Ethylene (CAS 74-85-1)

InChI

InChI=1S/C2H4/c1-2/h1-2H2

InChI Key

VGGSQFUCUMXWEO-UHFFFAOYSA-N

Formula

C2H4

SMILES

C=C

Molecular Weight¹

28.05

CAS

74-85-1

Other Names

Acetene
Athylen
Bicarburretted hydrogen
C2H4
Elayl
Liquid ethyene
Olefiant gas
UN 1038
UN 1962
ethene

ω : Acentric Factor.
PAff : Proton affinity (kJ/mol).
T_ig : Autoignition Temperature (K).
BasG : Gas basicity (kJ/mol).
Δ_cH°_gas : Standard gas enthalpy of combustion (kJ/mol).
C_p,gas : Ideal gas heat capacity (J/mol×K).
C_p,liquid : Liquid phase heat capacity (J/mol×K).
μ : Dipole Moment (debye).
η : Dynamic viscosity (Pa×s).
LFL : Lower Flammability Limit (% in Air).
UFL : Upper Flammability Limit (% in Air).
T_flash,oc : Flash Point (Open Cup Method) (K).
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°_{(+) ion} : Enthalpy of formation of positive ion at standard conditions (kJ/mol).
Δ_fH_{(+) ion,0K} : Enthalpy of formation of positive ion at 0K (kJ/mol).
Δ_fusH° : Enthalpy of fusion at standard conditions (kJ/mol).
Δ_fusH : Enthalpy of fusion at a given temperature (kJ/mol).
Δ_subH : Enthalpy of sublimation at a given temperature (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_c : Critical density (kg/m³).
ρ_g : Gas Density (kg/m³).
ρ_l : Liquid Density (kg/m³).
I_np : Non-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).
Δ_vapS : Entropy of vaporization at a given temperature (J/mol×K).
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).
V_COSTALD : COSTALD Characteristic Volume (m³/kmol).
ω_SRK : SRK acentric factor.
Z_c : Critical Compressibility.
Z_ra : Rackett Parameter.
¹: Molecular weight from the IUPAC atomic weights tables.

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Physical Properties

Property	Value	Unit	Source
ω	[0.0850; 0.0890]
ω	0.0850		PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
ω	0.0856		Passut and Danner (1973), critical constants and acentric factors Compiled value
ω	0.0870		ChemSep v8.3 pure component data Compiled value
ω	0.0890		KDB
PAff	680.50	kJ/mol	NIST
T_ig	723.15	K	KDB
BasG	651.50	kJ/mol	NIST
Δ_cH°_gas	-1411.20 ± 0.30	kJ/mol	NIST
μ	[0.00; 0.00]	debye
μ	0.00	debye	ChemSep v8.3 pure component data Compiled value
μ	0.00	debye	KDB
LFL	2.70	% in Air	KDB
UFL	28.60	% in Air	KDB
T_flash,oc	137.04	K	KDB
Δ_fG°	[68.16; 68.44]	kJ/mol
Δ_fG°	68.44	kJ/mol	ChemSep v8.3 pure component data Compiled value
Δ_fG°	68.16	kJ/mol	KDB
R_g	1.5380		KDB
Δ_fH°_gas	[52.34; 52.56]	kJ/mol
Δ_fH°_gas	52.56 ± 0.15	kJ/mol	Active Thermochemical Tables 1.112, gas-phase enthalpies of formation Compiled value
Δ_fH°_gas	52.51	kJ/mol	ChemSep v8.3 pure component data Compiled value
Δ_fH°_gas	52.34	kJ/mol	KDB
Δ_fH°_gas	52.40 ± 0.50	kJ/mol	NIST
Δ_fH°_{(+) ion}	1067.00 ± 0.80	kJ/mol	NIST
Δ_fH_{(+) ion,0K}	1080.00	kJ/mol	NIST
Δ_fusH°	-1.83	kJ/mol	Joback Calculated Property
IE	[10.50; 10.80]	eV
IE	10.51 ± 0.00	eV	NIST
IE	10.51	eV	NIST
IE	10.51 ± 0.00	eV	NIST
IE	10.51 ± 0.01	eV	NIST
IE	10.51 ± 0.01	eV	NIST
IE	10.51	eV	NIST
IE	10.50 ± 0.02	eV	NIST
IE	10.51 ± 0.01	eV	NIST
IE	10.51	eV	NIST
IE	10.51 ± 0.02	eV	NIST
IE	10.50	eV	NIST
IE	10.52 ± 0.00	eV	NIST
IE	10.52 ± 0.00	eV	NIST
IE	10.51	eV	NIST
IE	10.50	eV	NIST
IE	10.51 ± 0.00	eV	NIST
IE	10.51 ± 0.01	eV	NIST
IE	10.52 ± 0.00	eV	NIST
IE	10.51	eV	NIST
IE	10.51	eV	NIST
IE	10.51	eV	NIST
IE	10.56	eV	NIST
IE	10.51 ± 0.02	eV	NIST
IE	10.51 ± 0.05	eV	NIST
IE	10.50 ± 0.05	eV	NIST
IE	10.51	eV	NIST
IE	10.51 ± 0.01	eV	NIST
IE	10.50 ± 0.01	eV	NIST
IE	10.51 ± 0.00	eV	NIST
IE	10.50 ± 0.02	eV	NIST
IE	10.52 ± 0.01	eV	NIST
IE	10.51 ± 0.03	eV	NIST
IE	Outlier 10.80 ± 0.05	eV	NIST
IE	Outlier 10.68	eV	NIST
IE	10.50 ± 0.01	eV	NIST
IE	10.50	eV	NIST
IE	10.50	eV	NIST
log₁₀WS	[-0.40; -0.40]
log₁₀WS	-0.40		Aq. Solubility Prediction
log₁₀WS	-0.40		Estimated Solubility
logP_oct/wat	0.802		Crippen Calculated Property
McVol	34.740	ml/mol	McGowan Calculated Property
NFPA Fire	4		KDB
NFPA Health	1		KDB
NFPA Safety	2		KDB
P_c	[5020.00; 5119.95]	kPa
P_c	5020.00	kPa	Gas-Liquid Critical Properties of Ethylene + Hydrogen and Propylene + Hydrogen Binary Mixtures
P_c	5041.00	kPa	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 6 Compiled value
P_c	5041.63	kPa	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
P_c	5031.79	kPa	Passut and Danner (1973), critical constants and acentric factors Compiled value
P_c	5041.00	kPa	ChemSep v8.3 pure component data Compiled value
P_c	5042.00	kPa	Air Liquide Gas Encyclopedia
P_c	5041.00	kPa	KDB
P_c	5041.00 ± 4.00	kPa	NIST
P_c	5055.00 ± 5.04	kPa	NIST
P_c	5040.10 ± 5.00	kPa	NIST
P_c	5055.00 ± 5.00	kPa	NIST
P_c	5040.30 ± 0.20	kPa	NIST
P_c	5040.30 ± 0.20	kPa	NIST
P_c	5042.00 ± 4.00	kPa	NIST
P_c	5076.00 ± 2.00	kPa	NIST
P_c	Outlier 5119.95 ± 20.26	kPa	NIST
P_c	5061.00 ± 101.32	kPa	NIST
P_triple	[0.12; 0.13]	kPa
P_triple	0.12 ± 0.00	kPa	Staveley, Lobo and Calado (1981), triple points Compiled value
P_triple	0.13	kPa	ChemSep v8.3 pure component data Compiled value
P_triple	0.12	kPa	Air Liquide Gas Encyclopedia
P_triple	0.12 ± 0.01	kPa	NIST
P_triple	0.12	kPa	NIST
ρ_c	[214.05; 530.04]	kg/m³
ρ_c	214.20	kg/m³	Air Liquide Gas Encyclopedia
ρ_c	214.05 ± 0.11	kg/m³	NIST
ρ_c	214.14 ± 0.11	kg/m³	NIST
ρ_c	214.16 ± 0.02	kg/m³	NIST
ρ_c	Outlier 530.04 ± 0.20	kg/m³	NIST
ρ_c	215.97 ± 0.56	kg/m³	NIST
I_np	[158.00; 188.00]
I_np	166.00		NIST
I_np	175.00		NIST
I_np	177.00		NIST
I_np	177.00		NIST
I_np	178.00		NIST
I_np	178.00		NIST
I_np	178.10		NIST
I_np	164.00		NIST
I_np	183.00		NIST
I_np	158.00		NIST
I_np	166.00		NIST
I_np	165.00		NIST
I_np	178.00		NIST
I_np	180.00		NIST
I_np	166.00		NIST
I_np	165.00		NIST
I_np	165.00		NIST
I_np	165.00		NIST
I_np	165.00		NIST
I_np	188.00		NIST
I_np	180.00		NIST
I_np	166.00		NIST
I_np	178.00		NIST
I_np	183.00		NIST
I_np	158.00		NIST
S°_liquid	117.80	J/mol×K	NIST
T_boil	[168.08; 170.45]	K
T_boil	169.42	K	ChemSep v8.3 pure component data Compiled value
T_boil	169.38	K	Air Liquide Gas Encyclopedia
T_boil	169.38	K	KDB
T_boil	169.35 ± 0.02	K	NIST
T_boil	169.30 ± 0.20	K	NIST
T_boil	Outlier 168.08 ± 2.00	K	NIST
T_boil	169.25 ± 0.50	K	NIST
T_boil	169.00 ± 0.30	K	NIST
T_boil	169.25 ± 0.50	K	NIST
T_boil	169.43 ± 0.50	K	NIST
T_boil	169.30 ± 0.50	K	NIST
T_boil	Outlier 170.45 ± 0.70	K	NIST
T_c	[282.33; 283.10]	K
T_c	282.34	K	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 6 Compiled value
T_c	282.35	K	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
T_c	282.36	K	Passut and Danner (1973), critical constants and acentric factors Compiled value
T_c	282.34	K	ChemSep v8.3 pure component data Compiled value
T_c	282.35	K	Air Liquide Gas Encyclopedia
T_c	282.34	K	KDB
T_c	282.34 ± 0.02	K	NIST
T_c	282.33 ± 0.02	K	NIST
T_c	282.35 ± 0.02	K	NIST
T_c	282.33 ± 0.10	K	NIST
T_c	282.34 ± 0.00	K	NIST
T_c	282.34 ± 0.00	K	NIST
T_c	282.35 ± 0.03	K	NIST
T_c	282.65 ± 0.25	K	NIST
T_c	282.69 ± 0.30	K	NIST
T_c	Outlier 283.10 ± 0.60	K	NIST
T_fus	[103.70; 104.05]	K
T_fus	104.05	K	Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
T_fus	104.00	K	ChemSep v8.3 pure component data Compiled value
T_fus	104.00	K	Air Liquide Gas Encyclopedia
T_fus	104.00	K	KDB
T_fus	104.01	K	Aq. Solubility Prediction
T_fus	103.80 ± 0.20	K	NIST
T_fus	103.70 ± 0.50	K	NIST
T_fus	103.70 ± 1.00	K	NIST
T_triple	[103.80; 104.10]	K
T_triple	104.00	K	Staveley, Lobo and Calado (1981), triple points Compiled value
T_triple	104.00	K	ChemSep v8.3 pure component data Compiled value
T_triple	103.99	K	Air Liquide Gas Encyclopedia
T_triple	103.99 ± 0.05	K	NIST
T_triple	103.98 ± 0.01	K	NIST
T_triple	103.97 ± 0.02	K	NIST
T_triple	103.97 ± 0.03	K	NIST
T_triple	104.10 ± 0.50	K	NIST
T_triple	103.97 ± 0.02	K	NIST
T_triple	103.97 ± 0.15	K	NIST
T_triple	103.95 ± 0.10	K	NIST
T_triple	Outlier 103.80 ± 0.30	K	NIST
U_Qi	1.49		ChemSep v8.3 pure component data Compiled value
U_Ri	1.57		ChemSep v8.3 pure component data Compiled value
V_c	[0.129; 0.131]	m³/kmol
V_c	0.131	m³/kmol	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 6 Compiled value
V_c	0.129	m³/kmol	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
V_c	0.131	m³/kmol	ChemSep v8.3 pure component data Compiled value
V_c	0.131	m³/kmol	KDB
V_c	0.131	m³/kmol	NIST
V_c	0.131 ± 0.000	m³/kmol	NIST
V_c	0.131 ± 0.000	m³/kmol	NIST
V_c	0.129 ± 0.000	m³/kmol	NIST
V_COSTALD	0.13	m³/kmol	Hankinson and Thomson (1979), COSTALD parameters Compiled value
ω_SRK	0.83		Hankinson and Thomson (1979), COSTALD parameters Compiled value
Z_c	[0.2815210; 0.2820000]
Z_c	0.2820000		IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 6 Compiled value
Z_c	0.2820000		ChemSep v8.3 pure component data Compiled value
Z_c	0.2815210		KDB
Z_ra	[0.28; 0.28]
Z_ra	0.28		Hankinson and Thomson (1979), COSTALD parameters Compiled value
Z_ra	0.28		ChemSep v8.3 pure component data Compiled value
Z_ra	0.28		KDB

Cheméo can also estimate Enthalpy of vaporization at standard conditions for this compound, but it falls outside the models' validated range, so it is not shown here. Open the prediction tool to compute it on demand.

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
C_p,gas	[34.66; 59.25]	J/mol×K	[178.15; 463.60]

C_p,gas	34.66 ± 0.26	J/mol×K	178.15	NIST
C_p,gas	35.30 ± 0.26	J/mol×K	192.35	NIST
C_p,gas	36.29 ± 0.27	J/mol×K	210.40	NIST
C_p,gas	37.55 ± 0.28	J/mol×K	230.90	NIST
C_p,gas	39.02 ± 0.29	J/mol×K	250.60	NIST
C_p,gas	40.75 ± 0.02	J/mol×K	270.70	NIST
C_p,gas	41.02 ± 0.31	J/mol×K	271.80	NIST
C_p,gas	42.84 ± 0.32	J/mol×K	293.45	NIST
C_p,gas	43.47 ± 0.17	J/mol×K	300.00	NIST
C_p,gas	45.98 ± 0.04	J/mol×K	320.70	NIST
C_p,gas	49.74 ± 0.37	J/mol×K	367.70	NIST
C_p,gas	59.25 ± 0.44	J/mol×K	463.60	NIST
C_p,liquid	[67.17; 68.90]	J/mol×K	[110.00; 170.00]

C_p,liquid	68.90	J/mol×K	110.00	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
C_p,liquid	68.30	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
C_p,liquid	67.83	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
C_p,liquid	67.48	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
C_p,liquid	67.26	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
C_p,liquid	67.17	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
C_p,liquid	67.21	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
C_p,liquid	67.40	J/mol×K	170.00	NIST
C_p,liquid	67.24	J/mol×K	170.00	NIST
Δ_fusH	[3.35; 3.35]	kJ/mol	[103.95; 104.00]

Δ_fusH	3.35	kJ/mol	103.95	NIST
Δ_fusH	3.35	kJ/mol	103.97	NIST
Δ_fusH	3.35	kJ/mol	104.00	Air Liquide Gas Encyclopedia
Δ_fusH	3.35	kJ/mol	104.00	NIST
Δ_fusH	3.35	kJ/mol	104.00	NIST
Δ_subH	[15.00; 18.40]	kJ/mol	[90.00; 91.50]
Δ_subH	15.00	kJ/mol	90.00	NIST
Δ_subH	18.40	kJ/mol	91.50	NIST
Δ_vapH	[13.53; 14.40]	kJ/mol	[145.00; 267.00]

Δ_vapH	14.40	kJ/mol	145.00	NIST
Δ_vapH	14.40	kJ/mol	147.50	NIST
Δ_vapH	14.10	kJ/mol	151.00	NIST
Δ_vapH	14.30	kJ/mol	161.00	NIST
Δ_vapH	13.53	kJ/mol	169.38	Air Liquide Gas Encyclopedia
Δ_vapH	13.54	kJ/mol	169.40	KDB
Δ_vapH	13.54	kJ/mol	169.40	NIST
Δ_vapH	14.00	kJ/mol	170.00	NIST
Δ_vapH	13.70	kJ/mol	190.00	NIST
Δ_vapH	13.70	kJ/mol	221.50	NIST
Δ_vapH	13.60	kJ/mol	231.50	NIST
Δ_vapH	14.00	kJ/mol	267.00	NIST
P_vap	[1476.00; 4891.00]	kPa	[233.73; 280.98]

P_vap	1476.00	kPa	233.73	Vapor-Liquid Equilibrium (PTxy) Measurements and Modeling for the CO-C2H4 Binary System
P_vap	1932.30	kPa	243.08	Vapor-Liquid Equilibrium (PTxy) Measurements and Modeling for the CO-C2H4 Binary System
P_vap	2534.80	kPa	253.22	Vapor-Liquid Equilibrium (PTxy) Measurements and Modeling for the CO-C2H4 Binary System
P_vap	2732.00	kPa	256.22	Isothermal vapor-liquid equilibrium data for the ethylene + 1,1,2,3,3,3-hexafluoro-1-propene binary system between 258 and 308 K at pressures up to 4.56 MPa
P_vap	2903.00	kPa	258.59	Isothermal vapor-liquid equilibrium data for the ethylene + 1,1,2,3,3,3-hexafluoro-1-propene binary system between 258 and 308 K at pressures up to 4.56 MPa
P_vap	3083.00	kPa	261.02	Isothermal vapor-liquid equilibrium data for the ethylene + 1,1,2,3,3,3-hexafluoro-1-propene binary system between 258 and 308 K at pressures up to 4.56 MPa
P_vap	3247.50	kPa	263.22	Vapor-Liquid Equilibrium (PTxy) Measurements and Modeling for the CO-C2H4 Binary System
P_vap	3272.00	kPa	263.48	Isothermal vapor-liquid equilibrium data for the ethylene + 1,1,2,3,3,3-hexafluoro-1-propene binary system between 258 and 308 K at pressures up to 4.56 MPa
P_vap	3470.00	kPa	265.94	Isothermal vapor-liquid equilibrium data for the ethylene + 1,1,2,3,3,3-hexafluoro-1-propene binary system between 258 and 308 K at pressures up to 4.56 MPa
P_vap	3648.50	kPa	268.13	Vapor-liquid equilibria of ethylene (C2H4) + decafluorobutane (C4F10) at 268 to 298 K from experiment, molecular simulation and the Peng-Robinson equation of state
P_vap	3671.00	kPa	268.37	Isothermal vapor-liquid equilibrium data for the ethylene + 1,1,2,3,3,3-hexafluoro-1-propene binary system between 258 and 308 K at pressures up to 4.56 MPa
P_vap	3891.00	kPa	270.85	Isothermal vapor-liquid equilibrium data for the ethylene + 1,1,2,3,3,3-hexafluoro-1-propene binary system between 258 and 308 K at pressures up to 4.56 MPa
P_vap	4094.00	kPa	273.15	Phase equilibrium and critical point data for ethylene and chlorodifluoromethane binary mixtures using a new static-analytic apparatus
P_vap	4102.00	kPa	273.18	Vapor-Liquid Equilibrium (PTxy) Measurements and Modeling for the CO-C2H4 Binary System
P_vap	4113.00	kPa	273.29	Isothermal vapor-liquid equilibrium data for the ethylene + 1,1,2,3,3,3-hexafluoro-1-propene binary system between 258 and 308 K at pressures up to 4.56 MPa
P_vap	4339.00	kPa	275.68	Isothermal vapor-liquid equilibrium data for the ethylene + 1,1,2,3,3,3-hexafluoro-1-propene binary system between 258 and 308 K at pressures up to 4.56 MPa
P_vap	4588.00	kPa	278.16	Isothermal vapor-liquid equilibrium data for the ethylene + 1,1,2,3,3,3-hexafluoro-1-propene binary system between 258 and 308 K at pressures up to 4.56 MPa
P_vap	4611.20	kPa	278.36	Vapor-liquid equilibria of ethylene (C2H4) + decafluorobutane (C4F10) at 268 to 298 K from experiment, molecular simulation and the Peng-Robinson equation of state
P_vap	4891.00	kPa	280.98	Isothermal vapor-liquid equilibrium data for the ethylene + 1,1,2,3,3,3-hexafluoro-1-propene binary system between 258 and 308 K at pressures up to 4.56 MPa
ρ_g	[1.19; 2.09]	kg/m³	[169.38; 288.15]
ρ_g	2.09	kg/m³	169.38	Air Liquide Gas Encyclopedia
ρ_g	1.19	kg/m³	288.15	Air Liquide Gas Encyclopedia
ρ_l	[567.65; 577.00]	kg/m³	[163.00; 169.38]
ρ_l	577.00	kg/m³	163.00	KDB
ρ_l	567.65	kg/m³	169.38	Air Liquide Gas Encyclopedia
Δ_fusS	[32.23; 32.23]	J/mol×K	[103.95; 103.97]
Δ_fusS	32.23	J/mol×K	103.95	NIST
Δ_fusS	32.23	J/mol×K	103.97	NIST
γ	0.02	N/m	133.20	KDB
Δ_vapS	79.95	J/mol×K	169.40	NIST
λ_gas	[0.02; 0.04]	W/m×K	[283.47; 425.62]

λ_gas	0.02	W/m×K	283.47	Measurements of the thermal conductivity of ethene in the supercritical region
λ_gas	0.02	W/m×K	283.96	Measurements of the thermal conductivity of ethene in the supercritical region
λ_gas	0.02	W/m×K	284.89	Measurements of the thermal conductivity of ethene in the supercritical region
λ_gas	0.02	W/m×K	302.21	Measurements of the thermal conductivity of ethene in the supercritical region
λ_gas	0.02	W/m×K	303.10	Measurements of the thermal conductivity of ethene in the supercritical region
λ_gas	0.04	W/m×K	425.00	Measurements of the thermal conductivity of ethene in the supercritical region
λ_gas	0.04	W/m×K	425.62	Measurements of the thermal conductivity of ethene in the supercritical region

Correlations

Property	Value	Unit	Temperature (K)	Source
C_p,gas	[33.07; 110.46]	J/mol×K	[50.00; 1500.00]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A + exp(B/T + C + D·T + E·T²) Y is C_p,gas in J/mol×K, T in K
Coefficient A			3.30719e+01
Coefficient B			-8.60028e+02
Coefficient C			5.32031e+00
Coefficient D			-5.09703e-04
Coefficient E			1.62839e-07
Temperature range, min.			50.00
Temperature range, max.			1500.00

C_p,gas	33.07	J/mol×K	50.00	Calculated Property
C_p,gas	36.22	J/mol×K	211.11	Calculated Property
C_p,gas	50.23	J/mol×K	372.22	Calculated Property
C_p,gas	65.60	J/mol×K	533.33	Calculated Property
C_p,gas	78.06	J/mol×K	694.44	Calculated Property
C_p,gas	87.57	J/mol×K	855.56	Calculated Property
C_p,gas	94.91	J/mol×K	1016.67	Calculated Property
C_p,gas	100.81	J/mol×K	1177.78	Calculated Property
C_p,gas	105.85	J/mol×K	1338.89	Calculated Property
C_p,gas	110.46	J/mol×K	1500.00	Calculated Property
C_p,gas	[42.84; 101.68]	J/mol×K	[298.00; 1200.00]	NIST
Equation			Y = A + B·t + C·t² + D·t³ + E/t², t = T/1000 Y is C_p,gas in J/mol×K, T in K
Coefficient A			-6.38788e+00
Coefficient B			1.84402e+02
Coefficient C			-1.12972e+02
Coefficient D			2.84959e+01
Coefficient E			3.15540e-01
Reference			Chase, 1998
Comment			F=48.17332, G=163.1568, H=52.46694; Data last reviewed in September, 1965
Temperature range, min.			298.00
Temperature range, max.			1200.00

C_p,gas	42.84	J/mol×K	298.00	Calculated Property
C_p,gas	52.92	J/mol×K	398.22	Calculated Property
C_p,gas	62.26	J/mol×K	498.44	Calculated Property
C_p,gas	70.51	J/mol×K	598.67	Calculated Property
C_p,gas	77.68	J/mol×K	698.89	Calculated Property
C_p,gas	83.86	J/mol×K	799.11	Calculated Property
C_p,gas	89.20	J/mol×K	899.33	Calculated Property
C_p,gas	93.83	J/mol×K	999.56	Calculated Property
C_p,gas	97.94	J/mol×K	1099.78	Calculated Property
C_p,gas	101.68	J/mol×K	1200.00	Calculated Property
C_p,gas	[101.35; 131.27]	J/mol×K	[1200.00; 6000.00]	NIST
Equation			Y = A + B·t + C·t² + D·t³ + E/t², t = T/1000 Y is C_p,gas in J/mol×K, T in K
Coefficient A			1.06510e+02
Coefficient B			1.37326e+01
Coefficient C			-2.62848e+00
Coefficient D			1.74595e-01
Coefficient E			-2.61447e+01
Reference			Chase, 1998
Comment			F=-35.36237, G=275.0424, H=52.46694; Data last reviewed in September, 1965
Temperature range, min.			1200.00
Temperature range, max.			6000.00

C_p,gas	101.35	J/mol×K	1200.00	Calculated Property
C_p,gas	114.62	J/mol×K	1733.33	Calculated Property
C_p,gas	121.08	J/mol×K	2266.67	Calculated Property
C_p,gas	124.85	J/mol×K	2800.00	Calculated Property
C_p,gas	127.19	J/mol×K	3333.33	Calculated Property
C_p,gas	128.66	J/mol×K	3866.67	Calculated Property
C_p,gas	129.57	J/mol×K	4400.00	Calculated Property
C_p,gas	130.18	J/mol×K	4933.33	Calculated Property
C_p,gas	130.68	J/mol×K	5466.67	Calculated Property
C_p,gas	131.27	J/mol×K	6000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
C_p,liquid	[68.02; 110.75]	J/mol×K	[99.82; 259.95]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A + exp(B/T + C + D·T + E·T²) Y is C_p,liquid in J/mol×K, T in K
Coefficient A			6.80160e+01
Coefficient B			-2.24140e+04
Coefficient C			2.79842e+02
Coefficient D			-1.18020e+00
Coefficient E			1.73040e-03
Temperature range, min.			99.82
Temperature range, max.			259.95

C_p,liquid	68.02	J/mol×K	99.82	Calculated Property
C_p,liquid	68.02	J/mol×K	117.61	Calculated Property
C_p,liquid	68.02	J/mol×K	135.40	Calculated Property
C_p,liquid	68.02	J/mol×K	153.20	Calculated Property
C_p,liquid	68.10	J/mol×K	170.99	Calculated Property
C_p,liquid	69.00	J/mol×K	188.78	Calculated Property
C_p,liquid	72.00	J/mol×K	206.57	Calculated Property
C_p,liquid	77.55	J/mol×K	224.37	Calculated Property
C_p,liquid	87.30	J/mol×K	242.16	Calculated Property
C_p,liquid	110.75	J/mol×K	259.95	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.0006793; 0.0000437]	Pa×s	[103.10; 282.34]	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			-8.95560e+00
Coefficient B			2.88210e+02
Coefficient C			-2.19850e-01
Coefficient D			-1.08310e-05
Coefficient E			2.00000e+00
Comment			Range stopped at Tc; ChemSep gives it to 283 K.
Temperature range, min.			103.10
Temperature range, max.			282.34

η	0.0006793	Pa×s	103.10	Calculated Property
η	0.0003958	Pa×s	123.02	Calculated Property
η	0.0002609	Pa×s	142.93	Calculated Property
η	0.0001855	Pa×s	162.85	Calculated Property
η	0.0001384	Pa×s	182.76	Calculated Property
η	0.0001066	Pa×s	202.68	Calculated Property
η	0.0000839	Pa×s	222.59	Calculated Property
η	0.0000670	Pa×s	242.51	Calculated Property
η	0.0000539	Pa×s	262.42	Calculated Property
η	0.0000437	Pa×s	282.34	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Δ_vapH	[15.93; 0.00]	kJ/mol	[104.00; 282.34]	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 Δ_vapH in kJ/mol, T in K
Coefficient A			2.16580e+01
Coefficient B			1.21640e+00
Coefficient C			-2.15380e+00
Coefficient D			2.07680e+00
Coefficient E			-7.30960e-01
Critical temperature, Tc (K)			2.82340e+02
Comment			Range stopped at Tc; ChemSep gives it to 282.35 K.
Temperature range, min.			104.00
Temperature range, max.			282.34

Δ_vapH	15.93	kJ/mol	104.00	Calculated Property
Δ_vapH	15.23	kJ/mol	123.82	Calculated Property
Δ_vapH	14.53	kJ/mol	143.63	Calculated Property
Δ_vapH	13.77	kJ/mol	163.45	Calculated Property
Δ_vapH	12.92	kJ/mol	183.26	Calculated Property
Δ_vapH	11.93	kJ/mol	203.08	Calculated Property
Δ_vapH	10.73	kJ/mol	222.89	Calculated Property
Δ_vapH	9.21	kJ/mol	242.71	Calculated Property
Δ_vapH	7.06	kJ/mol	262.52	Calculated Property
Δ_vapH	0.00	kJ/mol	282.34	Calculated Property

Property	Value	Unit	Temperature (K)	Source
P_vap	[0.14; 5057.85]	kPa	[104.00; 282.35]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is P_vap in kPa, T in K
Coefficient A			1.40310e+01
Coefficient B			-1.49623e+03
Coefficient C			-1.04200e+01
Temperature range, min.			104.00
Temperature range, max.			282.35

P_vap	0.14	kPa	104.00	Calculated Property
P_vap	2.31	kPa	123.82	Calculated Property
P_vap	16.43	kPa	143.63	Calculated Property
P_vap	70.36	kPa	163.45	Calculated Property
P_vap	215.84	kPa	183.27	Calculated Property
P_vap	525.80	kPa	203.08	Calculated Property
P_vap	1084.87	kPa	222.90	Calculated Property
P_vap	1978.17	kPa	242.72	Calculated Property
P_vap	3282.00	kPa	262.53	Calculated Property
P_vap	5057.85	kPa	282.35	Calculated Property
P_vap	[0.12; 5039.04]	kPa	[104.00; 282.34]	ChemSep v8.3 pure component data Compiled value
Equation			Y = exp(A + B/T + C·ln(T) + D·T^E) Y is P_vap in kPa, T in K
Coefficient A			4.76245e+01
Coefficient B			-2.45842e+03
Coefficient C			-5.66004e+00
Coefficient D			1.94185e-05
Coefficient E			2.00000e+00
Comment			Range stopped at Tc; ChemSep gives it to 282.35 K.
Temperature range, min.			104.00
Temperature range, max.			282.34

P_vap	0.12	kPa	104.00	Calculated Property
P_vap	2.21	kPa	123.82	Calculated Property
P_vap	16.35	kPa	143.63	Calculated Property
P_vap	70.52	kPa	163.45	Calculated Property
P_vap	214.42	kPa	183.26	Calculated Property
P_vap	515.15	kPa	203.08	Calculated Property
P_vap	1051.12	kPa	222.89	Calculated Property
P_vap	1910.65	kPa	242.71	Calculated Property
P_vap	3196.94	kPa	262.52	Calculated Property
P_vap	5039.04	kPa	282.34	Calculated Property
P_vap	[0.13; 5023.31]	kPa	[104.01; 282.36]	KDB Vapor Pressure Data
Equation			ln(Y) = A + B/T + C·ln(T) + D·T² + E/T² Y is P_vap in kPa, T in K
Coefficient A			4.31991e+01
Coefficient B			-2.35577e+03
Coefficient C			-4.89843e+00
Coefficient D			1.64142e-05
Coefficient E			0.00000e+00
Temperature range, min.			104.01
Temperature range, max.			282.36

P_vap	0.13	kPa	104.01	Calculated Property
P_vap	2.27	kPa	123.83	Calculated Property
P_vap	16.54	kPa	143.64	Calculated Property
P_vap	70.85	kPa	163.46	Calculated Property
P_vap	215.10	kPa	183.28	Calculated Property
P_vap	517.00	kPa	203.09	Calculated Property
P_vap	1055.47	kPa	222.91	Calculated Property
P_vap	1917.59	kPa	242.73	Calculated Property
P_vap	3201.28	kPa	262.54	Calculated Property
P_vap	5023.31	kPa	282.36	Calculated Property
P_vap	[26.04; 276.54]	kPa	[149.37; 188.57]	NIST
Equation			ln(Y) = A + B/(T + C) Y is P_vap in kPa, T in K
Coefficient A			1.35222e+01
Coefficient B			-1.34505e+03
Coefficient C			-1.83070e+01
Reference			Michels and Wassenaar, 1950
Comment			Coefficents calculated by NIST from author's data.
Temperature range, min.			149.37
Temperature range, max.			188.57

P_vap	26.04	kPa	149.37	Calculated Property
P_vap	36.22	kPa	153.73	Calculated Property
P_vap	49.36	kPa	158.08	Calculated Property
P_vap	66.02	kPa	162.44	Calculated Property
P_vap	86.81	kPa	166.79	Calculated Property
P_vap	112.38	kPa	171.15	Calculated Property
P_vap	143.41	kPa	175.50	Calculated Property
P_vap	180.62	kPa	179.86	Calculated Property
P_vap	224.75	kPa	184.21	Calculated Property
P_vap	276.54	kPa	188.57	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ρ_l	[646.66; 238.57]	kg/m³	[103.18; 282.34]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A / B^(1 + (1 − T/C)^D) Y is ρ_l in kg/m³, T in K
Coefficient A			6.67160e+01
Coefficient B			2.95420e-01
Coefficient C			2.82360e+02
Coefficient D			3.24560e-01
Comment			Range stopped at Tc; ChemSep gives it to 282.35 K.
Temperature range, min.			103.18
Temperature range, max.			282.34

ρ_l	646.66	kg/m³	103.18	Calculated Property
ρ_l	621.65	kg/m³	123.09	Calculated Property
ρ_l	595.52	kg/m³	142.99	Calculated Property
ρ_l	568.00	kg/m³	162.90	Calculated Property
ρ_l	538.69	kg/m³	182.81	Calculated Property
ρ_l	506.95	kg/m³	202.71	Calculated Property
ρ_l	471.70	kg/m³	222.62	Calculated Property
ρ_l	430.77	kg/m³	242.53	Calculated Property
ρ_l	378.25	kg/m³	262.43	Calculated Property
ρ_l	238.57	kg/m³	282.34	Calculated Property

Property	Value	Unit	Temperature (K)	Source
γ	[0.03; 8.02e-04]	N/m	[104.00; 272.95]	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			-2.85900e-03
Coefficient B			2.36180e+02
Coefficient C			-7.98780e+00
Coefficient D			3.21450e-02
Coefficient E			-9.74690e-05
Temperature range, min.			104.00
Temperature range, max.			272.95

γ	0.03	N/m	104.00	Calculated Property
γ	0.02	N/m	122.77	Calculated Property
γ	0.02	N/m	141.54	Calculated Property
γ	0.02	N/m	160.32	Calculated Property
γ	0.01	N/m	179.09	Calculated Property
γ	0.01	N/m	197.86	Calculated Property
γ	0.01	N/m	216.63	Calculated Property
γ	0.01	N/m	235.41	Calculated Property
γ	0.00	N/m	254.18	Calculated Property
γ	8.02e-04	N/m	272.95	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λ_gas	[0.01; 0.07]	W/m×K	[170.00; 590.92]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A·T^B / (1 + C/T + D/T²) Y is λ_gas in W/m×K, T in K
Coefficient A			9.32470e-06
Coefficient B			1.46070e+00
Coefficient C			4.10480e+02
Coefficient D			-4.44050e+04
Temperature range, min.			170.00
Temperature range, max.			590.92

λ_gas	0.01	W/m×K	170.00	Calculated Property
λ_gas	0.01	W/m×K	216.77	Calculated Property
λ_gas	0.02	W/m×K	263.54	Calculated Property
λ_gas	0.02	W/m×K	310.31	Calculated Property
λ_gas	0.03	W/m×K	357.08	Calculated Property
λ_gas	0.03	W/m×K	403.84	Calculated Property
λ_gas	0.04	W/m×K	450.61	Calculated Property
λ_gas	0.05	W/m×K	497.38	Calculated Property
λ_gas	0.06	W/m×K	544.15	Calculated Property
λ_gas	0.07	W/m×K	590.92	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λ_liquid	[0.27; 0.08]	W/m×K	[100.00; 280.00]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A + exp(B/T + C + D·T + E·T²) Y is λ_liquid in W/m×K, T in K
Coefficient A			-1.94990e-01
Coefficient B			-1.11780e+01
Coefficient C			-3.11820e-01
Coefficient D			-3.48440e-03
Coefficient E			3.58730e-07
Temperature range, min.			100.00
Temperature range, max.			280.00

λ_liquid	0.27	W/m×K	100.00	Calculated Property
λ_liquid	0.25	W/m×K	120.00	Calculated Property
λ_liquid	0.22	W/m×K	140.00	Calculated Property
λ_liquid	0.20	W/m×K	160.00	Calculated Property
λ_liquid	0.18	W/m×K	180.00	Calculated Property
λ_liquid	0.15	W/m×K	200.00	Calculated Property
λ_liquid	0.13	W/m×K	220.00	Calculated Property
λ_liquid	0.11	W/m×K	240.00	Calculated Property
λ_liquid	0.10	W/m×K	260.00	Calculated Property
λ_liquid	0.08	W/m×K	280.00	Calculated Property

Similar Compounds

Find more compounds similar to Ethylene.

Mixtures

Find more mixtures with Ethylene.

Sources

KDB Vapor Pressure Data
Air Liquide Gas Encyclopedia
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).
Hankinson and Thomson (1979), COSTALD parameters ChEDL chemicals 1.5.2, from Hankinson, R. W.; Thomson, G. H. A New Correlation for Saturated Densities of Liquids and Their Mixtures. AIChE J. 1979, 25, 653-663.
IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 6 ChEDL chemicals 1.5.2, from Tsonopoulos, C.; Ambrose, D. Vapor-Liquid Critical Properties of Elements and Compounds. 6. Unsaturated Aliphatic Hydrocarbons. J. Chem. Eng. Data 1996, 41, 645-656.
Passut and Danner (1973), critical constants and acentric factors ChEDL chemicals 1.5.2, from Passut, C. A.; Danner, R. P. Acentric Factor. A Valuable Correlating Parameter for the Properties of Hydrocarbons. Ind. Eng. Chem. Process Des. Dev. 1973, 12, 365-368.
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.
Staveley, Lobo and Calado (1981), triple points ChEDL chemicals 1.5.2, from Staveley, L. A. K.; Lobo, L. Q.; Calado, J. C. G. Triple-Points of Low Melting Substances and Their Use in Cryogenic Work. Cryogenics 1981, 21, 131-144.
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
The experiments and correlations of the solubility of ethylene in toluene solvent
Phase behaviour in the vicinity of the three-phase solid liquid vapour line in asymmetric nonpolar systems at high pressures
High-pressure phase equilibrium for ethylene + 1-butanol at 283.65 K and 290.80 K
Solubilities of several non-polar gases in mixtures water + 2,2,2-trifluoroethanol at 298.15 K and 101.33 kPa
Phase behavior of vinyl fluoride in room-temperature ionic liquids [emim][Tf2N], [bmim][N(CN)2], [bmpy][BF4], [bmim][HFPS] and [omim][TFES]
Vapor-liquid equilibria of ethylene (C2H4) + decafluorobutane (C4F10) at 268 to 298 K from experiment, molecular simulation and the Peng-Robinson equation of state
Solubility of ethylene in toluene, norbornene, and toluene + norbornene mixture
Isothermal vapor-liquid equilibrium data for the ethylene + 1,1,2,3,3,3-hexafluoro-1-propene binary system between 258 and 308 K at pressures up to 4.56 MPa
Solubility of ethylene in methyl propionate
Isothermal vapor liquid equilibrium data for the ethene + 2,2,3- trifluoro-3-(trifluoromethyl)oxirane binary system between 258 and 308 K at pressures up to 4.5MPa
High-pressure phase equilibria data for mixtures involving ethene and perfluoro-n-octane from 293 to 353 K
Separation of methane/ethylene gas mixtures efficiently by using ZIF- 67/water-ethylene glycol slurry
Binary vapour-liquid equilibrium data for C7 and C9 straight-chain perfluorocarbons with ethylene
Measurement and prediction of phase equilibria of ethylene + vinyl acetate + methanol + poly(ethylene-co-vinyl acetate) systems
Phase behavior and densities of propylene + toluene and ethylene + toluene systems to 580 K and 70 MPa
Phase equilibrium and critical point data for ethylene and chlorodifluoromethane binary mixtures using a new static-analytic apparatus
Measurements of the thermal conductivity of ethene in the supercritical region
Measurement and prediction of phase equilibria of ethylene + methyl acrylate + poly(ethylene-co-methyl acrylate) systems
Mixture densities and viscosities of toluene with ethylene or propylene at temperatures to 530 K and pressures to 70 MPa
Solubility of gases in fluoroorganic alcohols. Part III. Solubilities of several non-polar gases in water + 1,1,1,3,3,3-hexafluoropropan-2-ol at 298.15 K and 101.33 kPa
Solubilities of gases in cycloethers. The solubility of 13 nonpolar gases in 2,5-dimethyltetrahydrofuran at 273.15 to 303.15 K and 101.32 kPa
Solubility of Ethene in n-Hexane and n-Heptane as Common Slurry-Phase Polymerization Solvents: Experimental Measurement and Modeling
Influence of a-Olefin Concentration and Length on the High-Pressure Phase Behavior of (a-Olefin + n-Hexane + LLDPE) Systems
Solubilities of Nonpolar Gases in Triethylene Glycol Dimethyl Ether, Tetraethylene Glycol Dimethyl Ether, Dimethyl Carbonate, and Diethyl Carbonate at 298.15 K and 101.33 kPa Partial Pressure of Gas
Solubilities of Nonpolar Gases in Dimethyl Carbonate and Diethyl Carbonate
High-Pressure Phase Equilibrium for Ethylene + Ethanol at 283.65 K
Vapor-Liquid Equilibrium Data for the Ethylene + Hexane System
High-Pressure Phase Equilibrium for Ethylene + 2-Propanol at 283.65 K
High-Pressure Phase Equilibrium for Ethylene + Methanol at 278.15 K and 283.65 K
Solubility of Ethylene in 2,2,4-Trimethylpentane at Various Temperatures and Pressures
High-Pressure Multiphase Behavior of the Ternary Systems (Ethene + Water + Acetone) and (Ethane + Water + Acetone)
Vapor-Liquid Equilibrium (PTxy) Measurements and Modeling for the CO-C2H4 Binary System
Solubilities of the Gaseous and Liquid Solutes and Their Thermodynamics of Solubilization in the Novel Room-Temperature Ionic Liquids at Infinite Dilution by Gas Chromatography
High-Pressure Vapor-Liquid Equilibrium for Ethylene + 2-Methyl-1-propanol
Gas-Liquid Critical Properties of Ethylene + Hydrogen and Propylene + Hydrogen Binary Mixtures
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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Chemical Properties of Ethylene (CAS 74-85-1)