Physical Properties
Property
Value
Unit
Source
ω
0.4872
Relay (1.0) Calculated Property
PAff
857.70
kJ/mol
NIST
BasG
826.80
kJ/mol
NIST
Δf G°
-182.69
kJ/mol
Joback Calculated Property
Δf H°gas
-309.13
kJ/mol
Relay (1.0) Calculated Property
Δfus H°
17.09
kJ/mol
Joback Calculated Property
Δvap H°
64.61
kJ/mol
Relay (1.0) Calculated Property
IE
[8.50; 9.20]
eV
IE
8.50
eV
NIST
IE
9.20
eV
NIST
log 10 WS
-2.53
Relay (1.0) Calculated Property
log Poct/wat
1.782
Crippen Calculated Property
McVol
121.350
ml/mol
McGowan Calculated Property
Pc
3224.64
kPa
Joback Calculated Property
Inp
[203.97; 1235.00]
Inp
1206.00
NIST
Inp
1205.70
NIST
Inp
1235.00
NIST
Inp
1171.00
NIST
Inp
1190.00
NIST
Inp
203.97
NIST
Inp
1206.00
NIST
Inp
1205.70
NIST
Inp
203.97
NIST
Inp
1190.00
NIST
Ip
[1744.00; 1744.00]
Ip
1744.00
NIST
Ip
1744.00
NIST
Tboil
489.76
K
Relay (1.0) Calculated Property
Tc
701.96
K
Relay (1.0) Calculated Property
Tfus
260.62
K
Relay (1.0) Calculated Property
Vc
0.448
m3 /kmol
Relay (1.0) Calculated Property
Temperature Dependent Properties
Property
Value
Unit
Temperature (K)
Source
Δfus H
[17.14; 21.15]
kJ/mol
[162.50; 269.90]
Δfus H
17.14
kJ/mol
162.50
NIST
Δfus H
21.15
kJ/mol
269.90
NIST
Δvap H
[53.50; 60.30]
kJ/mol
[296.00; 429.50]
Δvap H
60.30 ± 0.20
kJ/mol
296.00
NIST
Δvap H
53.50
kJ/mol
388.00
NIST
Δvap H
54.80
kJ/mol
429.50
NIST
Pressure Dependent Properties
Property
Value
Unit
Pressure (kPa)
Source
Tboilr
386.20
K
3.60
NIST
Correlations
Property
Value
Unit
Temperature (K)
Source
Cp,gas
[158.04; 370.19]
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 5.10000e-01
Coefficient B 6.65640e-01
Coefficient C -3.35360e-04
Coefficient D 3.94000e-08
Coefficient E 0.00000e+00
Temperature range, min. 273.00
Temperature range, max. 1000.00
Cp,gas
158.04
J/mol×K
273.00
Calculated Property
Cp,gas
195.77
J/mol×K
353.78
Calculated Property
Cp,gas
229.67
J/mol×K
434.56
Calculated Property
Cp,gas
259.87
J/mol×K
515.33
Calculated Property
Cp,gas
286.48
J/mol×K
596.11
Calculated Property
Cp,gas
309.64
J/mol×K
676.89
Calculated Property
Cp,gas
329.46
J/mol×K
757.67
Calculated Property
Cp,gas
346.08
J/mol×K
838.44
Calculated Property
Cp,gas
359.61
J/mol×K
919.22
Calculated Property
Cp,gas
370.19
J/mol×K
1000.00
Calculated Property
Property
Value
Unit
Temperature (K)
Source
η
[0.0025707; 0.0002036]
Pa×s
[272.46; 496.88]
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 -1.15782e+01
Coefficient B 1.52976e+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. 272.46
Temperature range, max. 496.88
η
0.0025707
Pa×s
272.46
Calculated Property
η
0.0016055
Pa×s
297.40
Calculated Property
η
0.0010784
Pa×s
322.33
Calculated Property
η
0.0007670
Pa×s
347.27
Calculated Property
η
0.0005710
Pa×s
372.20
Calculated Property
η
0.0004411
Pa×s
397.14
Calculated Property
η
0.0003513
Pa×s
422.07
Calculated Property
η
0.0002870
Pa×s
447.01
Calculated Property
η
0.0002395
Pa×s
471.94
Calculated Property
η
0.0002036
Pa×s
496.88
Calculated Property
Similar Compounds
Find more compounds similar to Benzoic acid, 3-methyl-, methyl ester .
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