Chemical Properties of 1-Dodecene (CAS 112-41-4)

InChI

InChI=1S/C12H24/c1-3-5-7-9-11-12-10-8-6-4-2/h3H,1,4-12H2,2H3

InChI Key

CRSBERNSMYQZNG-UHFFFAOYSA-N

Formula

C12H24

SMILES

C=CCCCCCCCCCC

Molecular Weight¹

168.32

CAS

112-41-4

Other Names

• Adacene 12
• Dodec-1-ene
• Dodecene-1
• Dodecylene «alpha»-
• NSC 12016
• Neodene 12
• n-Dodec-1-ene
• «alpha»-Dodecene
• «alpha»-Dodecylene

• ω : Acentric Factor.
• 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).
• 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_triple : Triple Point Pressure (kPa).
• P_vap : Vapor pressure (kPa).
• 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).
• Z_c : Critical Compressibility.
• ¹: Molecular weight from the IUPAC atomic weights tables.

Physical Properties

Property	Value	Unit	Source
ω	[0.5192; 0.5620]
ω	0.5192		PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
ω	0.5575		Passut and Danner (1973), critical constants and acentric factors Compiled value
ω	0.5620		ChemSep v8.3 pure component data Compiled value
ω	0.5580		KDB
ΔcH°liquid	-7925.90 ± 1.30	kJ/mol	NIST
μ	0.52	debye	ChemSep v8.3 pure component data Compiled value
ΔfG°	[136.10; 138.00]	kJ/mol
ΔfG°	136.10	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfG°	138.00	kJ/mol	KDB
ΔfH°gas	[-165.50; -165.20]	kJ/mol
ΔfH°gas	-165.40	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfH°gas	-165.50	kJ/mol	KDB
ΔfH°gas	-165.40 ± 2.10	kJ/mol	NIST
ΔfH°gas	-165.20	kJ/mol	NIST
ΔfH°liquid	-226.20 ± 2.10	kJ/mol	NIST
ΔfusH°	25.56	kJ/mol	Joback Calculated Property
ΔvapH°	[60.30; 60.80]	kJ/mol
ΔvapH°	60.78	kJ/mol	NIST
ΔvapH°	60.78 ± 0.20	kJ/mol	NIST
ΔvapH°	60.78 ± 0.29	kJ/mol	NIST
ΔvapH°	60.80 ± 0.30	kJ/mol	NIST
ΔvapH°	60.30	kJ/mol	NIST
IE	9.40	eV	Relay (1.0) Calculated Property
log10WS	-6.10		Relay (1.0) Calculated Property
logPoct/wat	4.703		Crippen Calculated Property
McVol	175.640	ml/mol	McGowan Calculated Property
NFPA Fire	1		KDB
Pc	[1854.25; 1930.00]	kPa
Pc	1930.00	kPa	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 6 Compiled value
Pc	1854.25	kPa	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Pc	1854.69	kPa	Passut and Danner (1973), critical constants and acentric factors Compiled value
Pc	1888.00	kPa	ChemSep v8.3 pure component data Compiled value
Pc	1930.00	kPa	KDB
Pc	1930.00 ± 200.00	kPa	NIST
Ptriple	5.00e-05	kPa	ChemSep v8.3 pure component data Compiled value
Inp	[199.30; 1200.00]
Inp	1183.00		NIST
Inp	1188.00		NIST
Inp	1189.00		NIST
Inp	1189.00		NIST
Inp	1190.00		NIST
Inp	1189.00		NIST
Inp	1187.90		NIST
Inp	1190.00		NIST
Inp	1194.00		NIST
Inp	1183.00		NIST
Inp	1183.00		NIST
Inp	1184.00		NIST
Inp	1182.00		NIST
Inp	1190.10		NIST
Inp	1183.00		NIST
Inp	1183.40		NIST
Inp	1183.80		NIST
Inp	1182.50		NIST
Inp	1189.00		NIST
Inp	1192.20		NIST
Inp	1193.00		NIST
Inp	1192.00		NIST
Inp	1193.00		NIST
Inp	1187.00		NIST
Inp	1191.30		NIST
Inp	1191.30		NIST
Inp	1191.30		NIST
Inp	1186.00		NIST
Inp	1195.00		NIST
Inp	1187.00		NIST
Inp	1191.30		NIST
Inp	1191.30		NIST
Inp	1191.30		NIST
Inp	1188.00		NIST
Inp	1188.76		NIST
Inp	1188.93		NIST
Inp	1189.04		NIST
Inp	1191.75		NIST
Inp	1191.82		NIST
Inp	1192.15		NIST
Inp	1189.00		NIST
Inp	1190.00		NIST
Inp	1192.00		NIST
Inp	1193.00		NIST
Inp	1188.00		NIST
Inp	1192.00		NIST
Inp	1189.00		NIST
Inp	1187.00		NIST
Inp	1191.00		NIST
Inp	1180.00		NIST
Inp	1192.00		NIST
Inp	1189.10		NIST
Inp	1189.00		NIST
Inp	1187.00		NIST
Inp	1189.00		NIST
Inp	1188.00		NIST
Inp	1197.00		NIST
Inp	1200.00		NIST
Inp	1188.00		NIST
Inp	1188.00		NIST
Inp	1186.00		NIST
Inp	1199.00		NIST
Inp	1183.00		NIST
Inp	1185.00		NIST
Inp	1192.00		NIST
Inp	1189.00		NIST
Inp	1190.00		NIST
Inp	1182.00		NIST
Inp	Outlier 199.30		NIST
Inp	Outlier 200.90		NIST
Inp	1199.00		NIST
Inp	1190.00		NIST
Inp	1192.20		NIST
Inp	Outlier 199.30		NIST
Ip	[1231.60; 1255.00]
Ip	1238.40		NIST
Ip	1240.60		NIST
Ip	1241.90		NIST
Ip	1236.00		NIST
Ip	1242.00		NIST
Ip	1242.00		NIST
Ip	1243.00		NIST
Ip	1236.00		NIST
Ip	1242.00		NIST
Ip	1243.00		NIST
Ip	1244.00		NIST
Ip	1237.00		NIST
Ip	1243.00		NIST
Ip	1243.00		NIST
Ip	1251.00		NIST
Ip	1252.00		NIST
Ip	1252.00		NIST
Ip	1253.00		NIST
Ip	1254.00		NIST
Ip	1246.00		NIST
Ip	1246.00		NIST
Ip	1247.00		NIST
Ip	1247.00		NIST
Ip	1249.00		NIST
Ip	1245.00		NIST
Ip	1235.10		NIST
Ip	1242.90		NIST
Ip	1236.30		NIST
Ip	1243.60		NIST
Ip	1231.60		NIST
Ip	1235.70		NIST
Ip	1241.90		NIST
Ip	1242.10		NIST
Ip	1232.20		NIST
Ip	1236.30		NIST
Ip	1242.50		NIST
Ip	1242.60		NIST
Ip	1251.00		NIST
Ip	1252.00		NIST
Ip	1253.00		NIST
Ip	1254.00		NIST
Ip	1252.80		NIST
Ip	1254.90		NIST
Ip	1252.80		NIST
Ip	1254.90		NIST
Ip	1246.00		NIST
Ip	1233.00		NIST
Ip	1233.00		NIST
Ip	1234.00		NIST
Ip	1244.20		NIST
Ip	1245.10		NIST
Ip	1245.90		NIST
Ip	1243.70		NIST
Ip	1244.00		NIST
Ip	1236.00		NIST
Ip	1236.00		NIST
Ip	1235.00		NIST
Ip	1242.00		NIST
Ip	1243.00		NIST
Ip	1234.00		NIST
Ip	1232.00		NIST
Ip	1255.00		NIST
Ip	1240.00		NIST
Ip	1241.00		NIST
Ip	1244.00		NIST
Ip	1245.00		NIST
Ip	1246.00		NIST
Ip	1235.00		NIST
Ip	1233.00		NIST
Ip	1245.90		NIST
Ip	1255.00		NIST
Ip	1246.00		NIST
S°liquid	484.80	J/mol×K	NIST
Tboil	[486.00; 486.90]	K
Tboil	486.15	K	ChemSep v8.3 pure component data Compiled value
Tboil	486.90	K	KDB
Tboil	486.00	K	NIST
Tboil	486.70	K	NIST
Tboil	486.00 ± 4.00	K	NIST
Tboil	486.00 ± 2.00	K	NIST
Tboil	486.55 ± 0.40	K	NIST
Tboil	486.00 ± 4.00	K	NIST
Tc	[657.00; 658.00]	K
Tc	658.00	K	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 6 Compiled value
Tc	657.00	K	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Tc	657.04	K	Passut and Danner (1973), critical constants and acentric factors Compiled value
Tc	657.10	K	ChemSep v8.3 pure component data Compiled value
Tc	658.00	K	KDB
Tc	658.00 ± 2.00	K	NIST
Tfus	[237.75; 239.60]	K
Tfus	237.95	K	Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
Tfus	237.95	K	ChemSep v8.3 pure component data Compiled value
Tfus	237.90	K	KDB
Tfus	237.75 ± 0.50	K	NIST
Tfus	237.88 ± 0.06	K	NIST
Tfus	237.89 ± 0.04	K	NIST
Tfus	237.92 ± 0.03	K	NIST
Tfus	237.92 ± 0.04	K	NIST
Tfus	237.80 ± 0.20	K	NIST
Tfus	237.89 ± 0.05	K	NIST
Tfus	237.92 ± 0.03	K	NIST
Tfus	Outlier 239.60 ± 0.50	K	NIST
Tfus	Outlier 239.60 ± 2.00	K	NIST
Ttriple	[237.93; 237.95]	K
Ttriple	237.95	K	ChemSep v8.3 pure component data Compiled value
Ttriple	237.93	K	KDB
Ttriple	237.93 ± 0.05	K	NIST
Ttriple	237.93 ± 0.05	K	NIST
UQi	6.88		ChemSep v8.3 pure component data Compiled value
URi	8.32		ChemSep v8.3 pure component data Compiled value
Vc	[0.681; 0.725]	m3/kmol
Vc	0.681	m3/kmol	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Vc	0.725	m3/kmol	ChemSep v8.3 pure component data Compiled value
Vc	0.689	m3/kmol	KDB
Zc	[0.2428840; 0.2510000]
Zc	0.2510000		ChemSep v8.3 pure component data Compiled value
Zc	0.2428840		KDB

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	360.66	J/mol×K	298.15	NIST
Csat	[341.60; 366.60]	J/mol×K	[240.00; 310.00]
Csat	341.60	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	341.90	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	344.00	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	347.30	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	348.60	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	351.60	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	356.50	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	360.70	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	361.70	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	366.60	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
ΔfusH	[4.55; 19.87]	kJ/mol	[212.90; 237.90]
ΔfusH	4.55	kJ/mol	212.90	NIST
ΔfusH	19.87	kJ/mol	237.90	NIST
ΔfusH	19.87	kJ/mol	237.90	NIST
ΔvapH	[42.97; 51.10]	kJ/mol	[444.50; 486.50]
ΔvapH	51.10	kJ/mol	444.50	NIST
ΔvapH	42.97	kJ/mol	486.50	KDB
Pvap	[21.70; 100.70]	kPa	[430.38; 484.11]
Pvap	21.70	kPa	430.38	Isobaric vapor-liquid equilibrium for binary systems containing benzothiophene
Pvap	33.60	kPa	443.18	Isobaric vapor-liquid equilibrium for binary systems containing benzothiophene
Pvap	44.00	kPa	453.99	Isobaric vapor-liquid equilibrium for binary systems containing benzothiophene
Pvap	52.60	kPa	459.86	Isobaric vapor-liquid equilibrium for binary systems containing benzothiophene
Pvap	61.60	kPa	464.81	Isobaric vapor-liquid equilibrium for binary systems containing benzothiophene
Pvap	70.70	kPa	470.91	Isobaric vapor-liquid equilibrium for binary systems containing benzothiophene
Pvap	80.80	kPa	476.45	Isobaric vapor-liquid equilibrium for binary systems containing benzothiophene
Pvap	90.20	kPa	480.78	Isobaric vapor-liquid equilibrium for binary systems containing benzothiophene
Pvap	100.70	kPa	484.11	Isobaric vapor-liquid equilibrium for binary systems containing benzothiophene
ρl	758.00	kg/m3	293.00	KDB
ΔfusS	[21.38; 83.54]	J/mol×K	[212.90; 237.90]
ΔfusS	21.38	J/mol×K	212.90	NIST
ΔfusS	83.54	J/mol×K	237.90	NIST
γ	0.03	N/m	298.20	KDB

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[227.56; 697.19]	J/mol×K	[237.95; 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			1.58385e+02
Coefficient B			-5.80709e+02
Coefficient C			6.66830e+00
Coefficient D			4.29289e-05
Coefficient E			-2.49786e-08
Temperature range, min.			237.95
Temperature range, max.			1500.00
Cp,gas	227.56	J/mol×K	237.95	Calculated Property
Cp,gas	330.03	J/mol×K	378.18	Calculated Property
Cp,gas	419.16	J/mol×K	518.41	Calculated Property
Cp,gas	490.03	J/mol×K	658.63	Calculated Property
Cp,gas	545.89	J/mol×K	798.86	Calculated Property
Cp,gas	590.29	J/mol×K	939.09	Calculated Property
Cp,gas	625.94	J/mol×K	1079.32	Calculated Property
Cp,gas	654.76	J/mol×K	1219.54	Calculated Property
Cp,gas	678.18	J/mol×K	1359.77	Calculated Property
Cp,gas	697.19	J/mol×K	1500.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[340.86; 553.45]	J/mol×K	[237.95; 526.00]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is Cp,liquid in J/mol×K, T in K
Coefficient A			1.13120e+03
Coefficient B			-9.23870e+00
Coefficient C			3.80190e-02
Coefficient D			-6.55230e-05
Coefficient E			4.30900e-08
Temperature range, min.			237.95
Temperature range, max.			526.00
Cp,liquid	340.86	J/mol×K	237.95	Calculated Property
Cp,liquid	347.63	J/mol×K	269.96	Calculated Property
Cp,liquid	362.27	J/mol×K	301.96	Calculated Property
Cp,liquid	381.58	J/mol×K	333.97	Calculated Property
Cp,liquid	403.45	J/mol×K	365.97	Calculated Property
Cp,liquid	426.87	J/mol×K	397.98	Calculated Property
Cp,liquid	451.88	J/mol×K	429.98	Calculated Property
Cp,liquid	479.65	J/mol×K	461.99	Calculated Property
Cp,liquid	512.40	J/mol×K	493.99	Calculated Property
Cp,liquid	553.45	J/mol×K	526.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.0043699; 0.0001579]	Pa×s	[237.90; 525.68]	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			-1.14990e+01
Coefficient B			1.44310e+03
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Temperature range, min.			237.90
Temperature range, max.			525.68
η	0.0043699	Pa×s	237.90	Calculated Property
η	0.0021298	Pa×s	269.88	Calculated Property
η	0.0012088	Pa×s	301.85	Calculated Property
η	0.0007646	Pa×s	333.83	Calculated Property
η	0.0005240	Pa×s	365.80	Calculated Property
η	0.0003816	Pa×s	397.78	Calculated Property
η	0.0002913	Pa×s	429.75	Calculated Property
η	0.0002309	Pa×s	461.73	Calculated Property
η	0.0001886	Pa×s	493.70	Calculated Property
η	0.0001579	Pa×s	525.68	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ΔvapH	[62.48; 0.00]	kJ/mol	[237.95; 657.10]	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			7.93930e+01
Coefficient B			6.72880e-01
Coefficient C			-4.49720e-01
Coefficient D			1.73220e-01
Coefficient E			1.00000e-03
Critical temperature, Tc (K)			6.57100e+02
Temperature range, min.			237.95
Temperature range, max.			657.10
ΔvapH	62.48	kJ/mol	237.95	Calculated Property
ΔvapH	59.42	kJ/mol	284.52	Calculated Property
ΔvapH	56.30	kJ/mol	331.09	Calculated Property
ΔvapH	53.04	kJ/mol	377.67	Calculated Property
ΔvapH	49.52	kJ/mol	424.24	Calculated Property
ΔvapH	45.60	kJ/mol	470.81	Calculated Property
ΔvapH	41.01	kJ/mol	517.38	Calculated Property
ΔvapH	35.28	kJ/mol	563.96	Calculated Property
ΔvapH	27.15	kJ/mol	610.53	Calculated Property
ΔvapH	0.00	kJ/mol	657.10	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.64]	kPa	[361.38; 516.86]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.47045e+01
Coefficient B			-4.19102e+03
Coefficient C			-7.06790e+01
Temperature range, min.			361.38
Temperature range, max.			516.86
Pvap	1.33	kPa	361.38	Calculated Property
Pvap	2.99	kPa	378.66	Calculated Property
Pvap	6.17	kPa	395.93	Calculated Property
Pvap	11.81	kPa	413.21	Calculated Property
Pvap	21.25	kPa	430.48	Calculated Property
Pvap	36.24	kPa	447.76	Calculated Property
Pvap	58.97	kPa	465.03	Calculated Property
Pvap	92.11	kPa	482.31	Calculated Property
Pvap	138.81	kPa	499.58	Calculated Property
Pvap	202.64	kPa	516.86	Calculated Property
Pvap	[5.00e-05; 1889.38]	kPa	[237.95; 657.10]	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			7.51142e+01
Coefficient B			-9.48560e+03
Coefficient C			-8.25170e+00
Coefficient D			4.98130e-18
Coefficient E			6.00000e+00
Temperature range, min.			237.95
Temperature range, max.			657.10
Pvap	5.00e-05	kPa	237.95	Calculated Property
Pvap	7.82e-03	kPa	284.52	Calculated Property
Pvap	0.24	kPa	331.09	Calculated Property
Pvap	2.85	kPa	377.67	Calculated Property
Pvap	17.44	kPa	424.24	Calculated Property
Pvap	69.16	kPa	470.81	Calculated Property
Pvap	202.94	kPa	517.38	Calculated Property
Pvap	483.19	kPa	563.96	Calculated Property
Pvap	998.67	kPa	610.53	Calculated Property
Pvap	1889.38	kPa	657.10	Calculated Property
Pvap	[3.08e-05; 1822.45]	kPa	[237.93; 657.00]	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			1.28985e+02
Coefficient B			-1.18314e+04
Coefficient C			-1.64625e+01
Coefficient D			7.72637e-06
Coefficient E			0.00000e+00
Temperature range, min.			237.93
Temperature range, max.			657.00
Pvap	3.08e-05	kPa	237.93	Calculated Property
Pvap	6.72e-03	kPa	284.49	Calculated Property
Pvap	0.24	kPa	331.06	Calculated Property
Pvap	2.91	kPa	377.62	Calculated Property
Pvap	17.85	kPa	424.18	Calculated Property
Pvap	69.97	kPa	470.75	Calculated Property
Pvap	202.95	kPa	517.31	Calculated Property
Pvap	479.00	kPa	563.87	Calculated Property
Pvap	980.89	kPa	610.44	Calculated Property
Pvap	1822.45	kPa	657.00	Calculated Property
Pvap	[6.38; 104.04]	kPa	[396.80; 487.62]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.40460e+01
Coefficient B			-3.72987e+03
Coefficient C			-9.08790e+01
Reference			Forziati, Camin, et al., 1950, 2
Temperature range, min.			396.80
Temperature range, max.			487.62
Pvap	6.38	kPa	396.80	Calculated Property
Pvap	9.42	kPa	406.89	Calculated Property
Pvap	13.58	kPa	416.98	Calculated Property
Pvap	19.14	kPa	427.07	Calculated Property
Pvap	26.44	kPa	437.16	Calculated Property
Pvap	35.87	kPa	447.26	Calculated Property
Pvap	47.85	kPa	457.35	Calculated Property
Pvap	62.86	kPa	467.44	Calculated Property
Pvap	81.40	kPa	477.53	Calculated Property
Pvap	104.04	kPa	487.62	Calculated Property
Pvap	[6.38; 104.04]	kPa	[396.80; 487.62]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.40460e+01
Coefficient B			-3.72987e+03
Coefficient C			-9.08790e+01
Reference			Forziati, Camin, et al., 1950
Temperature range, min.			396.80
Temperature range, max.			487.62
Pvap	6.38	kPa	396.80	Calculated Property
Pvap	9.42	kPa	406.89	Calculated Property
Pvap	13.58	kPa	416.98	Calculated Property
Pvap	19.14	kPa	427.07	Calculated Property
Pvap	26.44	kPa	437.16	Calculated Property
Pvap	35.87	kPa	447.26	Calculated Property
Pvap	47.85	kPa	457.35	Calculated Property
Pvap	62.86	kPa	467.44	Calculated Property
Pvap	81.40	kPa	477.53	Calculated Property
Pvap	104.04	kPa	487.62	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ρl	[796.94; 232.16]	kg/m3	[237.95; 657.10]	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			5.71106e+01
Coefficient B			2.46000e-01
Coefficient C			6.57100e+02
Coefficient D			2.85710e-01
Temperature range, min.			237.95
Temperature range, max.			657.10
ρl	796.94	kg/m3	237.95	Calculated Property
ρl	765.07	kg/m3	284.52	Calculated Property
ρl	731.66	kg/m3	331.09	Calculated Property
ρl	696.36	kg/m3	377.67	Calculated Property
ρl	658.59	kg/m3	424.24	Calculated Property
ρl	617.52	kg/m3	470.81	Calculated Property
ρl	571.64	kg/m3	517.38	Calculated Property
ρl	517.98	kg/m3	563.96	Calculated Property
ρl	448.43	kg/m3	610.53	Calculated Property
ρl	232.16	kg/m3	657.10	Calculated Property

Property	Value	Unit	Temperature (K)	Source
γ	[0.03; 0.00]	N/m	[237.95; 657.10]	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 γ in N/m, T in K
Coefficient A			5.50160e-02
Coefficient B			1.29180e+00
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			1.00000e-07
Critical temperature, Tc (K)			6.57100e+02
Temperature range, min.			237.95
Temperature range, max.			657.10
γ	0.03	N/m	237.95	Calculated Property
γ	0.03	N/m	284.52	Calculated Property
γ	0.02	N/m	331.09	Calculated Property
γ	0.02	N/m	377.67	Calculated Property
γ	0.01	N/m	424.24	Calculated Property
γ	0.01	N/m	470.81	Calculated Property
γ	0.01	N/m	517.38	Calculated Property
γ	0.00	N/m	563.96	Calculated Property
γ	0.00	N/m	610.53	Calculated Property
γ	0.00	N/m	657.10	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λgas	[0.02; 0.08]	W/m×K	[486.15; 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			4.44880e-05
Coefficient B			1.18550e+00
Coefficient C			8.61360e+02
Coefficient D			7.30930e+04
Temperature range, min.			486.15
Temperature range, max.			1000.00
λgas	0.02	W/m×K	486.15	Calculated Property
λgas	0.03	W/m×K	543.24	Calculated Property
λgas	0.03	W/m×K	600.34	Calculated Property
λgas	0.04	W/m×K	657.43	Calculated Property
λgas	0.05	W/m×K	714.53	Calculated Property
λgas	0.05	W/m×K	771.62	Calculated Property
λgas	0.06	W/m×K	828.72	Calculated Property
λgas	0.07	W/m×K	885.81	Calculated Property
λgas	0.07	W/m×K	942.91	Calculated Property
λgas	0.08	W/m×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λliquid	[0.15; 0.09]	W/m×K	[237.95; 486.15]	ChemSep v8.3 pure component data Compiled value
Equation			Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is λliquid in W/m×K, T in K
Coefficient A			1.98380e-01
Coefficient B			-2.13000e-04
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Temperature range, min.			237.95
Temperature range, max.			486.15
λliquid	0.15	W/m×K	237.95	Calculated Property
λliquid	0.14	W/m×K	265.53	Calculated Property
λliquid	0.14	W/m×K	293.11	Calculated Property
λliquid	0.13	W/m×K	320.68	Calculated Property
λliquid	0.12	W/m×K	348.26	Calculated Property
λliquid	0.12	W/m×K	375.84	Calculated Property
λliquid	0.11	W/m×K	403.42	Calculated Property
λliquid	0.11	W/m×K	430.99	Calculated Property
λliquid	0.10	W/m×K	458.57	Calculated Property
λliquid	0.09	W/m×K	486.15	Calculated Property

Similar Compounds

Find more compounds similar to 1-Dodecene.

Mixtures

• Benzo[b]thiophene + 1-Dodecene
• Formamide, N,N-dimethyl- + 1-Dodecene
• 1,3-Dioxolan-2-one, 4-methyl- + 1-Dodecene

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).
• 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.
• 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.
• Cheméo Relay (1.0)
• 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
• Crippen Method
• Infinite dilution activity coefficients, specific retention volumes and solvation thermodynamics of hydrocarbons in C78H158 branched alkane solvent
• Isobaric vapor-liquid equilibrium for binary systems containing benzothiophene
• 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
• Modeling of Liquid Liquid Interfacial Properties of Binary and Ternary Mixtures
• Joback Method
• KDB
• 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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