Physical Properties
Temperature Dependent Properties
Property
Value
Unit
Temperature (K)
Source
Δvap H
61.50
kJ/mol
459.50
NIST
Pressure Dependent Properties
Property
Value
Unit
Pressure (kPa)
Source
Tboilr
[397.20; 441.50]
K
[0.30; 2.70]
Tboilr
397.20
K
0.30
NIST
Tboilr
441.50 ± 0.50
K
2.70
NIST
Correlations
Property
Value
Unit
Temperature (K)
Source
Cp,gas
[209.18; 556.14]
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 -7.85570e+01
Coefficient B 1.27100e+00
Coefficient C -8.54600e-04
Coefficient D 2.18300e-07
Coefficient E 0.00000e+00
Temperature range, min. 273.00
Temperature range, max. 1000.00
Cp,gas
209.18
J/mol×K
273.00
Calculated Property
Cp,gas
273.80
J/mol×K
353.78
Calculated Property
Cp,gas
330.30
J/mol×K
434.56
Calculated Property
Cp,gas
379.35
J/mol×K
515.33
Calculated Property
Cp,gas
421.66
J/mol×K
596.11
Calculated Property
Cp,gas
457.91
J/mol×K
676.89
Calculated Property
Cp,gas
488.80
J/mol×K
757.67
Calculated Property
Cp,gas
515.00
J/mol×K
838.44
Calculated Property
Cp,gas
537.22
J/mol×K
919.22
Calculated Property
Cp,gas
556.14
J/mol×K
1000.00
Calculated Property
Property
Value
Unit
Temperature (K)
Source
η
[0.0068850; 0.0001771]
Pa×s
[265.65; 581.66]
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 -1.17154e+01
Coefficient B 1.78968e+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. 265.65
Temperature range, max. 581.66
η
0.0068850
Pa×s
265.65
Calculated Property
η
0.0031357
Pa×s
300.76
Calculated Property
η
0.0016834
Pa×s
335.87
Calculated Property
η
0.0010166
Pa×s
370.99
Calculated Property
η
0.0006699
Pa×s
406.10
Calculated Property
η
0.0004717
Pa×s
441.21
Calculated Property
η
0.0003498
Pa×s
476.32
Calculated Property
η
0.0002703
Pa×s
511.43
Calculated Property
η
0.0002159
Pa×s
546.54
Calculated Property
η
0.0001771
Pa×s
581.66
Calculated Property
Property
Value
Unit
Temperature (K)
Source
Pvap
[1.33; 202.64]
kPa
[427.16; 609.63]
The Yaws Handbook of Vapor Pressure
Equation ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A 1.45693e+01
Coefficient B -4.80231e+03
Coefficient C -9.09030e+01
Temperature range, min. 427.16
Temperature range, max. 609.63
Pvap
1.33
kPa
427.16
Calculated Property
Pvap
3.00
kPa
447.43
Calculated Property
Pvap
6.20
kPa
467.71
Calculated Property
Pvap
11.88
kPa
487.98
Calculated Property
Pvap
21.39
kPa
508.26
Calculated Property
Pvap
36.45
kPa
528.53
Calculated Property
Pvap
59.25
kPa
548.81
Calculated Property
Pvap
92.42
kPa
569.08
Calculated Property
Pvap
139.05
kPa
589.36
Calculated Property
Pvap
202.64
kPa
609.63
Calculated Property
Similar Compounds
Find more compounds similar to Benzene, 1,1'-(1,3-propanediyl)bis- .
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