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

• ω : Acentric Factor.
• AP : Aniline Point (K).
• 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).
• 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_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_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.
• 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	[0.4110; 0.4300]
ω	0.4300		PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
ω	0.4299		Passut and Danner (1973), critical constants and acentric factors Compiled value
ω	0.4110		ChemSep v8.3 pure component data Compiled value
ω	0.4300		KDB
AP	311.150	K	KDB
μ	0.60	debye	ChemSep v8.3 pure component data Compiled value
ΔfG°	[112.30; 112.80]	kJ/mol
ΔfG°	112.30	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfG°	112.80	kJ/mol	KDB
Δc,grossH	5965.13	kJ/mol	KDB
Δc,netH	5568.988	kJ/mol	KDB
ΔfH°gas	[-103.60; -103.50]	kJ/mol
ΔfH°gas	-103.50	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfH°gas	-103.60	kJ/mol	KDB
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
NFPA Fire	3		KDB
Pc	[2330.00; 2344.22]	kPa
Pc	2340.61	kPa	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Pc	2344.22	kPa	Passut and Danner (1973), critical constants and acentric factors Compiled value
Pc	2330.00	kPa	ChemSep v8.3 pure component data Compiled value
Pc	2340.00	kPa	KDB
Ptriple	2.04e-05	kPa	ChemSep v8.3 pure component data Compiled value
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
Ip	[923.00; 960.00]
Ip	952.00		NIST
Ip	953.00		NIST
Ip	950.00		NIST
Ip	950.00		NIST
Ip	946.00		NIST
Ip	949.80		NIST
Ip	949.70		NIST
Ip	950.50		NIST
Ip	947.70		NIST
Ip	949.80		NIST
Ip	950.50		NIST
Ip	929.00		NIST
Ip	960.00		NIST
Ip	931.00		NIST
Ip	930.00		NIST
Ip	923.00		NIST
Ip	929.00		NIST
Ip	930.00		NIST
S°liquid	392.54	J/mol×K	NIST
Tboil	[413.00; 422.15]	K
Tboil	420.03	K	ChemSep v8.3 pure component data Compiled value
Tboil	420.00	K	KDB
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	[592.00; 594.00]	K
Tc	594.00	K	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 6 Compiled value
Tc	592.00	K	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Tc	592.04	K	Passut and Danner (1973), critical constants and acentric factors Compiled value
Tc	594.00	K	ChemSep v8.3 pure component data Compiled value
Tc	594.00	K	KDB
Tc	594.00 ± 1.00	K	NIST
Tfus	[185.00; 192.06]	K
Tfus	191.85	K	Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
Tfus	191.91	K	ChemSep v8.3 pure component data Compiled value
Tfus	191.80	K	KDB
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	Outlier 185.00 ± 1.50	K	NIST
Tfus	Outlier 185.00 ± 5.00	K	NIST
Ttriple	[191.60; 191.91]	K
Ttriple	191.91	K	ChemSep v8.3 pure component data Compiled value
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
UQi	5.26		ChemSep v8.3 pure component data Compiled value
URi	6.29		ChemSep v8.3 pure component data Compiled value
Vc	[0.525; 0.526]	m3/kmol
Vc	0.526	m3/kmol	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 6 Compiled value
Vc	0.525	m3/kmol	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Vc	0.526	m3/kmol	ChemSep v8.3 pure component data Compiled value
Vc	0.526	m3/kmol	KDB
Vc	0.526	m3/kmol	NIST
VCOSTALD	0.53	m3/kmol	Hankinson and Thomson (1979), COSTALD parameters Compiled value
ωSRK	0.43		Hankinson and Thomson (1979), COSTALD parameters Compiled value
Zc	[0.2480000; 0.2492170]
Zc	0.2480000		ChemSep v8.3 pure component data Compiled value
Zc	0.2492170		KDB
Zra	[0.25; 0.25]
Zra	0.25		Hankinson and Thomson (1979), COSTALD parameters Compiled value
Zra	0.25		ChemSep v8.3 pure component data Compiled value
Zra	0.25		KDB

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	270.36	J/mol×K	298.15	NIST
Csat	[243.10; 308.40]	J/mol×K	[200.00; 380.00]
Csat	243.10	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	243.50	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	244.70	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	246.50	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	248.90	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	251.90	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	255.20	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	258.90	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	260.10	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	262.90	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	267.00	J/mol×K	290.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Csat	270.50	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	271.30	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
Csat	275.70	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
Csat	280.20	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
Csat	284.80	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
Csat	289.40	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
Csat	294.10	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
Csat	298.90	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
Csat	303.60	J/mol×K	370.00	Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Csat	308.40	J/mol×K	380.00	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	[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	[36.32; 42.00]	kJ/mol	[381.00; 420.00]
ΔvapH	42.00	kJ/mol	381.00	NIST
ΔvapH	36.32	kJ/mol	420.00	KDB
n0	1.41333		298.15	KDB
ρl	745.00	kg/m3	273.00	KDB
γ	0.02	N/m	298.20	KDB

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[150.27; 528.18]	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			1.22350e+02
Coefficient B			-6.22400e+02
Coefficient C			6.44424e+00
Coefficient D			-1.52360e-05
Coefficient E			-2.31690e-10
Temperature range, min.			200.00
Temperature range, max.			1500.00
Cp,gas	150.27	J/mol×K	200.00	Calculated Property
Cp,gas	225.07	J/mol×K	344.44	Calculated Property
Cp,gas	297.15	J/mol×K	488.89	Calculated Property
Cp,gas	355.52	J/mol×K	633.33	Calculated Property
Cp,gas	401.58	J/mol×K	777.78	Calculated Property
Cp,gas	438.15	J/mol×K	922.22	Calculated Property
Cp,gas	467.59	J/mol×K	1066.67	Calculated Property
Cp,gas	491.63	J/mol×K	1211.11	Calculated Property
Cp,gas	511.52	J/mol×K	1355.56	Calculated Property
Cp,gas	528.18	J/mol×K	1500.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[241.66; 367.10]	J/mol×K	[191.91; 475.00]	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			5.83090e+01
Coefficient B			1.19150e+02
Coefficient C			3.84224e+00
Coefficient D			4.20250e-03
Coefficient E			-1.58050e-06
Temperature range, min.			191.91
Temperature range, max.			475.00
Cp,liquid	241.66	J/mol×K	191.91	Calculated Property
Cp,liquid	246.13	J/mol×K	223.36	Calculated Property
Cp,liquid	254.30	J/mol×K	254.82	Calculated Property
Cp,liquid	265.16	J/mol×K	286.27	Calculated Property
Cp,liquid	278.16	J/mol×K	317.73	Calculated Property
Cp,liquid	292.98	J/mol×K	349.18	Calculated Property
Cp,liquid	309.42	J/mol×K	380.64	Calculated Property
Cp,liquid	327.33	J/mol×K	412.09	Calculated Property
Cp,liquid	346.59	J/mol×K	443.55	Calculated Property
Cp,liquid	367.10	J/mol×K	475.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.0043714; 0.0002047]	Pa×s	[191.91; 420.02]	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			-1.02960e+01
Coefficient B			1.05730e+03
Coefficient C			-1.24310e-01
Coefficient D			2.02810e-07
Coefficient E			2.00000e+00
Temperature range, min.			191.91
Temperature range, max.			420.02
η	0.0043714	Pa×s	191.91	Calculated Property
η	0.0022683	Pa×s	217.26	Calculated Property
η	0.0013488	Pa×s	242.60	Calculated Property
η	0.0008845	Pa×s	267.95	Calculated Property
η	0.0006237	Pa×s	293.29	Calculated Property
η	0.0004649	Pa×s	318.64	Calculated Property
η	0.0003618	Pa×s	343.98	Calculated Property
η	0.0002915	Pa×s	369.33	Calculated Property
η	0.0002415	Pa×s	394.67	Calculated Property
η	0.0002047	Pa×s	420.02	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ΔvapH	[50.87; 5.65]	kJ/mol	[191.91; 593.10]	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			5.07290e+01
Coefficient B			-7.20170e-01
Coefficient C			3.22760e+00
Coefficient D			-3.63470e+00
Coefficient E			1.46590e+00
Critical temperature, Tc (K)			5.94000e+02
Temperature range, min.			191.91
Temperature range, max.			593.10
ΔvapH	50.87	kJ/mol	191.91	Calculated Property
ΔvapH	48.68	kJ/mol	236.49	Calculated Property
ΔvapH	46.12	kJ/mol	281.06	Calculated Property
ΔvapH	43.33	kJ/mol	325.64	Calculated Property
ΔvapH	40.35	kJ/mol	370.22	Calculated Property
ΔvapH	37.13	kJ/mol	414.79	Calculated Property
ΔvapH	33.47	kJ/mol	459.37	Calculated Property
ΔvapH	28.96	kJ/mol	503.95	Calculated Property
ΔvapH	22.57	kJ/mol	548.52	Calculated Property
ΔvapH	5.65	kJ/mol	593.10	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.63]	kPa	[307.75; 446.60]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
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	[6.59e-06; 2443.07]	kPa	[191.91; 593.10]	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			1.13462e+02
Coefficient B			-9.41870e+03
Coefficient C			-1.45830e+01
Coefficient D			9.48630e-06
Coefficient E			2.00000e+00
Temperature range, min.			191.91
Temperature range, max.			593.10
Pvap	6.59e-06	kPa	191.91	Calculated Property
Pvap	3.91e-03	kPa	236.49	Calculated Property
Pvap	0.22	kPa	281.06	Calculated Property
Pvap	3.22	kPa	325.64	Calculated Property
Pvap	21.68	kPa	370.22	Calculated Property
Pvap	88.62	kPa	414.79	Calculated Property
Pvap	262.13	kPa	459.37	Calculated Property
Pvap	625.93	kPa	503.95	Calculated Property
Pvap	1296.11	kPa	548.52	Calculated Property
Pvap	2443.07	kPa	593.10	Calculated Property
Pvap	[8.72e-06; 2337.64]	kPa	[191.78; 593.25]	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			1.06010e+02
Coefficient B			-9.03620e+03
Coefficient C			-1.34814e+01
Coefficient D			8.71053e-06
Coefficient E			0.00000e+00
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
Pvap	[6.38; 104.03]	kPa	[339.76; 421.01]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.39969e+01
Coefficient B			-3.30504e+03
Coefficient C			-6.76150e+01
Reference			Forziati, Camin, et al., 1950
Temperature range, min.			339.76
Temperature range, max.			421.01
Pvap	6.38	kPa	339.76	Calculated Property
Pvap	9.42	kPa	348.79	Calculated Property
Pvap	13.57	kPa	357.82	Calculated Property
Pvap	19.14	kPa	366.84	Calculated Property
Pvap	26.45	kPa	375.87	Calculated Property
Pvap	35.88	kPa	384.90	Calculated Property
Pvap	47.87	kPa	393.93	Calculated Property
Pvap	62.87	kPa	402.95	Calculated Property
Pvap	81.41	kPa	411.98	Calculated Property
Pvap	104.03	kPa	421.01	Calculated Property
Pvap	[6.38; 104.03]	kPa	[339.76; 421.01]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.39969e+01
Coefficient B			-3.30504e+03
Coefficient C			-6.76150e+01
Reference			Forziati, Camin, et al., 1950, 2
Temperature range, min.			339.76
Temperature range, max.			421.01
Pvap	6.38	kPa	339.76	Calculated Property
Pvap	9.42	kPa	348.79	Calculated Property
Pvap	13.57	kPa	357.82	Calculated Property
Pvap	19.14	kPa	366.84	Calculated Property
Pvap	26.45	kPa	375.87	Calculated Property
Pvap	35.88	kPa	384.90	Calculated Property
Pvap	47.87	kPa	393.93	Calculated Property
Pvap	62.87	kPa	402.95	Calculated Property
Pvap	81.41	kPa	411.98	Calculated Property
Pvap	104.03	kPa	421.01	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ρl	[800.51; 247.23]	kg/m3	[191.91; 593.10]	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			2.28013e+01
Coefficient B			1.58020e-01
Coefficient C			5.94000e+02
Coefficient D			1.89690e-01
Temperature range, min.			191.91
Temperature range, max.			593.10
ρl	800.51	kg/m3	191.91	Calculated Property
ρl	770.84	kg/m3	236.49	Calculated Property
ρl	739.29	kg/m3	281.06	Calculated Property
ρl	705.39	kg/m3	325.64	Calculated Property
ρl	668.47	kg/m3	370.22	Calculated Property
ρl	627.50	kg/m3	414.79	Calculated Property
ρl	580.63	kg/m3	459.37	Calculated Property
ρl	524.20	kg/m3	503.95	Calculated Property
ρl	448.12	kg/m3	548.52	Calculated Property
ρl	247.23	kg/m3	593.10	Calculated Property

Property	Value	Unit	Temperature (K)	Source
γ	[0.03; 0.01]	N/m	[192.15; 419.15]	Jasper (1972), surface tension of pure liquid compounds Compiled value
Equation			Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is γ in N/m, T in K
Coefficient A			5.05215e-02
Coefficient B			-9.38000e-05
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Temperature range, min.			192.15
Temperature range, max.			419.15
γ	0.03	N/m	192.15	Calculated Property
γ	0.03	N/m	217.37	Calculated Property
γ	0.03	N/m	242.59	Calculated Property
γ	0.03	N/m	267.82	Calculated Property
γ	0.02	N/m	293.04	Calculated Property
γ	0.02	N/m	318.26	Calculated Property
γ	0.02	N/m	343.48	Calculated Property
γ	0.02	N/m	368.71	Calculated Property
γ	0.01	N/m	393.93	Calculated Property
γ	0.01	N/m	419.15	Calculated Property
γ	[0.03; 8.54e-06]	N/m	[191.91; 584.68]	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			-1.37850e-01
Coefficient B			-6.52270e+00
Coefficient C			-1.55570e+00
Coefficient D			-9.83370e-04
Coefficient E			4.68870e-07
Comment			Range stopped where the equation turns negative; ChemSep gives it to 593.1 K.
Temperature range, min.			191.91
Temperature range, max.			584.68
γ	0.03	N/m	191.91	Calculated Property
γ	0.03	N/m	235.55	Calculated Property
γ	0.02	N/m	279.19	Calculated Property
γ	0.02	N/m	322.83	Calculated Property
γ	0.02	N/m	366.47	Calculated Property
γ	0.01	N/m	410.11	Calculated Property
γ	0.01	N/m	453.75	Calculated Property
γ	0.01	N/m	497.39	Calculated Property
γ	0.00	N/m	541.03	Calculated Property
γ	8.54e-06	N/m	584.68	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λgas	[0.00; 0.10]	W/m×K	[191.91; 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			1.97610e-05
Coefficient B			1.29830e+00
Coefficient C			5.63960e+02
Coefficient D			2.48290e+04
Temperature range, min.			191.91
Temperature range, max.			1000.00
λgas	0.00	W/m×K	191.91	Calculated Property
λgas	0.01	W/m×K	281.70	Calculated Property
λgas	0.02	W/m×K	371.49	Calculated Property
λgas	0.02	W/m×K	461.27	Calculated Property
λgas	0.03	W/m×K	551.06	Calculated Property
λgas	0.04	W/m×K	640.85	Calculated Property
λgas	0.06	W/m×K	730.64	Calculated Property
λgas	0.07	W/m×K	820.42	Calculated Property
λgas	0.08	W/m×K	910.21	Calculated Property
λgas	0.10	W/m×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λliquid	[0.16; 0.07]	W/m×K	[191.91; 533.15]	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			2.46020e-02
Coefficient B			-1.18290e+02
Coefficient C			-4.09460e-01
Coefficient D			-5.61360e-03
Coefficient E			2.19090e-06
Temperature range, min.			191.91
Temperature range, max.			533.15
λliquid	0.16	W/m×K	191.91	Calculated Property
λliquid	0.15	W/m×K	229.83	Calculated Property
λliquid	0.14	W/m×K	267.74	Calculated Property
λliquid	0.12	W/m×K	305.66	Calculated Property
λliquid	0.11	W/m×K	343.57	Calculated Property
λliquid	0.10	W/m×K	381.49	Calculated Property
λliquid	0.09	W/m×K	419.40	Calculated Property
λliquid	0.09	W/m×K	457.32	Calculated Property
λliquid	0.08	W/m×K	495.23	Calculated Property
λliquid	0.07	W/m×K	533.15	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
• 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
• 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
• 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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