Chemical Properties of 1-Butene (CAS 106-98-9)

InChI

InChI=1S/C4H8/c1-3-4-2/h3H,1,4H2,2H3

InChI Key

VXNZUUAINFGPBY-UHFFFAOYSA-N

Formula

C4H8

SMILES

C=CCC

Molecular Weight¹

56.11

CAS

106-98-9

Other Names

• 1-C4H8
• 1-butylene
• But-1-ene
• Butene-1
• Ethylethylene
• «alpha»-Butene
• «alpha»-Butylene

• ω : Acentric Factor.
• T_ig : Autoignition Temperature (K).
• 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).
• Δ_fG° : Standard Gibbs free energy of formation (kJ/mol).
• R_g : Radius of Gyration.
• 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).
• 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.
• 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.
• 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	[0.1870; 0.1940]
ω	0.1870		PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
ω	0.1874		Passut and Danner (1973), critical constants and acentric factors Compiled value
ω	0.1940		ChemSep v8.3 pure component data Compiled value
ω	0.1910		KDB
Tig	658.15	K	KDB
ΔcH°gas	-2716.80 ± 0.75	kJ/mol	NIST
μ	[0.30; 0.34]	debye
μ	0.34	debye	ChemSep v8.3 pure component data Compiled value
μ	0.30	debye	KDB
LFL	1.60	% in Air	KDB
UFL	10.00	% in Air	KDB
ΔfG°	[70.41; 71.34]	kJ/mol
ΔfG°	70.41	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfG°	71.34	kJ/mol	KDB
Rg	2.7460		KDB
Δc,grossH	2696.55	kJ/mol	KDB
Δc,netH	2520.483	kJ/mol	KDB
ΔfH°gas	[-0.63; -0.03]	kJ/mol
ΔfH°gas	-0.03 ± 0.48	kJ/mol	Active Thermochemical Tables 1.112, gas-phase enthalpies of formation Compiled value
ΔfH°gas	-0.50	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfH°gas	-0.13	kJ/mol	KDB
ΔfH°gas	-0.63 ± 0.79	kJ/mol	NIST
ΔfusH°	4.84	kJ/mol	Joback Calculated Property
ΔvapH°	[20.10; 20.88]	kJ/mol
ΔvapH°	20.88	kJ/mol	NIST
ΔvapH°	20.10	kJ/mol	NIST
IE	[9.55; 10.00]	eV
IE	9.55 ± 0.06	eV	NIST
IE	9.55 ± 0.06	eV	NIST
IE	9.57	eV	NIST
IE	9.58	eV	NIST
IE	9.62 ± 0.05	eV	NIST
IE	9.59 ± 0.02	eV	NIST
IE	9.63 ± 0.02	eV	NIST
IE	9.62 ± 0.00	eV	NIST
IE	9.58	eV	NIST
IE	9.59	eV	NIST
IE	9.62	eV	NIST
IE	9.61 ± 0.02	eV	NIST
IE	9.58 ± 0.01	eV	NIST
IE	9.77 ± 0.01	eV	NIST
IE	Outlier 10.00	eV	NIST
IE	9.72	eV	NIST
log10WS	[-1.94; -1.94]
log10WS	-1.94		Aq. Solubility Prediction
log10WS	-1.94		Estimated Solubility
logPoct/wat	1.582		Crippen Calculated Property
McVol	62.920	ml/mol	McGowan Calculated Property
NFPA Fire	4		KDB
NFPA Health	1		KDB
Pc	[4000.00; 4022.60]	kPa
Pc	4005.10	kPa	Thermodynamic properties of the butenes Part I. Experimental densities, vapor pressures, and critical points
Pc	4000.00	kPa	Critical Temperatures and Pressures of Several Binary and Ternary Mixtures Concerning the Alkylation of 2-Methylpropane with 1-Butene in the Presence of Methane or Carbon Dioxide
Pc	4020.00	kPa	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 6 Compiled value
Pc	4022.60	kPa	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Pc	4019.64	kPa	Passut and Danner (1973), critical constants and acentric factors Compiled value
Pc	4020.00	kPa	ChemSep v8.3 pure component data Compiled value
Pc	4005.00	kPa	Air Liquide Gas Encyclopedia
Pc	4020.00	kPa	KDB
Pc	4020.00 ± 50.00	kPa	NIST
Ptriple	[6.94e-10; 6.94e-10]	kPa
Ptriple	6.94e-10	kPa	ChemSep v8.3 pure component data Compiled value
Ptriple	6.94e-10	kPa	Air Liquide Gas Encyclopedia
ρc	[232.84; 237.89]	kg/m3
ρc	237.89	kg/m3	Air Liquide Gas Encyclopedia
ρc	232.84 ± 2.81	kg/m3	NIST
Inp	[382.00; 402.00]
Inp	394.00		NIST
Inp	394.00		NIST
Inp	391.00		NIST
Inp	389.00		NIST
Inp	390.00		NIST
Inp	388.70		NIST
Inp	391.00		NIST
Inp	390.00		NIST
Inp	386.00		NIST
Inp	384.40		NIST
Inp	384.00		NIST
Inp	395.00		NIST
Inp	385.00		NIST
Inp	385.00		NIST
Inp	385.00		NIST
Inp	385.00		NIST
Inp	385.00		NIST
Inp	393.00		NIST
Inp	385.00		NIST
Inp	389.20		NIST
Inp	392.00		NIST
Inp	386.00		NIST
Inp	Outlier 400.00		NIST
Inp	388.00		NIST
Inp	385.00		NIST
Inp	Outlier 402.00		NIST
Inp	Outlier 400.00		NIST
Inp	390.00		NIST
Inp	392.00		NIST
Inp	382.00		NIST
Inp	385.00		NIST
Inp	385.00		NIST
Inp	385.00		NIST
Inp	388.00		NIST
Inp	386.00		NIST
Inp	387.00		NIST
Inp	386.00		NIST
Inp	390.00		NIST
Inp	384.00		NIST
Inp	391.00		NIST
Inp	383.00		NIST
Inp	387.00		NIST
Inp	386.00		NIST
Inp	386.00		NIST
Inp	387.00		NIST
Inp	387.00		NIST
Inp	387.00		NIST
Inp	386.00		NIST
Inp	390.00		NIST
Inp	390.00		NIST
Inp	392.00		NIST
Inp	390.00		NIST
Inp	386.00		NIST
Inp	394.00		NIST
Inp	388.70		NIST
Inp	384.00		NIST
Inp	385.00		NIST
Inp	388.00		NIST
Inp	389.20		NIST
Ip	[415.00; 436.00]
Ip	436.00		NIST
Ip	426.00		NIST
Ip	415.00		NIST
Ip	415.00		NIST
Ip	436.00		NIST
S°liquid	[213.84; 229.06]	J/mol×K
S°liquid	229.06	J/mol×K	NIST
S°liquid	227.00	J/mol×K	NIST
S°liquid	213.84	J/mol×K	NIST
Tboil	[266.45; 274.15]	K
Tboil	266.92	K	ChemSep v8.3 pure component data Compiled value
Tboil	266.84	K	Air Liquide Gas Encyclopedia
Tboil	266.89	K	KDB
Tboil	266.90	K	NIST
Tboil	266.90	K	NIST
Tboil	266.90 ± 0.60	K	NIST
Tboil	266.68 ± 0.30	K	NIST
Tboil	266.85 ± 0.60	K	NIST
Tboil	266.87 ± 0.55	K	NIST
Tboil	266.83 ± 0.20	K	NIST
Tboil	266.65 ± 1.50	K	NIST
Tboil	267.05 ± 1.00	K	NIST
Tboil	266.45 ± 0.50	K	NIST
Tboil	266.45 ± 0.50	K	NIST
Tboil	268.15 ± 2.00	K	NIST
Tboil	267.45 ± 1.00	K	NIST
Tboil	266.60 ± 0.50	K	NIST
Tboil	266.95 ± 1.00	K	NIST
Tboil	266.55 ± 0.50	K	NIST
Tboil	Outlier 274.15	K	NIST
Tc	[417.15; 419.60]	K
Tc	419.50	K	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 6 Compiled value
Tc	419.60	K	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Tc	419.59	K	Passut and Danner (1973), critical constants and acentric factors Compiled value
Tc	419.50	K	ChemSep v8.3 pure component data Compiled value
Tc	419.29	K	Air Liquide Gas Encyclopedia
Tc	419.50	K	KDB
Tc	419.50 ± 0.50	K	NIST
Tc	419.60	K	NIST
Tc	Outlier 417.15 ± 2.00	K	NIST
Tfus	[87.80; 87.93]	K
Tfus	87.85	K	Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
Tfus	87.80	K	ChemSep v8.3 pure component data Compiled value
Tfus	87.80	K	Air Liquide Gas Encyclopedia
Tfus	87.80	K	KDB
Tfus	87.93	K	Aq. Solubility Prediction
Ttriple	[87.80; 87.83]	K
Ttriple	87.83	K	Staveley, Lobo and Calado (1981), triple points Compiled value
Ttriple	87.80	K	ChemSep v8.3 pure component data Compiled value
Ttriple	87.80	K	Air Liquide Gas Encyclopedia
Ttriple	87.80 ± 0.01	K	NIST
Ttriple	87.82 ± 0.02	K	NIST
Ttriple	87.80 ± 0.05	K	NIST
Ttriple	87.83 ± 0.05	K	NIST
Ttriple	87.80 ± 0.01	K	NIST
Ttriple	87.82 ± 0.02	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	[0.240; 0.241]	m3/kmol
Vc	0.241	m3/kmol	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 6 Compiled value
Vc	Outlier 0.240	m3/kmol	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Vc	0.241	m3/kmol	ChemSep v8.3 pure component data Compiled value
Vc	0.241	m3/kmol	KDB
Vc	0.241	m3/kmol	NIST
VCOSTALD	0.24	m3/kmol	Hankinson and Thomson (1979), COSTALD parameters Compiled value
ωSRK	0.19		Hankinson and Thomson (1979), COSTALD parameters Compiled value
Zc	[0.2775330; 0.2780000]
Zc	0.2780000		IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 6 Compiled value
Zc	0.2780000		ChemSep v8.3 pure component data Compiled value
Zc	0.2775330		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

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[89.58; 101.21]	J/mol×K	[313.55; 363.25]
Cp,gas	89.58 ± 0.06	J/mol×K	313.55	NIST
Cp,gas	101.21 ± 0.07	J/mol×K	363.25	NIST
Cp,liquid	[105.40; 165.00]	J/mol×K	[90.00; 370.00]
Cp,liquid	109.20	J/mol×K	90.00	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	107.70	J/mol×K	100.00	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	106.60	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
Cp,liquid	105.90	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
Cp,liquid	105.50	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
Cp,liquid	105.40	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
Cp,liquid	105.70	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
Cp,liquid	106.20	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
Cp,liquid	106.90	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	107.80	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	108.90	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	110.20	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	111.60	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	113.10	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
Cp,liquid	114.60	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	116.00	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	118.00	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	119.16	J/mol×K	253.40	NIST
Cp,liquid	120.00	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	119.45	J/mol×K	260.00	NIST
Cp,liquid	122.00	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	122.00	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
Cp,liquid	124.00	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
Cp,liquid	127.00	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
Cp,liquid	128.60	J/mol×K	294.00	NIST
Cp,liquid	118.00	J/mol×K	298.15	NIST
Cp,liquid	129.00	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
Cp,liquid	128.96	J/mol×K	298.15	NIST
Cp,liquid	129.00	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
Cp,liquid	133.00	J/mol×K	310.00	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	137.00	J/mol×K	320.00	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	141.00	J/mol×K	330.00	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	146.00	J/mol×K	340.00	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	152.00	J/mol×K	350.00	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	158.00	J/mol×K	360.00	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	165.00	J/mol×K	370.00	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	[3.85; 3.96]	kJ/mol	[87.80; 87.82]
ΔfusH	3.85	kJ/mol	87.80	Air Liquide Gas Encyclopedia
ΔfusH	3.85	kJ/mol	87.80	NIST
ΔfusH	3.85	kJ/mol	87.80	NIST
ΔfusH	3.96	kJ/mol	87.81	NIST
ΔfusH	3.96	kJ/mol	87.81	NIST
ΔfusH	3.85	kJ/mol	87.82	NIST
ΔfusH	3.85	kJ/mol	87.82	NIST
ΔfusH	3.85	kJ/mol	87.82	NIST
ΔvapH	[21.87; 28.30]	kJ/mol	[159.00; 376.50]
ΔvapH	28.30	kJ/mol	159.00	NIST
ΔvapH	23.70	kJ/mol	202.00	NIST
ΔvapH	25.30	kJ/mol	202.00	NIST
ΔvapH	24.50	kJ/mol	219.00	NIST
ΔvapH	23.30	kJ/mol	237.00	NIST
ΔvapH	23.30	kJ/mol	242.00	NIST
ΔvapH	23.20	kJ/mol	244.50	NIST
ΔvapH	22.01	kJ/mol	266.84	Air Liquide Gas Encyclopedia
ΔvapH	22.07	kJ/mol	266.90	NIST
ΔvapH	21.92	kJ/mol	266.90	KDB
ΔvapH	21.87	kJ/mol	266.91	NIST
ΔvapH	21.90	kJ/mol	267.00	NIST
ΔvapH	22.80	kJ/mol	306.00	NIST
ΔvapH	22.50	kJ/mol	339.00	NIST
ΔvapH	22.00	kJ/mol	376.50	NIST
Pvap	[343.00; 1510.50]	kPa	[302.90; 364.53]
Pvap	343.00	kPa	302.90	Experimental vapour liquid equilibrium data and modeling for binary mixtures of 1-butene with 1,1,2,3,3,3-hexafluoro-1-propene, 2,2,3-trifluoro-3-(trifluoromethyl)oxirane, or difluoromethane
Pvap	396.00	kPa	307.83	Experimental vapour liquid equilibrium data and modeling for binary mixtures of 1-butene with 1,1,2,3,3,3-hexafluoro-1-propene, 2,2,3-trifluoro-3-(trifluoromethyl)oxirane, or difluoromethane
Pvap	454.50	kPa	312.57	Isothermal binary vapour liquid equilibrium for butanes and butenes with dimethylsulphide
Pvap	451.30	kPa	312.58	Vapour liquid equilibrium for the systems diethyl sulphide + 1-butene, +cis-2-butene, +2-methylpropane, +2-methylpropene, +n-butane, +trans-2-butene
Pvap	448.30	kPa	312.59	Phase equilibrium measurements for systems containing propanenitrile with tert-butyl ethyl ether and C4-hydrocarbons
Pvap	456.00	kPa	312.96	Experimental vapour liquid equilibrium data and modeling for binary mixtures of 1-butene with 1,1,2,3,3,3-hexafluoro-1-propene, 2,2,3-trifluoro-3-(trifluoromethyl)oxirane, or difluoromethane
Pvap	521.00	kPa	318.05	Experimental vapour liquid equilibrium data and modeling for binary mixtures of 1-butene with 1,1,2,3,3,3-hexafluoro-1-propene, 2,2,3-trifluoro-3-(trifluoromethyl)oxirane, or difluoromethane
Pvap	525.20	kPa	318.32	Vapor-Liquid Equilibrium for 1-Butanol + 1-Butene at (318.4 and 364.5) K and Vapor-Liquid Equilibrium of 1-Butanol + 2-Methylpropane, + n-Butane and 1-Butene + 2-Methylpropane at 318.4 K
Pvap	525.80	kPa	318.40	Vapor-Liquid Equilibrium for 1-Butanol + 1-Butene at (318.4 and 364.5) K and Vapor-Liquid Equilibrium of 1-Butanol + 2-Methylpropane, + n-Butane and 1-Butene + 2-Methylpropane at 318.4 K
Pvap	525.55	kPa	318.42	Vapour liquid equilibrium for the ethyl ethanoate + 1-butene, +cis-2-butene, +trans-2-butene, +2-methylpropene, +n-butane and +2-methylpropane
Pvap	593.00	kPa	322.94	Experimental vapour liquid equilibrium data and modeling for binary mixtures of 1-butene with 1,1,2,3,3,3-hexafluoro-1-propene, 2,2,3-trifluoro-3-(trifluoromethyl)oxirane, or difluoromethane
Pvap	596.14	kPa	323.27	Vapor-Liquid Equilibrium for 1-Propanol + 1-Butene, + cis-2-Butene, + 2-Methyl-propene, + trans-2-Butene, + n-Butane, and + 2-Methyl-propane
Pvap	671.00	kPa	328.06	Experimental vapour liquid equilibrium data and modeling for binary mixtures of 1-butene with 1,1,2,3,3,3-hexafluoro-1-propene, 2,2,3-trifluoro-3-(trifluoromethyl)oxirane, or difluoromethane
Pvap	759.00	kPa	332.97	Experimental vapour liquid equilibrium data and modeling for binary mixtures of 1-butene with 1,1,2,3,3,3-hexafluoro-1-propene, 2,2,3-trifluoro-3-(trifluoromethyl)oxirane, or difluoromethane
Pvap	855.00	kPa	337.99	Experimental vapour liquid equilibrium data and modeling for binary mixtures of 1-butene with 1,1,2,3,3,3-hexafluoro-1-propene, 2,2,3-trifluoro-3-(trifluoromethyl)oxirane, or difluoromethane
Pvap	957.00	kPa	342.98	Experimental vapour liquid equilibrium data and modeling for binary mixtures of 1-butene with 1,1,2,3,3,3-hexafluoro-1-propene, 2,2,3-trifluoro-3-(trifluoromethyl)oxirane, or difluoromethane
Pvap	1069.00	kPa	347.93	Experimental vapour liquid equilibrium data and modeling for binary mixtures of 1-butene with 1,1,2,3,3,3-hexafluoro-1-propene, 2,2,3-trifluoro-3-(trifluoromethyl)oxirane, or difluoromethane
Pvap	1197.00	kPa	353.18	Experimental vapour liquid equilibrium data and modeling for binary mixtures of 1-butene with 1,1,2,3,3,3-hexafluoro-1-propene, 2,2,3-trifluoro-3-(trifluoromethyl)oxirane, or difluoromethane
Pvap	1510.50	kPa	364.51	Vapor Liquid Equilibrium for Six Binary Systems of C4-Hydrocarbons + 2-Propanone
Pvap	1509.40	kPa	364.53	Vapor-Liquid Equilibrium for 1-Butanol + 1-Butene at (318.4 and 364.5) K and Vapor-Liquid Equilibrium of 1-Butanol + 2-Methylpropane, + n-Butane and 1-Butene + 2-Methylpropane at 318.4 K
ρg	[2.45; 2.67]	kg/m3	[266.84; 288.15]
ρg	2.67	kg/m3	266.84	Air Liquide Gas Encyclopedia
ρg	2.45	kg/m3	288.15	Air Liquide Gas Encyclopedia
ρl	[595.00; 625.63]	kg/m3	[266.84; 293.00]
ρl	625.63	kg/m3	266.84	Air Liquide Gas Encyclopedia
ρl	595.00	kg/m3	293.00	KDB
ΔfusS	[43.80; 45.09]	J/mol×K	[87.81; 87.82]
ΔfusS	45.09	J/mol×K	87.81	NIST
ΔfusS	45.09	J/mol×K	87.81	NIST
ΔfusS	43.80	J/mol×K	87.82	NIST
ΔfusS	43.83	J/mol×K	87.82	NIST
ΔfusS	43.80	J/mol×K	87.82	NIST
γ	0.01	N/m	293.20	KDB
ΔvapS	81.92	J/mol×K	266.91	NIST

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[65.06; 229.02]	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			5.35290e+01
Coefficient B			-6.19260e+02
Coefficient C			5.52324e+00
Coefficient D			9.66320e-05
Coefficient E			-3.90130e-08
Temperature range, min.			200.00
Temperature range, max.			1500.00
Cp,gas	65.06	J/mol×K	200.00	Calculated Property
Cp,gas	96.22	J/mol×K	344.44	Calculated Property
Cp,gas	126.82	J/mol×K	488.89	Calculated Property
Cp,gas	152.12	J/mol×K	633.33	Calculated Property
Cp,gas	172.47	J/mol×K	777.78	Calculated Property
Cp,gas	188.86	J/mol×K	922.22	Calculated Property
Cp,gas	202.15	J/mol×K	1066.67	Calculated Property
Cp,gas	212.98	J/mol×K	1211.11	Calculated Property
Cp,gas	221.82	J/mol×K	1355.56	Calculated Property
Cp,gas	229.02	J/mol×K	1500.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[108.44; 177.61]	J/mol×K	[81.29; 380.00]	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			1.00270e+02
Coefficient B			8.63450e+01
Coefficient C			8.25545e-01
Coefficient D			9.65460e-04
Coefficient E			2.02810e-05
Temperature range, min.			81.29
Temperature range, max.			380.00
Cp,liquid	108.44	J/mol×K	81.29	Calculated Property
Cp,liquid	107.34	J/mol×K	114.48	Calculated Property
Cp,liquid	107.62	J/mol×K	147.67	Calculated Property
Cp,liquid	108.78	J/mol×K	180.86	Calculated Property
Cp,liquid	110.91	J/mol×K	214.05	Calculated Property
Cp,liquid	114.47	J/mol×K	247.24	Calculated Property
Cp,liquid	120.34	J/mol×K	280.43	Calculated Property
Cp,liquid	130.19	J/mol×K	313.62	Calculated Property
Cp,liquid	147.20	J/mol×K	346.81	Calculated Property
Cp,liquid	177.61	J/mol×K	380.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.0176940; 0.0001224]	Pa×s	[87.80; 335.60]	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			-1.07640e+01
Coefficient B			5.91510e+02
Coefficient C			-1.73070e-03
Coefficient D			2.57230e-08
Coefficient E			2.00000e+00
Temperature range, min.			87.80
Temperature range, max.			335.60
η	0.0176940	Pa×s	87.80	Calculated Property
η	0.0035416	Pa×s	115.33	Calculated Property
η	0.0013178	Pa×s	142.87	Calculated Property
η	0.0006750	Pa×s	170.40	Calculated Property
η	0.0004165	Pa×s	197.93	Calculated Property
η	0.0002891	Pa×s	225.47	Calculated Property
η	0.0002174	Pa×s	253.00	Calculated Property
η	0.0001728	Pa×s	280.53	Calculated Property
η	0.0001432	Pa×s	308.07	Calculated Property
η	0.0001224	Pa×s	335.60	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ΔvapH	[30.59; 0.00]	kJ/mol	[87.80; 419.50]	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			3.53380e+01
Coefficient B			6.81860e-01
Coefficient C			-2.80990e-01
Coefficient D			-2.53690e-01
Coefficient E			2.60170e-01
Critical temperature, Tc (K)			4.19500e+02
Temperature range, min.			87.80
Temperature range, max.			419.50
ΔvapH	30.59	kJ/mol	87.80	Calculated Property
ΔvapH	28.77	kJ/mol	124.66	Calculated Property
ΔvapH	27.03	kJ/mol	161.51	Calculated Property
ΔvapH	25.33	kJ/mol	198.37	Calculated Property
ΔvapH	23.61	kJ/mol	235.22	Calculated Property
ΔvapH	21.76	kJ/mol	272.08	Calculated Property
ΔvapH	19.62	kJ/mol	308.93	Calculated Property
ΔvapH	16.92	kJ/mol	345.79	Calculated Property
ΔvapH	12.98	kJ/mol	382.64	Calculated Property
ΔvapH	0.00	kJ/mol	419.50	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.67]	kPa	[190.81; 285.85]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.41892e+01
Coefficient B			-2.33475e+03
Coefficient C			-2.28580e+01
Temperature range, min.			190.81
Temperature range, max.			285.85
Pvap	1.33	kPa	190.81	Calculated Property
Pvap	3.04	kPa	201.37	Calculated Property
Pvap	6.30	kPa	211.93	Calculated Property
Pvap	12.11	kPa	222.49	Calculated Property
Pvap	21.79	kPa	233.05	Calculated Property
Pvap	37.07	kPa	243.61	Calculated Property
Pvap	60.08	kPa	254.17	Calculated Property
Pvap	93.35	kPa	264.73	Calculated Property
Pvap	139.80	kPa	275.29	Calculated Property
Pvap	202.67	kPa	285.85	Calculated Property
Pvap	[2.93e-09; 3881.34]	kPa	[87.80; 419.50]	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			3.47581e+01
Coefficient B			-3.60500e+03
Coefficient C			-2.98356e+00
Coefficient D			6.66577e-07
Coefficient E			2.00000e+00
Temperature range, min.			87.80
Temperature range, max.			419.50
Pvap	2.93e-09	kPa	87.80	Calculated Property
Pvap	1.94e-04	kPa	124.66	Calculated Property
Pvap	0.07	kPa	161.51	Calculated Property
Pvap	2.29	kPa	198.37	Calculated Property
Pvap	23.98	kPa	235.22	Calculated Property
Pvap	125.39	kPa	272.08	Calculated Property
Pvap	423.02	kPa	308.93	Calculated Property
Pvap	1065.27	kPa	345.79	Calculated Property
Pvap	2188.29	kPa	382.64	Calculated Property
Pvap	3881.34	kPa	419.50	Calculated Property
Pvap	[3.40e-10; 3954.70]	kPa	[87.80; 419.59]	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			6.43474e+01
Coefficient B			-4.50983e+03
Coefficient C			-7.78979e+00
Coefficient D			9.81623e-06
Coefficient E			0.00000e+00
Temperature range, min.			87.80
Temperature range, max.			419.59
Pvap	3.40e-10	kPa	87.80	Calculated Property
Pvap	9.46e-05	kPa	124.67	Calculated Property
Pvap	0.05	kPa	161.53	Calculated Property
Pvap	2.21	kPa	198.40	Calculated Property
Pvap	24.13	kPa	235.26	Calculated Property
Pvap	125.23	kPa	272.13	Calculated Property
Pvap	414.88	kPa	308.99	Calculated Property
Pvap	1035.55	kPa	345.86	Calculated Property
Pvap	2150.34	kPa	382.72	Calculated Property
Pvap	3954.70	kPa	419.59	Calculated Property
Pvap	[2.41; 109.08]	kPa	[195.70; 269.40]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.43842e+01
Coefficient B			-2.53102e+03
Coefficient C			-8.25600e+00
Reference			Coffin and Maass, 1928, 2
Comment			Coefficents calculated by NIST from author's data.
Temperature range, min.			195.70
Temperature range, max.			269.40
Pvap	2.41	kPa	195.70	Calculated Property
Pvap	4.25	kPa	203.89	Calculated Property
Pvap	7.14	kPa	212.08	Calculated Property
Pvap	11.54	kPa	220.27	Calculated Property
Pvap	17.99	kPa	228.46	Calculated Property
Pvap	27.17	kPa	236.64	Calculated Property
Pvap	39.87	kPa	244.83	Calculated Property
Pvap	57.03	kPa	253.02	Calculated Property
Pvap	79.71	kPa	261.21	Calculated Property
Pvap	109.08	kPa	269.40	Calculated Property
Pvap	[2.41; 109.08]	kPa	[195.70; 269.40]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.43842e+01
Coefficient B			-2.53102e+03
Coefficient C			-8.25600e+00
Reference			Coffin and Maass, 1928
Comment			Coefficents calculated by NIST from author's data.
Temperature range, min.			195.70
Temperature range, max.			269.40
Pvap	2.41	kPa	195.70	Calculated Property
Pvap	4.25	kPa	203.89	Calculated Property
Pvap	7.14	kPa	212.08	Calculated Property
Pvap	11.54	kPa	220.27	Calculated Property
Pvap	17.99	kPa	228.46	Calculated Property
Pvap	27.17	kPa	236.64	Calculated Property
Pvap	39.87	kPa	244.83	Calculated Property
Pvap	57.03	kPa	253.02	Calculated Property
Pvap	79.71	kPa	261.21	Calculated Property
Pvap	109.08	kPa	269.40	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ρl	[798.31; 245.59]	kg/m3	[87.80; 419.50]	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			5.49842e+01
Coefficient B			2.51690e-01
Coefficient C			4.19540e+02
Coefficient D			2.66450e-01
Comment			Range stopped at Tc; ChemSep gives it to 419.53 K.
Temperature range, min.			87.80
Temperature range, max.			419.50
ρl	798.31	kg/m3	87.80	Calculated Property
ρl	766.98	kg/m3	124.66	Calculated Property
ρl	734.04	kg/m3	161.51	Calculated Property
ρl	699.11	kg/m3	198.37	Calculated Property
ρl	661.60	kg/m3	235.22	Calculated Property
ρl	620.62	kg/m3	272.08	Calculated Property
ρl	574.61	kg/m3	308.93	Calculated Property
ρl	520.45	kg/m3	345.79	Calculated Property
ρl	449.62	kg/m3	382.64	Calculated Property
ρl	245.59	kg/m3	419.50	Calculated Property

Property	Value	Unit	Temperature (K)	Source
γ	[0.04; 0.02]	N/m	[88.15; 266.65]	Jasper (1972), surface tension of pure liquid compounds Compiled value
Equation			Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is γ in N/m, T in K
Coefficient A			5.13277e-02
Coefficient B			-1.32300e-04
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Temperature range, min.			88.15
Temperature range, max.			266.65
γ	0.04	N/m	88.15	Calculated Property
γ	0.04	N/m	107.98	Calculated Property
γ	0.03	N/m	127.82	Calculated Property
γ	0.03	N/m	147.65	Calculated Property
γ	0.03	N/m	167.48	Calculated Property
γ	0.03	N/m	187.32	Calculated Property
γ	0.02	N/m	207.15	Calculated Property
γ	0.02	N/m	226.98	Calculated Property
γ	0.02	N/m	246.82	Calculated Property
γ	0.02	N/m	266.65	Calculated Property
γ	[0.04; 5.47e-06]	N/m	[87.80; 415.85]	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			-1.18290e-02
Coefficient B			1.09290e+01
Coefficient C			-2.94120e+00
Coefficient D			-5.65220e-04
Coefficient E			-7.44090e-06
Comment			Range stopped where the equation turns negative; ChemSep gives it to 419.5 K.
Temperature range, min.			87.80
Temperature range, max.			415.85
γ	0.04	N/m	87.80	Calculated Property
γ	0.04	N/m	124.25	Calculated Property
γ	0.03	N/m	160.70	Calculated Property
γ	0.03	N/m	197.15	Calculated Property
γ	0.02	N/m	233.60	Calculated Property
γ	0.02	N/m	270.05	Calculated Property
γ	0.01	N/m	306.50	Calculated Property
γ	0.01	N/m	342.95	Calculated Property
γ	0.00	N/m	379.40	Calculated Property
γ	5.47e-06	N/m	415.85	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λgas	[0.00; 0.12]	W/m×K	[87.80; 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			9.21150e-05
Coefficient B			1.11810e+00
Coefficient C			7.17190e+02
Coefficient D			1.30370e+04
Temperature range, min.			87.80
Temperature range, max.			1000.00
λgas	0.00	W/m×K	87.80	Calculated Property
λgas	0.01	W/m×K	189.16	Calculated Property
λgas	0.01	W/m×K	290.51	Calculated Property
λgas	0.03	W/m×K	391.87	Calculated Property
λgas	0.04	W/m×K	493.22	Calculated Property
λgas	0.05	W/m×K	594.58	Calculated Property
λgas	0.07	W/m×K	695.93	Calculated Property
λgas	0.08	W/m×K	797.29	Calculated Property
λgas	0.10	W/m×K	898.64	Calculated Property
λgas	0.12	W/m×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λliquid	[0.19; 0.09]	W/m×K	[87.80; 363.15]	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			7.12670e-02
Coefficient B			9.94710e+01
Coefficient C			-4.20110e+00
Coefficient D			1.43250e-02
Coefficient E			-4.11570e-05
Temperature range, min.			87.80
Temperature range, max.			363.15
λliquid	0.19	W/m×K	87.80	Calculated Property
λliquid	0.18	W/m×K	118.39	Calculated Property
λliquid	0.17	W/m×K	148.99	Calculated Property
λliquid	0.16	W/m×K	179.58	Calculated Property
λliquid	0.15	W/m×K	210.18	Calculated Property
λliquid	0.14	W/m×K	240.77	Calculated Property
λliquid	0.12	W/m×K	271.37	Calculated Property
λliquid	0.11	W/m×K	301.96	Calculated Property
λliquid	0.10	W/m×K	332.56	Calculated Property
λliquid	0.09	W/m×K	363.15	Calculated Property

Similar Compounds

Find more compounds similar to 1-Butene.

Mixtures

• 1-Butene + Propanenitrile
• 1-Butene + Butane, decafluoro-
• 1-Butene + Ethyl Acetate
• Dimethyl sulfide + 1-Butene
• 1-Butene + 1-Pentanol
• 1-Butene + 2-Pentanol
• 1-Butene + 3-Pentanol
• 1-Butene + 1-Propanol
• 1-Butene + Propene, hexafluoro-
• 1-Butene + Hexafluoropropylene oxide
• 1-Butene + Methane, difluoro-
• 1-Butene + Diethyl sulfide
• 1-Butene + 1-Propanol, 2-methyl-
• 2-Propanol, 2-methyl- + 1-Butene
• 1-Butene + Methyl Alcohol
• 1-Butene + Tetrahydropyran
• 1-Butene + 1-Butanol
• 1-Butene + Isobutane
• 1-Butene + 1-Butanol, 2-methyl-
• 1-Butene + 1-Butanol, 3-methyl-

Find more mixtures with 1-Butene.

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.
• Jasper (1972), surface tension of pure liquid compounds ChEDL chemicals 1.5.2, from Jasper, J. J. The Surface Tension of Pure Liquid Compounds. J. Phys. Chem. Ref. Data 1972, 1, 841-1010 (as transcribed in Lange's Handbook).
• 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
• 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
• Phase equilibrium measurements for systems containing propanenitrile with tert-butyl ethyl ether and C4-hydrocarbons
• 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
• Experimental vapour liquid equilibrium data and modeling for binary mixtures of 1-butene with 1,1,2,3,3,3-hexafluoro-1-propene, 2,2,3-trifluoro-3-(trifluoromethyl)oxirane, or difluoromethane
• Experimental (vapour + liquid) equilibrium data and modelling for binary mixtures of decafluorobutane with propane and 1-butene
• Influence of a-Olefin Concentration and Length on the High-Pressure Phase Behavior of (a-Olefin + n-Hexane + LLDPE) Systems
• 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
• Solubilities of Gases in the Ionic Liquid 1-n-Butyl-3-methylimidazolium Bis(trifluoromethylsulfonyl)imide
• 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
• Critical Temperatures and Pressures of Several Binary and Ternary Mixtures Concerning the Alkylation of 2-Methylpropane with 1-Butene in the Presence of Methane or Carbon Dioxide
• 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 1-Butene + Methanol, + 1-Propanol, + 2-Propanol, + 2-Butanol, and 2-Methyl-2-propanol (TBA) at 364.5 K
• Vapor-Liquid Equilibrium for 1-Butanol + 1-Butene at (318.4 and 364.5) K and Vapor-Liquid Equilibrium of 1-Butanol + 2-Methylpropane, + n-Butane and 1-Butene + 2-Methylpropane at 318.4 K
• 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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