Chemical Properties of 1-Pentene (CAS 109-67-1)

InChI

InChI=1S/C5H10/c1-3-5-4-2/h3H,1,4-5H2,2H3

InChI Key

YWAKXRMUMFPDSH-UHFFFAOYSA-N

Formula

C5H10

SMILES

C=CCCC

Molecular Weight¹

70.13

CAS

109-67-1

Other Names

• 1-C5H10
• 1-Pentene 95
• Pentene-1
• Propylethylene
• pent-1-ene
• «alpha»-n-Amylene

• ω : Acentric Factor.
• T_ig : Autoignition Temperature (K).
• AP : Aniline Point (K).
• Δ_cH°_liquid : Standard liquid enthalpy of combustion (kJ/mol).
• C_p,gas : Ideal gas heat capacity (J/mol×K).
• C_p,liquid : Liquid phase heat capacity (J/mol×K).
• μ : Dipole Moment (debye).
• η : Dynamic viscosity (Pa×s).
• LFL : Lower Flammability Limit (% in Air).
• UFL : Upper Flammability Limit (% in Air).
• T_flash,cc : Flash Point (Closed Cup Method) (K).
• T_flash,oc : Flash Point (Open Cup Method) (K).
• 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_fH°_liquid : Liquid phase enthalpy of formation at standard conditions (kJ/mol).
• Δ_fusH° : Enthalpy of fusion at standard conditions (kJ/mol).
• Δ_fusH : Enthalpy of fusion at a given temperature (kJ/mol).
• Δ_vapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
• Δ_vapH : Enthalpy of vaporization at a given temperature (kJ/mol).
• IE : Ionization energy (eV).
• log₁₀WS : Log10 of Water solubility in mol/l.
• logP_oct/wat : Octanol/Water partition coefficient.
• McVol : McGowan's characteristic volume (ml/mol).
• NFPA Fire : NFPA Fire Rating.
• NFPA Health : NFPA Health Rating.
• P_c : Critical Pressure (kPa).
• P_triple : Triple Point Pressure (kPa).
• P_vap : Vapor pressure (kPa).
• n₀ : Refractive Index.
• ρ_c : Critical density (kg/m³).
• ρ_l : Liquid Density (kg/m³).
• I_np : Non-polar retention indices.
• I_p : Polar retention indices.
• Δ_fusS : Entropy of fusion at a given temperature (J/mol×K).
• S°_liquid : Liquid phase molar entropy at standard conditions (J/mol×K).
• γ : Surface Tension (N/m).
• T_boil : Normal Boiling Point Temperature (K).
• T_c : Critical Temperature (K).
• λ_gas : Gas thermal conductivity (W/m×K).
• λ_liquid : Liquid thermal conductivity (W/m×K).
• T_fus : Normal melting (fusion) point (K).
• T_triple : Triple Point Temperature (K).
• U_Qi : UNIQUAC Qi Parameter.
• U_Ri : UNIQUAC Ri Parameter.
• V_c : Critical Volume (m³/kmol).
• 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	[0.2330; 0.2450]
ω	0.2450		PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
ω	0.2450		Passut and Danner (1973), critical constants and acentric factors Compiled value
ω	0.2370		ChemSep v8.3 pure component data Compiled value
ω	0.2330		KDB
Tig	548.15	K	KDB
AP	292.150	K	KDB
ΔcH°liquid	-3349.72 ± 0.58	kJ/mol	NIST
μ	[0.40; 0.51]	debye
μ	0.51	debye	ChemSep v8.3 pure component data Compiled value
μ	0.40	debye	KDB
LFL	1.40	% in Air	KDB
UFL	8.70	% in Air	KDB
Tflash,cc	255.37	K	KDB
Tflash,oc	222.04	K	KDB
ΔfG°	[78.37; 79.17]	kJ/mol
ΔfG°	78.37	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfG°	79.17	kJ/mol	KDB
Δc,grossH	3350.05	kJ/mol	KDB
Δc,netH	3130.009	kJ/mol	KDB
ΔfH°gas	[-29.30; -17.10]	kJ/mol
ΔfH°gas	-21.62	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfH°gas	-20.93	kJ/mol	KDB
ΔfH°gas	-21.70 ± 2.70	kJ/mol	NIST
ΔfH°gas	-23.30 ± 2.10	kJ/mol	NIST
ΔfH°gas	-17.10	kJ/mol	NIST
ΔfH°gas	-17.20	kJ/mol	NIST
ΔfH°gas	-25.70 ± 2.70	kJ/mol	NIST
ΔfH°gas	-29.30 ± 1.50	kJ/mol	NIST
ΔfH°liquid	[-54.50; -46.90]	kJ/mol
ΔfH°liquid	-46.90 ± 2.50	kJ/mol	NIST
ΔfH°liquid	-48.50 ± 1.90	kJ/mol	NIST
ΔfH°liquid	-46.94 ± 0.42	kJ/mol	NIST
ΔfH°liquid	-46.97 ± 0.64	kJ/mol	NIST
ΔfH°liquid	-50.90 ± 2.50	kJ/mol	NIST
ΔfH°liquid	-54.50 ± 1.20	kJ/mol	NIST
ΔfusH°	7.43	kJ/mol	Joback Calculated Property
ΔvapH°	[25.50; 29.82]	kJ/mol
ΔvapH°	29.82	kJ/mol	NIST
ΔvapH°	25.50	kJ/mol	NIST
ΔvapH°	25.50 ± 0.10	kJ/mol	NIST
IE	[9.42; 9.82]	eV
IE	9.49 ± 0.03	eV	NIST
IE	9.50	eV	NIST
IE	9.52 ± 0.05	eV	NIST
IE	9.42 ± 0.02	eV	NIST
IE	9.52 ± 0.02	eV	NIST
IE	9.52 ± 0.00	eV	NIST
IE	9.48	eV	NIST
IE	Outlier 9.82 ± 0.06	eV	NIST
IE	9.50 ± 0.02	eV	NIST
IE	9.50 ± 0.02	eV	NIST
IE	9.68 ± 0.01	eV	NIST
IE	9.54 ± 0.02	eV	NIST
log10WS	[-2.68; -2.68]
log10WS	-2.68		Aq. Solubility Prediction
log10WS	-2.68		Estimated Solubility
logPoct/wat	1.973		Crippen Calculated Property
McVol	77.010	ml/mol	McGowan Calculated Property
NFPA Fire	4		KDB
NFPA Health	1		KDB
Pc	[3526.11; 4067.91]	kPa
Pc	3560.00	kPa	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 6 Compiled value
Pc	3526.11	kPa	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Pc	Outlier 4067.91	kPa	Passut and Danner (1973), critical constants and acentric factors Compiled value
Pc	3560.00	kPa	ChemSep v8.3 pure component data Compiled value
Pc	3560.00	kPa	KDB
Pc	3560.00 ± 50.00	kPa	NIST
Pc	3550.00 ± 20.00	kPa	NIST
Pc	3551.00 ± 3.44	kPa	NIST
Ptriple	3.70e-08	kPa	ChemSep v8.3 pure component data Compiled value
ρc	[232.84; 234.95]	kg/m3
ρc	234.95 ± 3.51	kg/m3	NIST
ρc	232.84 ± 2.10	kg/m3	NIST
Inp	[478.00; 500.00]
Inp	489.00		NIST
Inp	481.10		NIST
Inp	485.00		NIST
Inp	483.00		NIST
Inp	480.00		NIST
Inp	488.80		NIST
Inp	489.00		NIST
Inp	491.00		NIST
Inp	488.00		NIST
Inp	488.00		NIST
Inp	489.00		NIST
Inp	481.30		NIST
Inp	488.80		NIST
Inp	Outlier 496.00		NIST
Inp	489.00		NIST
Inp	489.00		NIST
Inp	492.00		NIST
Inp	486.00		NIST
Inp	481.60		NIST
Inp	482.00		NIST
Inp	481.50		NIST
Inp	481.60		NIST
Inp	482.00		NIST
Inp	482.00		NIST
Inp	486.80		NIST
Inp	482.50		NIST
Inp	482.00		NIST
Inp	482.00		NIST
Inp	481.07		NIST
Inp	491.00		NIST
Inp	482.00		NIST
Inp	481.00		NIST
Inp	481.00		NIST
Inp	483.00		NIST
Inp	483.00		NIST
Inp	490.00		NIST
Inp	483.00		NIST
Inp	479.00		NIST
Inp	485.00		NIST
Inp	491.00		NIST
Inp	491.00		NIST
Inp	486.50		NIST
Inp	487.00		NIST
Inp	483.39		NIST
Inp	483.67		NIST
Inp	483.00		NIST
Inp	478.00		NIST
Inp	481.30		NIST
Inp	482.00		NIST
Inp	492.00		NIST
Inp	482.00		NIST
Inp	Outlier 500.00		NIST
Inp	488.00		NIST
Inp	489.00		NIST
Inp	491.00		NIST
Inp	492.00		NIST
Inp	492.00		NIST
Inp	495.00		NIST
Inp	488.00		NIST
Inp	483.00		NIST
Inp	483.00		NIST
Inp	487.00		NIST
Inp	483.00		NIST
Inp	486.00		NIST
Inp	483.00		NIST
Inp	483.00		NIST
Inp	483.00		NIST
Inp	491.00		NIST
Inp	479.00		NIST
Inp	489.00		NIST
Inp	484.00		NIST
Inp	488.00		NIST
Inp	488.00		NIST
Inp	483.00		NIST
Inp	488.00		NIST
Inp	488.00		NIST
Inp	483.00		NIST
Inp	485.00		NIST
Inp	492.00		NIST
Inp	492.00		NIST
Inp	492.00		NIST
Inp	479.00		NIST
Inp	483.00		NIST
Inp	484.00		NIST
Inp	488.00		NIST
Inp	492.00		NIST
Inp	495.00		NIST
Inp	481.30		NIST
Ip	[523.00; 534.00]
Ip	532.00		NIST
Ip	523.00		NIST
Ip	534.00		NIST
S°liquid	[262.55; 262.60]	J/mol×K
S°liquid	262.60	J/mol×K	NIST
S°liquid	262.60	J/mol×K	NIST
S°liquid	262.55	J/mol×K	NIST
Tboil	[273.15; 313.15]	K
Tboil	303.11	K	ChemSep v8.3 pure component data Compiled value
Tboil	303.11	K	KDB
Tboil	303.20	K	NIST
Tboil	303.10	K	NIST
Tboil	303.10 ± 0.60	K	NIST
Tboil	303.30 ± 1.00	K	NIST
Tboil	303.70 ± 0.50	K	NIST
Tboil	293.20 ± 0.60	K	NIST
Tboil	303.22 ± 0.04	K	NIST
Tboil	303.65 ± 1.00	K	NIST
Tboil	303.05 ± 0.30	K	NIST
Tboil	303.25 ± 0.50	K	NIST
Tboil	Outlier 273.15 ± 0.30	K	NIST
Tboil	303.45 ± 0.70	K	NIST
Tboil	303.15 ± 0.20	K	NIST
Tboil	303.15 ± 1.00	K	NIST
Tboil	303.17 ± 0.20	K	NIST
Tboil	303.30 ± 1.00	K	NIST
Tboil	303.10 ± 0.20	K	NIST
Tboil	303.25 ± 0.30	K	NIST
Tboil	303.15 ± 0.30	K	NIST
Tboil	303.30 ± 0.15	K	NIST
Tboil	303.25 ± 0.15	K	NIST
Tboil	303.35 ± 0.20	K	NIST
Tboil	303.25 ± 0.20	K	NIST
Tboil	303.40 ± 1.50	K	NIST
Tboil	303.20 ± 1.00	K	NIST
Tboil	313.15 ± 0.50	K	NIST
Tboil	313.00 ± 3.00	K	NIST
Tboil	312.65 ± 6.00	K	NIST
Tboil	309.90 ± 1.50	K	NIST
Tboil	309.00 ± 3.00	K	NIST
Tboil	309.00 ± 3.00	K	NIST
Tc	[463.77; 466.59]	K
Tc	Outlier 466.59	K	Vapor Pressures and Vapor Liquid Critical Properties of Four Pentene Isomers
Tc	464.80	K	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 6 Compiled value
Tc	464.70	K	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Tc	464.78	K	Passut and Danner (1973), critical constants and acentric factors Compiled value
Tc	464.80	K	ChemSep v8.3 pure component data Compiled value
Tc	464.80	K	KDB
Tc	464.80 ± 0.50	K	NIST
Tc	464.70	K	NIST
Tc	465.10 ± 0.30	K	NIST
Tc	463.77 ± 0.20	K	NIST
Tc	464.74 ± 0.03	K	NIST
Tfus	[107.75; 108.15]	K
Tfus	108.15	K	Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
Tfus	108.02	K	ChemSep v8.3 pure component data Compiled value
Tfus	107.90	K	KDB
Tfus	108.08	K	Aq. Solubility Prediction
Tfus	107.75 ± 0.20	K	NIST
Tfus	107.78 ± 0.20	K	NIST
Tfus	107.88 ± 0.10	K	NIST
Ttriple	[5.80; 108.02]	K
Ttriple	108.02	K	ChemSep v8.3 pure component data Compiled value
Ttriple	108.01 ± 0.00	K	NIST
Ttriple	107.79 ± 0.00	K	NIST
Ttriple	5.80 ± 0.01	K	NIST
Ttriple	107.90 ± 0.50	K	NIST
Ttriple	108.01 ± 0.00	K	NIST
Ttriple	107.79 ± 0.00	K	NIST
Ttriple	5.80 ± 0.01	K	NIST
Ttriple	107.90 ± 0.50	K	NIST
UQi	3.10		ChemSep v8.3 pure component data Compiled value
URi	3.60		ChemSep v8.3 pure component data Compiled value
Vc	[0.298; 0.300]	m3/kmol
Vc	0.298	m3/kmol	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 6 Compiled value
Vc	0.300	m3/kmol	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Vc	0.298	m3/kmol	ChemSep v8.3 pure component data Compiled value
Vc	0.298	m3/kmol	KDB
Vc	0.298	m3/kmol	NIST
VCOSTALD	0.30	m3/kmol	Hankinson and Thomson (1979), COSTALD parameters Compiled value
ωSRK	0.28		Hankinson and Thomson (1979), COSTALD parameters Compiled value
Zc	[0.2748820; 0.2750000]
Zc	0.2750000		IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 6 Compiled value
Zc	0.2750000		ChemSep v8.3 pure component data Compiled value
Zc	0.2748820		KDB
Zra	[0.27; 0.29]
Zra	0.29		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	[112.34; 157.69]	J/mol×K	[311.09; 471.08]
Cp,gas	112.34 ± 0.33	J/mol×K	311.09	NIST
Cp,gas	126.15 ± 0.38	J/mol×K	357.51	NIST
Cp,gas	139.08 ± 0.42	J/mol×K	402.32	NIST
Cp,gas	148.41 ± 0.45	J/mol×K	436.01	NIST
Cp,gas	157.69 ± 0.47	J/mol×K	471.08	NIST
Cp,liquid	[128.64; 169.00]	J/mol×K	[110.00; 360.00]
Cp,liquid	129.23	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	128.82	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	128.64	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	128.68	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	128.95	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	129.43	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	130.12	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	131.01	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	132.10	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	133.39	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	134.87	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	136.52	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	138.36	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	140.37	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	142.54	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	144.87	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	147.36	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	148.18	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	150.01	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	152.79	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	154.30	J/mol×K	294.00	NIST
Cp,liquid	154.87	J/mol×K	298.15	NIST
Cp,liquid	155.16	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	155.31	J/mol×K	298.15	NIST
Cp,liquid	154.00	J/mol×K	298.15	NIST
Cp,liquid	155.72	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	159.00	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	162.00	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	164.00	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	167.00	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	168.00	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	169.00	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
ΔfusH	[5.81; 5.94]	kJ/mol	[107.80; 108.02]
ΔfusH	5.88	kJ/mol	107.80	NIST
ΔfusH	5.88	kJ/mol	107.80	NIST
ΔfusH	5.81	kJ/mol	107.90	NIST
ΔfusH	5.81	kJ/mol	107.90	NIST
ΔfusH	5.81	kJ/mol	107.90	NIST
ΔfusH	5.81	kJ/mol	107.90	NIST
ΔfusH	5.81	kJ/mol	107.90	NIST
ΔfusH	5.81	kJ/mol	107.90	NIST
ΔfusH	5.81	kJ/mol	107.90	NIST
ΔfusH	5.94	kJ/mol	108.02	NIST
ΔfusH	5.94	kJ/mol	108.02	NIST
ΔvapH	[25.20; 29.10]	kJ/mol	[264.50; 340.50]
ΔvapH	29.10	kJ/mol	264.50	NIST
ΔvapH	26.20 ± 0.10	kJ/mol	284.00	NIST
ΔvapH	26.30	kJ/mol	290.50	NIST
ΔvapH	26.70	kJ/mol	295.00	NIST
ΔvapH	25.20 ± 0.10	kJ/mol	303.00	NIST
ΔvapH	25.20	kJ/mol	303.10	NIST
ΔvapH	26.90	kJ/mol	303.50	NIST
ΔvapH	25.20	kJ/mol	305.80	KDB
ΔvapH	25.70	kJ/mol	340.50	NIST
n0	1.36835		298.15	KDB
ρl	640.00	kg/m3	293.00	KDB
ΔfusS	[53.82; 55.00]	J/mol×K	[107.80; 108.02]
ΔfusS	54.56	J/mol×K	107.80	NIST
ΔfusS	54.56	J/mol×K	107.80	NIST
ΔfusS	53.82	J/mol×K	107.90	NIST
ΔfusS	53.82	J/mol×K	107.90	NIST
ΔfusS	55.00	J/mol×K	107.90	NIST
ΔfusS	53.82	J/mol×K	107.90	NIST
ΔfusS	53.82	J/mol×K	107.90	NIST
ΔfusS	54.97	J/mol×K	108.02	NIST
ΔfusS	54.97	J/mol×K	108.02	NIST
γ	0.02	N/m	298.20	KDB
λliquid	[0.11; 0.13]	W/m×K	[257.36; 301.75]
λliquid	0.13	W/m×K	257.36	Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λliquid	0.13	W/m×K	257.67	Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λliquid	0.13	W/m×K	257.93	Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λliquid	0.12	W/m×K	276.47	Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λliquid	0.12	W/m×K	276.82	Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λliquid	0.12	W/m×K	277.07	Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λliquid	0.11	W/m×K	294.04	Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λliquid	0.11	W/m×K	294.42	Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λliquid	0.11	W/m×K	294.66	Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λliquid	0.11	W/m×K	301.07	Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λliquid	0.11	W/m×K	301.46	Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λliquid	0.11	W/m×K	301.75	Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons

Datasets

Mass density, kg/m3

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
283.48	100.00	650.3
283.48	500.00	650.8
283.48	1000.00	651.6
283.48	3000.00	654.0
283.49	5000.00	656.3
283.49	10000.00	661.8
283.49	15000.00	666.9
283.49	20000.00	671.7
283.49	25000.00	676.2
283.49	30000.00	680.4
283.49	35000.00	684.5
283.49	40000.00	688.4
283.49	45000.00	692.1
283.49	50000.00	695.7
283.49	55000.00	699.1
283.49	60000.00	702.5
283.48	70000.00	708.8
283.48	80000.00	714.8
283.49	90000.00	720.4
283.49	100000.00	725.7
293.42	100.00	640.1
293.42	500.00	640.7
293.42	1000.00	641.4
293.42	3000.00	644.0
293.42	5000.00	646.5
293.42	10000.00	652.4
293.43	15000.00	657.9
293.43	20000.00	663.0
293.43	25000.00	667.8
293.44	30000.00	672.3
293.43	35000.00	676.7
293.42	40000.00	680.8
293.43	45000.00	684.7
293.43	50000.00	688.4
293.42	55000.00	692.0
293.42	60000.00	695.5
293.42	70000.00	702.2
293.42	80000.00	708.3
293.42	90000.00	714.1
293.42	100000.00	719.6
303.33	100.00	629.8
303.33	1000.00	631.1
303.33	3000.00	634.0
303.34	5000.00	636.7
303.34	10000.00	643.1
303.34	15000.00	649.0
303.34	20000.00	654.5
303.34	25000.00	659.6
303.34	30000.00	664.4
303.33	35000.00	668.9
303.34	40000.00	673.2
303.34	45000.00	677.3
303.34	50000.00	681.2
303.35	55000.00	685.0
303.35	60000.00	688.6
303.35	70000.00	695.6
303.34	80000.00	702.0
303.34	90000.00	707.9
303.35	100000.00	713.6
313.27	500.00	620.4
313.28	1000.00	621.3
313.27	3000.00	624.5
313.27	5000.00	627.5
313.27	10000.00	634.4
313.28	15000.00	640.8
313.28	20000.00	646.7
313.28	25000.00	652.1
313.28	30000.00	657.2
313.29	35000.00	661.9
313.29	40000.00	666.6
313.28	45000.00	670.8
313.28	50000.00	674.9
313.29	55000.00	678.8
313.29	60000.00	682.6
313.28	70000.00	689.9
313.29	80000.00	696.4
313.29	90000.00	702.6
313.29	100000.00	708.4
323.18	500.00	608.6
323.18	1000.00	609.3
323.18	3000.00	612.8
323.18	5000.00	616.1
323.19	10000.00	623.7
323.19	15000.00	630.6
323.19	20000.00	636.9
323.19	25000.00	642.7
323.19	30000.00	648.1
323.19	35000.00	653.1
323.19	40000.00	657.9
323.19	45000.00	662.4
323.19	50000.00	666.7
323.19	55000.00	670.8
323.19	60000.00	674.7
323.19	70000.00	682.2
323.19	80000.00	689.1
323.19	90000.00	695.4
323.19	100000.00	701.5
333.04	500.00	597.2
333.04	1000.00	598.1
333.04	3000.00	601.9
333.04	5000.00	605.6
333.04	10000.00	613.9
333.05	15000.00	621.4
333.05	20000.00	628.1
333.05	25000.00	634.3
333.05	30000.00	640.0
333.05	35000.00	645.3
333.05	40000.00	650.4
333.05	45000.00	655.1
333.05	50000.00	659.6
333.05	55000.00	663.9
333.05	60000.00	668.0
333.05	70000.00	675.8
333.06	80000.00	683.0
333.06	90000.00	689.6
333.05	100000.00	695.8
342.94	500.00	585.8
342.94	1000.00	586.8
342.95	3000.00	591.2
342.95	5000.00	595.3
342.95	10000.00	604.4
342.96	15000.00	612.5
342.96	20000.00	619.8
342.96	25000.00	626.3
342.96	30000.00	632.4
342.96	35000.00	638.1
342.96	40000.00	643.4
342.96	45000.00	648.4
342.96	50000.00	653.0
342.96	55000.00	657.5
342.96	60000.00	661.8
342.95	70000.00	669.9
342.95	80000.00	677.2
342.94	90000.00	684.0
342.95	100000.00	690.4
352.82	500.00	574.2
352.82	1000.00	575.6
352.82	3000.00	580.5
352.82	5000.00	585.1
352.82	10000.00	595.2
352.83	15000.00	603.9
352.83	20000.00	611.7
352.83	25000.00	618.7
352.83	30000.00	625.2
352.83	35000.00	631.2
352.83	40000.00	636.7
352.83	45000.00	641.9
352.83	50000.00	646.9
352.83	55000.00	651.5
352.84	60000.00	655.9
352.83	70000.00	664.3
352.83	80000.00	671.9
352.83	90000.00	679.0
352.83	100000.00	685.6
362.67	500.00	560.5
362.67	1000.00	561.8
362.67	3000.00	567.4
362.68	5000.00	572.6
362.68	10000.00	583.8
362.68	15000.00	593.3
362.68	20000.00	601.7
362.68	25000.00	609.2
362.68	30000.00	616.1
362.68	35000.00	622.4
362.68	40000.00	628.2
362.68	45000.00	633.7
362.68	50000.00	638.9
362.68	55000.00	643.7
362.68	60000.00	648.3
362.68	70000.00	657.1
362.67	80000.00	664.9
362.68	90000.00	672.2
362.67	100000.00	679.0
Reference

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[82.00; 289.15]	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			6.65200e+01
Coefficient B			-6.09440e+02
Coefficient C			5.77524e+00
Coefficient D			6.23950e-05
Coefficient E			-2.53540e-08
Temperature range, min.			200.00
Temperature range, max.			1500.00
Cp,gas	82.00	J/mol×K	200.00	Calculated Property
Cp,gas	122.47	J/mol×K	344.44	Calculated Property
Cp,gas	161.45	J/mol×K	488.89	Calculated Property
Cp,gas	193.28	J/mol×K	633.33	Calculated Property
Cp,gas	218.67	J/mol×K	777.78	Calculated Property
Cp,gas	239.02	J/mol×K	922.22	Calculated Property
Cp,gas	255.49	J/mol×K	1066.67	Calculated Property
Cp,gas	268.95	J/mol×K	1211.11	Calculated Property
Cp,gas	280.02	J/mol×K	1355.56	Calculated Property
Cp,gas	289.15	J/mol×K	1500.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[129.52; 179.33]	J/mol×K	[107.90; 372.00]	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			9.27530e+01
Coefficient B			1.17210e+02
Coefficient C			1.74594e+00
Coefficient D			7.44700e-03
Coefficient E			-2.67590e-06
Temperature range, min.			107.90
Temperature range, max.			372.00
Cp,liquid	129.52	J/mol×K	107.90	Calculated Property
Cp,liquid	128.33	J/mol×K	137.24	Calculated Property
Cp,liquid	129.94	J/mol×K	166.59	Calculated Property
Cp,liquid	133.22	J/mol×K	195.93	Calculated Property
Cp,liquid	137.82	J/mol×K	225.28	Calculated Property
Cp,liquid	143.61	J/mol×K	254.62	Calculated Property
Cp,liquid	150.59	J/mol×K	283.97	Calculated Property
Cp,liquid	158.82	J/mol×K	313.31	Calculated Property
Cp,liquid	168.36	J/mol×K	342.66	Calculated Property
Cp,liquid	179.33	J/mol×K	372.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.0115723; 0.0001848]	Pa×s	[108.02; 303.22]	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			-1.07959e+01
Coefficient B			6.82800e+02
Coefficient C			5.64316e-03
Coefficient D			-9.17681e-07
Coefficient E			2.00000e+00
Temperature range, min.			108.02
Temperature range, max.			303.22
η	0.0115723	Pa×s	108.02	Calculated Property
η	0.0040067	Pa×s	129.71	Calculated Property
η	0.0018760	Pa×s	151.40	Calculated Property
η	0.0010600	Pa×s	173.09	Calculated Property
η	0.0006787	Pa×s	194.78	Calculated Property
η	0.0004740	Pa×s	216.46	Calculated Property
η	0.0003527	Pa×s	238.15	Calculated Property
η	0.0002750	Pa×s	259.84	Calculated Property
η	0.0002223	Pa×s	281.53	Calculated Property
η	0.0001848	Pa×s	303.22	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ΔvapH	[32.10; 0.00]	kJ/mol	[108.02; 464.80]	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			3.07728e+01
Coefficient B			-5.70706e-01
Coefficient C			2.24340e+00
Coefficient D			-2.25807e+00
Coefficient E			9.28488e-01
Critical temperature, Tc (K)			4.64800e+02
Temperature range, min.			108.02
Temperature range, max.			464.80
ΔvapH	32.10	kJ/mol	108.02	Calculated Property
ΔvapH	31.44	kJ/mol	147.66	Calculated Property
ΔvapH	30.34	kJ/mol	187.30	Calculated Property
ΔvapH	28.89	kJ/mol	226.95	Calculated Property
ΔvapH	27.12	kJ/mol	266.59	Calculated Property
ΔvapH	25.01	kJ/mol	306.23	Calculated Property
ΔvapH	22.46	kJ/mol	345.87	Calculated Property
ΔvapH	19.21	kJ/mol	385.52	Calculated Property
ΔvapH	14.61	kJ/mol	425.16	Calculated Property
ΔvapH	0.00	kJ/mol	464.80	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.65]	kPa	[217.89; 325.69]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.40675e+01
Coefficient B			-2.58895e+03
Coefficient C			-3.00140e+01
Temperature range, min.			217.89
Temperature range, max.			325.69
Pvap	1.33	kPa	217.89	Calculated Property
Pvap	3.04	kPa	229.87	Calculated Property
Pvap	6.33	kPa	241.85	Calculated Property
Pvap	12.18	kPa	253.82	Calculated Property
Pvap	21.92	kPa	265.80	Calculated Property
Pvap	37.27	kPa	277.78	Calculated Property
Pvap	60.35	kPa	289.76	Calculated Property
Pvap	93.65	kPa	301.73	Calculated Property
Pvap	140.02	kPa	313.71	Calculated Property
Pvap	202.65	kPa	325.69	Calculated Property
Pvap	[1.15e-07; 3524.92]	kPa	[108.02; 464.80]	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			3.26218e+01
Coefficient B			-3.89340e+03
Coefficient C			-2.68650e+00
Coefficient D			1.95236e-06
Coefficient E			2.00000e+00
Comment			Range stopped at Tc; ChemSep gives it to 465.1 K.
Temperature range, min.			108.02
Temperature range, max.			464.80
Pvap	1.15e-07	kPa	108.02	Calculated Property
Pvap	8.08e-04	kPa	147.66	Calculated Property
Pvap	0.12	kPa	187.30	Calculated Property
Pvap	2.70	kPa	226.95	Calculated Property
Pvap	23.34	kPa	266.59	Calculated Property
Pvap	111.33	kPa	306.23	Calculated Property
Pvap	362.54	kPa	345.87	Calculated Property
Pvap	912.09	kPa	385.52	Calculated Property
Pvap	1914.46	kPa	425.16	Calculated Property
Pvap	3524.92	kPa	464.80	Calculated Property
Pvap	[9.78e-09; 3613.80]	kPa	[110.00; 464.78]	KDB Vapor Pressure Data
Equation			ln(Y) = A + B/T + C·ln(T) + D·T² + E/T² Y is Pvap in kPa, T in K
Coefficient A			8.33214e+01
Coefficient B			-5.67565e+03
Coefficient C			-1.07068e+01
Coefficient D			1.31421e-05
Coefficient E			0.00000e+00
Temperature range, min.			110.00
Temperature range, max.			464.78
Pvap	9.78e-09	kPa	110.00	Calculated Property
Pvap	3.44e-04	kPa	149.42	Calculated Property
Pvap	0.09	kPa	188.84	Calculated Property
Pvap	2.71	kPa	228.26	Calculated Property
Pvap	24.81	kPa	267.68	Calculated Property
Pvap	116.72	kPa	307.10	Calculated Property
Pvap	367.91	kPa	346.52	Calculated Property
Pvap	903.88	kPa	385.94	Calculated Property
Pvap	1898.08	kPa	425.36	Calculated Property
Pvap	3613.80	kPa	464.78	Calculated Property
Pvap	[53.69; 103.99]	kPa	[285.98; 303.87]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.36096e+01
Coefficient B			-2.33550e+03
Coefficient C			-4.33670e+01
Reference			Forziati, Camin, et al., 1950, 2
Temperature range, min.			285.98
Temperature range, max.			303.87
Pvap	53.69	kPa	285.98	Calculated Property
Pvap	58.06	kPa	287.97	Calculated Property
Pvap	62.70	kPa	289.96	Calculated Property
Pvap	67.63	kPa	291.94	Calculated Property
Pvap	72.87	kPa	293.93	Calculated Property
Pvap	78.42	kPa	295.92	Calculated Property
Pvap	84.29	kPa	297.91	Calculated Property
Pvap	90.50	kPa	299.89	Calculated Property
Pvap	97.06	kPa	301.88	Calculated Property
Pvap	103.99	kPa	303.87	Calculated Property
Pvap	[53.69; 103.99]	kPa	[285.98; 303.87]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.36096e+01
Coefficient B			-2.33550e+03
Coefficient C			-4.33670e+01
Reference			Forziati, Camin, et al., 1950
Temperature range, min.			285.98
Temperature range, max.			303.87
Pvap	53.69	kPa	285.98	Calculated Property
Pvap	58.06	kPa	287.97	Calculated Property
Pvap	62.70	kPa	289.96	Calculated Property
Pvap	67.63	kPa	291.94	Calculated Property
Pvap	72.87	kPa	293.93	Calculated Property
Pvap	78.42	kPa	295.92	Calculated Property
Pvap	84.29	kPa	297.91	Calculated Property
Pvap	90.50	kPa	299.89	Calculated Property
Pvap	97.06	kPa	301.88	Calculated Property
Pvap	103.99	kPa	303.87	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ρl	[816.39; 322.33]	kg/m3	[108.02; 464.80]	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			3.10934e+01
Coefficient B			1.85660e-01
Coefficient C			4.73430e+02
Coefficient D			2.35870e-01
Comment			Range stopped at Tc; ChemSep gives it to 473.42 K.
Temperature range, min.			108.02
Temperature range, max.			464.80
ρl	816.39	kg/m3	108.02	Calculated Property
ρl	782.55	kg/m3	147.66	Calculated Property
ρl	747.02	kg/m3	187.30	Calculated Property
ρl	709.39	kg/m3	226.95	Calculated Property
ρl	669.09	kg/m3	266.59	Calculated Property
ρl	625.23	kg/m3	306.23	Calculated Property
ρl	576.32	kg/m3	345.87	Calculated Property
ρl	519.47	kg/m3	385.52	Calculated Property
ρl	447.44	kg/m3	425.16	Calculated Property
ρl	322.33	kg/m3	464.80	Calculated Property

Property	Value	Unit	Temperature (K)	Source
γ	[0.04; 0.01]	N/m	[108.15; 303.25]	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			4.82192e-02
Coefficient B			-1.09900e-04
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Temperature range, min.			108.15
Temperature range, max.			303.25
γ	0.04	N/m	108.15	Calculated Property
γ	0.03	N/m	129.83	Calculated Property
γ	0.03	N/m	151.51	Calculated Property
γ	0.03	N/m	173.18	Calculated Property
γ	0.03	N/m	194.86	Calculated Property
γ	0.02	N/m	216.54	Calculated Property
γ	0.02	N/m	238.22	Calculated Property
γ	0.02	N/m	259.89	Calculated Property
γ	0.02	N/m	281.57	Calculated Property
γ	0.01	N/m	303.25	Calculated Property
γ	[0.04; 1.60e-05]	N/m	[108.02; 460.52]	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			-1.15520e-02
Coefficient B			7.08780e+00
Coefficient C			-2.83820e+00
Coefficient D			-1.12320e-03
Coefficient E			-5.27850e-06
Comment			Range stopped where the equation turns negative; ChemSep gives it to 464.8 K.
Temperature range, min.			108.02
Temperature range, max.			460.52
γ	0.04	N/m	108.02	Calculated Property
γ	0.03	N/m	147.19	Calculated Property
γ	0.03	N/m	186.35	Calculated Property
γ	0.02	N/m	225.52	Calculated Property
γ	0.02	N/m	264.69	Calculated Property
γ	0.01	N/m	303.85	Calculated Property
γ	0.01	N/m	343.02	Calculated Property
γ	0.01	N/m	382.19	Calculated Property
γ	0.00	N/m	421.35	Calculated Property
γ	1.60e-05	N/m	460.52	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λgas	[0.00; 0.11]	W/m×K	[108.02; 1000.00]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A·T^B / (1 + C/T + D/T²) Y is λgas in W/m×K, T in K
Coefficient A			2.64120e-06
Coefficient B			1.54900e+00
Coefficient C			-2.58910e+00
Coefficient D			2.43890e+04
Temperature range, min.			108.02
Temperature range, max.			1000.00
λgas	0.00	W/m×K	108.02	Calculated Property
λgas	0.01	W/m×K	207.13	Calculated Property
λgas	0.01	W/m×K	306.23	Calculated Property
λgas	0.03	W/m×K	405.34	Calculated Property
λgas	0.04	W/m×K	504.45	Calculated Property
λgas	0.05	W/m×K	603.56	Calculated Property
λgas	0.06	W/m×K	702.67	Calculated Property
λgas	0.08	W/m×K	801.78	Calculated Property
λgas	0.10	W/m×K	900.89	Calculated Property
λgas	0.11	W/m×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λliquid	[0.18; 0.08]	W/m×K	[108.02; 423.15]	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			-1.08250e-02
Coefficient B			-3.00650e+01
Coefficient C			-1.11720e+00
Coefficient D			-2.33270e-03
Coefficient E			-1.55410e-06
Temperature range, min.			108.02
Temperature range, max.			423.15
λliquid	0.18	W/m×K	108.02	Calculated Property
λliquid	0.17	W/m×K	143.03	Calculated Property
λliquid	0.16	W/m×K	178.05	Calculated Property
λliquid	0.15	W/m×K	213.06	Calculated Property
λliquid	0.14	W/m×K	248.08	Calculated Property
λliquid	0.12	W/m×K	283.09	Calculated Property
λliquid	0.11	W/m×K	318.11	Calculated Property
λliquid	0.10	W/m×K	353.12	Calculated Property
λliquid	0.09	W/m×K	388.14	Calculated Property
λliquid	0.08	W/m×K	423.15	Calculated Property

Similar Compounds

Find more compounds similar to 1-Pentene.

Mixtures

• 1-Pentene + N-Formylmorpholine
• 2-Pyrrolidinone, 1-methyl- + 1-Pentene
• 1-Pentene + Ethanol, 2,2'-oxybis-
• Triethylene glycol + 1-Pentene
• 1-Pentene + 1,8-Diaminooctane
• 1-Pentene + 1,1O-DIAMINODECANE
• 1,12-Dodecanediamine + 1-Pentene
• 1-Pentene + 1-Octadecanol
• 1-Pentene + 1-Eicosanol

Sources

• KDB Vapor Pressure Data
• 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.
• 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
• Activity coefficients at infinite dilution measurements for organic solutes in the ionic liquid N-butyl-4-methylpyridinium tosylate using GLC at T = (328.15, 333.15, 338.15, and 343.15)K
• Measurement and prediction of activity coefficients at infinite dilution ( ), vapor.liquid equilibria (VLE) and excess enthalpies (HE) of binary systems with 1,1-dialkyl-pyrrolidinium bis(trifluoromethylsulfonyl)imide using mod. UNIFAC (Dortmund)
• Activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid 1-butyl-1-methylpyrrolidinium trifluoromethanesulfonate using GLC
• Activity coefficients at infinite dilution measurements for organic solutes and water in the 1-hexyloxymethyl-3-methyl-imidazolium and 1,3-dihexyloxymethyl-imidazolium bis(trifluoromethylsulfonyl)-imide ionic liquids The cation influence
• Measurements of different thermodynamic properties of systems containing ionic liquids and correlation of these properties using modified UNIFAC (Dortmund)
• Activity coefficients at infinite dilution of organic solvents and water in 1-butyl-3-methylimidazolium dicyanamide. A literature review of hexane/hex-1-ene separation
• High selective water/butan-1-ol separation on investigation of limiting activity coefficients with [P8,8,8,8][[NTf2] ionic liquid
• Separation of binary mixtures based on limiting activity coefficients data using specific ammonium-based ionic liquid and modelling of thermodynamic functions
• New ionic liquid [P4,4,4,4][NTf2] in bio-butanol extraction on investigation of limiting activity coefficients
• Ammonium ionic liquids in extraction of bio-butan-1-ol from water phase using activity coefficients at infinite dilution
• Measurements of activity coefficients at infinite dilution for organic solutes in two quaternary ammonium-based ionic liquids [DDA][ClO4] and [DDA][BF4]
• Application of trihexyltetradecylphosphonium dicyanamide ionic liquid for various types of separations problems: Activity coefficients at infinite dilution measurements utilizing GLC method
• Systems with ionic liquids: Measurement of VLE and c1 data and prediction of their thermodynamic behavior using original UNIFAC, mod. UNIFAC(Do) and COSMO-RS(Ol)
• Measurements of activity coefficients at infinite dilution of aromatic and aliphatic hydrocarbons, alcohols, and water in the new ionic liquid [EMIM][SCN] using GLC
• Activity coefficients at infinite dilution measurements for organic solutes in the ionic liquid trihexyltetradecylphosphonium-bis-(2,4,4-trimethylpentyl)- phosphinate using g.l.c. at T = (303.15, 308.15, 313.15, and 318.15) K
• Activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid triethylsulphonium bis(trifluoromethylsulfonyl)imide
• Measurements of activity coefficients at infinite dilution of aliphatic and aromatic hydrocarbons, alcohols, thiophene, tetrahydrofuran, MTBE, and water in ionic liquid [BMIM][SCN] using GLC
• Activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid 4-methyl-N-butyl-pyridinium bis(trifluoromethylsulfonyl)-imide
• Activity coefficients at infinite dilution for solutes in the trioctylmethylammonium bis(trifluoromethylsulfonyl)imide ionic liquid using gas liquid chromatography
• Gas liquid chromatography measurements of activity coefficients at infinite dilution of various organic solutes and water in tri-iso-butylmethylphosphonium tosylate ionic liquid
• Measurements of activity coefficients at infinite dilution of organic compounds and water in isoquinolinium-based ionic liquid [C8iQuin][NTf2] using GLC
• Activity coefficients at infinite dilution of organic solutes in the ionic liquid trihexyl(tetradecyl)phosphonium tetrafluoroborate using gas liquid chromatography at T = (313.15, 333.15, 353.15, and 373.15) K
• Activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-butyl-3-methylimidazolium hexafluoroantimonate using gas liquid chromatography at T = (313.15, 323.15, and 333.15) K
• Activity coefficients at infinite dilution of organic solutes in the ionic liquid, methyl(trioctyl)ammonium thiosalicylate, [N1888][TS] by gas liquid chromatography at T = (303.15, 313.15, and 323.15) K
• Activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid 1-ethyl-3-methylimidazolium tetracyanoborate
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(3-hydroxypropyl)pyridinium bis(trifluoromethylsulfonyl)-amide
• Thermodynamics and activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid 1-butyl-1-methylpyrrolidinium tetracyanoborate
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 4-(2-methoxyethyl)-4-methylmorpholinium bis(trifluoromethylsulfonyl)-amide
• Activity coefficients at infinite dilution of organic solutes in the ionic liquid trihexyltetradecylphosphonium hexafluorophosphate using gas liquid chromatography at T = (313.15, 333.15, 353.15, and 363.15) K
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-methoxyethyl)-1-methylpiperidinium bis(trifluoromethylsulfonyl)-amide
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-methoxyethyl)-1-methylpyrrolidinium bis(trifluoromethylsulfonyl)-amide
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 4-(2-methoxyethyl)-4-methylmorpholinium trifluorotris(perfluoroethyl)phosphate
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-methoxyethyl)- 1-methylpiperidinium trifluorotris(perfluoroethyl)phosphate
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-methoxyethyl)- 1-methylpyrrolidinium trifluorotris(perfluoroethyl)phosphate
• Measurements of activity coefficients at infinite dilution for organic solutes and water in N-hexylisoquinolinium thiocyanate, [HiQuin][SCN] using GLC
• Activity coefficients at infinite dilution of organic solutes in N-formylmorpholine and N-methylpyrrolidone from gas-liquid chromatography
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-hydroxyethyl)- 3-methylimidazolium trifluorotris(perfluoroethyl)phosphate
• Activity coefficients at infinite dilution of organic solutes in diethylene glycol and triethylene glycol from gas-liquid chromatography
• Activity coefficients at infinite dilution of organic solutes in the ionic liquid trihexyltetradecylphosphonium bis(trifluoromethylsulfonyl)imide using gas-liquid chromatography at T = (313.15, 333.15, 353.15 and 373.15) K
• Measurements of activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-butyl-1-methylpyrrolidinium tricyanomethanide
• The study of activity coefficients at infinite dilution for organic solutes and water in 1-butyl-4-methylpyridinium dicyanamide, [B4MPy][DCA] using GLC
• Measurement of activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-ethyl-3-methylimidazolium 2-(2-methoxyethoxy) ethylsulfate at T = (308.15, 313.15, 323.15 and 333.15) K using gas + liquid chromatography
• Use of water in aiding olefin/paraffin (liquid + liquid) extraction via complexation with a silver bis(trifluoromethylsulfonyl)imide salt
• Thermodynamics and activity coefficients at infinite dilution for organic solutes, water and diols in the ionic liquid choline bis(trifluoromethylsulfonyl)imide
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 4-(3-hydroxypropyl)-4-methylmorpholinium bis(trifluoromethylsulfonyl)-amide
• Activity coefficients at infinite dilution, physicochemical and thermodynamic properties for organic solutes and water in the ionic liquid ethyl-dimethyl-(2-methoxyethyl)ammonium trifluorotris-(perfluoroethyl)phosphate
• Screening of environmental friendly ionic liquid as a solvent for the different types of separations problem: Insight from activity coefficients at infinite dilution measurement using (gas + liquid) chromatography technique
• A 1-alkylcyanopyridinium-based ionic liquid in the separation processes
• Thermodynamics and selectivity of separation based on activity coefficients at infinite dilution of various solutes in 1-allyl-3-methylimidazolium bis{(trifluoromethyl)sulfonyl}imide ionic liquid
• Thermodynamics and limiting activity coefficients measurements for organic solutes and water in the ionic liquid 1-dodecyl-3-methylimidzolium bis(trifluoromethylsulfonyl) imide
• Separation of binary mixtures hexane/hex-1-ene, cyclohexane/cyclohexene and ethylbenzene/styrene based on limiting activity coefficients
• Separation of water/butan-1-ol based on activity coefficients at infinite dilution in 1,3-didecyl-2-methylimidazolium dicyanamide ionic liquid
• Separation of binary mixtures hexane/hex-1-ene, cyclohexane/cyclohexene and ethylbenzene/styrene based on gamma infinity data measurements
• Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid trihexyl-tetradecyl-phosphonium tricyanomethanide
• The use of ionic liquids for separation of binary hydrocarbons mixtures based on gamma infinity data measurements
• Activity Coefficients at Infinite Dilution of Organic Solutes and Water in Tributylethylphosphonium Diethylphosphate Using Gas Liquid Chromatography: Thermodynamic Properties of Mixtures Containing Ionic Liquids
• Vapor Pressures and Vapor Liquid Critical Properties of Four Pentene Isomers
• Liquid Density of n-Pentene, n-Hexene, and n-Heptene at Temperatures from 283.15 to 363.15 K and Pressures up to 100 MPa
• Assessment of Pyrrolidinium-Based Ionic Liquid for the Separation of Binary Mixtures Based on Activity Coefficients at Infinite Dilution
• Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
• Thermodynamic Properties of Mixtures Containing Ionic Liquids. 5. Activity Coefficients at Infinite Dilution of Hydrocarbons, Alcohols, Esters, and Aldehydes in 1-Methyl-3-butyl-imidazolium Bis(trifluoromethyl-sulfonyl) Imide Using Gas-Liquid Chromatography
• Thermodynamic Properties of Mixtures Containing Ionic Liquids. 6. Activity Coefficients at Infinite Dilution of Hydrocarbons, Alcohols, Esters, and Aldehydes in 1-Methyl-3-octyl-imidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
• Thermodynamic Properties of Mixtures Containing Ionic Liquids. 8. Activity Coefficients at Infinite Dilution of Hydrocarbons, Alcohols, Esters, and Aldehydes in 1-Hexyl-3-methylimidazolium Bis(trifluoromethylsulfonyl) Imide Using Gas-Liquid Chromatography
• Thermodynamic Properties of Mixtures Containing Ionic Liquids. 9. Activity Coefficients at Infinite Dilution of Hydrocarbons, Alcohols, Esters, and Aldehydes in Trimethyl-butylammonium Bis(trifluoromethylsulfonyl) Imide Using Gas-Liquid Chromatography and Static Method
• Activity Coefficients at Infinite Dilution Measurements for Organic Solutes and Water in the Ionic Liquid 1-Butyl-3-methyl-pyridinium Trifluoromethanesulfonate
• Determination of Activity Coefficients at Infinite Dilution of 35 Solutes in the Ionic Liquid, 1-Butyl-3-methylimidazolium Tosylate, Using Gas-Liquid Chromatography
• Activity Coefficients at Infinite Dilution for Hydrocarbons in Fatty Alcohols Determined by Gas-Liquid Chromatography
• Activity Coefficients at Infinite Dilution by GLC in Alkanediamines as Stationary Phases
• Enhancing liquid-phase olefin-paraffin separations using novel silver-based ionic liquids
• Determination of Activity Coefficients at Infinite Dilution of Solutes in the Ionic Liquid, Trihexyltetradecylphosphonium Bis(trifluoromethylsulfonyl) Imide, Using Gas-Liquid Chromatography at T ) (303.15, 308.15, 313.15, and 318.15) K
• Activity Coefficients at Infinite Dilution Measurements for Organic Solutes and Water in the Ionic Liquid 1-Hexyl-3-methylimidazolium Thiocyanate
• 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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