Chemical Properties of Tridecane (CAS 629-50-5)

InChI

InChI=1S/C13H28/c1-3-5-7-9-11-13-12-10-8-6-4-2/h3-13H2,1-2H3

InChI Key

IIYFAKIEWZDVMP-UHFFFAOYSA-N

Formula

C13H28

SMILES

CCCCCCCCCCCCC

Molecular Weight¹

184.36

CAS

629-50-5

Other Names

• Tridecane, n-
• n-tridecane

• ω : Acentric Factor.
• α_p : Isobaric thermal expansion coefficient (1/K).
• 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).
• 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_subH° : Enthalpy of sublimation 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_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.
• Δ_fusS : Entropy of fusion at a given temperature (J/mol×K).
• S°_gas : Molar entropy at standard conditions (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_fus(P) : Melting 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.

Contents

1. Physical Properties
2. Temperature Dependent Properties
3. Pressure Dependent Properties
4. Datasets
5. Correlations
6. Similar Compounds
7. Mixtures
8. Sources

Physical Properties

Property	Value	Unit	Source
ω	[0.6100; 0.6231]
ω	0.6230		PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
ω	0.6231		Passut and Danner (1973), critical constants and acentric factors Compiled value
ω	0.6100		ChemSep v8.3 pure component data Compiled value
ω	0.6190		KDB
ΔcH°liquid	-8739.70 ± 1.40	kJ/mol	NIST
μ	0.00	debye	ChemSep v8.3 pure component data Compiled value
ΔfG°	[57.71; 58.49]	kJ/mol
ΔfG°	57.71	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfG°	58.49	kJ/mol	KDB
ΔfH°gas	[-311.77; -311.50]	kJ/mol
ΔfH°gas	-311.77	kJ/mol	ChemSep v8.3 pure component data Compiled value
ΔfH°gas	-311.70	kJ/mol	KDB
ΔfH°gas	-311.50 ± 1.60	kJ/mol	NIST
ΔfH°liquid	-377.70 ± 1.60	kJ/mol	NIST
ΔfusH°	29.43	kJ/mol	Joback Calculated Property
ΔsubH°	91.40	kJ/mol	NIST
ΔvapH°	[66.20; 66.70]	kJ/mol
ΔvapH°	66.43	kJ/mol	NIST
ΔvapH°	66.70	kJ/mol	NIST
ΔvapH°	66.50 ± 0.20	kJ/mol	NIST
ΔvapH°	66.40 ± 0.30	kJ/mol	NIST
ΔvapH°	66.20	kJ/mol	NIST
IE	9.72	eV	Relay (1.0) Calculated Property
log10WS	-6.76		Relay (1.0) Calculated Property
logPoct/wat	5.317		Crippen Calculated Property
McVol	194.030	ml/mol	McGowan Calculated Property
Pc	[1678.95; 1725.00]	kPa
Pc	1680.00	kPa	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 2 Compiled value
Pc	1678.95	kPa	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Pc	1723.69	kPa	Passut and Danner (1973), critical constants and acentric factors Compiled value
Pc	1680.00	kPa	ChemSep v8.3 pure component data Compiled value
Pc	1680.00	kPa	KDB
Pc	1700.00 ± 100.00	kPa	NIST
Pc	1679.00 ± 20.00	kPa	NIST
Pc	1720.00	kPa	NIST
Pc	1725.00 ± 34.47	kPa	NIST
Ptriple	2.51e-04	kPa	ChemSep v8.3 pure component data Compiled value
ρc	[221.23; 224.92]	kg/m3
ρc	221.23 ± 18.44	kg/m3	NIST
ρc	224.92 ± 5.53	kg/m3	NIST
Inp	[218.83; 221.55]
Inp	218.83		NIST
Inp	221.55		NIST
S°gas	661.45	J/mol×K	NIST
S°liquid	522.87	J/mol×K	NIST
Tboil	[505.00; 508.63]	K
Tboil	508.63	K	ChemSep v8.3 pure component data Compiled value
Tboil	508.62	K	KDB
Tboil	507.20	K	NIST
Tboil	508.60	K	NIST
Tboil	507.15 ± 0.60	K	NIST
Tboil	508.60 ± 0.30	K	NIST
Tboil	507.75 ± 0.40	K	NIST
Tboil	506.00 ± 2.00	K	NIST
Tboil	507.00 ± 1.50	K	NIST
Tboil	Outlier 505.00 ± 4.00	K	NIST
Tboil	507.00 ± 4.00	K	NIST
Tc	[674.00; 676.20]	K
Tc	675.00	K	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 2 Compiled value
Tc	676.00	K	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Tc	675.76	K	Passut and Danner (1973), critical constants and acentric factors Compiled value
Tc	675.00	K	ChemSep v8.3 pure component data Compiled value
Tc	675.00	K	KDB
Tc	675.00 ± 1.00	K	NIST
Tc	675.80 ± 0.40	K	NIST
Tc	676.00 ± 0.60	K	NIST
Tc	675.80 ± 0.40	K	NIST
Tc	675.98	K	NIST
Tc	Outlier 674.00 ± 0.80	K	NIST
Tc	675.80	K	NIST
Tc	676.20 ± 1.00	K	NIST
Tc	676.20 ± 0.60	K	NIST
Tc	674.90 ± 1.00	K	NIST
Tfus	[265.00; 269.01]	K
Tfus	269.01	K	Phase diagrams of binary systems containing n-alkanes, or cyclohexane, or 1-alkanols and 2,3-pentanedione at atmospheric and high pressure
Tfus	269.01	K	Influence of High Pressure on the Liquidus Curve Shape in Binary Hydrocarbon Mixtures: Experimental Data, Correlation, and Prediction
Tfus	268.15	K	Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
Tfus	267.76	K	ChemSep v8.3 pure component data Compiled value
Tfus	267.76	K	KDB
Tfus	267.85 ± 0.50	K	NIST
Tfus	266.00 ± 2.00	K	NIST
Tfus	267.74 ± 0.02	K	NIST
Tfus	267.74 ± 0.02	K	NIST
Tfus	267.76 ± 0.01	K	NIST
Tfus	267.00 ± 2.00	K	NIST
Tfus	267.73 ± 0.10	K	NIST
Tfus	267.76 ± 0.10	K	NIST
Tfus	267.82 ± 0.07	K	NIST
Tfus	267.80 ± 0.20	K	NIST
Tfus	267.74 ± 0.08	K	NIST
Tfus	267.74 ± 0.08	K	NIST
Tfus	267.76 ± 0.02	K	NIST
Tfus	267.90 ± 0.50	K	NIST
Tfus	267.90 ± 0.60	K	NIST
Tfus	267.70 ± 1.00	K	NIST
Tfus	Outlier 265.00 ± 3.00	K	NIST
Tfus	267.00 ± 3.00	K	NIST
Tfus	266.00 ± 3.00	K	NIST
Tfus	267.00 ± 2.00	K	NIST
Ttriple	[267.76; 267.79]	K
Ttriple	Outlier 267.76	K	ChemSep v8.3 pure component data Compiled value
Ttriple	267.78 ± 0.05	K	NIST
Ttriple	267.79 ± 0.02	K	NIST
Ttriple	267.78 ± 0.40	K	NIST
Ttriple	267.78 ± 0.20	K	NIST
Ttriple	267.79 ± 0.40	K	NIST
Ttriple	267.79 ± 0.20	K	NIST
UQi	7.64		ChemSep v8.3 pure component data Compiled value
URi	9.22		ChemSep v8.3 pure component data Compiled value
Vc	[0.823; 0.823]	m3/kmol
Vc	0.823	m3/kmol	IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 2 Compiled value
Vc	0.823	m3/kmol	PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Vc	0.823	m3/kmol	ChemSep v8.3 pure component data Compiled value
Vc	0.823	m3/kmol	KDB
Vc	0.823	m3/kmol	NIST
VCOSTALD	0.83	m3/kmol	Hankinson and Thomson (1979), COSTALD parameters Compiled value
ωSRK	0.63		Hankinson and Thomson (1979), COSTALD parameters Compiled value
Zc	[0.2460000; 0.2463590]
Zc	0.2460000		IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 2 Compiled value
Zc	0.2460000		ChemSep v8.3 pure component data Compiled value
Zc	0.2463590		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	[406.89; 409.40]	J/mol×K	[298.15; 303.15]
Cp,liquid	406.89	J/mol×K	298.15	NIST
Cp,liquid	409.40	J/mol×K	303.15	NIST
ΔfusH	[7.66; 28.90]	kJ/mol	[255.00; 267.80]
ΔfusH	7.66	kJ/mol	255.00	NIST
ΔfusH	28.90	kJ/mol	267.70	NIST
ΔfusH	28.49	kJ/mol	267.80	NIST
ΔfusH	28.49	kJ/mol	267.80	NIST
ΔvapH	[45.65; 65.60]	kJ/mol	[308.00; 507.80]
ΔvapH	65.60	kJ/mol	308.00	NIST
ΔvapH	65.30	kJ/mol	309.00	NIST
ΔvapH	64.90	kJ/mol	314.00	NIST
ΔvapH	64.60	kJ/mol	318.00	NIST
ΔvapH	64.20	kJ/mol	324.00	NIST
ΔvapH	63.30	kJ/mol	334.00	NIST
ΔvapH	62.40	kJ/mol	344.00	NIST
ΔvapH	61.70	kJ/mol	348.00	NIST
ΔvapH	62.30	kJ/mol	349.00	NIST
ΔvapH	54.50	kJ/mol	464.00	NIST
ΔvapH	45.65	kJ/mol	507.80	KDB
n0	1.41550		318.15	Thermodynamic properties of (an ester + an alkane). XVI. Experimental HEm and V Em values and a new correlation method for (an alkyl ethanoate + an n-alkane) at 318.15 K
ρl	[720.20; 756.00]	kg/m3	[293.00; 344.15]
ρl	756.00	kg/m3	293.00	KDB
ρl	720.20	kg/m3	344.15	High-pressure densities and interfacial tensions of binary systems containing carbon dioxide + n-alkanes: (n-Dodecane, n-tridecane, n-tetradecane)
ΔfusS	[30.04; 106.27]	J/mol×K	[255.00; 267.80]
ΔfusS	30.04	J/mol×K	255.00	NIST
ΔfusS	106.27	J/mol×K	267.80	NIST
γ	[0.02; 0.03]	N/m	[293.15; 303.15]
γ	0.02	N/m	293.15	Density, Refractive Index, Viscosity, and Surface Tension of Binary Mixtures of exo-Tetrahydrodicyclopentadiene with Some n-Alkanes from (293.15 to 313.15) K
γ	0.03	N/m	293.20	KDB
γ	0.02	N/m	303.15	Density, Refractive Index, Viscosity, and Surface Tension of Binary Mixtures of exo-Tetrahydrodicyclopentadiene with Some n-Alkanes from (293.15 to 313.15) K

Pressure Dependent Properties

Property	Value	Unit	Pressure (kPa)	Source
Tfus(P)	[268.21; 343.15]	K	[100.00; 495170.00]
Tfus(P)	268.21	K	100.00	High pressure (solid + liquid) equilibria of n-alkane mixtures: experimental results, correlation and prediction
Tfus(P)	293.15	K	133010.00	High pressure (solid + liquid) equilibria of n-alkane mixtures: experimental results, correlation and prediction
Tfus(P)	303.15	K	197120.00	High pressure (solid + liquid) equilibria of n-alkane mixtures: experimental results, correlation and prediction
Tfus(P)	313.15	K	265400.00	High pressure (solid + liquid) equilibria of n-alkane mixtures: experimental results, correlation and prediction
Tfus(P)	323.15	K	337830.00	High pressure (solid + liquid) equilibria of n-alkane mixtures: experimental results, correlation and prediction
Tfus(P)	333.15	K	414420.00	High pressure (solid + liquid) equilibria of n-alkane mixtures: experimental results, correlation and prediction
Tfus(P)	343.15	K	495170.00	High pressure (solid + liquid) equilibria of n-alkane mixtures: experimental results, correlation and prediction

Datasets

1. Isobaric coefficient of expansion, 1/K (1)
2. Mass density, kg/m3 (2)

Isobaric coefficient of expansion, 1/K

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Isobaric coefficient of expansion, 1/K - Liquid
288.15	5000.00	0.0009
288.15	10000.00	0.0009
288.15	15000.00	0.0008
288.15	20000.00	0.0008
288.15	25000.00	0.0008
288.15	30000.00	0.0008
288.15	35000.00	0.0008
288.15	40000.00	0.0008
288.15	45000.00	0.0008
288.15	50000.00	0.0007
288.15	55000.00	0.0007
298.15	5000.00	0.0009
298.15	10000.00	0.0009
298.15	15000.00	0.0008
298.15	20000.00	0.0008
298.15	25000.00	0.0008
298.15	30000.00	0.0008
298.15	35000.00	0.0008
298.15	40000.00	0.0008
298.15	45000.00	0.0008
298.15	50000.00	0.0007
298.15	55000.00	0.0007
308.15	5000.00	0.0009
308.15	10000.00	0.0009
308.15	15000.00	0.0009
308.15	20000.00	0.0008
308.15	25000.00	0.0008
308.15	30000.00	0.0008
308.15	35000.00	0.0008
308.15	40000.00	0.0008
308.15	45000.00	0.0008
308.15	50000.00	0.0007
308.15	55000.00	0.0007
318.15	5000.00	0.0009
318.15	10000.00	0.0009
318.15	15000.00	0.0009
318.15	20000.00	0.0008
318.15	25000.00	0.0008
318.15	30000.00	0.0008
318.15	35000.00	0.0008
318.15	40000.00	0.0008
318.15	45000.00	0.0007
318.15	50000.00	0.0007
318.15	55000.00	0.0007
328.15	5000.00	0.0009
328.15	10000.00	0.0009
328.15	15000.00	0.0009
328.15	20000.00	0.0008
328.15	25000.00	0.0008
328.15	30000.00	0.0008
328.15	35000.00	0.0008
328.15	40000.00	0.0008
328.15	45000.00	0.0007
328.15	50000.00	0.0007
328.15	55000.00	0.0007
338.15	5000.00	0.0010
338.15	10000.00	0.0009
338.15	15000.00	0.0009
338.15	20000.00	0.0009
338.15	25000.00	0.0008
338.15	30000.00	0.0008
338.15	35000.00	0.0008
338.15	40000.00	0.0008
338.15	45000.00	0.0007
338.15	50000.00	0.0007
338.15	55000.00	0.0007
348.15	5000.00	0.0010
348.15	10000.00	0.0009
348.15	15000.00	0.0009
348.15	20000.00	0.0009
348.15	25000.00	0.0008
348.15	30000.00	0.0008
348.15	35000.00	0.0008
348.15	40000.00	0.0008
348.15	45000.00	0.0007
348.15	50000.00	0.0007
348.15	55000.00	0.0007
Reference

Mass density, kg/m3

Fixed		Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mass density, kg/m3 - Liquid
313.01	1023.00	743.49
313.01	2030.00	744.27
313.01	3025.00	745.05
313.01	4027.00	745.74
313.01	5014.00	746.51
313.01	6024.00	747.18
313.01	7021.00	747.95
313.01	8036.00	748.69
313.01	9019.00	749.41
313.01	10018.00	750.14
313.01	11030.00	750.86
313.01	12006.00	751.51
313.01	13017.00	752.24
313.01	14035.00	752.95
313.01	15021.00	753.59
313.01	16019.00	754.27
313.01	17019.00	754.94
313.01	18024.00	755.61
313.01	19025.00	756.27
313.01	20043.00	756.91
313.01	21011.00	757.52
313.01	22020.00	758.16
313.01	23018.00	758.79
313.01	24004.00	759.44
313.01	25036.00	760.12
322.92	1017.00	736.15
322.92	2006.00	736.94
322.92	3025.00	737.83
322.92	4021.00	738.62
322.92	5021.00	739.42
322.92	6043.00	740.18
322.92	7018.00	740.9
322.92	8022.00	741.72
322.92	9008.00	742.44
322.92	10012.00	743.18
322.92	11015.00	743.93
322.92	12006.00	744.71
322.92	13030.00	745.38
322.92	14010.00	746.12
322.92	15026.00	746.81
322.92	16024.00	747.53
322.92	17016.00	748.22
322.92	18010.00	748.89
322.92	19007.00	749.56
322.92	20023.00	750.22
322.92	21020.00	750.92
322.92	22010.00	751.57
322.92	23040.00	752.26
322.92	24006.00	752.95
322.92	25006.00	753.6
332.78	1015.00	729.19
332.78	2020.00	730.06
332.78	3022.00	730.83
332.78	4016.00	731.63
332.78	5020.00	732.47
332.78	6016.00	733.27
332.78	7006.00	734.09
332.78	8018.00	734.9
332.78	9013.00	735.71
332.78	10008.00	736.52
332.78	11016.00	737.3
332.78	12007.00	738.05
332.78	13012.00	738.79
332.78	14021.00	739.55
332.78	15011.00	740.26
332.78	16020.00	741.03
332.78	17015.00	741.74
332.78	18005.00	742.47
332.78	19017.00	743.19
332.78	20014.00	743.89
332.78	21016.00	744.66
332.78	22046.00	745.35
332.78	22994.00	745.97
332.78	24032.00	746.67
332.78	25030.00	747.38
342.64	1022.00	722.03
342.64	2014.00	722.93
342.64	3025.00	723.84
342.64	4021.00	724.7
342.64	5020.00	725.59
342.64	6020.00	726.44
342.64	7008.00	727.27
342.64	8026.00	728.15
342.64	9007.00	728.98
342.64	10010.00	729.81
342.64	11012.00	730.63
342.64	12014.00	731.46
342.64	13011.00	732.27
342.64	14008.00	733.03
342.64	15029.00	733.84
342.64	16006.00	734.58
342.64	17016.00	735.35
342.64	18019.00	736.09
342.64	19006.00	736.85
342.64	20001.00	737.59
342.64	21023.00	738.34
342.64	22008.00	739.06
342.64	23005.00	739.79
342.64	24032.00	740.52
342.64	25024.00	741.14
352.47	1013.00	714.88
352.47	2022.00	715.88
352.47	3010.00	716.8
352.47	4020.00	717.71
352.47	5019.00	718.65
352.47	6011.00	719.55
352.47	7017.00	720.47
352.47	8014.00	721.35
352.47	9022.00	722.24
352.47	10031.00	723.11
352.47	11010.00	723.98
352.47	12003.00	724.82
352.47	13024.00	725.71
352.47	14013.00	726.54
352.47	15007.00	727.34
352.47	16016.00	728.16
352.47	17007.00	728.94
352.47	18020.00	729.77
352.47	19011.00	730.53
352.47	20013.00	731.29
352.47	21032.00	732.07
352.47	22020.00	732.84
352.47	23020.00	733.6
352.47	24021.00	734.36
352.47	25024.00	735.14
362.25	1020.00	707.72
362.25	2026.00	708.74
362.25	3018.00	709.77
362.25	4006.00	710.71
362.25	5021.00	711.73
362.25	6019.00	712.7
362.25	7029.00	713.67
362.25	8017.00	714.54
362.25	9011.00	715.51
362.25	10011.00	716.42
362.25	11021.00	717.35
362.25	12018.00	718.24
362.25	13014.00	719.11
362.25	14000.00	719.97
362.25	15017.00	720.85
362.25	16026.00	721.7
362.25	17019.00	722.52
362.25	18034.00	723.36
362.25	19016.00	724.17
362.25	20004.00	725.0
362.25	21015.00	725.8
362.25	22022.00	726.63
362.25	23008.00	727.42
362.25	24034.00	728.22
362.25	25010.00	729.02
Reference

Fixed		Measured
Pressure, kPa - Liquid	Temperature, K - Liquid	Mass density, kg/m3 - Liquid
100.00	283.15	763.6
100.00	288.15	760.0
100.00	293.15	756.4
100.00	298.15	752.6
100.00	303.15	749.2
100.00	308.15	745.6
100.00	313.15	742.0
100.00	318.15	738.4
100.00	323.15	734.8
10000.00	283.15	769.7
10000.00	288.15	766.2
10000.00	293.15	762.8
10000.00	298.15	759.3
10000.00	303.15	755.9
10000.00	308.15	752.5
10000.00	313.15	749.1
10000.00	318.15	745.7
10000.00	323.15	742.3
20000.00	283.15	775.5
20000.00	288.15	772.1
20000.00	293.15	768.9
20000.00	298.15	765.5
20000.00	303.15	762.3
20000.00	308.15	759.1
20000.00	313.15	755.7
20000.00	318.15	752.5
20000.00	323.15	749.3
30000.00	283.15	781.0
30000.00	288.15	777.7
30000.00	293.15	774.6
30000.00	298.15	771.4
30000.00	303.15	768.3
30000.00	308.15	765.1
30000.00	313.15	761.9
30000.00	318.15	758.8
30000.00	323.15	755.7
40000.00	283.15	786.1
40000.00	288.15	783.0
40000.00	293.15	780.0
40000.00	298.15	776.8
40000.00	303.15	773.8
40000.00	308.15	770.8
40000.00	313.15	767.7
40000.00	318.15	764.7
40000.00	323.15	761.8
50000.00	283.15	791.0
50000.00	288.15	788.0
50000.00	293.15	785.1
50000.00	298.15	782.0
50000.00	303.15	779.0
50000.00	308.15	776.1
50000.00	313.15	773.2
50000.00	318.15	770.3
50000.00	323.15	767.3
60000.00	283.15	795.6
60000.00	288.15	792.7
60000.00	293.15	789.8
60000.00	298.15	786.9
60000.00	303.15	784.0
60000.00	308.15	781.1
60000.00	313.15	778.3
60000.00	318.15	775.4
60000.00	323.15	772.6
Reference

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[229.48; 803.77]	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			1.91240e+02
Coefficient B			-6.57520e+02
Coefficient C			6.95324e+00
Coefficient D			-1.14980e-04
Coefficient E			3.34090e-08
Temperature range, min.			200.00
Temperature range, max.			1500.00
Cp,gas	229.48	J/mol×K	200.00	Calculated Property
Cp,gas	340.95	J/mol×K	344.44	Calculated Property
Cp,gas	451.09	J/mol×K	488.89	Calculated Property
Cp,gas	540.44	J/mol×K	633.33	Calculated Property
Cp,gas	610.56	J/mol×K	777.78	Calculated Property
Cp,gas	665.92	J/mol×K	922.22	Calculated Property
Cp,gas	710.39	J/mol×K	1066.67	Calculated Property
Cp,gas	746.86	J/mol×K	1211.11	Calculated Property
Cp,gas	777.47	J/mol×K	1355.56	Calculated Property
Cp,gas	803.77	J/mol×K	1500.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Cp,liquid	[395.22; 555.88]	J/mol×K	[267.76; 508.62]	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			3.71670e+01
Coefficient B			1.23480e+02
Coefficient C			4.61224e+00
Coefficient D			3.31470e-03
Coefficient E			-1.11940e-06
Temperature range, min.			267.76
Temperature range, max.			508.62
Cp,liquid	395.22	J/mol×K	267.76	Calculated Property
Cp,liquid	406.11	J/mol×K	294.52	Calculated Property
Cp,liquid	419.38	J/mol×K	321.28	Calculated Property
Cp,liquid	434.63	J/mol×K	348.05	Calculated Property
Cp,liquid	451.56	J/mol×K	374.81	Calculated Property
Cp,liquid	469.98	J/mol×K	401.57	Calculated Property
Cp,liquid	489.74	J/mol×K	428.33	Calculated Property
Cp,liquid	510.71	J/mol×K	455.10	Calculated Property
Cp,liquid	532.79	J/mol×K	481.86	Calculated Property
Cp,liquid	555.88	J/mol×K	508.62	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.0033509; 0.0000564]	Pa×s	[267.67; 675.00]	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			-8.14591e+01
Coefficient B			4.30955e+03
Coefficient C			1.08192e+01
Coefficient D			-1.13950e-05
Coefficient E			2.00000e+00
Temperature range, min.			267.67
Temperature range, max.			675.00
η	0.0033509	Pa×s	267.67	Calculated Property
η	0.0013118	Pa×s	312.93	Calculated Property
η	0.0007023	Pa×s	358.19	Calculated Property
η	0.0004455	Pa×s	403.45	Calculated Property
η	0.0003088	Pa×s	448.71	Calculated Property
η	0.0002228	Pa×s	493.96	Calculated Property
η	0.0001623	Pa×s	539.22	Calculated Property
η	0.0001171	Pa×s	584.48	Calculated Property
η	0.0000826	Pa×s	629.74	Calculated Property
η	0.0000564	Pa×s	675.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ΔvapH	[68.93; 0.00]	kJ/mol	[267.76; 675.00]	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			9.73282e+01
Coefficient B			6.67983e-01
Coefficient C			4.62399e-01
Coefficient D			-1.32997e+00
Coefficient E			6.49193e-01
Critical temperature, Tc (K)			6.75000e+02
Temperature range, min.			267.76
Temperature range, max.			675.00
ΔvapH	68.93	kJ/mol	267.76	Calculated Property
ΔvapH	64.47	kJ/mol	313.01	Calculated Property
ΔvapH	60.16	kJ/mol	358.26	Calculated Property
ΔvapH	55.95	kJ/mol	403.51	Calculated Property
ΔvapH	51.72	kJ/mol	448.76	Calculated Property
ΔvapH	47.28	kJ/mol	494.00	Calculated Property
ΔvapH	42.30	kJ/mol	539.25	Calculated Property
ΔvapH	36.17	kJ/mol	584.50	Calculated Property
ΔvapH	27.41	kJ/mol	629.75	Calculated Property
ΔvapH	0.00	kJ/mol	675.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.66]	kPa	[378.46; 540.38]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.48906e+01
Coefficient B			-4.50848e+03
Coefficient C			-6.97210e+01
Temperature range, min.			378.46
Temperature range, max.			540.38
Pvap	1.33	kPa	378.46	Calculated Property
Pvap	2.98	kPa	396.45	Calculated Property
Pvap	6.12	kPa	414.44	Calculated Property
Pvap	11.71	kPa	432.43	Calculated Property
Pvap	21.08	kPa	450.42	Calculated Property
Pvap	35.96	kPa	468.42	Calculated Property
Pvap	58.60	kPa	486.41	Calculated Property
Pvap	91.70	kPa	504.40	Calculated Property
Pvap	138.49	kPa	522.39	Calculated Property
Pvap	202.66	kPa	540.38	Calculated Property
Pvap	[2.59e-04; 1700.53]	kPa	[267.76; 675.00]	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			1.36418e+02
Coefficient B			-1.27667e+04
Coefficient C			-1.74542e+01
Coefficient D			7.99709e-06
Coefficient E			2.00000e+00
Temperature range, min.			267.76
Temperature range, max.			675.00
Pvap	2.59e-04	kPa	267.76	Calculated Property
Pvap	0.02	kPa	313.01	Calculated Property
Pvap	0.43	kPa	358.26	Calculated Property
Pvap	3.86	kPa	403.51	Calculated Property
Pvap	19.99	kPa	448.76	Calculated Property
Pvap	71.21	kPa	494.00	Calculated Property
Pvap	196.04	kPa	539.25	Calculated Property
Pvap	450.95	kPa	584.50	Calculated Property
Pvap	914.78	kPa	629.75	Calculated Property
Pvap	1700.53	kPa	675.00	Calculated Property
Pvap	[3.88e-04; 1719.36]	kPa	[267.76; 675.80]	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			1.01620e+02
Coefficient B			-1.09918e+04
Coefficient C			-1.23037e+01
Coefficient D			4.95821e-06
Coefficient E			0.00000e+00
Temperature range, min.			267.76
Temperature range, max.			675.80
Pvap	3.88e-04	kPa	267.76	Calculated Property
Pvap	0.02	kPa	313.10	Calculated Property
Pvap	0.46	kPa	358.44	Calculated Property
Pvap	3.95	kPa	403.77	Calculated Property
Pvap	20.15	kPa	449.11	Calculated Property
Pvap	71.97	kPa	494.45	Calculated Property
Pvap	199.64	kPa	539.79	Calculated Property
Pvap	461.69	kPa	585.12	Calculated Property
Pvap	935.28	kPa	630.46	Calculated Property
Pvap	1719.36	kPa	675.80	Calculated Property
Pvap	[5.53; 102.80]	kPa	[412.50; 509.21]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.41109e+01
Coefficient B			-3.88928e+03
Coefficient C			-9.88660e+01
Reference			Camin and Rossini, 1955
Temperature range, min.			412.50
Temperature range, max.			509.21
Pvap	5.53	kPa	412.50	Calculated Property
Pvap	8.34	kPa	423.25	Calculated Property
Pvap	12.25	kPa	433.99	Calculated Property
Pvap	17.57	kPa	444.74	Calculated Property
Pvap	24.65	kPa	455.48	Calculated Property
Pvap	33.91	kPa	466.23	Calculated Property
Pvap	45.82	kPa	476.97	Calculated Property
Pvap	60.88	kPa	487.72	Calculated Property
Pvap	79.67	kPa	498.46	Calculated Property
Pvap	102.80	kPa	509.21	Calculated Property

Property	Value	Unit	Temperature (K)	Source
ρl	[773.74; 227.26]	kg/m3	[267.76; 675.00]	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			5.49157e+01
Coefficient B			2.41640e-01
Coefficient C			6.75000e+02
Coefficient D			2.92540e-01
Temperature range, min.			267.76
Temperature range, max.			675.00
ρl	773.74	kg/m3	267.76	Calculated Property
ρl	742.29	kg/m3	313.01	Calculated Property
ρl	709.39	kg/m3	358.26	Calculated Property
ρl	674.66	kg/m3	403.51	Calculated Property
ρl	637.59	kg/m3	448.76	Calculated Property
ρl	597.35	kg/m3	494.00	Calculated Property
ρl	552.53	kg/m3	539.25	Calculated Property
ρl	500.26	kg/m3	584.50	Calculated Property
ρl	432.82	kg/m3	629.75	Calculated Property
ρl	227.26	kg/m3	675.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
γ	[0.03; 0.01]	N/m	[268.15; 508.15]	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			5.15487e-02
Coefficient B			-8.72000e-05
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Temperature range, min.			268.15
Temperature range, max.			508.15
γ	0.03	N/m	268.15	Calculated Property
γ	0.03	N/m	294.82	Calculated Property
γ	0.02	N/m	321.48	Calculated Property
γ	0.02	N/m	348.15	Calculated Property
γ	0.02	N/m	374.82	Calculated Property
γ	0.02	N/m	401.48	Calculated Property
γ	0.01	N/m	428.15	Calculated Property
γ	0.01	N/m	454.82	Calculated Property
γ	0.01	N/m	481.48	Calculated Property
γ	0.01	N/m	508.15	Calculated Property
γ	[0.03; 9.90e-07]	N/m	[267.76; 668.08]	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			-9.09410e-02
Coefficient B			-4.11400e+01
Coefficient C			-1.57110e+00
Coefficient D			-1.74550e-03
Coefficient E			8.99060e-07
Comment			Range stopped where the equation turns negative; ChemSep gives it to 675 K.
Temperature range, min.			267.76
Temperature range, max.			668.08
γ	0.03	N/m	267.76	Calculated Property
γ	0.02	N/m	312.24	Calculated Property
γ	0.02	N/m	356.72	Calculated Property
γ	0.02	N/m	401.20	Calculated Property
γ	0.01	N/m	445.68	Calculated Property
γ	0.01	N/m	490.16	Calculated Property
γ	0.01	N/m	534.64	Calculated Property
γ	0.00	N/m	579.12	Calculated Property
γ	0.00	N/m	623.60	Calculated Property
γ	9.90e-07	N/m	668.08	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λgas	[0.01; 0.09]	W/m×K	[267.76; 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			5.04710e-06
Coefficient B			1.48060e+00
Coefficient C			5.53990e+02
Coefficient D			7.55440e+03
Temperature range, min.			267.76
Temperature range, max.			1000.00
λgas	0.01	W/m×K	267.76	Calculated Property
λgas	0.01	W/m×K	349.12	Calculated Property
λgas	0.02	W/m×K	430.48	Calculated Property
λgas	0.02	W/m×K	511.84	Calculated Property
λgas	0.03	W/m×K	593.20	Calculated Property
λgas	0.04	W/m×K	674.56	Calculated Property
λgas	0.05	W/m×K	755.92	Calculated Property
λgas	0.06	W/m×K	837.28	Calculated Property
λgas	0.08	W/m×K	918.64	Calculated Property
λgas	0.09	W/m×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
λliquid	[0.14; 0.09]	W/m×K	[267.76; 508.62]	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			3.72940e-02
Coefficient B			-1.93160e+02
Coefficient C			-1.10800e-01
Coefficient D			-5.82950e-03
Coefficient E			2.25510e-06
Temperature range, min.			267.76
Temperature range, max.			508.62
λliquid	0.14	W/m×K	267.76	Calculated Property
λliquid	0.14	W/m×K	294.52	Calculated Property
λliquid	0.13	W/m×K	321.28	Calculated Property
λliquid	0.13	W/m×K	348.05	Calculated Property
λliquid	0.12	W/m×K	374.81	Calculated Property
λliquid	0.11	W/m×K	401.57	Calculated Property
λliquid	0.11	W/m×K	428.33	Calculated Property
λliquid	0.10	W/m×K	455.10	Calculated Property
λliquid	0.10	W/m×K	481.86	Calculated Property
λliquid	0.09	W/m×K	508.62	Calculated Property

Similar Compounds

Find more compounds similar to Tridecane.

Mixtures

• Tridecane + Acetic acid, methyl ester
• Tridecane + Ethyl Acetate
• Tridecane + Acetic acid, propyl ester
• Tridecane + Acetic acid, butyl ester
• Acetic acid, pentyl ester + Tridecane
• Carbon dioxide + Ethanol + Tridecane
• n-Hexane + Tridecane
• Acetonitrile + Tridecane
• Tridecane + Methyl propionate
• Propanoic acid, ethyl ester + Tridecane
• Propanoic acid, propyl ester + Tridecane
• Propanoic acid, butyl ester + Tridecane
• Propanoic acid, pentyl ester + Tridecane
• Propane, 1-nitro- + Tridecane
• Carbon dioxide + Tridecane
• Nitrogen + Carbon dioxide + Tridecane
• Tridecane + 2,3-Pentadione
• Tridecane + Thiophene, tetrahydro-, 1,1-dioxide
• Tridecane + Benzene, 1,4-diethyl- + Thiophene, tetrahydro-, 1,1-dioxide
• Tridecane + Pentane, 3-methyl-

Find more mixtures with Tridecane.

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 2 ChEDL chemicals 1.5.2, from Ambrose, D.; Tsonopoulos, C. Vapor-Liquid Critical Properties of Elements and Compounds. 2. Normal Alkanes. J. Chem. Eng. Data 1995, 40, 531-546.
• 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)
• 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
• High pressure (solid + liquid) equilibria of n-alkane mixtures: experimental results, correlation and prediction
• Phase diagrams of binary systems containing n-alkanes, or cyclohexane, or 1-alkanols and 2,3-pentanedione at atmospheric and high pressure
• Infinite dilution activity coefficients, specific retention volumes and solvation thermodynamics of hydrocarbons in C78H158 branched alkane solvent
• High-pressure vapor liquid equilibria for CO2 + alkanol systems and densities of n-dodecane and n-tridecane
• Solution thermodynamics near the liquid liquid critical point I. First-order excess derivatives
• Determination and correlation of liquid-liquid equilibria for nine binary acetonitrile + n-alkane systems
• Experimental and theoretical study of interaction between organic compounds and 1- (4-sulfobutyl)-3-methylimidazolium based ionic liquids
• High-pressure densities and interfacial tensions of binary systems containing carbon dioxide + n-alkanes: (n-Dodecane, n-tridecane, n-tetradecane)
• Study of interaction between organic compounds and mono or dicationic oxygenated ionic liquids using gas chromatography
• Measurement and correlation of the interfacial tension for paraffin + CO2 and (CO2+N2) mixture gas at elevated temperatures and pressures
• CO2 and alkane minimum miscible pressure estimation by the extrapolation of interfacial tension
• Thermodynamic properties of (an ester + an alkane). XVI. Experimental HEm and V Em values and a new correlation method for (an alkyl ethanoate + an n-alkane) at 318.15 K
• Thermodynamic properties of (an ester + and alkane). XVII. Experimental He and Ve values for (an alkyl propanoate + an alkane) at 318.15K
• Activity coefficients at infinite dilution of organic solutes in methylphosphonate based ionic liquids using gas-liquid chromatography
• Experiment and correlation of the equilibrium interfacial tension for paraffin + CO2 modified with ethanol
• Interfacial Tension Measurement and Calculation of (Carbon Dioxide + n-Alkane) Binary Mixtures
• Measurement and Correlation of High Pressure Phase Equilibria for CO2 + Alkanes and CO2 + Crude Oil Systems
• Influence of High Pressure on the Liquidus Curve Shape in Binary Hydrocarbon Mixtures: Experimental Data, Correlation, and Prediction
• Activity Coefficients at Infinite Dilution of Organic Compounds in Four New Imidazolium-Based Ionic Liquids
• Liquid Liquid Equilibria of the Ternary Systems Undecane + 1,4-Diethylbenzene + Tetrahydrothiophene 1,1-Dioxide and Tridecane + 1,4-Diethylbenzene + Tetrahydrothiophene 1,1-Dioxide at T = (323.15, 348.15, and 373.15) K
• Density, Refractive Index, Viscosity, and Surface Tension of Binary Mixtures of exo-Tetrahydrodicyclopentadiene with Some n-Alkanes from (293.15 to 313.15) K
• Evaluation of the Performance of Trigeminal Tricationic Ionic Liquids for Separation Problems
• (p, rho, T) Behavior for the Binary Mixtures Carbon Dioxide + Heptane and Carbon Dioxide + Tridecane
• Thermophysical Characterization of Liquids Using Precise Density and Isobaric Heat Capacity Measurements As a Function of Pressure
• Partition Coefficients of Organic Compounds in New Imidazolium and Tetralkylammonium Based Ionic Liquids Using Inverse Gas Chromatography
• Isobaric Thermal Expansivity for Nonpolar Compounds
• Study of Ether-, Alcohol-, or Cyano-Functionalized Ionic Liquids Using Inverse Gas Chromatography
• 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.
Calculated This icon marks a calculated value or equation: a prediction, not a measurement.
Compiled This icon marks a compiled value or equation: taken from a data compilation such as ChemSep, not from an original measurement report.
These property values are available through the Cheméo API. A free account gives you an access key.