Chemical Properties of Ethene, chloro- (CAS 75-01-4)

InChI

InChI=1S/C2H3Cl/c1-2-3/h2H,1H2

InChI Key

BZHJMEDXRYGGRV-UHFFFAOYSA-N

Formula

C2H3Cl

SMILES

C=CCl

Molecular Weight¹

62.50

CAS

75-01-4

Other Names

• C2H3Cl
• Chlorethene
• Chlorethylene
• Chloroethylene
• Chlorure de vinyle
• Cloruro di vinile
• Ethylene monochloride
• Ethylene, chloro-
• Monochloroethene
• Monochloroethylene
• Rcra waste number U043
• Trovidur
• UN 1086
• VC
• VCM
• Vinyl C monomer
• Vinyl chloride monomer
• Vinylchlorid
• Vinyle(chlorure de)
• Winylu chlorek
• chloroethene
• vinyl chloride

• ω : Acentric Factor.
• T_ig : Autoignition Temperature (K).
• 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).
• LFL : Lower Flammability Limit (% in Air).
• UFL : Upper Flammability Limit (% in Air).
• T_flash,cc : Flash Point (Closed Cup Method) (K).
• Δ_fG° : Standard Gibbs free energy of formation (kJ/mol).
• Δ_fH°_gas : Enthalpy of formation at standard conditions (kJ/mol).
• Δ_fH°_liquid : Liquid phase enthalpy of formation at standard conditions (kJ/mol).
• Δ_fusH° : Enthalpy of fusion at standard conditions (kJ/mol).
• Δ_fusH : Enthalpy of fusion at a given temperature (kJ/mol).
• Δ_vapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
• Δ_vapH : Enthalpy of vaporization at a given temperature (kJ/mol).
• IE : Ionization energy (eV).
• log₁₀WS : Log10 of Water solubility in mol/l.
• logP_oct/wat : Octanol/Water partition coefficient.
• McVol : McGowan's characteristic volume (ml/mol).
• NFPA Fire : NFPA Fire Rating.
• NFPA Health : NFPA Health Rating.
• NFPA Safety : NFPA Safety Rating.
• P_c : Critical Pressure (kPa).
• P_triple : Triple Point Pressure (kPa).
• P_vap : Vapor pressure (kPa).
• ρ_l : Liquid Density (kg/m³).
• I_np : Non-polar retention indices.
• I_p : Polar retention indices.
• Δ_fusS : Entropy of fusion at a given temperature (J/mol×K).
• S°_liquid : Liquid phase molar entropy at standard conditions (J/mol×K).
• γ : Surface Tension (N/m).
• T_boil : Normal Boiling Point Temperature (K).
• T_c : Critical Temperature (K).
• λ_gas : Gas thermal conductivity (W/m×K).
• λ_liquid : Liquid thermal conductivity (W/m×K).
• T_fus : Normal melting (fusion) point (K).
• T_triple : Triple Point Temperature (K).
• U_Qi : UNIQUAC Qi Parameter.
• U_Ri : UNIQUAC Ri Parameter.
• V_c : Critical Volume (m³/kmol).
• Z_c : Critical Compressibility.
• Z_ra : Rackett Parameter.
• ¹: Molecular weight from the IUPAC atomic weights tables.

Physical Properties

Property	Value	Unit	Source
ω	[0.1001; 0.1220]
ω	0.1001		ChemSep v8.3 pure component data Compiled value
ω	0.1220		KDB
Tig	745.37	K	KDB
μ	[1.45; 1.45]	debye
μ	1.45	debye	ChemSep v8.3 pure component data Compiled value
μ	1.45	debye	KDB
LFL	4.00	% in Air	KDB
UFL	26.00	% in Air	KDB
Tflash,cc	194.26	K	KDB
ΔfG°	[41.95; 51.54]	kJ/mol
ΔfG°	41.95	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfG°	51.54	kJ/mol	KDB
ΔfH°gas	[21.00; 38.10]	kJ/mol
ΔfH°gas	28.45	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfH°gas	35.17	kJ/mol	KDB
ΔfH°gas	22.00 ± 3.00	kJ/mol	NIST
ΔfH°gas	29.00	kJ/mol	NIST
ΔfH°gas	21.00	kJ/mol	NIST
ΔfH°gas	35.30 ± 1.40	kJ/mol	NIST
ΔfH°gas	38.10 ± 0.84	kJ/mol	NIST
ΔfH°liquid	0.90 ± 3.20	kJ/mol	NIST
ΔfusH°	3.85	kJ/mol	Joback Calculated Property
ΔvapH°	21.00 ± 1.00	kJ/mol	NIST
IE	[9.98; 10.20]	eV
IE	9.99 ± 0.02	eV	NIST
IE	9.98 ± 0.02	eV	NIST
IE	9.99 ± 0.02	eV	NIST
IE	10.01	eV	NIST
IE	10.00	eV	NIST
IE	10.00 ± 0.01	eV	NIST
IE	10.00 ± 0.01	eV	NIST
IE	10.00 ± 0.02	eV	NIST
IE	10.00 ± 0.01	eV	NIST
IE	9.99	eV	NIST
IE	10.00 ± 0.01	eV	NIST
IE	Outlier 10.20	eV	NIST
IE	Outlier 10.20	eV	NIST
IE	10.15	eV	NIST
log10WS	[-1.75; -1.75]
log10WS	-1.75		Aq. Solubility Prediction
log10WS	-1.75		Estimated Solubility
logPoct/wat	1.369		Crippen Calculated Property
McVol	46.980	ml/mol	McGowan Calculated Property
NFPA Fire	4		KDB
NFPA Health	2		KDB
NFPA Safety	2		KDB
Pc	[5155.00; 5670.00]	kPa
Pc	5670.00	kPa	ChemSep v8.3 pure component data Compiled value
Pc	5155.00	kPa	KDB
Ptriple	1.92e-05	kPa	ChemSep v8.3 pure component data Compiled value
Inp	[353.00; 378.00]
Inp	362.00		NIST
Inp	363.00		NIST
Inp	364.00		NIST
Inp	366.00		NIST
Inp	366.00		NIST
Inp	Outlier 378.00		NIST
Inp	353.00		NIST
Inp	353.00		NIST
Inp	366.00		NIST
Ip	[505.00; 603.00]
Ip	603.00		NIST
Ip	505.00		NIST
Ip	603.00		NIST
S°liquid	118.00	J/mol×K	NIST
Tboil	[259.05; 259.45]	K
Tboil	259.25	K	ChemSep v8.3 pure component data Compiled value
Tboil	259.35	K	KDB
Tboil	259.35	K	NIST
Tboil	259.45 ± 0.20	K	NIST
Tboil	259.05 ± 0.40	K	NIST
Tboil	259.30 ± 0.20	K	NIST
Tc	[424.61; 432.00]	K
Tc	432.00	K	ChemSep v8.3 pure component data Compiled value
Tc	424.61	K	KDB
Tfus	[94.43; 119.45]	K
Tfus	119.36	K	ChemSep v8.3 pure component data Compiled value
Tfus	119.40	K	KDB
Tfus	119.45	K	Aq. Solubility Prediction
Tfus	119.35	K	NIST
Tfus	Outlier 94.43 ± 0.10	K	NIST
Tfus	119.36 ± 0.02	K	NIST
Tfus	113.50 ± 0.20	K	NIST
Ttriple	[119.31; 119.36]	K
Ttriple	119.36	K	ChemSep v8.3 pure component data Compiled value
Ttriple	119.31 ± 0.02	K	NIST
Ttriple	119.31 ± 0.02	K	NIST
UQi	1.49		ChemSep v8.3 pure component data Compiled value
URi	1.91		ChemSep v8.3 pure component data Compiled value
Vc	0.179	m3/kmol	ChemSep v8.3 pure component data Compiled value
Zc	0.2830000		ChemSep v8.3 pure component data Compiled value
Zra	0.28		ChemSep v8.3 pure component data Compiled value

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	89.45	J/mol×K	298.15	NIST
Csat	[84.96; 89.83]	J/mol×K	[120.00; 300.00]
Csat	84.96	J/mol×K	120.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Csat	85.01	J/mol×K	130.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Csat	85.04	J/mol×K	140.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Csat	85.06	J/mol×K	150.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Csat	85.06	J/mol×K	160.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Csat	85.06	J/mol×K	170.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Csat	85.05	J/mol×K	180.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Csat	85.05	J/mol×K	190.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Csat	85.05	J/mol×K	200.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Csat	85.07	J/mol×K	210.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Csat	85.10	J/mol×K	220.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Csat	85.16	J/mol×K	230.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Csat	85.24	J/mol×K	240.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Csat	85.37	J/mol×K	250.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Csat	85.62	J/mol×K	260.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Csat	86.10	J/mol×K	270.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Csat	86.32	J/mol×K	273.15	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Csat	86.90	J/mol×K	280.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Csat	88.11	J/mol×K	290.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Csat	89.47	J/mol×K	298.15	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Csat	89.83	J/mol×K	300.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
ΔfusH	[4.92; 4.92]	kJ/mol	[119.30; 119.31]
ΔfusH	4.92	kJ/mol	119.30	NIST
ΔfusH	4.92	kJ/mol	119.30	NIST
ΔfusH	4.92	kJ/mol	119.31	NIST
ΔfusH	4.92	kJ/mol	119.31	NIST
ΔvapH	[22.26; 23.30]	kJ/mol	[234.50; 265.50]
ΔvapH	23.30	kJ/mol	234.50	NIST
ΔvapH	22.90	kJ/mol	243.00	NIST
ΔvapH	22.26	kJ/mol	259.40	KDB
ΔvapH	22.70	kJ/mol	265.50	NIST
Pvap	[172.00; 601.50]	kPa	[273.10; 313.15]
Pvap	172.00	kPa	273.10	Vapor-Liquid Equilibria on Seven Binary Systems: Ethylene Oxide + 2-Methylpropane; Acetophenone + Phenol; cis-1,3-Dichloropropene + 1,2-Dichloropropane; 1,5-Hexadiene + Allyl Chloride; Isopropyl Acetate + Acetonitrile; Vinyl Chloride + Methyl Chloride; and 1,4-Butanediol + c-Butyrolactone
Pvap	601.50	kPa	313.15	Vapor-Liquid Equilibria on Seven Binary Systems: Ethylene Oxide + 2-Methylpropane; Acetophenone + Phenol; cis-1,3-Dichloropropene + 1,2-Dichloropropane; 1,5-Hexadiene + Allyl Chloride; Isopropyl Acetate + Acetonitrile; Vinyl Chloride + Methyl Chloride; and 1,4-Butanediol + c-Butyrolactone
ρl	969.00	kg/m3	259.00	KDB
ΔfusS	[41.20; 41.20]	J/mol×K	[119.31; 119.31]
ΔfusS	41.20	J/mol×K	119.31	NIST
ΔfusS	41.20	J/mol×K	119.31	NIST

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[44.11; 114.49]	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			3.90130e+01
Coefficient B			-6.67910e+02
Coefficient C			5.02724e+00
Coefficient D			-3.08950e-04
Coefficient E			9.12450e-08
Comment			ChemSep eq 16, IdealGasHeatCapacityCp
Temperature range, min.			200.00
Temperature range, max.			1500.00
Cp,gas	44.11	J/mol×K	200.00	Calculated Property
Cp,gas	58.95	J/mol×K	344.44	Calculated Property
Cp,gas	73.20	J/mol×K	488.89	Calculated Property
Cp,gas	84.33	J/mol×K	633.33	Calculated Property
Cp,gas	92.71	J/mol×K	777.78	Calculated Property
Cp,gas	99.09	J/mol×K	922.22	Calculated Property
Cp,gas	104.08	J/mol×K	1066.67	Calculated Property
Cp,gas	108.10	J/mol×K	1211.11	Calculated Property
Cp,gas	111.50	J/mol×K	1355.56	Calculated Property
Cp,gas	114.49	J/mol×K	1500.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[55.51; 121.54]	J/mol×K	[200.00; 400.00]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A + exp(B/T + C + D·T + E·T²) Y is Cp,liquid in J/mol×K, T in K
Coefficient A			2.99280e+01
Coefficient B			1.67460e+02
Coefficient C			-1.26916e+00
Coefficient D			2.33190e-02
Coefficient E			-2.47470e-05
Comment			ChemSep eq 16, LiquidHeatCapacityCp
Temperature range, min.			200.00
Temperature range, max.			400.00
Cp,liquid	55.51	J/mol×K	200.00	Calculated Property
Cp,liquid	61.25	J/mol×K	222.22	Calculated Property
Cp,liquid	67.92	J/mol×K	244.44	Calculated Property
Cp,liquid	75.42	J/mol×K	266.67	Calculated Property
Cp,liquid	83.54	J/mol×K	288.89	Calculated Property
Cp,liquid	92.02	J/mol×K	311.11	Calculated Property
Cp,liquid	100.49	J/mol×K	333.33	Calculated Property
Cp,liquid	108.54	J/mol×K	355.56	Calculated Property
Cp,liquid	115.70	J/mol×K	377.78	Calculated Property
Cp,liquid	121.54	J/mol×K	400.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.0024991; 0.0000856]	Pa×s	[130.00; 400.00]	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			-3.58600e+00
Coefficient B			3.86190e+02
Coefficient C			-1.10140e+00
Coefficient D			-9.11640e-07
Coefficient E			2.00000e+00
Comment			ChemSep eq 101, LiquidViscosity
Temperature range, min.			130.00
Temperature range, max.			400.00
η	0.0024991	Pa×s	130.00	Calculated Property
η	0.0011301	Pa×s	160.00	Calculated Property
η	0.0006328	Pa×s	190.00	Calculated Property
η	0.0004035	Pa×s	220.00	Calculated Property
η	0.0002803	Pa×s	250.00	Calculated Property
η	0.0002067	Pa×s	280.00	Calculated Property
η	0.0001591	Pa×s	310.00	Calculated Property
η	0.0001265	Pa×s	340.00	Calculated Property
η	0.0001031	Pa×s	370.00	Calculated Property
η	0.0000856	Pa×s	400.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ΔvapH	[31.16; 7.93]	kJ/mol	[119.36; 415.55]	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			2.65810e+01
Coefficient B			-2.11890e+00
Coefficient C			8.30300e+00
Coefficient D			-9.85510e+00
Coefficient E			4.06850e+00
Critical temperature, Tc (K)			4.32000e+02
Comment			ChemSep eq 106, HeatOfVaporization
Temperature range, min.			119.36
Temperature range, max.			415.55
ΔvapH	31.16	kJ/mol	119.36	Calculated Property
ΔvapH	29.48	kJ/mol	152.27	Calculated Property
ΔvapH	27.34	kJ/mol	185.18	Calculated Property
ΔvapH	25.05	kJ/mol	218.09	Calculated Property
ΔvapH	22.80	kJ/mol	251.00	Calculated Property
ΔvapH	20.64	kJ/mol	283.91	Calculated Property
ΔvapH	18.49	kJ/mol	316.82	Calculated Property
ΔvapH	16.09	kJ/mol	349.73	Calculated Property
ΔvapH	12.97	kJ/mol	382.64	Calculated Property
ΔvapH	7.93	kJ/mol	415.55	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.69]	kPa	[187.41; 277.61]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.38927e+01
Coefficient B			-2.09601e+03
Coefficient C			-3.33500e+01
Temperature range, min.			187.41
Temperature range, max.			277.61
Pvap	1.33	kPa	187.41	Calculated Property
Pvap	3.06	kPa	197.43	Calculated Property
Pvap	6.38	kPa	207.45	Calculated Property
Pvap	12.30	kPa	217.48	Calculated Property
Pvap	22.13	kPa	227.50	Calculated Property
Pvap	37.59	kPa	237.52	Calculated Property
Pvap	60.77	kPa	247.54	Calculated Property
Pvap	94.12	kPa	257.57	Calculated Property
Pvap	140.40	kPa	267.59	Calculated Property
Pvap	202.69	kPa	277.61	Calculated Property
Pvap	[1.47e-04; 5260.95]	kPa	[119.36; 432.00]	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			2.35953e+01
Coefficient B			-3.20411e+03
Coefficient C			-1.15716e+00
Coefficient D			-3.15182e-06
Coefficient E			2.00000e+00
Comment			ChemSep eq 101, VaporPressure
Temperature range, min.			119.36
Temperature range, max.			432.00
Pvap	1.47e-04	kPa	119.36	Calculated Property
Pvap	0.04	kPa	154.10	Calculated Property
Pvap	1.57	kPa	188.84	Calculated Property
Pvap	17.23	kPa	223.57	Calculated Property
Pvap	95.00	kPa	258.31	Calculated Property
Pvap	336.26	kPa	293.05	Calculated Property
Pvap	879.20	kPa	327.79	Calculated Property
Pvap	1851.09	kPa	362.52	Calculated Property
Pvap	3318.63	kPa	397.26	Calculated Property
Pvap	5260.95	kPa	432.00	Calculated Property
Pvap	[1.65e-05; 5873.76]	kPa	[119.36; 432.00]	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			9.48913e+01
Coefficient B			-5.42760e+03
Coefficient C			-1.26907e+01
Coefficient D			1.80238e-05
Coefficient E			0.00000e+00
Temperature range, min.			119.36
Temperature range, max.			432.00
Pvap	1.65e-05	kPa	119.36	Calculated Property
Pvap	0.02	kPa	154.10	Calculated Property
Pvap	1.32	kPa	188.84	Calculated Property
Pvap	17.50	kPa	223.57	Calculated Property
Pvap	99.05	kPa	258.31	Calculated Property
Pvap	340.45	kPa	293.05	Calculated Property
Pvap	862.76	kPa	327.79	Calculated Property
Pvap	1809.24	kPa	362.52	Calculated Property
Pvap	3375.42	kPa	397.26	Calculated Property
Pvap	5873.76	kPa	432.00	Calculated Property
Pvap	[0.14; 101.54]	kPa	[165.30; 259.40]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.37832e+01
Coefficient B			-2.05565e+03
Coefficient C			-3.50510e+01
Reference			McDonald, Shrader, et al., 1959, 2
Temperature range, min.			165.30
Temperature range, max.			259.40
Pvap	0.14	kPa	165.30	Calculated Property
Pvap	0.44	kPa	175.76	Calculated Property
Pvap	1.20	kPa	186.21	Calculated Property
Pvap	2.90	kPa	196.67	Calculated Property
Pvap	6.28	kPa	207.12	Calculated Property
Pvap	12.44	kPa	217.58	Calculated Property
Pvap	22.90	kPa	228.03	Calculated Property
Pvap	39.59	kPa	238.49	Calculated Property
Pvap	64.88	kPa	248.94	Calculated Property
Pvap	101.54	kPa	259.40	Calculated Property
Pvap	[0.14; 101.54]	kPa	[165.30; 259.40]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.37832e+01
Coefficient B			-2.05565e+03
Coefficient C			-3.50510e+01
Reference			McDonald, Shrader, et al., 1959
Temperature range, min.			165.30
Temperature range, max.			259.40
Pvap	0.14	kPa	165.30	Calculated Property
Pvap	0.44	kPa	175.76	Calculated Property
Pvap	1.20	kPa	186.21	Calculated Property
Pvap	2.90	kPa	196.67	Calculated Property
Pvap	6.28	kPa	207.12	Calculated Property
Pvap	12.44	kPa	217.58	Calculated Property
Pvap	22.90	kPa	228.03	Calculated Property
Pvap	39.59	kPa	238.49	Calculated Property
Pvap	64.88	kPa	248.94	Calculated Property
Pvap	101.54	kPa	259.40	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ρl	[1154.83; 597.12]	kg/m3	[119.36; 415.55]	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			9.30099e+01
Coefficient B			2.68660e-01
Coefficient C			4.32000e+02
Coefficient D			2.69300e-01
Comment			ChemSep eq 105, LiquidDensity
Temperature range, min.			119.36
Temperature range, max.			415.55
ρl	1154.83	kg/m3	119.36	Calculated Property
ρl	1114.50	kg/m3	152.27	Calculated Property
ρl	1072.14	kg/m3	185.18	Calculated Property
ρl	1027.28	kg/m3	218.09	Calculated Property
ρl	979.29	kg/m3	251.00	Calculated Property
ρl	927.16	kg/m3	283.91	Calculated Property
ρl	869.27	kg/m3	316.82	Calculated Property
ρl	802.63	kg/m3	349.73	Calculated Property
ρl	720.41	kg/m3	382.64	Calculated Property
ρl	597.12	kg/m3	415.55	Calculated Property

Property	Value	Unit	Temperature (K)	Source
γ	[0.05; 8.39e-04]	N/m	[119.36; 415.55]	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			-2.25240e-02
Coefficient B			7.05610e-01
Coefficient C			-2.40280e+00
Coefficient D			-1.92150e-03
Coefficient E			-3.22560e-06
Comment			ChemSep eq 16, SurfaceTension
Temperature range, min.			119.36
Temperature range, max.			415.55
γ	0.05	N/m	119.36	Calculated Property
γ	0.04	N/m	152.27	Calculated Property
γ	0.03	N/m	185.18	Calculated Property
γ	0.03	N/m	218.09	Calculated Property
γ	0.02	N/m	251.00	Calculated Property
γ	0.02	N/m	283.91	Calculated Property
γ	0.01	N/m	316.82	Calculated Property
γ	0.01	N/m	349.73	Calculated Property
γ	0.00	N/m	382.64	Calculated Property
γ	8.39e-04	N/m	415.55	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λgas	[0.00; 0.08]	W/m×K	[119.36; 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			-2.60510e+02
Coefficient B			5.86230e-01
Coefficient C			-1.78380e+08
Coefficient D			-1.66910e+09
Comment			ChemSep eq 102, VaporThermalConductivity
Temperature range, min.			119.36
Temperature range, max.			1000.00
λgas	0.00	W/m×K	119.36	Calculated Property
λgas	0.01	W/m×K	217.21	Calculated Property
λgas	0.01	W/m×K	315.06	Calculated Property
λgas	0.02	W/m×K	412.91	Calculated Property
λgas	0.03	W/m×K	510.76	Calculated Property
λgas	0.04	W/m×K	608.60	Calculated Property
λgas	0.05	W/m×K	706.45	Calculated Property
λgas	0.06	W/m×K	804.30	Calculated Property
λgas	0.07	W/m×K	902.15	Calculated Property
λgas	0.08	W/m×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λliquid	[0.19; 0.08]	W/m×K	[119.36; 377.59]	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			6.03410e-02
Coefficient B			1.55360e+02
Coefficient C			-4.67850e+00
Coefficient D			1.55230e-02
Coefficient E			-3.81650e-05
Comment			ChemSep eq 16, LiquidThermalConductivity
Temperature range, min.			119.36
Temperature range, max.			377.59
λliquid	0.19	W/m×K	119.36	Calculated Property
λliquid	0.17	W/m×K	148.05	Calculated Property
λliquid	0.17	W/m×K	176.74	Calculated Property
λliquid	0.16	W/m×K	205.44	Calculated Property
λliquid	0.14	W/m×K	234.13	Calculated Property
λliquid	0.13	W/m×K	262.82	Calculated Property
λliquid	0.12	W/m×K	291.51	Calculated Property
λliquid	0.10	W/m×K	320.21	Calculated Property
λliquid	0.09	W/m×K	348.90	Calculated Property
λliquid	0.08	W/m×K	377.59	Calculated Property

Similar Compounds

Find more compounds similar to Ethene, chloro-.

Mixtures

• Chloromethane + Ethene, chloro-
• Ethene, chloro- + Water

Sources

• KDB Vapor Pressure Data
• 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
• Vapor-Liquid Equilibria on Seven Binary Systems: Ethylene Oxide + 2-Methylpropane; Acetophenone + Phenol; cis-1,3-Dichloropropene + 1,2-Dichloropropane; 1,5-Hexadiene + Allyl Chloride; Isopropyl Acetate + Acetonitrile; Vinyl Chloride + Methyl Chloride; and 1,4-Butanediol + c-Butyrolactone
• Determination of Henry's Law Constants Using Internal Standards with Benchmark Values
• Low Pressure Solubilities of Vinyl Chloride in Ionic Liquids
• Joback Method
• KDB
• Aqueous Solubility Prediction Method
• Estimated Solubility Method
• McGowan Method
• NIST Webbook
• The Yaws Handbook of Vapor Pressure
• Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD

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