Chemical Properties of 1-Tridecene (CAS 2437-56-1)

InChI

InChI=1S/C13H26/c1-3-5-7-9-11-13-12-10-8-6-4-2/h3H,1,4-13H2,2H3

InChI Key

VQOXUMQBYILCKR-UHFFFAOYSA-N

Formula

C13H26

SMILES

C=CCCCCCCCCCCC

Molecular Weight¹

182.35

CAS

2437-56-1

Other Names

• 1-C13H26
• Tridec-1-ene
• Tridecene-1
• n-Tridec-1-ene
• «alpha»-Tridecene

• ω : Acentric Factor.
• C_p,gas : Ideal gas 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_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_l : Liquid Density (kg/m³).
• I_np : Non-polar retention indices.
• I_p : Polar retention indices.
• γ : Surface Tension (N/m).
• T_boil : Normal Boiling Point Temperature (K).
• T_c : Critical Temperature (K).
• T_fus : Normal melting (fusion) point (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	[0.5980; 0.5981]
ω	0.5980		PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
ω	0.5981		Passut and Danner (1973), critical constants and acentric factors Compiled value
ω	0.5980		KDB
ΔfG°	146.40	kJ/mol	KDB
ΔfH°gas	-186.10	kJ/mol	KDB
ΔfusH°	28.15	kJ/mol	Joback Calculated Property
ΔvapH°	65.30	kJ/mol	NIST
IE	[9.30; 9.38]	eV
IE	9.30 ± 0.05	eV	NIST
IE	9.38	eV	NIST
log10WS	-6.39		Relay (1.0) Calculated Property
logPoct/wat	5.093		Crippen Calculated Property
McVol	189.730	ml/mol	McGowan Calculated Property
Pc	[1700.00; 1703.01]	kPa
Pc	1700.00	kPa	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Pc	1703.01	kPa	Passut and Danner (1973), critical constants and acentric factors Compiled value
Pc	1700.00	kPa	KDB
Inp	[219.50; 1295.00]
Inp	1283.00		NIST
Inp	1288.00		NIST
Inp	1289.00		NIST
Inp	1289.00		NIST
Inp	1289.00		NIST
Inp	1289.00		NIST
Inp	1290.00		NIST
Inp	1288.70		NIST
Inp	1283.00		NIST
Inp	1284.00		NIST
Inp	1284.00		NIST
Inp	1283.00		NIST
Inp	1287.00		NIST
Inp	1288.00		NIST
Inp	1289.00		NIST
Inp	1290.00		NIST
Inp	1293.00		NIST
Inp	1289.50		NIST
Inp	1292.00		NIST
Inp	1291.30		NIST
Inp	1291.90		NIST
Inp	1291.50		NIST
Inp	1291.30		NIST
Inp	1292.20		NIST
Inp	1292.00		NIST
Inp	1290.00		NIST
Inp	1287.00		NIST
Inp	1291.50		NIST
Inp	1291.30		NIST
Inp	1292.20		NIST
Inp	1291.30		NIST
Inp	1291.90		NIST
Inp	1289.00		NIST
Inp	1288.97		NIST
Inp	1289.08		NIST
Inp	1289.22		NIST
Inp	1292.10		NIST
Inp	1292.16		NIST
Inp	1292.37		NIST
Inp	1289.00		NIST
Inp	1292.00		NIST
Inp	1295.00		NIST
Inp	1293.00		NIST
Inp	1292.00		NIST
Inp	1294.00		NIST
Inp	1294.00		NIST
Inp	1292.00		NIST
Inp	1287.00		NIST
Inp	1292.00		NIST
Inp	1290.00		NIST
Inp	1284.00		NIST
Inp	1292.00		NIST
Inp	1281.00		NIST
Inp	1295.00		NIST
Inp	1289.00		NIST
Inp	1289.00		NIST
Inp	1289.00		NIST
Inp	1288.00		NIST
Inp	1283.00		NIST
Inp	1292.00		NIST
Inp	1292.00		NIST
Inp	1290.00		NIST
Inp	1293.00		NIST
Inp	1292.00		NIST
Inp	1283.00		NIST
Inp	1283.00		NIST
Inp	1289.00		NIST
Inp	1289.00		NIST
Inp	Outlier 219.50		NIST
Inp	1293.00		NIST
Inp	1291.50		NIST
Inp	1287.00		NIST
Inp	1291.90		NIST
Inp	1292.10		NIST
Inp	1292.00		NIST
Inp	1283.00		NIST
Ip	[1331.60; 1373.00]
Ip	1337.20		NIST
Ip	1339.40		NIST
Ip	1340.90		NIST
Ip	1337.00		NIST
Ip	1344.10		NIST
Ip	1343.90		NIST
Ip	Outlier 1373.00		NIST
Ip	1353.00		NIST
Ip	1334.00		NIST
Ip	1341.00		NIST
Ip	1342.00		NIST
Ip	1343.00		NIST
Ip	1336.00		NIST
Ip	1342.00		NIST
Ip	1342.00		NIST
Ip	1343.00		NIST
Ip	1335.00		NIST
Ip	1342.00		NIST
Ip	1343.00		NIST
Ip	1351.00		NIST
Ip	1352.00		NIST
Ip	1352.00		NIST
Ip	1353.00		NIST
Ip	1354.00		NIST
Ip	1346.00		NIST
Ip	1347.00		NIST
Ip	1347.00		NIST
Ip	1348.00		NIST
Ip	1348.00		NIST
Ip	1349.00		NIST
Ip	1334.60		NIST
Ip	1342.60		NIST
Ip	1335.50		NIST
Ip	1343.10		NIST
Ip	1331.60		NIST
Ip	1334.50		NIST
Ip	1340.80		NIST
Ip	1341.80		NIST
Ip	1331.90		NIST
Ip	1335.80		NIST
Ip	1342.00		NIST
Ip	1342.50		NIST
Ip	1351.00		NIST
Ip	1352.00		NIST
Ip	1353.00		NIST
Ip	1354.00		NIST
Ip	1332.00		NIST
Ip	1343.00		NIST
Ip	1340.00		NIST
Ip	1357.00		NIST
Ip	1341.00		NIST
Ip	1352.00		NIST
Ip	1343.00		NIST
Tboil	[501.00; 507.00]	K
Tboil	505.90	K	KDB
Tboil	505.00	K	NIST
Tboil	506.00	K	NIST
Tboil	501.00 ± 5.00	K	NIST
Tboil	507.00 ± 2.00	K	NIST
Tboil	503.00 ± 8.00	K	NIST
Tc	[674.00; 674.26]	K
Tc	674.00	K	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Tc	674.26	K	Passut and Danner (1973), critical constants and acentric factors Compiled value
Tc	674.00	K	KDB
Tfus	[250.03; 251.00]	K
Tfus	250.15	K	Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
Tfus	250.10	K	KDB
Tfus	250.05 ± 0.50	K	NIST
Tfus	250.03 ± 0.06	K	NIST
Tfus	250.04 ± 0.04	K	NIST
Tfus	250.08 ± 0.03	K	NIST
Tfus	250.04 ± 0.05	K	NIST
Tfus	250.08 ± 0.03	K	NIST
Tfus	251.00 ± 0.50	K	NIST
Tfus	251.00 ± 2.00	K	NIST
Vc	[0.740; 0.745]	m3/kmol
Vc	0.740	m3/kmol	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Vc	0.745	m3/kmol	KDB
Zc	0.2258480		KDB

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
ΔvapH	[44.98; 53.90]	kJ/mol	[461.00; 505.90]
ΔvapH	53.90	kJ/mol	461.00	NIST
ΔvapH	44.98	kJ/mol	505.90	KDB
ρl	766.00	kg/m3	293.00	KDB
γ	0.03	N/m	298.20	KDB

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[271.45; 661.50]	J/mol×K	[273.00; 1000.00]	Joback Predicted correlation
Equation			Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is Cp,gas in J/mol×K, T in K
Coefficient A			-1.19200e+01
Coefficient B			1.21882e+00
Coefficient C			-7.06300e-04
Coefficient D			1.60900e-07
Coefficient E			0.00000e+00
Temperature range, min.			273.00
Temperature range, max.			1000.00
Cp,gas	271.45	J/mol×K	273.00	Calculated Property
Cp,gas	338.00	J/mol×K	353.78	Calculated Property
Cp,gas	397.55	J/mol×K	434.56	Calculated Property
Cp,gas	450.63	J/mol×K	515.33	Calculated Property
Cp,gas	497.73	J/mol×K	596.11	Calculated Property
Cp,gas	539.38	J/mol×K	676.89	Calculated Property
Cp,gas	576.06	J/mol×K	757.67	Calculated Property
Cp,gas	608.31	J/mol×K	838.44	Calculated Property
Cp,gas	636.62	J/mol×K	919.22	Calculated Property
Cp,gas	661.50	J/mol×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.0036440; 0.0002312]	Pa×s	[250.26; 471.86]	Joback Predicted correlation
Equation			Y = exp(A + B/T + C·ln(T) + D·T^E) Y is η in Pa×s, T in K
Coefficient A			-1.14861e+01
Coefficient B			1.46936e+03
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Comment			Liquid phase. Joback/Reid (1987), valid from Tf to 0.7·Tc.
Temperature range, min.			250.26
Temperature range, max.			471.86
η	0.0036440	Pa×s	250.26	Calculated Property
η	0.0021536	Pa×s	274.88	Calculated Property
η	0.0013878	Pa×s	299.50	Calculated Property
η	0.0009560	Pa×s	324.12	Calculated Property
η	0.0006942	Pa×s	348.75	Calculated Property
η	0.0005258	Pa×s	373.37	Calculated Property
η	0.0004121	Pa×s	397.99	Calculated Property
η	0.0003324	Pa×s	422.62	Calculated Property
η	0.0002745	Pa×s	447.24	Calculated Property
η	0.0002312	Pa×s	471.86	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.67]	kPa	[375.70; 536.43]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.50003e+01
Coefficient B			-4.56047e+03
Coefficient C			-6.57330e+01
Temperature range, min.			375.70
Temperature range, max.			536.43
Pvap	1.33	kPa	375.70	Calculated Property
Pvap	2.97	kPa	393.56	Calculated Property
Pvap	6.10	kPa	411.42	Calculated Property
Pvap	11.66	kPa	429.28	Calculated Property
Pvap	20.97	kPa	447.14	Calculated Property
Pvap	35.80	kPa	464.99	Calculated Property
Pvap	58.39	kPa	482.85	Calculated Property
Pvap	91.47	kPa	500.71	Calculated Property
Pvap	138.31	kPa	518.57	Calculated Property
Pvap	202.67	kPa	536.43	Calculated Property
Pvap	[6.09e-05; 1729.77]	kPa	[250.08; 675.00]	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			8.60269e+01
Coefficient B			-1.02545e+04
Coefficient C			-9.94660e+00
Coefficient D			3.11629e-06
Coefficient E			0.00000e+00
Temperature range, min.			250.08
Temperature range, max.			675.00
Pvap	6.09e-05	kPa	250.08	Calculated Property
Pvap	7.96e-03	kPa	297.29	Calculated Property
Pvap	0.23	kPa	344.51	Calculated Property
Pvap	2.56	kPa	391.72	Calculated Property
Pvap	15.59	kPa	438.93	Calculated Property
Pvap	62.51	kPa	486.15	Calculated Property
Pvap	186.90	kPa	533.36	Calculated Property
Pvap	452.30	kPa	580.57	Calculated Property
Pvap	937.11	kPa	627.79	Calculated Property
Pvap	1729.77	kPa	675.00	Calculated Property
Pvap	[6.95; 101.04]	kPa	[415.80; 505.81]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.40700e+01
Coefficient B			-3.85623e+03
Coefficient C			-9.79360e+01
Reference			Camin and Rossini, 1955
Temperature range, min.			415.80
Temperature range, max.			505.81
Pvap	6.95	kPa	415.80	Calculated Property
Pvap	10.06	kPa	425.80	Calculated Property
Pvap	14.25	kPa	435.80	Calculated Property
Pvap	19.78	kPa	445.80	Calculated Property
Pvap	26.96	kPa	455.80	Calculated Property
Pvap	36.14	kPa	465.81	Calculated Property
Pvap	47.70	kPa	475.81	Calculated Property
Pvap	62.05	kPa	485.81	Calculated Property
Pvap	79.67	kPa	495.81	Calculated Property
Pvap	101.04	kPa	505.81	Calculated Property

Property	Value	Unit	Temperature (K)	Source
γ	[0.03; 0.01]	N/m	[260.15; 505.95]	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			5.21565e-02
Coefficient B			-8.84000e-05
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Temperature range, min.			260.15
Temperature range, max.			505.95
γ	0.03	N/m	260.15	Calculated Property
γ	0.03	N/m	287.46	Calculated Property
γ	0.02	N/m	314.77	Calculated Property
γ	0.02	N/m	342.08	Calculated Property
γ	0.02	N/m	369.39	Calculated Property
γ	0.02	N/m	396.71	Calculated Property
γ	0.01	N/m	424.02	Calculated Property
γ	0.01	N/m	451.33	Calculated Property
γ	0.01	N/m	478.64	Calculated Property
γ	0.01	N/m	505.95	Calculated Property

Similar Compounds

Find more compounds similar to 1-Tridecene.

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).
• 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.
• Cheméo Relay (1.0)
• Crippen Method
• Crippen Method
• Infinite dilution activity coefficients, specific retention volumes and solvation thermodynamics of hydrocarbons in C78H158 branched alkane solvent
• Joback Method
• KDB
• McGowan Method
• NIST Webbook
• The Yaws Handbook of Vapor Pressure

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