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).
• 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_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).
• T_fus : Normal melting (fusion) point (K).
• T_fus : Melting point (K).
• T_triple : Triple Point Temperature (K).
• V_c : Critical Volume (m³/kmol).
• 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	0.6190		KDB
ΔcH°liquid	-8739.70 ± 1.40	kJ/mol	NIST
ΔfG°	58.49	kJ/mol	KDB
ΔfH°gas	[-311.70; -311.50]	kJ/mol
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	[1679.00; 1725.00]	kPa
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
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; 508.62]	K
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	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	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	[267.78; 267.79]	K
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
Vc	[0.823; 0.823]	m3/kmol
Vc	0.823	m3/kmol	KDB
Vc	0.823	m3/kmol	NIST
Zc	0.2463590		KDB
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	[268.21; 343.15]	K	[100.00; 495170.00]
Tfus	268.21	K	100.00	High pressure (solid + liquid) equilibria of n-alkane mixtures: experimental results, correlation and prediction
Tfus	293.15	K	133010.00	High pressure (solid + liquid) equilibria of n-alkane mixtures: experimental results, correlation and prediction
Tfus	303.15	K	197120.00	High pressure (solid + liquid) equilibria of n-alkane mixtures: experimental results, correlation and prediction
Tfus	313.15	K	265400.00	High pressure (solid + liquid) equilibria of n-alkane mixtures: experimental results, correlation and prediction
Tfus	323.15	K	337830.00	High pressure (solid + liquid) equilibria of n-alkane mixtures: experimental results, correlation and prediction
Tfus	333.15	K	414420.00	High pressure (solid + liquid) equilibria of n-alkane mixtures: experimental results, correlation and prediction
Tfus	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	[281.26; 690.01]	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			-8.92900e+00
Coefficient B			1.23884e+00
Coefficient C			-6.83400e-04
Coefficient D			1.43500e-07
Coefficient E			0.00000e+00
Temperature range, min.			273.00
Temperature range, max.			1000.00
Cp,gas	281.26	J/mol×K	273.00	Calculated Property
Cp,gas	350.17	J/mol×K	353.78	Calculated Property
Cp,gas	412.14	J/mol×K	434.56	Calculated Property
Cp,gas	467.64	J/mol×K	515.33	Calculated Property
Cp,gas	517.11	J/mol×K	596.11	Calculated Property
Cp,gas	561.01	J/mol×K	676.89	Calculated Property
Cp,gas	599.80	J/mol×K	757.67	Calculated Property
Cp,gas	633.93	J/mol×K	838.44	Calculated Property
Cp,gas	663.85	J/mol×K	919.22	Calculated Property
Cp,gas	690.01	J/mol×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.0027998; 0.0002323]	Pa×s	[267.62; 472.97]	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			-1.16121e+01
Coefficient B			1.53452e+03
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Temperature range, min.			267.62
Temperature range, max.			472.97
η	0.0027998	Pa×s	267.62	Calculated Property
η	0.0017845	Pa×s	290.44	Calculated Property
η	0.0012145	Pa×s	313.26	Calculated Property
η	0.0008709	Pa×s	336.07	Calculated Property
η	0.0006515	Pa×s	358.89	Calculated Property
η	0.0005045	Pa×s	381.70	Calculated Property
η	0.0004022	Pa×s	404.52	Calculated Property
η	0.0003284	Pa×s	427.34	Calculated Property
η	0.0002738	Pa×s	450.15	Calculated Property
η	0.0002323	Pa×s	472.97	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	[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

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 + 4,7-Methano-1H-indene, octahydro-

Find more mixtures with Tridecane.

Sources

• KDB Vapor Pressure Data
• Cheméo Relay (1.0)
• 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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