Chemical Properties of 1-NONENE (CAS 124-11-8)

InChI

InChI=1S/C9H18/c1-3-5-7-9-8-6-4-2/h3H,1,4-9H2,2H3

InChI Key

JRZJOMJEPLMPRA-UHFFFAOYSA-N

Formula

C9H18

SMILES

C=CCCCCCCC

Molecular Weight¹

126.24

CAS

124-11-8

Other Names

• 1-C9H18
• NSC 73961
• Non-1-ene
• Nonene-(1)
• Nonylene
• n-Non-1-ene

• ω : Acentric Factor.
• 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).
• Δ_fG° : Standard Gibbs free energy of formation (kJ/mol).
• Δ_fH°_gas : Enthalpy of formation at standard conditions (kJ/mol).
• Δ_fusH° : Enthalpy of fusion at standard conditions (kJ/mol).
• Δ_fusH : Enthalpy of fusion at a given temperature (kJ/mol).
• Δ_vapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
• Δ_vapH : Enthalpy of vaporization at a given temperature (kJ/mol).
• IE : Ionization energy (eV).
• log₁₀WS : Log10 of Water solubility in mol/l.
• logP_oct/wat : Octanol/Water partition coefficient.
• McVol : McGowan's characteristic volume (ml/mol).
• P_c : Critical Pressure (kPa).
• P_vap : Vapor pressure (kPa).
• ρ_c : Critical density (kg/m³).
• I_np : Non-polar retention indices.
• I : Polar retention indices.
• S°_liquid : Liquid phase molar entropy at standard conditions (J/mol×K).
• 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).
• ¹: Molecular weight from the IUPAC atomic weights tables.

Physical Properties

Property	Value	Unit	Source
ω	0.4055		Relay (1.0) Calculated Property
ΔfG°	112.74	kJ/mol	Joback Calculated Property
ΔfH°gas	-107.74	kJ/mol	Relay (1.0) Calculated Property
ΔfusH°	17.79	kJ/mol	Joback Calculated Property
ΔvapH°	[44.70; 45.50]	kJ/mol
ΔvapH°	44.70 ± 0.20	kJ/mol	NIST
ΔvapH°	45.50	kJ/mol	NIST
IE	9.42 ± 0.01	eV	NIST
log10WS	[-5.05; -5.05]
log10WS	-5.05		Aq. Solubility Prediction
log10WS	-5.05		Estimated Solubility
logPoct/wat	3.533		Crippen Calculated Property
McVol	133.370	ml/mol	McGowan Calculated Property
Pc	2402.92	kPa	Joback Calculated Property
ρc	239.85	kg/m3	NIST
Inp	[879.00; 900.00]
Inp	885.00		NIST
Inp	882.00		NIST
Inp	889.00		NIST
Inp	889.00		NIST
Inp	881.00		NIST
Inp	885.20		NIST
Inp	882.00		NIST
Inp	886.00		NIST
Inp	888.00		NIST
Inp	889.00		NIST
Inp	889.00		NIST
Inp	889.00		NIST
Inp	888.70		NIST
Inp	888.00		NIST
Inp	888.00		NIST
Inp	890.00		NIST
Inp	889.00		NIST
Inp	889.00		NIST
Inp	883.00		NIST
Inp	883.00		NIST
Inp	883.40		NIST
Inp	883.00		NIST
Inp	881.00		NIST
Inp	882.00		NIST
Inp	883.00		NIST
Inp	882.00		NIST
Inp	889.50		NIST
Inp	890.30		NIST
Inp	882.70		NIST
Inp	883.00		NIST
Inp	882.80		NIST
Inp	882.20		NIST
Inp	887.00		NIST
Inp	883.00		NIST
Inp	890.00		NIST
Inp	895.00		NIST
Inp	887.00		NIST
Inp	894.00		NIST
Inp	890.00		NIST
Inp	889.20		NIST
Inp	882.00		NIST
Inp	890.00		NIST
Inp	893.00		NIST
Inp	892.00		NIST
Inp	888.90		NIST
Inp	889.50		NIST
Inp	890.20		NIST
Inp	895.90		NIST
Inp	896.00		NIST
Inp	884.00		NIST
Inp	888.90		NIST
Inp	889.50		NIST
Inp	890.20		NIST
Inp	889.00		NIST
Inp	888.00		NIST
Inp	888.92		NIST
Inp	888.92		NIST
Inp	888.98		NIST
Inp	891.78		NIST
Inp	891.75		NIST
Inp	891.84		NIST
Inp	887.00		NIST
Inp	892.00		NIST
Inp	889.00		NIST
Inp	883.00		NIST
Inp	894.00		NIST
Inp	889.00		NIST
Inp	892.00		NIST
Inp	892.00		NIST
Inp	893.00		NIST
Inp	895.00		NIST
Inp	891.00		NIST
Inp	892.00		NIST
Inp	880.00		NIST
Inp	886.00		NIST
Inp	891.00		NIST
Inp	886.00		NIST
Inp	888.00		NIST
Inp	886.00		NIST
Inp	886.00		NIST
Inp	888.80		NIST
Inp	886.00		NIST
Inp	890.00		NIST
Inp	884.00		NIST
Inp	Outlier 899.00		NIST
Inp	892.00		NIST
Inp	888.00		NIST
Inp	887.00		NIST
Inp	889.00		NIST
Inp	880.00		NIST
Inp	889.00		NIST
Inp	882.00		NIST
Inp	891.00		NIST
Inp	Outlier 900.00		NIST
Inp	888.00		NIST
Inp	889.00		NIST
Inp	Outlier 879.00		NIST
Inp	887.00		NIST
Inp	896.00		NIST
Inp	889.00		NIST
Inp	884.00		NIST
Inp	889.00		NIST
Inp	890.00		NIST
Inp	894.00		NIST
Inp	895.00		NIST
Inp	891.00		NIST
Inp	888.80		NIST
Inp	892.00		NIST
Inp	883.00		NIST
Inp	890.20		NIST
Inp	889.50		NIST
Inp	888.92		NIST
Inp	887.00		NIST
I	[923.00; 960.00]
I	952.00		NIST
I	953.00		NIST
I	950.00		NIST
I	950.00		NIST
I	946.00		NIST
I	949.80		NIST
I	949.70		NIST
I	950.50		NIST
I	947.70		NIST
I	949.80		NIST
I	950.50		NIST
I	929.00		NIST
I	960.00		NIST
I	931.00		NIST
I	930.00		NIST
I	923.00		NIST
I	929.00		NIST
I	930.00		NIST
S°liquid	392.54	J/mol×K	NIST
Tboil	[413.00; 422.15]	K
Tboil	420.10	K	NIST
Tboil	418.80 ± 0.80	K	NIST
Tboil	420.00 ± 1.50	K	NIST
Tboil	418.00 ± 20.00	K	NIST
Tboil	418.00 ± 3.00	K	NIST
Tboil	419.10 ± 2.50	K	NIST
Tboil	417.90 ± 0.30	K	NIST
Tboil	420.40 ± 1.50	K	NIST
Tboil	419.51 ± 0.40	K	NIST
Tboil	419.99 ± 0.20	K	NIST
Tboil	422.15 ± 1.00	K	NIST
Tboil	418.50 ± 1.50	K	NIST
Tboil	420.00 ± 4.00	K	NIST
Tboil	Outlier 413.00 ± 5.00	K	NIST
Tc	594.00 ± 1.00	K	NIST
Tfus	[185.00; 192.06]	K
Tfus	191.33	K	Aq. Solubility Prediction
Tfus	191.40 ± 1.00	K	NIST
Tfus	192.06 ± 0.15	K	NIST
Tfus	191.74 ± 0.06	K	NIST
Tfus	191.78 ± 0.03	K	NIST
Tfus	189.60 ± 2.00	K	NIST
Tfus	185.00 ± 1.50	K	NIST
Tfus	185.00 ± 5.00	K	NIST
Ttriple	[191.60; 191.91]	K
Ttriple	191.60 ± 0.00	K	NIST
Ttriple	191.91 ± 0.00	K	NIST
Ttriple	191.60 ± 0.00	K	NIST
Ttriple	191.91 ± 0.00	K	NIST
Vc	0.526	m3/kmol	NIST

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[257.31; 331.38]	J/mol×K	[402.00; 568.30]
Cp,gas	257.31	J/mol×K	402.00	Joback Calculated Property
Cp,gas	270.92	J/mol×K	429.72	Joback Calculated Property
Cp,gas	284.01	J/mol×K	457.43	Joback Calculated Property
Cp,gas	296.58	J/mol×K	485.15	Joback Calculated Property
Cp,gas	308.66	J/mol×K	512.86	Joback Calculated Property
Cp,gas	320.25	J/mol×K	540.58	Joback Calculated Property
Cp,gas	331.38	J/mol×K	568.30	Joback Calculated Property
Cp,liquid	270.36	J/mol×K	298.15	NIST
η	[0.0002389; 0.0050451]	Pa×s	[189.43; 402.00]
η	0.0050451	Pa×s	189.43	Joback Calculated Property
η	0.0020331	Pa×s	224.86	Joback Calculated Property
η	0.0010493	Pa×s	260.29	Joback Calculated Property
η	0.0006345	Pa×s	295.72	Joback Calculated Property
η	0.0004273	Pa×s	331.14	Joback Calculated Property
η	0.0003106	Pa×s	366.57	Joback Calculated Property
η	0.0002389	Pa×s	402.00	Joback Calculated Property
ΔfusH	[19.97; 19.97]	kJ/mol	[191.60; 191.60]
ΔfusH	19.97	kJ/mol	191.60	NIST
ΔfusH	19.97	kJ/mol	191.60	NIST
ΔfusH	19.97	kJ/mol	191.60	NIST
ΔfusH	19.97	kJ/mol	191.60	NIST
ΔvapH	42.00	kJ/mol	381.00	NIST

Correlations

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.63]	kPa	[307.75; 446.60]	The Yaws Handbook of Vapor Pressure
Equation			ln(Pvp) = A + B/(T + C)
Coefficient A			1.44429e+01
Coefficient B			-3.57259e+03
Coefficient C			-5.53600e+01
Temperature range, min.			307.75
Temperature range, max.			446.60
Pvap	1.33	kPa	307.75	Calculated Property
Pvap	3.01	kPa	323.18	Calculated Property
Pvap	6.23	kPa	338.61	Calculated Property
Pvap	11.96	kPa	354.03	Calculated Property
Pvap	21.52	kPa	369.46	Calculated Property
Pvap	36.65	kPa	384.89	Calculated Property
Pvap	59.51	kPa	400.32	Calculated Property
Pvap	92.72	kPa	415.74	Calculated Property
Pvap	139.29	kPa	431.17	Calculated Property
Pvap	202.63	kPa	446.60	Calculated Property
Pvap	[8.72e-06; 2337.64]	kPa	[191.78; 593.25]	KDB Vapor Pressure Data
Equation			ln(Pvp) = A + B/T + C*ln(T) + D*T^2
Coefficient A			1.06010e+02
Coefficient B			-9.03620e+03
Coefficient C			-1.34814e+01
Coefficient D			8.71053e-06
Temperature range, min.			191.78
Temperature range, max.			593.25
Pvap	8.72e-06	kPa	191.78	Calculated Property
Pvap	4.46e-03	kPa	236.39	Calculated Property
Pvap	0.23	kPa	281.00	Calculated Property
Pvap	3.26	kPa	325.60	Calculated Property
Pvap	21.45	kPa	370.21	Calculated Property
Pvap	86.63	kPa	414.82	Calculated Property
Pvap	254.53	kPa	459.43	Calculated Property
Pvap	604.99	kPa	504.03	Calculated Property
Pvap	1247.15	kPa	548.64	Calculated Property
Pvap	2337.64	kPa	593.25	Calculated Property

Similar Compounds

Find more compounds similar to 1-NONENE.

Mixtures

• 1,2-Ethanediol + 1-NONENE
• 1-NONENE + Ethanol, 2,2'-oxybis-

Sources

• KDB Vapor Pressure Data
• Cheméo Relay (1.0)
• Crippen Method
• Infinite dilution activity coefficients, specific retention volumes and solvation thermodynamics of hydrocarbons in C78H158 branched alkane solvent
• Measurements of different thermodynamic properties of systems containing ionic liquids and correlation of these properties using modified UNIFAC (Dortmund)
• 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 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
• 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 trihexyltetradecylphosphonium hexafluorophosphate using gas liquid chromatography at T = (313.15, 333.15, 353.15, and 363.15) K
• 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
• 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
• Activity coefficients at infinite dilution of hydrocarbons in glycols: Experimental data and thermodynamic modeling with the GCA-EoS
• Separation of (water/butan-1-ol) binary systems based on activity coefficients at infinite dilution with phosphonium ionic liquid
• Assessment of Pyrrolidinium-Based Ionic Liquid for the Separation of Binary Mixtures Based on Activity Coefficients at Infinite Dilution
• 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
• Determination of Partitioning Coefficients of Numerous Organic Solutes between a Long-Chain Aliphatic Alcohol and the Gas Phase as a Function of Temperature
• 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
• Joback Method
• KDB
• Aqueous Solubility Prediction Method
• Estimated Solubility Method
• McGowan Method
• NIST Webbook
• The Yaws Handbook of Vapor Pressure

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