,liquid	147.09	J/mol×K	395.57	Calculated Property
Cp,liquid	157.28	J/mol×K	427.19	Calculated Property
Cp,liquid	170.63	J/mol×K	458.81	Calculated Property
Cp,liquid	188.14	J/mol×K	490.42	Calculated Property
Cp,liquid	211.24	J/mol×K	522.04	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.0018308; 0.0000837]	Pa×s	[237.49; 550.00]	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			2.57470e+01
Coefficient B			-3.85450e+02
Coefficient C			-5.59120e+00
Coefficient D			2.79370e-06
Coefficient E			2.00000e+00
Temperature range, min.			237.49
Temperature range, max.			550.00
η	0.0018308	Pa×s	237.49	Calculated Property
η	0.0011032	Pa×s	272.21	Calculated Property
η	0.0007000	Pa×s	306.94	Calculated Property
η	0.0004652	Pa×s	341.66	Calculated Property
η	0.0003221	Pa×s	376.38	Calculated Property
η	0.0002315	Pa×s	411.11	Calculated Property
η	0.0001720	Pa×s	445.83	Calculated Property
η	0.0001317	Pa×s	480.55	Calculated Property
η	0.0001036	Pa×s	515.28	Calculated Property
η	0.0000837	Pa×s	550.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ΔvapH	[38.30; 14.26]	kJ/mol	[237.49; 544.54]	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			5.07243e+01
Coefficient B			5.17321e-01
Coefficient C			2.05828e-01
Coefficient D			-6.37156e-01
Coefficient E			2.65499e-01
Critical temperature, Tc (K)			5.61000e+02
Temperature range, min.			237.49
Temperature range, max.			544.54
ΔvapH	38.30	kJ/mol	237.49	Calculated Property
ΔvapH	36.49	kJ/mol	271.61	Calculated Property
ΔvapH	34.67	kJ/mol	305.72	Calculated Property
ΔvapH	32.84	kJ/mol	339.84	Calculated Property
ΔvapH	30.94	kJ/mol	373.96	Calculated Property
ΔvapH	28.93	kJ/mol	408.07	Calculated Property
ΔvapH	26.69	kJ/mol	442.19	Calculated Property
ΔvapH	24.02	kJ/mol	476.31	Calculated Property
ΔvapH	20.47	kJ/mol	510.42	Calculated Property
ΔvapH	14.26	kJ/mol	544.54	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[0.24; 5372.05]	kPa	[237.49; 561.60]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.47712e+01
Coefficient B			-3.23907e+03
Coefficient C			-3.76700e+01
Temperature range, min.			237.49
Temperature range, max.			561.60
Pvap	0.24	kPa	237.49	Calculated Property
Pvap	2.82	kPa	273.50	Calculated Property
Pvap	17.39	kPa	309.51	Calculated Property
Pvap	70.10	kPa	345.53	Calculated Property
Pvap	210.97	kPa	381.54	Calculated Property
Pvap	515.27	kPa	417.55	Calculated Property
Pvap	1078.15	kPa	453.56	Calculated Property
Pvap	2005.48	kPa	489.58	Calculated Property
Pvap	3403.86	kPa	525.59	Calculated Property
Pvap	5372.05	kPa	561.60	Calculated Property
Pvap	[0.24; 5269.59]	kPa	[237.49; 561.00]	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			7.45713e+01
Coefficient B			-6.50317e+03
Coefficient C			-8.96027e+00
Coefficient D			7.32894e-06
Coefficient E			2.00000e+00
Comment			Range stopped at Tc; ChemSep gives it to 561.6 K.
Temperature range, min.			237.49
Temperature range, max.			561.00
Pvap	0.24	kPa	237.49	Calculated Property
Pvap	2.88	kPa	273.44	Calculated Property
Pvap	17.63	kPa	309.38	Calculated Property
Pvap	69.76	kPa	345.33	Calculated Property
Pvap	205.34	kPa	381.27	Calculated Property
Pvap	491.40	kPa	417.22	Calculated Property
Pvap	1014.77	kPa	453.16	Calculated Property
Pvap	1884.36	kPa	489.11	Calculated Property
Pvap	3240.01	kPa	525.05	Calculated Property
Pvap	5269.59	kPa	561.00	Calculated Property
Pvap	[0.24; 5298.45]	kPa	[237.49; 561.00]	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			8.39680e+01
Coefficient B			-6.90490e+03
Coefficient C			-1.03825e+01
Coefficient D			8.36813e-06
Coefficient E			0.00000e+00
Temperature range, min.			237.49
Temperature range, max.			561.00
Pvap	0.24	kPa	237.49	Calculated Property
Pvap	2.96	kPa	273.44	Calculated Property
Pvap	18.38	kPa	309.38	Calculated Property
Pvap	72.99	kPa	345.33	Calculated Property
Pvap	213.97	kPa	381.27	Calculated Property
Pvap	508.21	kPa	417.22	Calculated Property
Pvap	1040.46	kPa	453.16	Calculated Property
Pvap	1916.26	kPa	489.11	Calculated Property
Pvap	3272.72	kPa	525.05	Calculated Property
Pvap	5298.45	kPa	561.00	Calculated Property
Pvap	[0.39; 162.68]	kPa	[242.33; 372.60]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.51629e+01
Coefficient B			-3.50405e+03
Coefficient C			-2.46700e+01
Reference			Pearce and Peters, 1929
Comment			Coefficents calculated by NIST from author's data.
Temperature range, min.			242.33
Temperature range, max.			372.60
Pvap	0.39	kPa	242.33	Calculated Property
Pvap	1.07	kPa	256.80	Calculated Property
Pvap	2.60	kPa	271.28	Calculated Property
Pvap	5.71	kPa	285.75	Calculated Property
Pvap	11.55	kPa	300.23	Calculated Property
Pvap	21.79	kPa	314.70	Calculated Property
Pvap	38.69	kPa	329.18	Calculated Property
Pvap	65.22	kPa	343.65	Calculated Property
Pvap	105.07	kPa	358.13	Calculated Property
Pvap	162.68	kPa	372.60	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ρl	[1330.51; 522.31]	kg/m3	[237.49; 561.00]	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			1.18177e+02
Coefficient B			2.70530e-01
Coefficient C			5.61610e+02
Coefficient D			2.91570e-01
Comment			Range stopped at Tc; ChemSep gives it to 561.6 K.
Temperature range, min.			237.49
Temperature range, max.			561.00
ρl	1330.51	kg/m3	237.49	Calculated Property
ρl	1281.51	kg/m3	273.44	Calculated Property
ρl	1230.02	kg/m3	309.38	Calculated Property
ρl	1175.45	kg/m3	345.33	Calculated Property
ρl	1116.90	kg/m3	381.27	Calculated Property
ρl	1053.00	kg/m3	417.22	Calculated Property
ρl	981.36	kg/m3	453.16	Calculated Property
ρl	897.20	kg/m3	489.11	Calculated Property
ρl	787.62	kg/m3	525.05	Calculated Property
ρl	522.31	kg/m3	561.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
γ	[0.04; 0.02]	N/m	[237.45; 356.65]	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			7.44358e-02
Coefficient B			-1.42800e-04
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Temperature range, min.			237.45
Temperature range, max.			356.65
γ	0.04	N/m	237.45	Calculated Property
γ	0.04	N/m	250.69	Calculated Property
γ	0.04	N/m	263.94	Calculated Property
γ	0.03	N/m	277.18	Calculated Property
γ	0.03	N/m	290.43	Calculated Property
γ	0.03	N/m	303.67	Calculated Property
γ	0.03	N/m	316.92	Calculated Property
γ	0.03	N/m	330.16	Calculated Property
γ	0.03	N/m	343.41	Calculated Property
γ	0.02	N/m	356.65	Calculated Property
γ	[0.04; 6.82e-04]	N/m	[237.49; 544.54]	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			-2.27070e-02
Coefficient B			7.47800e+01
Coefficient C			-2.95400e+00
Coefficient D			5.60540e-04
Coefficient E			-4.19540e-06
Temperature range, min.			237.49
Temperature range, max.			544.54
γ	0.04	N/m	237.49	Calculated Property
γ	0.04	N/m	271.61	Calculated Property
γ	0.03	N/m	305.72	Calculated Property
γ	0.03	N/m	339.84	Calculated Property
γ	0.02	N/m	373.96	Calculated Property
γ	0.02	N/m	408.07	Calculated Property
γ	0.01	N/m	442.19	Calculated Property
γ	0.01	N/m	476.31	Calculated Property
γ	0.00	N/m	510.42	Calculated Property
γ	6.82e-04	N/m	544.54	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λgas	[0.01; 0.06]	W/m×K	[237.49; 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			2.35920e-04
Coefficient B			9.39450e-01
Coefficient C			1.36860e+03
Coefficient D			2.37940e+04
Temperature range, min.			237.49
Temperature range, max.			1000.00
λgas	0.01	W/m×K	237.49	Calculated Property
λgas	0.01	W/m×K	322.21	Calculated Property
λgas	0.01	W/m×K	406.94	Calculated Property
λgas	0.02	W/m×K	491.66	Calculated Property
λgas	0.03	W/m×K	576.38	Calculated Property
λgas	0.03	W/m×K	661.11	Calculated Property
λgas	0.04	W/m×K	745.83	Calculated Property
λgas	0.05	W/m×K	830.55	Calculated Property
λgas	0.06	W/m×K	915.28	Calculated Property
λgas	0.06	W/m×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λliquid	[0.15; 0.08]	W/m×K	[244.26; 499.82]	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			1.59450e-02
Coefficient B			-1.10670e+02
Coefficient C			-7.40130e-01
Coefficient D			-3.26640e-03
Coefficient E			-5.07860e-07
Temperature range, min.			244.26
Temperature range, max.			499.82
λliquid	0.15	W/m×K	244.26	Calculated Property
λliquid	0.14	W/m×K	272.66	Calculated Property
λliquid	0.13	W/m×K	301.05	Calculated Property
λliquid	0.13	W/m×K	329.45	Calculated Property
λliquid	0.12	W/m×K	357.84	Calculated Property
λliquid	0.11	W/m×K	386.24	Calculated Property
λliquid	0.10	W/m×K	414.63	Calculated Property
λliquid	0.10	W/m×K	443.03	Calculated Property
λliquid	0.09	W/m×K	471.42	Calculated Property
λliquid	0.08	W/m×K	499.82	Calculated Property

Similar Compounds

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

Mixtures

• Methyl formate + Ethane, 1,2-dichloro-
• Ethyl formate + Ethane, 1,2-dichloro-
• Formic acid, propyl ester + Ethane, 1,2-dichloro-
• Formic acid, butyl ester + Ethane, 1,2-dichloro-
• Formic acid, pentyl ester + Ethane, 1,2-dichloro-
• Benzenamine, 4-methyl-2-nitro- + Ethane, 1,2-dichloro-
• Ethane, 1,2-dichloro- + Methane, nitro-
• 1-Propanol + Ethane, 1,2-dichloro-
• Propanoic acid, butyl ester + Ethane, 1,2-dichloro-
• Acetic acid, butyl ester + Ethane, 1,2-dichloro-
• Butanoic acid, butyl ester + Ethane, 1,2-dichloro-
• Ethane, 1,2-dichloro- + Phosphoramidic acid, phenyl-, diphenyl ester
• Ethyl Acetate + Ethane, 1,2-dichloro-
• Butanoic acid, ethyl ester + Ethane, 1,2-dichloro-
• Pentanoic acid, ethyl ester + Ethane, 1,2-dichloro-
• Propanoic acid, ethyl ester + Ethane, 1,2-dichloro-
• Ethane, 1,2-dichloro- + 1,4-Dioxane
• Benzene, bromo- + Benzene, chloro- + Ethane, 1,2-dichloro-
• Benzene, nitro- + Benzene, bromo- + Ethane, 1,2-dichloro-
• Benzene, nitro- + Benzene, chloro- + Ethane, 1,2-dichloro-

Find more mixtures with Ethane, 1,2-dichloro-.

Sources

• KDB Vapor Pressure Data
• Active Thermochemical Tables 1.112, gas-phase enthalpies of formation ChEDL chemicals 1.5.2, from Active Thermochemical Tables (ATcT), version 1.112, Argonne National Laboratory; Ruscic, B. et al. Active Thermochemical Tables: Thermochemistry for the 21st Century. J. Phys.: Conf. Ser. 2005, 16, 561.
• 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.
• 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
• Temperature and Pressure Dependence of the Volumetric Properties of Binary Liquid Mixtures Containing Dihaloalkanes
• 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
• Bubble points of some binary mixtures formed by o-cresol at 95.75 kPa
• Isobaric vapour liquid equilibria for binary mixtures of 1,2-dibromoethane with 1,2-dichloroethane, trichloromethane, and 1,1,2,2-tetrachloroethane at atmospheric pressure
• Excess Gibbs energies of selected binary mixtures formed by N,N-dimethyl formamide at 95.5 kPa
• Co-solvent effects in LLE of 1-hydroxyethyl-3-methylimidazolium based ionic liquids + 2-propanol + dichloromethane or 1,2-dichloroethane
• A simple apparatus for data solubility determination
• Vapour pressure and excess Gibbs energy of binary 1,2-dichloroethane + cyclohexanone, chloroform + cyclopentanone and chloroform + cyclohexanone mixtures at temperatures from 298.15 to 318.15 K
• Isothermal vapour liquid equilibria of binary systems of 1,2-dichloroethane with ethers
• Vapor-liquid equilibrium and excess Gibbs energies of some binary mixtures of acrylonitrile at 95.5 kPa
• Isothermal vapour liquid equilibria for 1,2-dichloroethane + nitromethane and + nitroethane binary systems at temperatures between 333.15 and 353.15K
• Using binary mixtures of dicationic ionic liquids for determination ofactivity coefficients at infinite dilution by gas-liquid chromatography
• Determination and correlation of solubilities of 1,2-bis(2-oxo-5,5-dimethyl-1,3,2-dioxyphosphacyclohexyl-2-imino) ethane in selected solvents
• tert-Butyl chloride as a probe of the solvophobic effects
• Speeds of sound, isentropic compressibilities and refractive indices for some binary mixtures of nitromethane with chloroalkane at temperatures from 298.15 to 318.15 K. Comparison with theories
• Solid-liquid equilibrium of diphenyl anilinophosphonate in the different organic solvents
• Hydrogen bond interactions in the blends of 1,4-dioxane with some 1, 2- disubstituted ethanes at T = (298.15, 308.15 and 318.15) K
• Measurements of activity coefficients at infinite dilution for organic solutes in two quaternary ammonium-based ionic liquids [DDA][ClO4] and [DDA][BF4]
• (Vapor + liquid) equilibria for the binary mixtures (1-propanol + dibromomethane, or + bromochloromethane, or + 1,2-dichloroethane or +1-bromo-2-chloroethane) at T = 313.15 K.
• Excess volumes and speeds of sound of mixtures of 1,2-dibromoethane with chlorinated ethanes and ethenes at 303.15 K
• Thermodynamic study of (alkyl esters + a,x-alkyl dihalides) I: HE and V E for 25 binary mixtures {xCu-1H2u-1CO2C2H5 + (1-x)a,x-ClCH2(CH2)v-2CH2Cl}, where u = 1 to 5, a = 1 and v = x = 2 to 6
• Isothermal (vapour + liquid) equilibria in the binary mixtures (1,2-dichloroethane and 1,1,1-trichloroethane with cyclopentanone) within the temperature range (298.15 to 313.15) K
• Thermodynamic study of (alkyl esters + a,x-alkyl dihalides)III. HE m and V E m for 20 binary mixtures {xCu-1H2u-1CO2C4H9 + (1 - x)a,x-ClCH2(CH2)v-2CH2Cl}, where u = 1 to 4, a = 1 and v = x = 2 to 6
• 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
• Thermodynamic study of (alkyl esters + a,x-alkyl dihalides) V. Hex and Vex for 25 binary mixtures {xCu-1H2u-1CO2CH3 + (1-x)a,x-ClCH2(CH2)v-2CH2Cl}, where u = 1 to 5, a = 1 and v = x = 2 to 6
• Isobaric (vapour + liquid) equilibria data for the binary systems {1,2-dichloroethane (1) + toluene (2)} and {1,2-dichloroethane (1) + acetic acid (2)} at atmospheric pressure
• Activity coefficients and excess Gibbs free energy of some binary mixtures formed by p-cresol at 95.23 kPa
• Excess molar enthalpies and (vapour + liquid) equilibria for mixtures containing N,N-dialkylamides and a,x-dichloroalkanes
• Excess enthalpies and isothermal (vapour + liquid) equilibria of (1-methyl-2-pyrrolidone + 1-chloroalkane or +,?-dichloroalkane) mixtures
• Thermodynamic study of (alkyl esters + a,x-alkyl dihalides) VII. HE m and VE m for 20 binary mixtures {xCu 1H2u 1CO2C3H7 + (1 x)a,x-ClCH2(CH2)v 2CH2Cl}, where u = 1 to 4, a = 1 and v = x = 2 to 6. An analysis of behavior using the COSMO-RS methodology
• Studies on thermodynamic properties of binary mixtures of hexan-1-ol with halogenated compounds at T = (308.15 and 313.15) K
• Thermophysical and sonochemical behaviour of binary mixtures of decan-1-ol with halohydrocarbons at (T = 293.15 and 313.15) K
• Activity coefficient at infinite dilution measurements for organic solutes (polar and non-polar) in fatty compounds: Saturated fatty acids
• Activity coefficient at infinite dilution measurements for organic solutes (polar and non-polar) in fatty compounds Part II: C18 fatty acids
• (Liquid + liquid) equilibria of quaternary systems containing water, phosphoric acid, dichloromethane and 1,2-dichloroethane
• Activity coefficients at infinite dilution of organic solutes in 1-hexyl-3- methylimidazolium trifluoroacetate and influence of interfacial adsorption using gas liquid chromatography
• Salting-out effect on the (liquid + liquid) equilibrium for the ternary systems (water + phosphoric acid + dichloromethane or 1,2-dichloroethane)
• Solvation parameter model and thermodynamic parameters in a dicationic ionic liquid based on pyrrolidinium
• Theoretical and experimental study on volumetric and electromagnetic properties of binary systems consisting of 1,2-dichloroethane with benzene and its derivatives at T = (293.15 to 333.15) K
• Solubility of 4-methyl-2-nitroaniline in fourteen organic solvents from T = (278.15 to 313.15) K and mixing properties of solutions
• Influence of chlorine atom on interactions between halo-hydrocarbons and 1-nonanol: Density and speed of sound measurements
• The additivity of surface and volumetric properties of alpha,omega-dihalogenoalkanes
• Excess molar enthalpies of dimethylsulfoxide with chloroethanes and chloroethenes at 298.15K
• Volumetric properties of binary liquid mixtures of alcohols with 1,2-dichloroethane at different temperatures and atmospheric pressure
• Volumetric properties of binary liquid mixtures of ketones with chloroalkanes at different temperatures and atmospheric pressure
• Volumetric and electromagnetic properties of binary mixtures consist of benzene derivatives at different temperature and ternary mixtures with 1,2-dichloroethane at T = 293.15 K with application of the Prigogine-Flory-Patterson theory and PC-SAFT
• Solubility Measurement and Correlation for e-2,4,6,8,10,12-Hexanitro-2,4,6,8,10,12-hexaazaisowurtzitane in Five Organic Solvents at Temperatures between 283.15 and 333.15 K and Different Chloralkane + Ethyl Acetate Binary Solvents at Temperatures between 283.15 and 323.15 K
• Solubility Measurement and the Correlation of 1-Naphthaleneacetic Acid in Pure and Methanol + Water Binary Solvents from T = (278.25 to 323.55) K
• Solid Liquid Phase Equilibrium of N,N'-Piperazinebis(neopentylglycol)phosphoramidate in Selected Solvents from T = (293.15 to 333.15) K
• Synthesis and Solubility of 5,5-Dimethyl-2-(phenyl(phenylamino)methyl)-1,3,2-dioxaphosphinane 2-oxide in Selected Solvents between 278.15 K and 347.15 K
• Measurement and Correlation of Solubility of Resorcinol Bis(cyclic 2,2-dimethyl-1,3-propanediol phosphate) in Selected Solvents from T = 293.15 to 333.15 K
• Solubility Measurement and Thermodynamic Modeling of N-(4-Methylphenyl-Z-3-chloro-2-(phenylthio)propenamide in 12 Pure Solvents at Temperatures Ranging from 278.15 to 318.15 K
• Solution Thermodynamics of Benzotriazole in Different Pure Solvents
• Isothermal Vapor-Liquid Equilibria and Excess Gibbs Energies for Binary Mixtures of Cyclic Ethers with 1,2-Dichloroethane
• Densities and Excess Molar Volumes for the Binary and Ternary Systems of (1,4-Dioxane, 1-Propanol or 2-Propanol, and 1,2-Dichloroethane) at T = (288.15 to 318.15) K. Experimental Measurements and Prigogine-Flory-Patterson Modeling
• Isobaric Vapor-Liquid Equilibrium for the Binary Systems of 1,2-Dichloroethane + sec-Butyl Acetate, n-Propyl Acetate, and tert-Butyl Acetate at 101.3 kPa
• Physico-Chemical Properties of LiFSI Solutions I. LiFSI with Valeronitrile, Dichloromethane, 1,2-Dichloroethane, and 1,2-Dichlorobenzene
• Thermodynamic Parameters of a New Synthesized Tricationic Ionic Liquid Stationary Phase by Inverse Gas Chromatography
• Thermodynamic Studies of Solubility for Naphthalene in 12 Solvents from 279 to 330 K
• Measurement and Correlation of Solubilities of 5,5'-Dinitramino-3,3'-bi[1,2,4-triazolate] Carbohydrazide Salt (CBNT) in Various Pure Solvents and a Binary Mixture (Dimethyl Sulfoxide + Water) from 298.15 to 343.15 K
• Determination and Correlation of Solubilities of 1,3,5-Trifluoro-2,4,6-triiodobenzene in Different Solvents from 289.25 to 332.15 K
• Isobaric Vapor Liquid Equilibrium Data for the 1,2-Dichloroethane-1-Butanol System
• Heat Capacities of alpha,omega-Dichloroalkanes at Temperatures from 284.15 K to 353.15 K and a Group Additivity Analysis
• Vapor-Liquid Equilibria and Excess Molar Enthalpies for N-Methyl-2-pyrrolidone with Chloroethanes and Chloroethenes
• 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
• Isothermal Vapor-Liquid Equilibria of ethyl acetate + dibromomethane, or + bromochloromethane or + 1,2-dichloroethane or +1-bromo-2-chloroethane at T = 313.15 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 Partitioning Coefficients of Numerous Organic Solutes between a Long-Chain Aliphatic Alcohol and the Gas Phase as a Function of Temperature
• 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
• Activity Coefficients at Infinite Dilution in 1-Alkyl-3-methylimidazolium Tetrafluoroborate Ionic Liquids
• Measurement and Correlation of Griseofulvin Solubility in Different Solvents at Temperatures from (281.95 to 357.60) K
• Solubilities of 2,4-Dinitro-l-phenylalanine in Monosolvents at (273.15 to 368.15) K
• Thermophysical properties of the binary mixtures of 1,2-Dichloroethane with Chlorobenzene and Bromobenzene from 298.15 to 313.15 K
• Solubilities of (a,Z)-2-Amino-a-(methoxyimino)-4-thiazoleethanethioic Acid S-2-Benzothiazolyl Ester in Different Pure Solvents and Binary Mixtures of Tetrahydrofuran + Dichloromethane or 1,2-Dichloroethane
• Activity Coefficients at Infinite Dilution in Methylimidazolium Nitrate Ionic Liquids
• Measurement and Correlation of the Solubility of Prednisone Acetate in Different Solvents
• Volumetric Properties of Binary Mixtures of 1,2-Dichloroethane with Polyethers from (283.15 to 333.15) K and at Atmospheric Pressure
• Solubilities of Tris(o-phenylenedioxy)cyclotriphosphazene in Selected Solvents
• Determination of Gas Concentrations in Liquids by Nuclear Magnetic Resonance: Hydrogen in Organic Solvents
• Solubilities of 3-Methoxy-N-phenylaniline and 3-(Methylthio)-N-phenylaniline in Five Organic Solvents (285 K to 333.75 K)
• Determination of Henry's Law Constants Using Internal Standards with Benchmark Values
• Volumetric Study for the Binary Nitromethane with Chloroalkane Mixtures at Temperatures in the Range (298.15 to 318.15) K
• Solubilities of 1,3,2-Dioxaphosphorinane-2-methanol-a,a-5,5-tetramethyl 2-oxide in Selected Solvents at 273.15 K to 343.15 K
• Solubilities of 1,3,2-Dioxaphosphorinane-2-methanol-a,5,5-trimethyl-a-phenyl-2-oxide in Selected Solvents between 278.15 K and 343.15 K
• Determination and Correlation of Solubilities of 2-Isopropylthioxanthone (ITX) in Seven Different Solvents from (299.15 to 329.85) K
• Densities and Isothermal Compressibilities at Pressures up to 20 MPa of the Systems N,N-Dimethylformamide or N,N-Dimethylacetamide + r,o-Dichloroalkane
• Densities and Isothermal Compressibilities at Pressures up to 20 MPa of the Systems 1-Methyl-2-pyrrolidone + 1-Chloroalkane or + r,u-Dichloroalkane
• Solubility of Imidacloprid in Different Solvents
• Isobaric Vapor Liquid Equilibrium for Dimethylsulfoxide with Chloroethanes and Chloroethenes
• Solubility of Enrofloxacin Sodium in Various Solvents at Various Temperatures
• Solubility of Canthaxanthin in Pure Solvents from (293.15 to 343.15) K
• Vapor-Liquid Equilibria of Binary Mixtures Formed by Hexan-1-ol with Chloroethanes and Chloroethenes at 95.6 kPa
• Densities and Viscosities of (1-Propanol + 1,2-Dichloroethane), (1-Propanol + Benzaldehyde), (Benzaldehyde + 1,2-Dichloroethane), and (1-Propanol + 1,2-Dichloroethane + Benzaldehyde) Mixtures from T = 288.15 K to 313.15 K
• Studies on Transport and Thermodynamic Properties of Binary Mixtures of Hexan-1-ol with Halogenated Compounds at 293.15 K
• Densities and Excess Molar Volumes of the Binary Mixtures of Cyclohexanone with Chloroalkanes at Temperatures between (288.15 and 318.15) 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
• Densities and Excess Molar Volumes of the Binary Mixtures of Cyclopentanone with Chloroalkanes at T = (288.15, 298.15, 308.15, and 318.15) K
• Joback Method
• KDB
• Aqueous Solubility Prediction Method
• Estimated Solubility Method
• McGowan Method
• NIST Webbook
• The Yaws Handbook of Vapor Pressure

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