Physical Properties
Temperature Dependent Properties
Pressure Dependent Properties
Property
Value
Unit
Pressure (kPa)
Source
Tboilr
369.20
K
1.60
NIST
Correlations
Property
Value
Unit
Temperature (K)
Source
Cp,gas
[218.54; 524.26]
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 1.15700e+00
Coefficient B 9.25840e-01
Coefficient C -5.01500e-04
Coefficient D 9.87600e-08
Coefficient E 0.00000e+00
Temperature range, min. 273.00
Temperature range, max. 1000.00
Cp,gas
218.54
J/mol×K
273.00
Calculated Property
Cp,gas
270.30
J/mol×K
353.78
Calculated Property
Cp,gas
316.89
J/mol×K
434.56
Calculated Property
Cp,gas
358.61
J/mol×K
515.33
Calculated Property
Cp,gas
395.77
J/mol×K
596.11
Calculated Property
Cp,gas
428.70
J/mol×K
676.89
Calculated Property
Cp,gas
457.70
J/mol×K
757.67
Calculated Property
Cp,gas
483.08
J/mol×K
838.44
Calculated Property
Cp,gas
505.17
J/mol×K
919.22
Calculated Property
Cp,gas
524.26
J/mol×K
1000.00
Calculated Property
Property
Value
Unit
Temperature (K)
Source
η
[0.0026273; 0.0002900]
Pa×s
[277.99; 470.26]
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 -1.13314e+01
Coefficient B 1.49823e+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. 277.99
Temperature range, max. 470.26
η
0.0026273
Pa×s
277.99
Calculated Property
η
0.0017884
Pa×s
299.35
Calculated Property
η
0.0012813
Pa×s
320.71
Calculated Property
η
0.0009571
Pa×s
342.08
Calculated Property
η
0.0007398
Pa×s
363.44
Calculated Property
η
0.0005885
Pa×s
384.80
Calculated Property
η
0.0004795
Pa×s
406.17
Calculated Property
η
0.0003988
Pa×s
427.53
Calculated Property
η
0.0003375
Pa×s
448.90
Calculated Property
η
0.0002900
Pa×s
470.26
Calculated Property
Property
Value
Unit
Temperature (K)
Source
Pvap
[1.33; 202.64]
kPa
[364.18; 514.40]
The Yaws Handbook of Vapor Pressure
Equation ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A 1.49652e+01
Coefficient B -4.23681e+03
Coefficient C -7.55210e+01
Temperature range, min. 364.18
Temperature range, max. 514.40
Pvap
1.33
kPa
364.18
Calculated Property
Pvap
2.97
kPa
380.87
Calculated Property
Pvap
6.10
kPa
397.56
Calculated Property
Pvap
11.67
kPa
414.25
Calculated Property
Pvap
21.00
kPa
430.94
Calculated Property
Pvap
35.85
kPa
447.64
Calculated Property
Pvap
58.45
kPa
464.33
Calculated Property
Pvap
91.53
kPa
481.02
Calculated Property
Pvap
138.35
kPa
497.71
Calculated Property
Pvap
202.64
kPa
514.40
Calculated Property
Similar Compounds
Find more compounds similar to 2-Decanone .
Mixtures
Sources
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 7 ChEDL chemicals 1.5.2, from Kudchadker, A. P.; Ambrose, D.; Tsonopoulos, C. Vapor-Liquid Critical Properties of Elements and Compounds. 7. Oxygen Compounds Other Than Alkanols and Cycloalkanols. J. Chem. Eng. Data 2001, 46, 457-479.
Cheméo Relay (1.0)
Crippen Method
Excess molar enthalpies of binary mixtures containing 2-decanone or dipentyl ether with long-chain n-alkanes at T = 298.15 K
Joback Method
Aqueous Solubility Prediction Method
Estimated Solubility Method
McGowan Method
NIST Webbook
The Yaws Handbook of Vapor Pressure
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