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»-
• Dodecylene «alpha»-
• N-DODEC-1-ENE
• NSC 12016
• Neodene 12
• «alpha»-Dodecene
• «alpha»-Dodecylene
• «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).
• 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).
• 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).
• 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.
• ¹: Molecular weight from the IUPAC atomic weights tables.

Physical Properties

Property	Value	Unit	Source
ω	0.5580		KDB
ΔcH°liquid	-7925.90 ± 1.30	kJ/mol	NIST
ΔfG°	138.00	kJ/mol	KDB
ΔfH°gas	[-165.50; -165.20]	kJ/mol
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
log10WS	-4.70		Crippen Calculated Property
logPoct/wat	4.703		Crippen Calculated Property
McVol	175.640	ml/mol	McGowan Calculated Property
NFPA Fire	1		KDB
Pc	[1930.00; 1930.00]	kPa
Pc	1930.00	kPa	KDB
Pc	1930.00 ± 200.00	kPa	NIST
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	1192.20		NIST
Inp	Outlier 199.30		NIST
Inp	1199.00		NIST
Inp	1190.00		NIST
I	[1231.60; 1255.00]
I	1238.40		NIST
I	1240.60		NIST
I	1241.90		NIST
I	1236.00		NIST
I	1242.00		NIST
I	1242.00		NIST
I	1243.00		NIST
I	1236.00		NIST
I	1242.00		NIST
I	1243.00		NIST
I	1244.00		NIST
I	1237.00		NIST
I	1243.00		NIST
I	1243.00		NIST
I	1251.00		NIST
I	1252.00		NIST
I	1252.00		NIST
I	1253.00		NIST
I	1254.00		NIST
I	1246.00		NIST
I	1246.00		NIST
I	1247.00		NIST
I	1247.00		NIST
I	1249.00		NIST
I	1245.00		NIST
I	1235.10		NIST
I	1242.90		NIST
I	1236.30		NIST
I	1243.60		NIST
I	1231.60		NIST
I	1235.70		NIST
I	1241.90		NIST
I	1242.10		NIST
I	1232.20		NIST
I	1236.30		NIST
I	1242.50		NIST
I	1242.60		NIST
I	1251.00		NIST
I	1252.00		NIST
I	1253.00		NIST
I	1254.00		NIST
I	1252.80		NIST
I	1254.90		NIST
I	1252.80		NIST
I	1254.90		NIST
I	1246.00		NIST
I	1233.00		NIST
I	1233.00		NIST
I	1234.00		NIST
I	1244.20		NIST
I	1245.10		NIST
I	1245.90		NIST
I	1243.70		NIST
I	1244.00		NIST
I	1236.00		NIST
I	1236.00		NIST
I	1235.00		NIST
I	1242.00		NIST
I	1243.00		NIST
I	1234.00		NIST
I	1232.00		NIST
I	1255.00		NIST
I	1240.00		NIST
I	1241.00		NIST
I	1244.00		NIST
I	1245.00		NIST
I	1246.00		NIST
I	1233.00		NIST
I	1245.90		NIST
I	1235.00		NIST
I	1255.00		NIST
I	1246.00		NIST
S°liquid	484.80	J/mol×K	NIST
Tboil	486.90	K	KDB
Tc	[658.00; 658.00]	K
Tc	658.00	K	KDB
Tc	658.00 ± 2.00	K	NIST
Tfus	[237.75; 239.60]	K
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; 237.93]	K
Ttriple	237.93	K	KDB
Ttriple	237.93 ± 0.05	K	NIST
Vc	0.689	m3/kmol	KDB
Zc	0.2428840		KDB

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[389.04; 477.70]	J/mol×K	[470.64; 634.56]
T(K) Ideal gas heat capacity (J/mol×K) 400 420 440 460 480 500 550 600
Cp,gas	389.04	J/mol×K	470.64	Joback Calculated Property
Cp,gas	405.36	J/mol×K	497.96	Joback Calculated Property
Cp,gas	421.03	J/mol×K	525.28	Joback Calculated Property
Cp,gas	436.09	J/mol×K	552.60	Joback Calculated Property
Cp,gas	450.54	J/mol×K	579.92	Joback Calculated Property
Cp,gas	464.40	J/mol×K	607.24	Joback Calculated Property
Cp,gas	477.70	J/mol×K	634.56	Joback Calculated Property
Cp,liquid	360.66	J/mol×K	298.15	NIST
η	[0.0002149; 0.0054785]	Pa×s	[223.24; 470.64]
T(K) Dynamic viscosity (Pa×s) 0 1.00e-3 2.00e-3 3.00e-3 4.00e-3 5.00e-3 6.00e-3 300 400
η	0.0054785	Pa×s	223.24	Joback Calculated Property
η	0.0020968	Pa×s	264.47	Joback Calculated Property
η	0.0010398	Pa×s	305.71	Joback Calculated Property
η	0.0006092	Pa×s	346.94	Joback Calculated Property
η	0.0003999	Pa×s	388.17	Joback Calculated Property
η	0.0002846	Pa×s	429.41	Joback Calculated Property
η	0.0002149	Pa×s	470.64	Joback Calculated Property
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]
T(K) Vapor pressure (kPa) 20 40 60 80 100 440 460 480
Pvap	21.70	kPa	430.38	Isobari...
Pvap	33.60	kPa	443.18	Isobari...
Pvap	44.00	kPa	453.99	Isobari...
Pvap	52.60	kPa	459.86	Isobari...
Pvap	61.60	kPa	464.81	Isobari...
Pvap	70.70	kPa	470.91	Isobari...
Pvap	80.80	kPa	476.45	Isobari...
Pvap	90.20	kPa	480.78	Isobari...
Pvap	100.70	kPa	484.11	Isobari...
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
Pvap	[1.33; 202.64]	kPa	[361.38; 516.86]	The Yaw...
Equation			ln(Pvp) = A + B/(T + C)
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
T(K) Vapor pressure (kPa) 0 50 100 150 200 400 450 500
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	[3.08e-05; 1822.45]	kPa	[237.93; 657.00]	KDB Vap...
Equation			ln(Pvp) = A + B/T + C*ln(T) + D*T^2
Coefficient A			1.28985e+02
Coefficient B			-1.18314e+04
Coefficient C			-1.64625e+01
Coefficient D			7.72637e-06
Temperature range, min.			237.93
Temperature range, max.			657.00
T(K) Vapor pressure (kPa) 0 500 1000 1500 2000 300 400 500 600
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

Similar Compounds

Find more compounds similar to 1-Dodecene.

Mixtures

• Benzo[b]thiophene + 1-Dodecene
• Formamide, N,N-dimethyl- + 1-Dodecene
• Propylene Carbonate + 1-Dodecene

Sources

• KDB Vapor Pressure Data
• 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

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Outlier This icon means that the value is more than 2 standard deviations away from the property mean.