Chemical Properties of 1-Heptene (CAS 592-76-7)

InChI

InChI=1S/C7H14/c1-3-5-7-6-4-2/h3H,1,4-7H2,2H3

InChI Key

ZGEGCLOFRBLKSE-UHFFFAOYSA-N

Formula

C7H14

SMILES

C=CCCCCC

Molecular Weight¹

98.19

CAS

592-76-7

Other Names

• 1-C7H14
• 1-n-Heptene
• Heptylene
• NSC 74130
• hept-1-ene
• heptene-1
• n-Hept-1-ene
• «alpha»-Heptylene

• 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).
• C_sat : Molar heat capacity at saturation pressure (J/mol×K).
• μ : Dipole Moment (debye).
• η : Dynamic viscosity (Pa×s).
• LFL : Lower Flammability Limit (% in Air).
• 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).
• 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.

Contents

1. Physical Properties
2. Temperature Dependent Properties
3. Datasets
4. Correlations
5. Similar Compounds
6. Mixtures
7. Sources

Physical Properties

Property	Value	Unit	Source
ω	[0.3316; 0.3580]
ω	0.3316		PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
ω	0.3580		Passut and Danner (1973), critical constants and acentric factors Compiled value
ω	0.3430		ChemSep v8.3 pure component data Compiled value
ω	0.3580		KDB
Tig	533.15	K	KDB
AP	300.350	K	KDB
ΔcH°liquid	[-4658.30; -4650.98]	kJ/mol
ΔcH°liquid	-4657.00 ± 0.75	kJ/mol	NIST
ΔcH°liquid	-4658.30 ± 1.20	kJ/mol	NIST
ΔcH°liquid	-4650.98 ± 0.79	kJ/mol	NIST
μ	[0.30; 0.63]	debye
μ	0.63	debye	ChemSep v8.3 pure component data Compiled value
μ	0.30	debye	KDB
LFL	1.00	% in Air	KDB
Tflash,oc	269.26	K	KDB
ΔfG°	[94.82; 95.88]	kJ/mol
ΔfG°	94.82	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfG°	95.88	kJ/mol	KDB
Δc,grossH	4658.34	kJ/mol	KDB
Δc,netH	4350.272	kJ/mol	KDB
ΔfH°gas	[-63.70; -62.30]	kJ/mol
ΔfH°gas	-62.89	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfH°gas	-62.34	kJ/mol	KDB
ΔfH°gas	-63.00	kJ/mol	NIST
ΔfH°gas	-63.70	kJ/mol	NIST
ΔfH°gas	-62.30	kJ/mol	NIST
ΔfH°liquid	[-98.37; -97.00]	kJ/mol
ΔfH°liquid	-97.70 ± 0.63	kJ/mol	NIST
ΔfH°liquid	-98.37 ± 0.88	kJ/mol	NIST
ΔfH°liquid	-97.00 ± 1.20	kJ/mol	NIST
ΔfusH°	12.61	kJ/mol	Joback Calculated Property
ΔvapH°	35.70	kJ/mol	NIST
IE	[9.27; 9.44]	eV
IE	9.34 ± 0.08	eV	NIST
IE	9.38 ± 0.05	eV	NIST
IE	9.30 ± 0.10	eV	NIST
IE	9.27 ± 0.02	eV	NIST
IE	9.44 ± 0.00	eV	NIST
log10WS	[-3.73; -3.73]
log10WS	-3.73		Aq. Solubility Prediction
log10WS	-3.73		Estimated Solubility
logPoct/wat	2.753		Crippen Calculated Property
McVol	105.190	ml/mol	McGowan Calculated Property
Pc	[2826.85; 2920.00]	kPa
Pc	2920.00	kPa	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 6 Compiled value
Pc	2837.10	kPa	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Pc	2826.85	kPa	Passut and Danner (1973), critical constants and acentric factors Compiled value
Pc	2920.00	kPa	ChemSep v8.3 pure component data Compiled value
Pc	2920.00	kPa	KDB
Pc	2920.00 ± 40.00	kPa	NIST
Ptriple	1.86e-06	kPa	ChemSep v8.3 pure component data Compiled value
ρc	235.65 ± 3.93	kg/m3	NIST
Inp	[681.00; 700.00]
Inp	688.60		NIST
Inp	681.10		NIST
Inp	685.00		NIST
Inp	683.00		NIST
Inp	681.00		NIST
Inp	685.90		NIST
Inp	686.00		NIST
Inp	688.60		NIST
Inp	688.70		NIST
Inp	688.60		NIST
Inp	688.70		NIST
Inp	681.80		NIST
Inp	682.30		NIST
Inp	691.80		NIST
Inp	691.80		NIST
Inp	689.00		NIST
Inp	688.00		NIST
Inp	689.00		NIST
Inp	688.10		NIST
Inp	688.90		NIST
Inp	682.00		NIST
Inp	682.60		NIST
Inp	689.00		NIST
Inp	692.00		NIST
Inp	689.00		NIST
Inp	689.00		NIST
Inp	690.00		NIST
Inp	693.90		NIST
Inp	693.90		NIST
Inp	693.80		NIST
Inp	693.80		NIST
Inp	693.80		NIST
Inp	693.80		NIST
Inp	690.00		NIST
Inp	689.00		NIST
Inp	688.80		NIST
Inp	689.20		NIST
Inp	689.60		NIST
Inp	690.00		NIST
Inp	690.00		NIST
Inp	690.90		NIST
Inp	687.30		NIST
Inp	687.70		NIST
Inp	688.00		NIST
Inp	688.40		NIST
Inp	688.80		NIST
Inp	689.20		NIST
Inp	Outlier 697.00		NIST
Inp	684.00		NIST
Inp	681.80		NIST
Inp	682.20		NIST
Inp	681.90		NIST
Inp	681.50		NIST
Inp	683.00		NIST
Inp	682.00		NIST
Inp	684.50		NIST
Inp	682.90		NIST
Inp	684.90		NIST
Inp	683.60		NIST
Inp	684.90		NIST
Inp	682.00		NIST
Inp	682.00		NIST
Inp	689.00		NIST
Inp	689.00		NIST
Inp	683.00		NIST
Inp	684.00		NIST
Inp	683.00		NIST
Inp	689.40		NIST
Inp	682.10		NIST
Inp	682.00		NIST
Inp	685.00		NIST
Inp	683.00		NIST
Inp	683.50		NIST
Inp	682.80		NIST
Inp	683.00		NIST
Inp	687.00		NIST
Inp	690.00		NIST
Inp	682.00		NIST
Inp	682.00		NIST
Inp	683.00		NIST
Inp	683.00		NIST
Inp	682.00		NIST
Inp	684.00		NIST
Inp	687.00		NIST
Inp	689.00		NIST
Inp	691.00		NIST
Inp	685.00		NIST
Inp	688.50		NIST
Inp	695.00		NIST
Inp	695.00		NIST
Inp	688.00		NIST
Inp	689.00		NIST
Inp	689.40		NIST
Inp	690.90		NIST
Inp	689.30		NIST
Inp	690.00		NIST
Inp	688.00		NIST
Inp	689.00		NIST
Inp	689.40		NIST
Inp	686.00		NIST
Inp	689.01		NIST
Inp	689.10		NIST
Inp	689.22		NIST
Inp	691.74		NIST
Inp	691.87		NIST
Inp	691.94		NIST
Inp	685.00		NIST
Inp	Outlier 699.00		NIST
Inp	688.00		NIST
Inp	685.00		NIST
Inp	681.30		NIST
Inp	683.00		NIST
Inp	682.00		NIST
Inp	682.00		NIST
Inp	693.00		NIST
Inp	687.00		NIST
Inp	689.00		NIST
Inp	690.00		NIST
Inp	693.00		NIST
Inp	686.00		NIST
Inp	689.00		NIST
Inp	687.00		NIST
Inp	683.76		NIST
Inp	689.00		NIST
Inp	686.00		NIST
Inp	691.00		NIST
Inp	689.00		NIST
Inp	689.00		NIST
Inp	694.00		NIST
Inp	693.00		NIST
Inp	689.00		NIST
Inp	687.00		NIST
Inp	686.00		NIST
Inp	683.00		NIST
Inp	684.00		NIST
Inp	683.00		NIST
Inp	684.00		NIST
Inp	Outlier 700.00		NIST
Inp	689.00		NIST
Inp	690.00		NIST
Inp	687.00		NIST
Inp	687.00		NIST
Inp	690.00		NIST
Inp	689.00		NIST
Inp	692.00		NIST
Inp	692.00		NIST
Inp	681.00		NIST
Inp	683.00		NIST
Inp	689.00		NIST
Inp	688.60		NIST
Inp	685.90		NIST
Inp	688.70		NIST
Inp	682.00		NIST
Inp	693.80		NIST
Inp	688.80		NIST
Inp	690.90		NIST
Inp	682.20		NIST
Inp	684.50		NIST
Inp	684.00		NIST
Inp	685.00		NIST
Inp	687.00		NIST
Inp	695.00		NIST
Inp	689.30		NIST
Inp	686.00		NIST
Inp	691.87		NIST
Inp	688.00		NIST
Inp	681.30		NIST
Ip	[731.00; 751.00]
Ip	751.00		NIST
Ip	751.00		NIST
Ip	747.00		NIST
Ip	748.00		NIST
Ip	749.00		NIST
Ip	Outlier 731.00		NIST
Ip	747.70		NIST
Ip	747.30		NIST
Ip	749.00		NIST
Ip	747.30		NIST
Ip	747.70		NIST
Ip	749.00		NIST
Ip	741.00		NIST
Ip	736.00		NIST
Ip	740.00		NIST
Ip	750.00		NIST
Ip	751.00		NIST
Ip	Outlier 731.00		NIST
Ip	747.70		NIST
Ip	741.00		NIST
Ip	740.00		NIST
S°liquid	[327.65; 328.90]	J/mol×K
S°liquid	327.65	J/mol×K	NIST
S°liquid	328.90	J/mol×K	NIST
Tboil	[365.50; 375.65]	K
Tboil	366.79	K	ChemSep v8.3 pure component data Compiled value
Tboil	366.79	K	KDB
Tboil	366.80	K	NIST
Tboil	366.70 ± 0.80	K	NIST
Tboil	366.83 ± 0.30	K	NIST
Tboil	368.15 ± 2.00	K	NIST
Tboil	366.25 ± 0.50	K	NIST
Tboil	368.65 ± 3.00	K	NIST
Tboil	366.45 ± 0.50	K	NIST
Tboil	365.50 ± 1.00	K	NIST
Tboil	366.10 ± 1.00	K	NIST
Tboil	366.70 ± 0.50	K	NIST
Tboil	366.70 ± 1.00	K	NIST
Tboil	366.45 ± 0.60	K	NIST
Tboil	366.50 ± 0.50	K	NIST
Tboil	366.15 ± 2.00	K	NIST
Tboil	366.77 ± 0.50	K	NIST
Tboil	366.80 ± 0.30	K	NIST
Tboil	366.25 ± 1.00	K	NIST
Tboil	366.77 ± 0.40	K	NIST
Tboil	366.55 ± 1.00	K	NIST
Tboil	367.15 ± 2.00	K	NIST
Tboil	366.80 ± 0.60	K	NIST
Tboil	366.85 ± 0.50	K	NIST
Tboil	366.55 ± 0.50	K	NIST
Tboil	367.15 ± 2.00	K	NIST
Tboil	368.05 ± 0.50	K	NIST
Tboil	367.65 ± 1.00	K	NIST
Tboil	366.15 ± 0.60	K	NIST
Tboil	367.65 ± 2.00	K	NIST
Tboil	366.60 ± 0.30	K	NIST
Tboil	368.25 ± 2.00	K	NIST
Tboil	367.35 ± 1.00	K	NIST
Tboil	366.80 ± 1.00	K	NIST
Tboil	366.67 ± 0.50	K	NIST
Tboil	366.70 ± 0.20	K	NIST
Tboil	366.60 ± 0.20	K	NIST
Tboil	368.05 ± 1.00	K	NIST
Tboil	367.15 ± 1.00	K	NIST
Tboil	367.40 ± 2.00	K	NIST
Tboil	365.65 ± 2.00	K	NIST
Tboil	Outlier 371.00 ± 3.00	K	NIST
Tboil	368.15 ± 2.00	K	NIST
Tboil	Outlier 375.65 ± 5.00	K	NIST
Tboil	Outlier 371.15 ± 3.00	K	NIST
Tboil	Outlier 371.15 ± 3.00	K	NIST
Tboil	368.15 ± 3.00	K	NIST
Tboil	370.65 ± 5.00	K	NIST
Tc	[533.29; 537.30]	K
Tc	537.30	K	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 6 Compiled value
Tc	537.20	K	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Tc	Outlier 533.29	K	Passut and Danner (1973), critical constants and acentric factors Compiled value
Tc	537.30	K	ChemSep v8.3 pure component data Compiled value
Tc	537.30	K	KDB
Tc	537.30 ± 0.40	K	NIST
Tc	537.23 ± 0.05	K	NIST
Tfus	[148.15; 154.26]	K
Tfus	153.80	K	Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
Tfus	154.12	K	ChemSep v8.3 pure component data Compiled value
Tfus	153.40	K	KDB
Tfus	153.69	K	Aq. Solubility Prediction
Tfus	154.26 ± 0.08	K	NIST
Tfus	154.26 ± 0.05	K	NIST
Tfus	154.26 ± 0.04	K	NIST
Tfus	153.86 ± 0.08	K	NIST
Tfus	154.08 ± 0.07	K	NIST
Tfus	154.11 ± 0.04	K	NIST
Tfus	153.95 ± 0.30	K	NIST
Tfus	Outlier 148.15 ± 1.50	K	NIST
Tfus	153.15 ± 1.50	K	NIST
Tfus	154.10 ± 0.30	K	NIST
Ttriple	[153.40; 154.31]	K
Ttriple	154.31	K	Staveley, Lobo and Calado (1981), triple points Compiled value
Ttriple	154.12	K	ChemSep v8.3 pure component data Compiled value
Ttriple	154.30 ± 0.05	K	NIST
Ttriple	153.89 ± 0.05	K	NIST
Ttriple	153.40 ± 0.20	K	NIST
Ttriple	154.30 ± 0.05	K	NIST
Ttriple	153.89 ± 0.05	K	NIST
Ttriple	153.40 ± 0.20	K	NIST
UQi	4.18		ChemSep v8.3 pure component data Compiled value
URi	4.94		ChemSep v8.3 pure component data Compiled value
Vc	[0.405; 0.409]	m3/kmol
Vc	0.409	m3/kmol	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 6 Compiled value
Vc	0.405	m3/kmol	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Vc	0.409	m3/kmol	ChemSep v8.3 pure component data Compiled value
Vc	0.409	m3/kmol	KDB
Vc	0.409	m3/kmol	NIST
VCOSTALD	0.41	m3/kmol	Hankinson and Thomson (1979), COSTALD parameters Compiled value
ωSRK	0.36		Hankinson and Thomson (1979), COSTALD parameters Compiled value
Zc	[0.2670000; 0.2673330]
Zc	0.2670000		IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 6 Compiled value
Zc	0.2670000		ChemSep v8.3 pure component data Compiled value
Zc	0.2673330		KDB
Zra	[0.26; 0.26]
Zra	0.26		Hankinson and Thomson (1979), COSTALD parameters Compiled value
Zra	0.26		ChemSep v8.3 pure component data Compiled value
Zra	0.26		KDB

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[211.79; 212.84]	J/mol×K	[295.10; 298.15]
Cp,liquid	212.84	J/mol×K	295.10	NIST
Cp,liquid	211.79	J/mol×K	298.15	NIST
Csat	[181.40; 212.40]	J/mol×K	[160.00; 300.00]
Csat	181.40	J/mol×K	160.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Csat	181.70	J/mol×K	170.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Csat	182.40	J/mol×K	180.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Csat	183.40	J/mol×K	190.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Csat	184.80	J/mol×K	200.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Csat	186.50	J/mol×K	210.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Csat	188.50	J/mol×K	220.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Csat	190.70	J/mol×K	230.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Csat	193.20	J/mol×K	240.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Csat	196.00	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
Csat	198.90	J/mol×K	260.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Csat	202.10	J/mol×K	270.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Csat	203.10	J/mol×K	273.15	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Csat	205.40	J/mol×K	280.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Csat	208.80	J/mol×K	290.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Csat	211.80	J/mol×K	298.15	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Csat	212.40	J/mol×K	300.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
ΔfusH	[12.64; 12.66]	kJ/mol	[153.40; 154.30]
ΔfusH	12.66	kJ/mol	153.40	NIST
ΔfusH	12.66	kJ/mol	153.40	NIST
ΔfusH	12.64	kJ/mol	154.30	NIST
ΔfusH	12.66	kJ/mol	154.30	NIST
ΔvapH	[31.09; 35.93]	kJ/mol	[283.50; 366.80]
ΔvapH	35.90	kJ/mol	283.50	NIST
ΔvapH	35.93	kJ/mol	300.00	NIST
ΔvapH	35.30	kJ/mol	306.50	NIST
ΔvapH	34.50	kJ/mol	317.50	NIST
ΔvapH	34.60	kJ/mol	339.50	NIST
ΔvapH	33.90	kJ/mol	347.00	NIST
ΔvapH	31.09	kJ/mol	366.80	KDB
n0	[1.39713; 1.39992]		[293.15; 298.15]
n0	1.39992		293.15	Excess Volume of the 1-Propanol + 1-Alkene Systems in Terms of an Equation of State with Association
n0	1.39713		298.15	KDB
ρl	697.00	kg/m3	293.00	KDB
ΔfusS	[82.54; 82.54]	J/mol×K	[153.40; 153.40]
ΔfusS	82.54	J/mol×K	153.40	NIST
ΔfusS	82.54	J/mol×K	153.40	NIST
γ	0.02	N/m	298.20	KDB
λliquid	[0.11; 0.13]	W/m×K	[262.46; 321.08]
λliquid	0.13	W/m×K	262.46	Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λliquid	0.13	W/m×K	262.75	Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λliquid	0.13	W/m×K	262.97	Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λliquid	0.13	W/m×K	280.48	Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λliquid	0.13	W/m×K	280.80	Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λliquid	0.13	W/m×K	281.03	Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λliquid	0.12	W/m×K	297.36	Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λliquid	0.12	W/m×K	297.71	Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λliquid	0.12	W/m×K	297.95	Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λliquid	0.11	W/m×K	320.47	Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λliquid	0.11	W/m×K	320.83	Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λliquid	0.11	W/m×K	321.08	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
283.53	100.00	705.5
283.53	500.00	705.9
283.53	1000.00	706.4
283.53	3000.00	708.2
283.53	5000.00	710.0
283.53	10000.00	714.3
283.52	15000.00	718.3
283.52	20000.00	722.2
283.52	25000.00	725.9
283.52	30000.00	729.4
283.52	35000.00	732.9
283.52	40000.00	736.1
283.53	45000.00	739.3
283.53	50000.00	742.4
283.52	55000.00	745.3
283.53	60000.00	748.2
283.54	70000.00	753.8
283.53	80000.00	759.0
283.53	90000.00	763.9
283.54	100000.00	768.7
293.45	100.00	697.0
293.45	500.00	697.4
293.45	1000.00	697.9
293.46	3000.00	699.9
293.45	5000.00	701.8
293.46	10000.00	706.4
293.46	15000.00	710.7
293.45	20000.00	714.8
293.45	25000.00	718.7
293.45	30000.00	722.4
293.45	35000.00	726.0
293.46	40000.00	729.4
293.46	45000.00	732.8
293.46	50000.00	736.0
293.45	55000.00	739.0
293.45	60000.00	742.0
293.45	70000.00	747.8
293.45	80000.00	753.2
293.45	90000.00	758.3
293.45	100000.00	763.1
303.37	100.00	688.4
303.37	500.00	688.9
303.38	1000.00	689.5
303.38	3000.00	691.6
303.38	5000.00	693.6
303.38	10000.00	698.5
303.38	15000.00	703.1
303.38	20000.00	707.4
303.38	25000.00	711.5
303.38	30000.00	715.4
303.38	35000.00	719.2
303.38	40000.00	722.8
303.38	45000.00	726.2
303.38	50000.00	729.5
303.37	55000.00	732.8
303.38	60000.00	735.9
303.38	70000.00	741.8
303.38	80000.00	747.4
303.38	90000.00	752.6
303.37	100000.00	757.7
313.29	100.00	680.6
313.30	500.00	681.1
313.31	1000.00	681.8
313.31	3000.00	684.0
313.30	5000.00	686.2
313.31	10000.00	691.3
313.31	15000.00	696.3
313.30	20000.00	700.9
313.30	25000.00	705.2
313.30	30000.00	709.3
313.30	35000.00	713.3
313.30	40000.00	717.0
313.30	45000.00	720.6
313.30	50000.00	724.0
313.30	55000.00	727.4
313.30	60000.00	730.6
313.30	70000.00	736.8
313.30	80000.00	742.6
313.30	90000.00	748.0
313.30	100000.00	753.1
323.18	100.00	670.5
323.18	500.00	671.0
323.18	1000.00	671.6
323.18	3000.00	674.1
323.19	5000.00	676.4
323.18	10000.00	682.0
323.19	15000.00	687.1
323.19	20000.00	692.0
323.18	25000.00	696.6
323.18	30000.00	700.9
323.18	35000.00	705.0
323.18	40000.00	708.9
323.18	45000.00	712.7
323.18	50000.00	716.3
323.18	55000.00	719.7
323.18	60000.00	723.1
323.18	70000.00	729.6
323.18	80000.00	735.5
323.19	90000.00	741.1
323.19	100000.00	746.4
333.04	100.00	661.5
333.04	500.00	662.0
333.04	1000.00	662.7
333.05	3000.00	665.3
333.05	5000.00	667.9
333.05	10000.00	673.8
333.05	15000.00	679.3
333.05	20000.00	684.5
333.05	25000.00	689.3
333.05	30000.00	693.8
333.05	35000.00	698.1
333.05	40000.00	702.2
333.05	45000.00	706.2
333.05	50000.00	709.9
333.05	55000.00	713.5
333.05	60000.00	717.0
333.05	70000.00	723.7
333.05	80000.00	729.9
333.05	90000.00	735.7
333.05	100000.00	741.1
342.91	100.00	652.7
342.91	500.00	653.3
342.91	1000.00	654.0
342.91	3000.00	656.9
342.92	5000.00	659.6
342.92	10000.00	666.0
342.91	15000.00	671.8
342.92	20000.00	677.4
342.92	25000.00	682.4
342.91	30000.00	687.1
342.91	35000.00	691.7
342.92	40000.00	696.0
342.92	45000.00	700.1
342.92	50000.00	703.9
342.92	55000.00	707.7
342.92	60000.00	711.3
342.92	70000.00	718.3
342.92	80000.00	724.6
342.92	90000.00	730.6
342.92	100000.00	736.2
352.80	100.00	644.3
352.80	500.00	644.9
352.81	1000.00	645.7
352.81	3000.00	648.8
352.81	5000.00	651.6
352.81	10000.00	658.4
352.81	15000.00	664.7
352.81	20000.00	670.5
352.81	25000.00	675.8
352.81	30000.00	680.9
352.81	35000.00	685.6
352.80	40000.00	690.0
352.80	45000.00	694.3
352.80	50000.00	698.4
352.81	55000.00	702.3
352.81	60000.00	706.0
352.80	70000.00	713.2
352.80	80000.00	719.7
352.80	90000.00	725.9
352.80	100000.00	731.7
362.68	100.00	633.6
362.68	500.00	634.3
362.69	1000.00	635.0
362.69	3000.00	638.5
362.69	5000.00	641.7
362.70	10000.00	649.1
362.70	15000.00	655.8
362.69	20000.00	661.9
362.70	25000.00	667.6
362.69	30000.00	672.8
362.69	35000.00	677.8
362.69	40000.00	682.5
362.69	45000.00	687.0
362.69	50000.00	691.2
362.69	55000.00	695.2
362.69	60000.00	699.1
362.69	70000.00	706.6
362.69	80000.00	713.4
362.69	90000.00	719.7
362.68	100000.00	725.7
Reference

Fixed		Measured
Pressure, kPa - Liquid	Temperature, K - Liquid	Mass density, kg/m3 - Liquid
98.00	298.15	694.51
98.00	303.15	689.57
98.00	312.83	680.92
98.00	322.39	672.17
98.00	327.49	668.07
98.00	340.21	655.95
98.00	354.73	643.5
98.00	360.03	638.93
24510.00	298.15	718.23
24510.00	303.15	715.0
24510.00	327.47	697.97
24510.00	360.06	672.86
24510.00	392.79	646.48
24510.00	424.11	619.97
24510.00	452.35	595.84
24510.00	473.70	578.48
49030.00	298.15	734.7
49030.00	303.15	733.1
49030.00	327.49	718.4
49030.00	359.96	699.31
49030.00	392.68	676.29
49030.00	424.17	653.79
49030.00	452.34	628.89
49030.00	473.56	612.5
98060.00	298.15	765.58
98060.00	303.15	761.82
98060.00	327.48	746.71
98060.00	359.87	730.37
98060.00	392.74	714.89
98060.00	424.17	697.03
98060.00	452.25	676.86
98060.00	473.47	665.45
147100.00	298.15	783.57
147100.00	303.15	780.46
147100.00	327.63	767.87
147100.00	359.74	750.76
147100.00	392.61	734.09
147100.00	424.04	717.45
147100.00	452.28	702.95
147100.00	473.33	692.3
196130.00	298.15	800.85
196130.00	303.15	797.46
196130.00	327.63	786.42
196130.00	359.75	773.85
196130.00	392.46	758.9
196130.00	423.82	745.35
196130.00	452.22	733.49
196130.00	473.28	723.12
245160.00	298.15	816.79
245160.00	303.15	815.3
245160.00	327.67	805.58
245160.00	359.63	791.61
245160.00	392.40	776.73
245160.00	424.07	760.78
245160.00	452.27	750.38
245160.00	473.35	737.15
Reference

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[116.17; 408.53]	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			9.40670e+01
Coefficient B			-6.09560e+02
Coefficient C			6.13524e+00
Coefficient D			4.63160e-05
Coefficient E			-2.11050e-08
Temperature range, min.			200.00
Temperature range, max.			1500.00
Cp,gas	116.17	J/mol×K	200.00	Calculated Property
Cp,gas	173.83	J/mol×K	344.44	Calculated Property
Cp,gas	229.17	J/mol×K	488.89	Calculated Property
Cp,gas	274.19	J/mol×K	633.33	Calculated Property
Cp,gas	309.96	J/mol×K	777.78	Calculated Property
Cp,gas	338.52	J/mol×K	922.22	Calculated Property
Cp,gas	361.58	J/mol×K	1066.67	Calculated Property
Cp,gas	380.38	J/mol×K	1211.11	Calculated Property
Cp,gas	395.81	J/mol×K	1355.56	Calculated Property
Cp,gas	408.53	J/mol×K	1500.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[180.60; 275.04]	J/mol×K	[151.79; 430.00]	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			5.84190e+01
Coefficient B			8.92590e+01
Coefficient C			3.64124e+00
Coefficient D			3.92710e-03
Coefficient E			-8.61810e-07
Temperature range, min.			151.79
Temperature range, max.			430.00
Cp,liquid	180.60	J/mol×K	151.79	Calculated Property
Cp,liquid	182.20	J/mol×K	182.70	Calculated Property
Cp,liquid	187.27	J/mol×K	213.61	Calculated Property
Cp,liquid	194.74	J/mol×K	244.53	Calculated Property
Cp,liquid	204.13	J/mol×K	275.44	Calculated Property
Cp,liquid	215.19	J/mol×K	306.35	Calculated Property
Cp,liquid	227.83	J/mol×K	337.26	Calculated Property
Cp,liquid	242.01	J/mol×K	368.18	Calculated Property
Cp,liquid	257.74	J/mol×K	399.09	Calculated Property
Cp,liquid	275.04	J/mol×K	430.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.0046995; 0.0001398]	Pa×s	[154.12; 429.92]	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			-1.02900e+01
Coefficient B			8.27040e+02
Coefficient C			-8.71440e-02
Coefficient D			1.05200e-07
Coefficient E			2.00000e+00
Temperature range, min.			154.12
Temperature range, max.			429.92
η	0.0046995	Pa×s	154.12	Calculated Property
η	0.0019016	Pa×s	184.76	Calculated Property
η	0.0009939	Pa×s	215.41	Calculated Property
η	0.0006099	Pa×s	246.05	Calculated Property
η	0.0004168	Pa×s	276.70	Calculated Property
η	0.0003071	Pa×s	307.34	Calculated Property
η	0.0002391	Pa×s	337.99	Calculated Property
η	0.0001941	Pa×s	368.63	Calculated Property
η	0.0001627	Pa×s	399.28	Calculated Property
η	0.0001398	Pa×s	429.92	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ΔvapH	[43.46; 15.34]	kJ/mol	[154.12; 517.23]	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			5.63137e+01
Coefficient B			1.14539e+00
Coefficient C			-1.73144e+00
Coefficient D			1.61594e+00
Coefficient E			-6.50835e-01
Critical temperature, Tc (K)			5.37300e+02
Temperature range, min.			154.12
Temperature range, max.			517.23
ΔvapH	43.46	kJ/mol	154.12	Calculated Property
ΔvapH	41.13	kJ/mol	194.47	Calculated Property
ΔvapH	38.92	kJ/mol	234.81	Calculated Property
ΔvapH	36.74	kJ/mol	275.16	Calculated Property
ΔvapH	34.49	kJ/mol	315.50	Calculated Property
ΔvapH	32.08	kJ/mol	355.85	Calculated Property
ΔvapH	29.39	kJ/mol	396.19	Calculated Property
ΔvapH	26.24	kJ/mol	436.54	Calculated Property
ΔvapH	22.17	kJ/mol	476.88	Calculated Property
ΔvapH	15.34	kJ/mol	517.23	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.63]	kPa	[266.18; 391.88]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.43101e+01
Coefficient B			-3.15735e+03
Coefficient C			-4.10140e+01
Temperature range, min.			266.18
Temperature range, max.			391.88
Pvap	1.33	kPa	266.18	Calculated Property
Pvap	3.02	kPa	280.15	Calculated Property
Pvap	6.27	kPa	294.11	Calculated Property
Pvap	12.03	kPa	308.08	Calculated Property
Pvap	21.66	kPa	322.05	Calculated Property
Pvap	36.86	kPa	336.01	Calculated Property
Pvap	59.80	kPa	349.98	Calculated Property
Pvap	93.04	kPa	363.95	Calculated Property
Pvap	139.54	kPa	377.91	Calculated Property
Pvap	202.63	kPa	391.88	Calculated Property
Pvap	[1.11e-06; 2887.59]	kPa	[154.12; 537.30]	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			1.03011e+02
Coefficient B			-7.60567e+03
Coefficient C			-1.34323e+01
Coefficient D			1.23163e-05
Coefficient E			2.00000e+00
Comment			Range stopped at Tc; ChemSep gives it to 537.4 K.
Temperature range, min.			154.12
Temperature range, max.			537.30
Pvap	1.11e-06	kPa	154.12	Calculated Property
Pvap	2.19e-03	kPa	196.70	Calculated Property
Pvap	0.19	kPa	239.27	Calculated Property
Pvap	3.41	kPa	281.85	Calculated Property
Pvap	24.46	kPa	324.42	Calculated Property
Pvap	101.81	kPa	367.00	Calculated Property
Pvap	301.96	kPa	409.57	Calculated Property
Pvap	722.24	kPa	452.15	Calculated Property
Pvap	1506.77	kPa	494.72	Calculated Property
Pvap	2887.59	kPa	537.30	Calculated Property
Pvap	[1.28e-06; 2846.43]	kPa	[154.27; 537.29]	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			8.49146e+01
Coefficient B			-7.03286e+03
Coefficient C			-1.05363e+01
Coefficient D			8.19459e-06
Coefficient E			0.00000e+00
Temperature range, min.			154.27
Temperature range, max.			537.29
Pvap	1.28e-06	kPa	154.27	Calculated Property
Pvap	2.12e-03	kPa	196.83	Calculated Property
Pvap	0.18	kPa	239.39	Calculated Property
Pvap	3.25	kPa	281.94	Calculated Property
Pvap	24.06	kPa	324.50	Calculated Property
Pvap	103.16	kPa	367.06	Calculated Property
Pvap	311.67	kPa	409.62	Calculated Property
Pvap	747.67	kPa	452.17	Calculated Property
Pvap	1536.71	kPa	494.73	Calculated Property
Pvap	2846.43	kPa	537.29	Calculated Property
Pvap	[2.28; 87.86]	kPa	[273.19; 361.89]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.43177e+01
Coefficient B			-3.22517e+03
Coefficient C			-3.41930e+01
Reference			Bent, Cuthbertson, et al., 1936
Comment			Coefficents calculated by NIST from author's data.
Temperature range, min.			273.19
Temperature range, max.			361.89
Pvap	2.28	kPa	273.19	Calculated Property
Pvap	3.89	kPa	283.05	Calculated Property
Pvap	6.37	kPa	292.90	Calculated Property
Pvap	10.06	kPa	302.76	Calculated Property
Pvap	15.39	kPa	312.61	Calculated Property
Pvap	22.87	kPa	322.47	Calculated Property
Pvap	33.11	kPa	332.32	Calculated Property
Pvap	46.80	kPa	342.18	Calculated Property
Pvap	64.76	kPa	352.03	Calculated Property
Pvap	87.86	kPa	361.89	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ρl	[799.93; 254.41]	kg/m3	[154.12; 536.53]	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			2.56334e+01
Coefficient B			1.69520e-01
Coefficient C			5.37300e+02
Coefficient D			1.87400e-01
Temperature range, min.			154.12
Temperature range, max.			536.53
ρl	799.93	kg/m3	154.12	Calculated Property
ρl	771.42	kg/m3	196.61	Calculated Property
ρl	741.04	kg/m3	239.10	Calculated Property
ρl	708.34	kg/m3	281.59	Calculated Property
ρl	672.65	kg/m3	324.08	Calculated Property
ρl	632.91	kg/m3	366.57	Calculated Property
ρl	587.32	kg/m3	409.06	Calculated Property
ρl	532.19	kg/m3	451.55	Calculated Property
ρl	457.41	kg/m3	494.04	Calculated Property
ρl	254.41	kg/m3	536.53	Calculated Property

Property	Value	Unit	Temperature (K)	Source
γ	[0.03; 0.01]	N/m	[153.15; 366.75]	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			4.93492e-02
Coefficient B			-9.91000e-05
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Temperature range, min.			153.15
Temperature range, max.			366.75
γ	0.03	N/m	153.15	Calculated Property
γ	0.03	N/m	176.88	Calculated Property
γ	0.03	N/m	200.62	Calculated Property
γ	0.03	N/m	224.35	Calculated Property
γ	0.02	N/m	248.08	Calculated Property
γ	0.02	N/m	271.82	Calculated Property
γ	0.02	N/m	295.55	Calculated Property
γ	0.02	N/m	319.28	Calculated Property
γ	0.02	N/m	343.02	Calculated Property
γ	0.01	N/m	366.75	Calculated Property
γ	[0.04; 6.85e-04]	N/m	[154.12; 517.23]	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			-1.05680e-02
Coefficient B			2.40260e+01
Coefficient C			-3.05950e+00
Coefficient D			-1.79300e-04
Coefficient E			-5.16340e-06
Temperature range, min.			154.12
Temperature range, max.			517.23
γ	0.04	N/m	154.12	Calculated Property
γ	0.03	N/m	194.47	Calculated Property
γ	0.03	N/m	234.81	Calculated Property
γ	0.02	N/m	275.16	Calculated Property
γ	0.02	N/m	315.50	Calculated Property
γ	0.01	N/m	355.85	Calculated Property
γ	0.01	N/m	396.19	Calculated Property
γ	0.01	N/m	436.54	Calculated Property
γ	0.00	N/m	476.88	Calculated Property
γ	6.85e-04	N/m	517.23	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λgas	[0.00; 0.11]	W/m×K	[154.12; 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			1.36760e-05
Coefficient B			1.34100e+00
Coefficient C			3.65190e+02
Coefficient D			6.25180e+03
Temperature range, min.			154.12
Temperature range, max.			1000.00
λgas	0.00	W/m×K	154.12	Calculated Property
λgas	0.01	W/m×K	248.11	Calculated Property
λgas	0.02	W/m×K	342.09	Calculated Property
λgas	0.03	W/m×K	436.08	Calculated Property
λgas	0.04	W/m×K	530.07	Calculated Property
λgas	0.05	W/m×K	624.05	Calculated Property
λgas	0.06	W/m×K	718.04	Calculated Property
λgas	0.07	W/m×K	812.03	Calculated Property
λgas	0.09	W/m×K	906.01	Calculated Property
λgas	0.11	W/m×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λliquid	[0.17; 0.08]	W/m×K	[154.12; 433.15]	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			-3.80530e-02
Coefficient B			-3.41580e+01
Coefficient C			-1.00570e+00
Coefficient D			-2.33530e-03
Coefficient E			-3.77020e-08
Temperature range, min.			154.12
Temperature range, max.			433.15
λliquid	0.17	W/m×K	154.12	Calculated Property
λliquid	0.16	W/m×K	185.12	Calculated Property
λliquid	0.15	W/m×K	216.13	Calculated Property
λliquid	0.14	W/m×K	247.13	Calculated Property
λliquid	0.13	W/m×K	278.13	Calculated Property
λliquid	0.12	W/m×K	309.14	Calculated Property
λliquid	0.11	W/m×K	340.14	Calculated Property
λliquid	0.10	W/m×K	371.14	Calculated Property
λliquid	0.09	W/m×K	402.15	Calculated Property
λliquid	0.08	W/m×K	433.15	Calculated Property

Similar Compounds

Find more compounds similar to 1-Heptene.

Mixtures

• 1,2-Ethanediol + 1-Heptene + TETRAMETHYLAMMONIUM CHLORIDE
• 1-Heptene + N-Formylmorpholine
• 1-Heptene + 2-Pyrrolidinone, 1-methyl-
• 1-Heptene + TETRAMETHYLAMMONIUM CHLORIDE + Glycerin
• 1-Heptene + Pyridine
• 2-Furanmethanol + 1-Heptene
• Acetic acid, pentyl ester + 1-Heptene
• 1,2-Ethanediol + 1-Heptene
• 1-Heptene + Ethanol, 2,2'-oxybis-
• 1-Heptene + Triethylene glycol
• 1-Heptene + Propanamide, N,N-bis(2-ethylhexyl)-2-methyl-
• 1-Heptene + 1,8-Diaminooctane
• 1-Heptene + 1,1O-DIAMINODECANE
• 1-Heptene + 1,12-Dodecanediamine
• 1-Heptene + 1-Octadecanol
• 1-Heptene + 1-Eicosanol
• 1-Heptene + N^1,n^3 dibutylimidazolidine 2-thione
• 1-Propanol + 1-Heptene

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.
• 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
• Determination of activity coefficients at infinite dilution of organic solutes in the ionic liquid, trihexyl(tetradecyl)-phosphonium tris(pentafluoroethyl) trifluorophosphate, by gas liquid chromatography
• Determination of activity coefficients at infinite dilution of organic solutes in the ionic liquid, tributylmethylphosphonium methylsulphate by gas liquid chromatography
• Infinite dilution activity coefficients, specific retention volumes and solvation thermodynamics of hydrocarbons in C78H158 branched alkane solvent
• 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 of alkanes and alkenes in 1-alkyl-3-methylimidazolium tetrafluoroborate
• 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
• Abraham model linear free energy relationships for describing the partitioning and solubility behavior of nonelectrolyte organic solutes dissolved in pyridine at 298.15 K
• 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
• Measurements of activity coefficient at infinite dilution for organic solutes in tetramethylammonium chloride + ethylene glycol deep eutectic solvent using gas-liquid chromatography
• Tetramethylammonium chloride + glycerol deep eutectic solvent as separation agent for organic liquid mixtures: Assessment from experimental limiting activity coefficients
• Thermodynamics and activity coefficients at infinite dilution for organic solutes in the ionic liquid 1-butyl-1-methylpyrrolidinium dicyanamide
• 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
• Activity coefficients at infinite dilution for hydrocarbons in furfuryl alcohol at T=(278.15 and 298.15) K, determined by g.l.c.
• 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)
• Measurement of activity coefficients at infinite dilution using polar and non-polar solutes in the ionic liquid 1-methyl-3-octyl-imidazolium diethyleneglycolmonomethylethersulfate at T = (288.15, 298.15, and 313.15) K
• 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 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 of organic solutes in the ionic liquid 1-ethyl-3-methylimidazolium trifluoromethanesulfonate using gas liquid chromatography at T = (313.15, 323.15, and 333.15) K
• Activity coefficients at infinite dilution for solutes in the trioctylmethylammonium bis(trifluoromethylsulfonyl)imide ionic liquid using gas liquid chromatography
• Activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-octyl-3-methylimidazolium hexafluorophosphate using gas liquid chromatography at T = (313.15, 323.15, and 333.15) K
• 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 solutes and water in 1-propyl-1-methylpiperidinium bis{(trifluoromethyl)sulfonyl}imide ionic liquid using g.l.c.
• 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 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
• Measurements of activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-hexyl-3-methylimidazolium tetracyanoborate
• 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
• Measurements of activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-ethyl-3-methylimidazolium methanesulfonate
• 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
• Physicochemical properties and activity coefficients at infinite dilution for organic solutes and water in a novel bicyclic guanidinium superbase-derived protic ionic liquid
• Experimental and theoretical study on infinite dilution activity coefficients of various solutes in piperidinium ionic liquids
• 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
• Thermodynamics and activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-butyl-1-methylmorpholinium 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 for organic solutes and water in 1-ethyl-1-methylpyrrolidinium lactate
• 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
• Separation of aliphatic from aromatic hydrocarbons and sulphur compounds from fuel based on measurements of activity coefficients at infinite dilution for organic solutes and water in the ionic liquid N,N-diethyl-N-methyl-N-(2-methoxy-ethyl)ammonium bis(trifluoromethylsulfonyl)imide
• Thermodynamics and limiting activity coefficients measurements for organic solutes and water in the ionic liquid 1-dodecyl-3-methylimidzolium bis(trifluoromethylsulfonyl) imide
• Activity coefficients at infinite dilution of hydrocarbons in glycols: Experimental data and thermodynamic modeling with the GCA-EoS
• 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
• Thermodynamic study of molecular interaction-selectivity in separation processes based on limiting activity coefficients
• Abraham model correlations for describing the thermodynamic properties of solute transfer into pentyl acetate based on headspace chromatographic and solubility measurements
• The use of ionic liquids for separation of binary hydrocarbons mixtures based on gamma infinity data measurements
• Separation of (water/butan-1-ol) binary systems based on activity coefficients at infinite dilution with phosphonium ionic liquid
• Activity Coefficients at Infinite Dilution of Organic Solutes and Water in Tributylethylphosphonium Diethylphosphate Using Gas Liquid Chromatography: Thermodynamic Properties of Mixtures Containing Ionic Liquids
• 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
• Activity Coefficients at Infinite Dilution of Various Solutes in Tetrapropylammonium Bromide + 1,6-Hexanediol Deep Eutectic Solvent
• Determination of Activity Coefficients at Infinite Dilution of Solutes in N,N'-Di(2-ethylhexyl)isobutyramide Using Inverse Gas-Liquid Chromatography
• Assessment of Pyrrolidinium-Based Ionic Liquid for the Separation of Binary Mixtures Based on Activity Coefficients at Infinite Dilution
• Activity Coefficients at Infinite Dilution of Organic Solutes in 1-Hexyl-3-methylimidazolium Hexafluorophosphate from Gas-Liquid Chromatography
• Determination of Activity Coefficients at Infinite Dilution of Solutes in the Ionic Liquid 1-Hexyl-3-methylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography at the Temperatures 298.15 K and 323.15 K
• Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
• Determination of Activity Coefficients at Infinite Dilution of Polar and Nonpolar Solutes in the Ionic Liquid 1-Ethyl-3-methyl- imidazolium Bis(trifluoromethylsulfonyl) Imidate Using Gas-Liquid Chromatography at the Temperature 303.15 K or 318.15 K
• 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
• Infinite Dilution Activity Coefficients for Trihexyltetradecyl Phosphonium Ionic Liquids: Measurements and COSMO-RS Prediction
• 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
• Excess Volume of the 1-Propanol + 1-Alkene Systems in Terms of an Equation of State with Association
• Measurements of Activity Coefficients at Infinite Dilution for Organic Solutes and Water in the Ionic Liquid 1-Butyl-1-methylpiperydinium Thiocyanate
• Activity Coefficients at Infinite Dilution by GLC in Alkanediamines as Stationary Phases
• Experimental Study and Correlation Models of the Density and Viscosity of 1-Hexene and 1-Heptene at Temperatures from (298 to 473) K and Pressures up to 245 MPa
• 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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