Chemical Properties of 1-Decene (CAS 872-05-9)

InChI

InChI=1S/C10H20/c1-3-5-7-9-10-8-6-4-2/h3H,1,4-10H2,2H3

InChI Key

AFFLGGQVNFXPEV-UHFFFAOYSA-N

Formula

C10H20

SMILES

C=CCCCCCCCC

Molecular Weight¹

140.27

CAS

872-05-9

Other Names

• 1-C10H20
• 1-n-Decene
• DECYLENE
• Dec-1-ene
• Decene-1
• Gulftene 10
• Linealene 10
• N-1-DECENE
• NSC 62122
• Neodene 10
• «alpha»-Decene
• «alpha»-Decene

• ω : Acentric Factor.
• T_ig : Autoignition Temperature (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).
• η : Dynamic viscosity (Pa×s).
• T_flash,cc : Flash Point (Closed Cup Method) (K).
• Δ_fG° : Standard Gibbs free energy of formation (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.
• P_c : Critical 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 : 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).
• T_fus : Normal melting (fusion) point (K).
• T_triple : Triple Point Temperature (K).
• V_c : Critical Volume (m³/kmol).
• Z_c : Critical Compressibility.
• Z_ra : Rackett Parameter.
• ¹: Molecular weight from the IUPAC atomic weights tables.

Physical Properties

Property	Value	Unit	Source
ω	0.4910		KDB
Tig	508.15	K	KDB
ΔcH°liquid	-6619.60 ± 1.80	kJ/mol	NIST
Tflash,cc	326.48	K	KDB
ΔfG°	121.10	kJ/mol	KDB
ΔfH°gas	[-124.60; -123.40]	kJ/mol
ΔfH°gas	-124.20	kJ/mol	KDB
ΔfH°gas	-124.60	kJ/mol	NIST
ΔfH°gas	-123.40	kJ/mol	NIST
ΔfH°liquid	-173.80 ± 1.90	kJ/mol	NIST
ΔfusH°	20.38	kJ/mol	Joback Calculated Property
ΔvapH°	[50.40; 50.50]	kJ/mol
ΔvapH°	50.44	kJ/mol	NIST
ΔvapH°	50.43 ± 0.20	kJ/mol	NIST
ΔvapH°	50.40 ± 0.20	kJ/mol	NIST
ΔvapH°	50.50	kJ/mol	NIST
IE	[9.42; 9.59]	eV
IE	9.42 ± 0.01	eV	NIST
IE	9.48	eV	NIST
IE	9.42 ± 0.01	eV	NIST
IE	9.59 ± 0.01	eV	NIST
log10WS	[-5.51; -5.51]
log10WS	-5.51		Aq. Sol...
log10WS	-5.51		Estimat...
logPoct/wat	3.923		Crippen Calculated Property
McVol	147.460	ml/mol	McGowan Calculated Property
NFPA Fire	2		KDB
Pc	[2220.00; 2220.00]	kPa
Pc	2220.00	kPa	KDB
Pc	2220.00 ± 100.00	kPa	NIST
ρc	238.45 ± 14.03	kg/m3	NIST
Inp	[153.90; 997.00]
Inp	985.00		NIST
Inp	982.00		NIST
Inp	989.00		NIST
Inp	990.00		NIST
Inp	985.10		NIST
Inp	985.00		NIST
Inp	988.00		NIST
Inp	989.00		NIST
Inp	989.00		NIST
Inp	989.00		NIST
Inp	988.60		NIST
Inp	990.00		NIST
Inp	989.00		NIST
Inp	988.00		NIST
Inp	989.00		NIST
Inp	982.00		NIST
Inp	983.00		NIST
Inp	982.00		NIST
Inp	990.00		NIST
Inp	989.20		NIST
Inp	990.10		NIST
Inp	982.70		NIST
Inp	982.20		NIST
Inp	987.00		NIST
Inp	988.00		NIST
Inp	990.00		NIST
Inp	992.00		NIST
Inp	988.00		NIST
Inp	988.00		NIST
Inp	992.50		NIST
Inp	993.00		NIST
Inp	992.00		NIST
Inp	987.00		NIST
Inp	993.00		NIST
Inp	993.00		NIST
Inp	989.20		NIST
Inp	989.50		NIST
Inp	990.70		NIST
Inp	985.00		NIST
Inp	989.20		NIST
Inp	989.50		NIST
Inp	990.70		NIST
Inp	988.00		NIST
Inp	988.74		NIST
Inp	988.81		NIST
Inp	988.83		NIST
Inp	991.63		NIST
Inp	991.76		NIST
Inp	991.73		NIST
Inp	988.00		NIST
Inp	991.00		NIST
Inp	982.00		NIST
Inp	997.00		NIST
Inp	989.00		NIST
Inp	989.00		NIST
Inp	989.00		NIST
Inp	991.00		NIST
Inp	991.00		NIST
Inp	992.00		NIST
Inp	992.00		NIST
Inp	989.00		NIST
Inp	989.00		NIST
Inp	988.00		NIST
Inp	988.80		NIST
Inp	988.00		NIST
Inp	988.00		NIST
Inp	997.00		NIST
Inp	988.00		NIST
Inp	988.00		NIST
Inp	987.00		NIST
Inp	986.00		NIST
Inp	990.00		NIST
Inp	991.00		NIST
Inp	982.00		NIST
Inp	988.00		NIST
Inp	Outlier 157.60		NIST
Inp	Outlier 153.90		NIST
I	[1020.00; 1061.00]
I	1052.00		NIST
I	1054.00		NIST
I	1055.00		NIST
I	1048.00		NIST
I	1050.00		NIST
I	1046.00		NIST
I	1047.00		NIST
I	1046.00		NIST
I	1051.70		NIST
I	1055.30		NIST
I	1048.50		NIST
I	1049.80		NIST
I	1051.70		NIST
I	1055.30		NIST
I	1048.50		NIST
I	1049.80		NIST
I	1047.00		NIST
I	1061.00		NIST
I	Outlier 1020.00		NIST
I	1054.00		NIST
I	1043.00		NIST
I	1035.00		NIST
I	1039.00		NIST
S°liquid	425.01	J/mol×K	NIST
Tboil	443.60	K	KDB
Tc	[617.00; 617.00]	K
Tc	617.00	K	KDB
Tc	617.00 ± 2.00	K	NIST
Tfus	[206.90; 207.06]	K
Tfus	206.90	K	KDB
Tfus	207.06	K	Aq. Sol...
Ttriple	[206.47; 206.89]	K
Ttriple	206.89 ± 0.05	K	NIST
Ttriple	206.89 ± 0.06	K	NIST
Ttriple	206.88 ± 0.06	K	NIST
Ttriple	206.47 ± 0.20	K	NIST
Vc	[0.584; 0.584]	m3/kmol
Vc	0.584	m3/kmol	KDB
Vc	0.584	m3/kmol	NIST
Zc	0.2527230		KDB
Zra	0.25		KDB

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[299.13; 378.63]	J/mol×K	[424.88; 590.50]
T(K) Ideal gas heat capacity (J/mol×K) 300 320 340 360 380 450 500 550
Cp,gas	299.13	J/mol×K	424.88	Joback Calculated Property
Cp,gas	313.75	J/mol×K	452.48	Joback Calculated Property
Cp,gas	327.80	J/mol×K	480.09	Joback Calculated Property
Cp,gas	341.30	J/mol×K	507.69	Joback Calculated Property
Cp,gas	354.26	J/mol×K	535.29	Joback Calculated Property
Cp,gas	366.70	J/mol×K	562.90	Joback Calculated Property
Cp,gas	378.63	J/mol×K	590.50	Joback Calculated Property
Cp,liquid	300.83	J/mol×K	298.15	NIST
η	[0.0002345; 0.0053123]	Pa×s	[200.70; 424.88]
T(K) Dynamic viscosity (Pa×s) 0 1.00e-3 2.00e-3 3.00e-3 4.00e-3 5.00e-3 200 300 400
η	0.0053123	Pa×s	200.70	Joback Calculated Property
η	0.0020999	Pa×s	238.06	Joback Calculated Property
η	0.0010678	Pa×s	275.43	Joback Calculated Property
η	0.0006382	Pa×s	312.79	Joback Calculated Property
η	0.0004257	Pa×s	350.15	Joback Calculated Property
η	0.0003070	Pa×s	387.52	Joback Calculated Property
η	0.0002345	Pa×s	424.88	Joback Calculated Property
ΔfusH	[7.95; 13.81]	kJ/mol	[198.30; 206.90]
ΔfusH	7.95	kJ/mol	198.30	NIST
ΔfusH	13.81	kJ/mol	206.90	NIST
ΔfusH	13.81	kJ/mol	206.90	NIST
ΔvapH	[38.66; 45.10]	kJ/mol	[402.50; 443.70]
ΔvapH	45.10	kJ/mol	402.50	NIST
ΔvapH	43.80	kJ/mol	414.00	NIST
ΔvapH	38.66	kJ/mol	443.70	KDB
n0	[1.42139; 1.42140]		[293.15; 293.15]
n0	1.42139		293.15	Excess ...
n0	1.42140		293.15	Isobari...
ρl	741.00	kg/m3	293.00	KDB
ΔfusS	[40.09; 66.73]	J/mol×K	[198.30; 206.90]
ΔfusS	40.09	J/mol×K	198.30	NIST
ΔfusS	66.73	J/mol×K	206.90	NIST
γ	0.02	N/m	298.20	KDB

Correlations

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.63]	kPa	[326.18; 467.83]	The Yaw...
Equation			ln(Pvp) = A + B/(T + C)
Coefficient A			1.48286e+01
Coefficient B			-3.90202e+03
Coefficient C			-5.78340e+01
Temperature range, min.			326.18
Temperature range, max.			467.83
T(K) Vapor pressure (kPa) 0 50 100 150 200 350 400 450
Pvap	1.33	kPa	326.18	Calculated Property
Pvap	2.98	kPa	341.92	Calculated Property
Pvap	6.14	kPa	357.66	Calculated Property
Pvap	11.74	kPa	373.40	Calculated Property
Pvap	21.13	kPa	389.14	Calculated Property
Pvap	36.05	kPa	404.87	Calculated Property
Pvap	58.72	kPa	420.61	Calculated Property
Pvap	91.83	kPa	436.35	Calculated Property
Pvap	138.58	kPa	452.09	Calculated Property
Pvap	202.63	kPa	467.83	Calculated Property
Pvap	[1.46e-05; 2193.34]	kPa	[206.89; 617.05]	KDB Vap...
Equation			ln(Pvp) = A + B/T + C*ln(T) + D*T^2
Coefficient A			1.10936e+02
Coefficient B			-9.75380e+03
Coefficient C			-1.41204e+01
Coefficient D			8.63327e-06
Temperature range, min.			206.89
Temperature range, max.			617.05
T(K) Vapor pressure (kPa) 0 500 1000 1500 2000 200 400 600
Pvap	1.46e-05	kPa	206.89	Calculated Property
Pvap	5.24e-03	kPa	252.46	Calculated Property
Pvap	0.23	kPa	298.04	Calculated Property
Pvap	3.04	kPa	343.61	Calculated Property
Pvap	19.43	kPa	389.18	Calculated Property
Pvap	77.82	kPa	434.76	Calculated Property
Pvap	229.39	kPa	480.33	Calculated Property
Pvap	550.65	kPa	525.90	Calculated Property
Pvap	1151.02	kPa	571.48	Calculated Property
Pvap	2193.34	kPa	617.05	Calculated Property

Similar Compounds

Find more compounds similar to 1-Decene.

Mixtures

• 1-Propanol + 1-Decene
• 1-Decene + Dimethyl ether
• n-Hexane + 1-Decene
• 1-Decene + Octane
• 1-Decene + 1-Hexanol
• Propanamide, N,N-bis(2-ethylhexyl)-2-methyl- + 1-Decene
• 1-Decene + 1,8-Diaminooctane
• 1-Decene + 1,10-Diaminodecane
• 1-Decene + 1,12-Dodecanediamine

Sources

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• Crippen Method
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• 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
• Thermodynamics and activity coefficients at infinite dilution for organic solutes in the ionic liquid 1-butyl-1-methylpyrrolidinium dicyanamide
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• 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
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• 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
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• 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
• 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
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• 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
• Excess Volume of the 1-Propanol + 1-Alkene Systems in Terms of an Equation of State with Association
• Activity Coefficients at Infinite Dilution by GLC in Alkanediamines as Stationary Phases
• Biomass-Derived Platform Chemicals: Thermodynamic Studies on the Extraction of 5-Hydroxymethylfurfural from Ionic Liquids
• Isothermal Phase Equilibria and Excess Molar Enthalpies for Binary Systems with Dimethyl Ether at 323.15 K
• Isobaric Vapor-Liquid Equilibria of Hexane + 1-Decene and Octane + 1-Decene Mixtures
• Paramagnetic Ionic Liquid 1-Butyl-3-methylimidazolium Tetrabromidocobaltate(II): Activity Coefficients at Infinite Dilution of Organic Solutes and Crystal Structure
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• Joback Method
• KDB
• Aqueous Solubility Prediction Method
• Estimated Solubility Method
• McGowan Method
• NIST Webbook
• The Yaws Handbook of Vapor Pressure

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