Chemical Properties of 2-Butene, (E)- (CAS 624-64-6)

InChI

InChI=1S/C4H8/c1-3-4-2/h3-4H,1-2H3/b4-3+

InChI Key

IAQRGUVFOMOMEM-ONEGZZNKSA-N

Formula

C4H8

SMILES

CC=CC

Molecular Weight¹

56.11

CAS

624-64-6

Other Names

• (E)-2-C4H8
• (E)-2-butene
• (E)-but-2-ene
• 2-Butene, trans-
• 2-trans-Butene
• Butene-2,trans
• TANS-1,2-DIMETHYLETHYLENE
• t rans-2-Butene
• t-Butene-2
• trans-1,2-Dimethylethylene
• trans-2-butene
• trans-Butene

• ω : Acentric Factor.
• PAff : Proton affinity (kJ/mol).
• 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).
• Δ_fG° : Standard Gibbs free energy of formation (kJ/mol).
• Δ_c,grossH : Heat of Combustion, Gross form (kJ/mol).
• Δ_c,netH : Heat of Combustion, Net Form (kJ/mol).
• Δ_fH°_gas : 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).
• logP_oct/wat : Octanol/Water partition coefficient.
• McVol : McGowan's characteristic volume (ml/mol).
• NFPA Fire : NFPA Fire Rating.
• NFPA Health : NFPA Health Rating.
• P_c : Critical Pressure (kPa).
• P_triple : Triple Point Pressure (kPa).
• P_vap : Vapor pressure (kPa).
• 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).
• 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.

Physical Properties

Property	Value	Unit	Source
ω	[0.2050; 0.2180]
ω	0.2140		PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
ω	0.2138		Passut and Danner (1973), critical constants and acentric factors Compiled value
ω	0.2180		ChemSep v8.3 pure component data Compiled value
ω	0.2050		KDB
PAff	747.00	kJ/mol	NIST
BasG	719.90	kJ/mol	NIST
ΔcH°gas	-2706.60 ± 0.96	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
ΔfG°	[63.01; 63.20]	kJ/mol
ΔfG°	63.20	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfG°	63.01	kJ/mol	KDB
Δc,grossH	2684.37	kJ/mol	KDB
Δc,netH	2508.308	kJ/mol	KDB
ΔfH°gas	[-11.18; -10.80]	kJ/mol
ΔfH°gas	-11.18 ± 0.51	kJ/mol	Active Thermochemical Tables 1.112, gas-phase enthalpies of formation Compiled value
ΔfH°gas	-11.00	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfH°gas	-11.18	kJ/mol	KDB
ΔfH°gas	-10.80 ± 1.00	kJ/mol	NIST
ΔfusH°	6.32	kJ/mol	Joback Calculated Property
ΔvapH°	[21.30; 21.97]	kJ/mol
ΔvapH°	21.97	kJ/mol	NIST
ΔvapH°	21.30	kJ/mol	NIST
IE	[9.09; 9.50]	eV
IE	9.10 ± 0.01	eV	NIST
IE	9.09	eV	NIST
IE	9.10 ± 0.02	eV	NIST
IE	9.10 ± 0.01	eV	NIST
IE	9.12 ± 0.02	eV	NIST
IE	9.11	eV	NIST
IE	9.12 ± 0.01	eV	NIST
IE	9.09	eV	NIST
IE	9.14	eV	NIST
IE	9.11	eV	NIST
IE	9.12	eV	NIST
IE	9.13 ± 0.01	eV	NIST
IE	9.13	eV	NIST
IE	9.37	eV	NIST
IE	Outlier 9.50	eV	NIST
IE	9.32	eV	NIST
IE	9.11	eV	NIST
logPoct/wat	1.582		Crippen Calculated Property
McVol	62.920	ml/mol	McGowan Calculated Property
NFPA Fire	4		KDB
NFPA Health	1		KDB
Pc	[3985.00; 4103.66]	kPa
Pc	4027.30	kPa	Thermodynamic properties of the butenes Part I. Experimental densities, vapor pressures, and critical points
Pc	4100.00	kPa	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 6 Compiled value
Pc	4103.66	kPa	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Pc	4102.38	kPa	Passut and Danner (1973), critical constants and acentric factors Compiled value
Pc	4100.00	kPa	ChemSep v8.3 pure component data Compiled value
Pc	Outlier 3985.00	kPa	KDB
Pc	4100.00 ± 20.00	kPa	NIST
Ptriple	0.07	kPa	ChemSep v8.3 pure component data Compiled value
ρc	236.21 ± 1.12	kg/m3	NIST
Inp	[383.00; 417.00]
Inp	413.00		NIST
Inp	414.00		NIST
Inp	410.20		NIST
Inp	402.00		NIST
Inp	400.00		NIST
Inp	406.90		NIST
Inp	410.00		NIST
Inp	410.00		NIST
Inp	405.00		NIST
Inp	406.50		NIST
Inp	404.40		NIST
Inp	406.10		NIST
Inp	406.49		NIST
Inp	405.00		NIST
Inp	407.00		NIST
Inp	406.70		NIST
Inp	403.00		NIST
Inp	407.00		NIST
Inp	406.00		NIST
Inp	407.00		NIST
Inp	406.00		NIST
Inp	412.00		NIST
Inp	412.00		NIST
Inp	407.00		NIST
Inp	412.30		NIST
Inp	414.00		NIST
Inp	406.42		NIST
Inp	408.40		NIST
Inp	408.00		NIST
Inp	411.00		NIST
Inp	406.00		NIST
Inp	Outlier 383.00		NIST
Inp	417.00		NIST
Inp	410.00		NIST
Inp	411.00		NIST
Inp	406.00		NIST
Inp	408.00		NIST
Inp	406.00		NIST
Inp	406.00		NIST
Inp	405.00		NIST
Inp	412.00		NIST
Inp	409.00		NIST
Inp	408.00		NIST
Inp	411.00		NIST
Inp	406.42		NIST
Inp	410.00		NIST
Inp	406.00		NIST
Inp	411.00		NIST
Ip	[450.00; 464.00]
Ip	464.00		NIST
Ip	450.00		NIST
Ip	450.00		NIST
S°liquid	[163.50; 205.31]	J/mol×K
S°liquid	163.50	J/mol×K	NIST
S°liquid	205.31	J/mol×K	NIST
S°liquid	204.97	J/mol×K	NIST
Tboil	[273.98; 274.75]	K
Tboil	274.03	K	ChemSep v8.3 pure component data Compiled value
Tboil	274.03	K	KDB
Tboil	274.20	K	NIST
Tboil	274.00	K	NIST
Tboil	274.20 ± 0.40	K	NIST
Tboil	274.05 ± 0.50	K	NIST
Tboil	273.98 ± 0.55	K	NIST
Tboil	274.01 ± 0.20	K	NIST
Tboil	274.11 ± 0.15	K	NIST
Tboil	274.15 ± 0.50	K	NIST
Tboil	Outlier 274.75 ± 0.60	K	NIST
Tboil	Outlier 274.75 ± 0.60	K	NIST
Tc	[428.60; 428.63]	K
Tc	428.60	K	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 6 Compiled value
Tc	428.60	K	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Tc	428.63	K	Passut and Danner (1973), critical constants and acentric factors Compiled value
Tc	428.60	K	ChemSep v8.3 pure component data Compiled value
Tc	428.63	K	KDB
Tc	428.60 ± 0.10	K	NIST
Tc	428.60	K	NIST
Tc	428.61 ± 0.30	K	NIST
Tfus	[167.35; 167.62]	K
Tfus	167.62	K	ChemSep v8.3 pure component data Compiled value
Tfus	167.62	K	KDB
Tfus	167.35 ± 0.50	K	NIST
Ttriple	[167.30; 167.62]	K
Ttriple	167.62	K	Staveley, Lobo and Calado (1981), triple points Compiled value
Ttriple	167.62	K	ChemSep v8.3 pure component data Compiled value
Ttriple	167.62 ± 0.02	K	NIST
Ttriple	167.61 ± 0.02	K	NIST
Ttriple	167.30 ± 0.20	K	NIST
Ttriple	167.62 ± 0.02	K	NIST
Ttriple	167.61 ± 0.02	K	NIST
Ttriple	167.30 ± 0.20	K	NIST
UQi	2.56		ChemSep v8.3 pure component data Compiled value
URi	2.92		ChemSep v8.3 pure component data Compiled value
Vc	[0.238; 0.238]	m3/kmol
Vc	0.238	m3/kmol	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 6 Compiled value
Vc	0.238	m3/kmol	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Vc	0.238	m3/kmol	ChemSep v8.3 pure component data Compiled value
Vc	0.238	m3/kmol	KDB
Vc	0.238	m3/kmol	NIST
VCOSTALD	0.24	m3/kmol	Hankinson and Thomson (1979), COSTALD parameters Compiled value
ωSRK	0.22		Hankinson and Thomson (1979), COSTALD parameters Compiled value
Zc	[0.2661250; 0.2760000]
Zc	0.2740000		IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 6 Compiled value
Zc	0.2760000		ChemSep v8.3 pure component data Compiled value
Zc	0.2661250		KDB
Zra	[0.27; 0.27]
Zra	0.27		Hankinson and Thomson (1979), COSTALD parameters Compiled value
Zra	0.27		ChemSep v8.3 pure component data Compiled value
Zra	0.27		KDB

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

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[87.78; 102.63]	J/mol×K	[298.60; 371.50]
Cp,gas	87.78	J/mol×K	298.60	NIST
Cp,gas	94.93	J/mol×K	332.90	NIST
Cp,gas	102.63	J/mol×K	371.50	NIST
Cp,liquid	[110.50; 124.40]	J/mol×K	[170.00; 270280.00]
Cp,liquid	110.50	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
Cp,liquid	110.90	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
Cp,liquid	111.50	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
Cp,liquid	112.40	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
Cp,liquid	113.50	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
Cp,liquid	114.70	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
Cp,liquid	116.10	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
Cp,liquid	117.50	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
Cp,liquid	119.00	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
Cp,liquid	122.05	J/mol×K	259.60	NIST
Cp,liquid	120.50	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
Cp,liquid	121.90	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
Cp,liquid	124.40	J/mol×K	280.00	NIST
Cp,liquid	122.34	J/mol×K	270280.00	NIST
ΔfusH	[9.76; 9.86]	kJ/mol	[167.30; 167.62]
ΔfusH	9.86	kJ/mol	167.30	NIST
ΔfusH	9.86	kJ/mol	167.30	NIST
ΔfusH	9.76	kJ/mol	167.60	NIST
ΔfusH	9.76	kJ/mol	167.60	NIST
ΔfusH	9.76	kJ/mol	167.61	NIST
ΔfusH	9.76	kJ/mol	167.61	NIST
ΔfusH	9.76	kJ/mol	167.62	NIST
ΔfusH	9.76	kJ/mol	167.62	NIST
ΔvapH	[22.72; 24.20]	kJ/mol	[238.50; 405.00]
ΔvapH	24.20	kJ/mol	238.50	NIST
ΔvapH	24.20	kJ/mol	238.50	NIST
ΔvapH	23.90	kJ/mol	244.00	NIST
ΔvapH	23.90	kJ/mol	246.00	NIST
ΔvapH	23.83	kJ/mol	273.40	NIST
ΔvapH	22.72	kJ/mol	274.00	NIST
ΔvapH	22.80 ± 0.10	kJ/mol	274.00	NIST
ΔvapH	22.76 ± 0.63	kJ/mol	274.00	NIST
ΔvapH	22.76	kJ/mol	274.00	KDB
ΔvapH	22.76 ± 0.63	kJ/mol	274.00	NIST
ΔvapH	22.80 ± 0.10	kJ/mol	274.00	NIST
ΔvapH	22.76	kJ/mol	274.04	NIST
ΔvapH	22.76	kJ/mol	274.04	NIST
ΔvapH	23.60	kJ/mol	294.00	NIST
ΔvapH	23.30	kJ/mol	349.00	NIST
ΔvapH	23.20	kJ/mol	405.00	NIST
Pvap	[317.30; 1269.20]	kPa	[308.14; 364.50]
Pvap	317.30	kPa	308.14	Vapor-Liquid Equilibrium for Thiophene + Butane, + trans-But-2-ene, + 2-Methylpropane, and + 2-Methylpropene
Pvap	413.80	kPa	317.29	Isothermal binary vapour liquid equilibrium for butanes and butenes with dimethylsulphide
Pvap	417.30	kPa	317.46	Vapour liquid equilibrium for the systems diethyl sulphide + 1-butene, +cis-2-butene, +2-methylpropane, +2-methylpropene, +n-butane, +trans-2-butene
Pvap	423.50	kPa	318.34	Vapor-Liquid Equilibrium for Tetrahydrothiophene + n-Butane, + trans-2-Butene, + 2-Methylpropane, and + 2-Methylpropene
Pvap	605.54	kPa	332.04	Vapor Liquid Equilibrium for the Trans-2-Butene + Methanol, + Ethanol, + 2-Propanol, + 2-Butanol and + 2-Methyl-2-Propanol Systems at 332 K
Pvap	606.54	kPa	332.05	Vapor-Liquid Equilibrium for 1-Propanol + 1-Butene, + cis-2-Butene, + 2-Methyl-propene, + trans-2-Butene, + n-Butane, and + 2-Methyl-propane
Pvap	605.74	kPa	332.06	Vapor Liquid Equilibrium for the Trans-2-Butene + Methanol, + Ethanol, + 2-Propanol, + 2-Butanol and + 2-Methyl-2-Propanol Systems at 332 K
Pvap	606.94	kPa	332.07	Vapor Liquid Equilibrium for the Trans-2-Butene + Methanol, + Ethanol, + 2-Propanol, + 2-Butanol and + 2-Methyl-2-Propanol Systems at 332 K
Pvap	606.14	kPa	332.08	Vapor Liquid Equilibrium for the Trans-2-Butene + Methanol, + Ethanol, + 2-Propanol, + 2-Butanol and + 2-Methyl-2-Propanol Systems at 332 K
Pvap	606.44	kPa	332.08	Vapor Liquid Equilibrium for the Trans-2-Butene + Methanol, + Ethanol, + 2-Propanol, + 2-Butanol and + 2-Methyl-2-Propanol Systems at 332 K
Pvap	666.10	kPa	335.86	Vapor-Liquid Equilibrium for Thiophene + Butane, + trans-But-2-ene, + 2-Methylpropane, and + 2-Methylpropene
Pvap	868.50	kPa	347.06	Vapor-Liquid Equilibrium for Tetrahydrothiophene + n-Butane, + trans-2-Butene, + 2-Methylpropane, and + 2-Methylpropene
Pvap	929.20	kPa	350.30	Vapor-Liquid Equilibrium for Dimethyl Disulfide + Butane, + trans-But-2-ene, + 2-Methylpropane, + 2-Methylpropene, + Ethanol, and 2-Ethoxy-2-methylpropane
Pvap	1269.20	kPa	364.50	Vapor Liquid Equilibrium for Six Binary Systems of C4-Hydrocarbons + 2-Propanone
ρl	604.00	kg/m3	293.00	KDB
ΔfusS	[58.20; 58.94]	J/mol×K	[167.30; 167.62]
ΔfusS	58.94	J/mol×K	167.30	NIST
ΔfusS	58.94	J/mol×K	167.30	NIST
ΔfusS	58.21	J/mol×K	167.61	NIST
ΔfusS	58.21	J/mol×K	167.61	NIST
ΔfusS	58.20	J/mol×K	167.62	NIST
ΔfusS	58.20	J/mol×K	167.62	NIST
γ	0.01	N/m	293.20	KDB
ΔvapS	[83.04; 83.04]	J/mol×K	[274.04; 274.04]
ΔvapS	83.04	J/mol×K	274.04	NIST
ΔvapS	83.04	J/mol×K	274.04	NIST

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[69.39; 229.19]	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			6.00060e+01
Coefficient B			-6.49720e+02
Coefficient C			5.46024e+00
Coefficient D			1.46610e-04
Coefficient E			-5.15660e-08
Temperature range, min.			200.00
Temperature range, max.			1500.00
Cp,gas	69.39	J/mol×K	200.00	Calculated Property
Cp,gas	97.28	J/mol×K	344.44	Calculated Property
Cp,gas	126.07	J/mol×K	488.89	Calculated Property
Cp,gas	150.61	J/mol×K	633.33	Calculated Property
Cp,gas	170.81	J/mol×K	777.78	Calculated Property
Cp,gas	187.37	J/mol×K	922.22	Calculated Property
Cp,gas	201.02	J/mol×K	1066.67	Calculated Property
Cp,gas	212.28	J/mol×K	1211.11	Calculated Property
Cp,gas	221.57	J/mol×K	1355.56	Calculated Property
Cp,gas	229.19	J/mol×K	1500.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[110.07; 123.69]	J/mol×K	[167.62; 280.00]	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			9.87300e+01
Coefficient B			5.49960e+02
Coefficient C			-6.07643e+00
Coefficient D			3.86070e-02
Coefficient E			-4.43920e-05
Temperature range, min.			167.62
Temperature range, max.			280.00
Cp,liquid	110.07	J/mol×K	167.62	Calculated Property
Cp,liquid	110.80	J/mol×K	180.11	Calculated Property
Cp,liquid	111.77	J/mol×K	192.59	Calculated Property
Cp,liquid	112.97	J/mol×K	205.08	Calculated Property
Cp,liquid	114.37	J/mol×K	217.57	Calculated Property
Cp,liquid	115.96	J/mol×K	230.05	Calculated Property
Cp,liquid	117.71	J/mol×K	242.54	Calculated Property
Cp,liquid	119.61	J/mol×K	255.03	Calculated Property
Cp,liquid	121.61	J/mol×K	267.51	Calculated Property
Cp,liquid	123.69	J/mol×K	280.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.0011162; 0.0001106]	Pa×s	[167.62; 373.00]	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			-1.60564e+01
Coefficient B			8.33299e+02
Coefficient C			8.49646e-01
Coefficient D			-2.29223e-06
Coefficient E			2.00000e+00
Temperature range, min.			167.62
Temperature range, max.			373.00
η	0.0011162	Pa×s	167.62	Calculated Property
η	0.0006730	Pa×s	190.44	Calculated Property
η	0.0004542	Pa×s	213.26	Calculated Property
η	0.0003315	Pa×s	236.08	Calculated Property
η	0.0002560	Pa×s	258.90	Calculated Property
η	0.0002060	Pa×s	281.72	Calculated Property
η	0.0001710	Pa×s	304.54	Calculated Property
η	0.0001454	Pa×s	327.36	Calculated Property
η	0.0001259	Pa×s	350.18	Calculated Property
η	0.0001106	Pa×s	373.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ΔvapH	[27.66; 0.00]	kJ/mol	[167.62; 428.60]	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			3.34760e+01
Coefficient B			3.13550e-01
Coefficient C			4.14780e-01
Coefficient D			-7.55550e-01
Coefficient E			4.06950e-01
Critical temperature, Tc (K)			4.28600e+02
Temperature range, min.			167.62
Temperature range, max.			428.60
ΔvapH	27.66	kJ/mol	167.62	Calculated Property
ΔvapH	26.44	kJ/mol	196.62	Calculated Property
ΔvapH	25.16	kJ/mol	225.62	Calculated Property
ΔvapH	23.79	kJ/mol	254.61	Calculated Property
ΔvapH	22.29	kJ/mol	283.61	Calculated Property
ΔvapH	20.59	kJ/mol	312.61	Calculated Property
ΔvapH	18.55	kJ/mol	341.61	Calculated Property
ΔvapH	15.96	kJ/mol	370.60	Calculated Property
ΔvapH	12.25	kJ/mol	399.60	Calculated Property
ΔvapH	0.00	kJ/mol	428.60	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.67]	kPa	[197.14; 293.48]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.42351e+01
Coefficient B			-2.38673e+03
Coefficient C			-2.60150e+01
Temperature range, min.			197.14
Temperature range, max.			293.48
Pvap	1.33	kPa	197.14	Calculated Property
Pvap	3.03	kPa	207.84	Calculated Property
Pvap	6.29	kPa	218.55	Calculated Property
Pvap	12.08	kPa	229.25	Calculated Property
Pvap	21.74	kPa	239.96	Calculated Property
Pvap	36.99	kPa	250.66	Calculated Property
Pvap	59.98	kPa	261.37	Calculated Property
Pvap	93.24	kPa	272.07	Calculated Property
Pvap	139.71	kPa	282.78	Calculated Property
Pvap	202.67	kPa	293.48	Calculated Property
Pvap	[0.09; 4076.22]	kPa	[167.62; 428.60]	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			4.96942e+01
Coefficient B			-4.02670e+03
Coefficient C			-5.51780e+00
Coefficient D			7.91760e-06
Coefficient E			2.00000e+00
Comment			Range stopped at Tc; ChemSep gives it to 428.63 K.
Temperature range, min.			167.62
Temperature range, max.			428.60
Pvap	0.09	kPa	167.62	Calculated Property
Pvap	1.46	kPa	196.62	Calculated Property
Pvap	10.48	kPa	225.62	Calculated Property
Pvap	45.85	kPa	254.61	Calculated Property
Pvap	144.14	kPa	283.61	Calculated Property
Pvap	360.52	kPa	312.61	Calculated Property
Pvap	766.39	kPa	341.61	Calculated Property
Pvap	1448.02	kPa	370.60	Calculated Property
Pvap	2508.80	kPa	399.60	Calculated Property
Pvap	4076.22	kPa	428.60	Calculated Property
Pvap	[0.07; 4122.32]	kPa	[167.62; 428.63]	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			6.78830e+01
Coefficient B			-4.65896e+03
Coefficient C			-8.40556e+00
Coefficient D			1.22646e-05
Coefficient E			0.00000e+00
Temperature range, min.			167.62
Temperature range, max.			428.63
Pvap	0.07	kPa	167.62	Calculated Property
Pvap	1.31	kPa	196.62	Calculated Property
Pvap	10.07	kPa	225.62	Calculated Property
Pvap	45.41	kPa	254.62	Calculated Property
Pvap	144.23	kPa	283.62	Calculated Property
Pvap	361.04	kPa	312.63	Calculated Property
Pvap	765.95	kPa	341.63	Calculated Property
Pvap	1446.20	kPa	370.63	Calculated Property
Pvap	2514.05	kPa	399.63	Calculated Property
Pvap	4122.32	kPa	428.63	Calculated Property
Pvap	[1.98; 101.78]	kPa	[201.70; 274.13]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.39159e+01
Coefficient B			-2.26152e+03
Coefficient C			-3.07750e+01
Reference			Guttman and Pitzer, 1945
Comment			Coefficents calculated by NIST from author's data.
Temperature range, min.			201.70
Temperature range, max.			274.13
Pvap	1.98	kPa	201.70	Calculated Property
Pvap	3.60	kPa	209.75	Calculated Property
Pvap	6.19	kPa	217.80	Calculated Property
Pvap	10.20	kPa	225.84	Calculated Property
Pvap	16.15	kPa	233.89	Calculated Property
Pvap	24.68	kPa	241.94	Calculated Property
Pvap	36.57	kPa	249.99	Calculated Property
Pvap	52.70	kPa	258.03	Calculated Property
Pvap	74.07	kPa	266.08	Calculated Property
Pvap	101.78	kPa	274.13	Calculated Property
Pvap	[1.98; 101.78]	kPa	[201.70; 274.13]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.39159e+01
Coefficient B			-2.26152e+03
Coefficient C			-3.07750e+01
Reference			Guttman and Pitzer, 1945, 2
Comment			Coefficents calculated by NIST from author's data.
Temperature range, min.			201.70
Temperature range, max.			274.13
Pvap	1.98	kPa	201.70	Calculated Property
Pvap	3.60	kPa	209.75	Calculated Property
Pvap	6.19	kPa	217.80	Calculated Property
Pvap	10.20	kPa	225.84	Calculated Property
Pvap	16.15	kPa	233.89	Calculated Property
Pvap	24.68	kPa	241.94	Calculated Property
Pvap	36.57	kPa	249.99	Calculated Property
Pvap	52.70	kPa	258.03	Calculated Property
Pvap	74.07	kPa	266.08	Calculated Property
Pvap	101.78	kPa	274.13	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ρl	[734.08; 237.38]	kg/m3	[167.62; 428.60]	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			6.46513e+01
Coefficient B			2.72350e-01
Coefficient C			4.28600e+02
Coefficient D			2.85430e-01
Temperature range, min.			167.62
Temperature range, max.			428.60
ρl	734.08	kg/m3	167.62	Calculated Property
ρl	707.19	kg/m3	196.62	Calculated Property
ρl	678.90	kg/m3	225.62	Calculated Property
ρl	648.88	kg/m3	254.61	Calculated Property
ρl	616.62	kg/m3	283.61	Calculated Property
ρl	581.35	kg/m3	312.61	Calculated Property
ρl	541.71	kg/m3	341.61	Calculated Property
ρl	495.01	kg/m3	370.60	Calculated Property
ρl	433.83	kg/m3	399.60	Calculated Property
ρl	237.38	kg/m3	428.60	Calculated Property

Property	Value	Unit	Temperature (K)	Source
γ	[0.03; 5.55e-08]	N/m	[167.62; 427.30]	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			-7.11160e-03
Coefficient B			8.43810e+01
Coefficient C			-4.11490e+00
Coefficient D			4.75210e-03
Coefficient E			-1.67550e-05
Comment			Range stopped where the equation turns negative; ChemSep gives it to 428.6 K.
Temperature range, min.			167.62
Temperature range, max.			427.30
γ	0.03	N/m	167.62	Calculated Property
γ	0.03	N/m	196.47	Calculated Property
γ	0.02	N/m	225.33	Calculated Property
γ	0.02	N/m	254.18	Calculated Property
γ	0.01	N/m	283.03	Calculated Property
γ	0.01	N/m	311.88	Calculated Property
γ	0.01	N/m	340.74	Calculated Property
γ	0.00	N/m	369.59	Calculated Property
γ	0.00	N/m	398.44	Calculated Property
γ	5.55e-08	N/m	427.30	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λgas	[0.00; 0.14]	W/m×K	[167.62; 1257.00]	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			7.85630e-05
Coefficient B			1.05650e+00
Coefficient C			1.47530e+01
Coefficient D			1.05810e+05
Temperature range, min.			167.62
Temperature range, max.			1257.00
λgas	0.00	W/m×K	167.62	Calculated Property
λgas	0.01	W/m×K	288.66	Calculated Property
λgas	0.03	W/m×K	409.70	Calculated Property
λgas	0.04	W/m×K	530.75	Calculated Property
λgas	0.06	W/m×K	651.79	Calculated Property
λgas	0.07	W/m×K	772.83	Calculated Property
λgas	0.09	W/m×K	893.87	Calculated Property
λgas	0.11	W/m×K	1014.92	Calculated Property
λgas	0.12	W/m×K	1135.96	Calculated Property
λgas	0.14	W/m×K	1257.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λliquid	[0.15; 0.07]	W/m×K	[167.60; 392.74]	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			6.00040e-02
Coefficient B			3.68810e+02
Coefficient C			-7.37370e+00
Coefficient D			2.50780e-02
Coefficient E			-4.95260e-05
Temperature range, min.			167.60
Temperature range, max.			392.74
λliquid	0.15	W/m×K	167.60	Calculated Property
λliquid	0.14	W/m×K	192.62	Calculated Property
λliquid	0.14	W/m×K	217.63	Calculated Property
λliquid	0.13	W/m×K	242.65	Calculated Property
λliquid	0.12	W/m×K	267.66	Calculated Property
λliquid	0.11	W/m×K	292.68	Calculated Property
λliquid	0.10	W/m×K	317.69	Calculated Property
λliquid	0.09	W/m×K	342.71	Calculated Property
λliquid	0.08	W/m×K	367.72	Calculated Property
λliquid	0.07	W/m×K	392.74	Calculated Property

Similar Compounds

Find more compounds similar to 2-Butene, (E)-.

Mixtures

• 2-Butene, (E)- + Ethyl Acetate
• Dimethyl sulfide + 2-Butene, (E)-
• 2-Butene, (E)- + 1-Pentanol
• 2-Pentanol + 2-Butene, (E)-
• 2-Butene, (E)- + 3-Pentanol
• 1-Propanol + 2-Butene, (E)-
• 2-Butene, (E)- + Diethyl sulfide
• 1-Propanol, 2-methyl- + 2-Butene, (E)-
• 2-Propanol, 2-methyl- + 2-Butene, (E)-
• 2-Butene, (E)- + Methyl Alcohol
• Tetrahydropyran + 2-Butene, (E)-
• Ethanol + 2-Butene, (E)-
• 2-Propanol + 2-Butene, (E)-
• 1-Butanol, 2-methyl- + 2-Butene, (E)-
• 1-Butanol, 3-methyl- + 2-Butene, (E)-
• Amylene hydrate + 2-Butene, (E)-
• Allyl alcohol + 2-Butene, (E)-
• Acetone + 2-Butene, (E)-
• Thiophene, tetrahydro- + 2-Butene, (E)-
• 1-Butanol + 2-Butene, (E)-

Find more mixtures with 2-Butene, (E)-.

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.
• 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
• Crippen Method
• Thermodynamic properties of the butenes Part I. Experimental densities, vapor pressures, and critical points
• Vapour liquid equilibrium for the ethyl ethanoate + 1-butene, +cis-2-butene, +trans-2-butene, +2-methylpropene, +n-butane and +2-methylpropane
• Henry s law constants of 1-butene, 2-methylpropene, trans-2-butene, and 1,3-butadiene in methanol at 374 490K
• Isothermal binary vapour liquid equilibrium for butanes and butenes with dimethylsulphide
• Vapour liquid equilibrium for the systems diethyl sulphide + 1-butene, +cis-2-butene, +2-methylpropane, +2-methylpropene, +n-butane, +trans-2-butene
• Henry's constants and infinite dilution activity coefficients of propane, propene, butane, isobutene, 1-butene, isobutane, trans-2-butene and 1,3-butadiene in 1-propanol at T=(260 to 340) K
• Henry's constants and infinite dilution activity coefficients of propane, propene, butane, isobutane, 1-butene, isobutene, trans-2-butene, and 1,3-butadiene in isobutanol and tert-butanol
• Henry's constants and infinite dilution activity coefficients of propane, propene, butane, isobutane, 1-butene, isobutene, trans-2-butene, and 1,3-butadiene in 1-pentanol, 2-pentanol and 3-pentanol
• Vapor Liquid Equilibrium for the Trans-2-Butene + Methanol, + Ethanol, + 2-Propanol, + 2-Butanol and + 2-Methyl-2-Propanol Systems at 332 K
• Henry's Constants and Infinite Dilution Activity Coefficients of Propane, Propene, Butane, Isobutane, 1-Butene, Isobutene, trans-2-Butene, and 1,3-butadiene in 2-propanol at 250-330 K
• Henry's Constants and Infinite Dilution Activity Coefficients of Propane, Propene, Butane, Isobutane, 1-Butene, Isobutene, trans-2-Butene and 1,3-Butadiene in 1-Butanol and 2-Butanol at (250 to 330) K
• Henry's law constants and infinite dilution activity coefficients of propane, propene, butane, isobutane, 1-butene, isobutene, trans-2-butene, and 1,3-butadiene in 2-methyl-1-butanol, 3-methyl-1-butanol, and 2-methyl-2-butanol
• Vapor-Liquid Equilibrium for 1-Propanol + 1-Butene, + cis-2-Butene, + 2-Methyl-propene, + trans-2-Butene, + n-Butane, and + 2-Methyl-propane
• Henry's Law Constants and Infinite Dilution Activity Coefficients of Propane, Propene, Butane, 2-Methylpropane, 1-Butene, 2-Methylpropene, trans-2-Butene, cis-2-Butene, 1,3-Butadiene, Dimethyl Ether, Chloroethane, and 1,1-Difluoroethane in 2-Propen-1-ol
• Henry s Law Constants and Infinite Dilution Activity Coefficients of Propane, Propene, Butane, 2-Methylpropane, 1-Butene, 2-Methylpropene, trans-2-Butene, cis-2-Butene, 1,3-Butadiene, Dimethyl Ether, Chloroethane, and 1,1-Difluoroethane in 2-Methyl-3-buten-2-ol and 3-Methyl-3-buten-1-ol
• Vapor Liquid Equilibrium for Six Binary Systems of C4-Hydrocarbons + 2-Propanone
• Henry's Law Constants and Infinite Dilution Activity Coefficients of Propane, Propene, Butane, 2-Methylpropane, 1-Butene, 2-Methylpropene, trans-2-Butene, cis-2-Butene, 1,3-Butadiene, Dimethyl Ether, Chloroethane, and 1,1-Difluoroethane in Benzene, Toluene, o-Xylene, m-Xylene, p-Xylene, and Styrene
• Henry's Law Constants and Infinite Dilution Activity Coefficients of Propane, Propene, Butane, 2-Methylpropane, 1-Butene, 2-Methylpropene, trans-2-Butene, cis-2-Butene, 1,3-Butadiene, Dimethyl Ether, Chloroethane, and 1,1-Difluoroethane in 2-Methylphenol, 3-Methylphenol, and 4-Methylphenol
• Vapor-Liquid Equilibrium for Thiophene + Butane, + trans-But-2-ene, + 2-Methylpropane, and + 2-Methylpropene
• Vapor-Liquid Equilibrium for Dimethyl Disulfide + Butane, + trans-But-2-ene, + 2-Methylpropane, + 2-Methylpropene, + Ethanol, and 2-Ethoxy-2-methylpropane
• Henry s Law Constants and Infinite Dilution Activity Coefficients of Propane, Propene, Butane, 2-Methylpropane, 1-Butene, 2-Methylpropene, trans-2-Butene, cis-2-Butene, 1,3-Butadiene, Dimethylether, Chloroethane, 1,1-Difluoroethane, and Hexane in Tetrahydropyran
• Vapor Liquid Equilibrium for the Systems trans-2-Butene + Methanol, + 1-Propanol, + 2-Propanol, + 2-Butanol, and + 2-Methyl-2-propanol at 364.5 K
• Vapor-Liquid Equilibrium for Tetrahydrothiophene + n-Butane, + trans-2-Butene, + 2-Methylpropane, and + 2-Methylpropene
• Joback Method
• KDB
• 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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