Physical Properties
Property
Value
Unit
Source
ω
0.4092
Relay (1.0) Calculated Property
Δf G°
-99.38
kJ/mol
Joback Calculated Property
Δf H°gas
-313.56
kJ/mol
Relay (1.0) Calculated Property
Δfus H°
11.55
kJ/mol
Joback Calculated Property
Δvap H°
38.25
kJ/mol
NIST
IE
9.28
eV
Relay (1.0) Calculated Property
log 10 WS
-1.99
Relay (1.0) Calculated Property
log Poct/wat
2.069
Crippen Calculated Property
McVol
115.360
ml/mol
McGowan Calculated Property
Pc
2773.00
kPa
Joback Calculated Property
Tboil
381.00
K
NIST
Tc
557.21
K
Relay (1.0) Calculated Property
Tfus
151.29
K
Relay (1.0) Calculated Property
Vc
0.432
m3 /kmol
Relay (1.0) Calculated Property
Temperature Dependent Properties
Property
Value
Unit
Temperature (K)
Source
Δvap H
32.55
kJ/mol
381.00
NIST
Pressure Dependent Properties
Property
Value
Unit
Pressure (kPa)
Source
Tboilr
378.70
K
96.00
NIST
Correlations
Property
Value
Unit
Temperature (K)
Source
Cp,gas
[169.07; 399.50]
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 2.03430e+01
Coefficient B 6.11560e-01
Coefficient C -2.49200e-04
Coefficient D 1.68000e-08
Coefficient E 0.00000e+00
Temperature range, min. 273.00
Temperature range, max. 1000.00
Cp,gas
169.07
J/mol×K
273.00
Calculated Property
Cp,gas
206.25
J/mol×K
353.78
Calculated Property
Cp,gas
240.42
J/mol×K
434.56
Calculated Property
Cp,gas
271.62
J/mol×K
515.33
Calculated Property
Cp,gas
299.91
J/mol×K
596.11
Calculated Property
Cp,gas
325.33
J/mol×K
676.89
Calculated Property
Cp,gas
347.95
J/mol×K
757.67
Calculated Property
Cp,gas
367.82
J/mol×K
838.44
Calculated Property
Cp,gas
384.98
J/mol×K
919.22
Calculated Property
Cp,gas
399.50
J/mol×K
1000.00
Calculated Property
Property
Value
Unit
Temperature (K)
Source
η
[0.0068890; 0.0002105]
Pa×s
[175.88; 384.99]
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 -1.13997e+01
Coefficient B 1.12947e+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. 175.88
Temperature range, max. 384.99
η
0.0068890
Pa×s
175.88
Calculated Property
η
0.0032563
Pa×s
199.11
Calculated Property
η
0.0018001
Pa×s
222.35
Calculated Property
η
0.0011132
Pa×s
245.58
Calculated Property
η
0.0007481
Pa×s
268.82
Calculated Property
η
0.0005355
Pa×s
292.05
Calculated Property
η
0.0004027
Pa×s
315.28
Calculated Property
η
0.0003149
Pa×s
338.52
Calculated Property
η
0.0002542
Pa×s
361.75
Calculated Property
η
0.0002105
Pa×s
384.99
Calculated Property
Similar Compounds
Find more compounds similar to Propane, 2-methyl-1-propoxy- .
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