Physical Properties
Property
Value
Unit
Source
ω
0.2960
Relay (1.0) Calculated Property
Δc H°liquid
-4399.77
kJ/mol
NIST
Δf G°
114.52
kJ/mol
Joback Calculated Property
Δf H°gas
-21.83
kJ/mol
Relay (1.0) Calculated Property
Δf H°liquid
-58.24
kJ/mol
NIST
Δfus H°
11.19
kJ/mol
Joback Calculated Property
Δvap H°
[52.40; 52.80]
kJ/mol
Δvap H°
52.80 ± 0.20
kJ/mol
NIST
Δvap H°
52.40
kJ/mol
NIST
IE
9.27
eV
Relay (1.0) Calculated Property
log 10 WS
-2.59
Relay (1.0) Calculated Property
log Poct/wat
2.986
Crippen Calculated Property
McVol
112.060
ml/mol
McGowan Calculated Property
Pc
3526.27
kPa
Joback Calculated Property
Inp
[1039.00; 1060.00]
Inp
1039.00
NIST
Inp
1060.00
NIST
Inp
1044.00
NIST
Inp
1051.00
NIST
Inp
1060.00
NIST
Inp
1051.00
NIST
Tboil
453.64
K
Relay (1.0) Calculated Property
Tc
683.25
K
Relay (1.0) Calculated Property
Tfus
236.17
K
Relay (1.0) Calculated Property
Vc
0.400
m3 /kmol
Relay (1.0) Calculated Property
Temperature Dependent Properties
Property
Value
Unit
Temperature (K)
Source
Δvap H
[47.00; 51.40]
kJ/mol
[354.00; 360.00]
Δvap H
51.40
kJ/mol
354.00
NIST
Δvap H
47.00
kJ/mol
360.00
NIST
Pressure Dependent Properties
Property
Value
Unit
Pressure (kPa)
Source
Tboilr
361.50 ± 0.50
K
4.50
NIST
Correlations
Property
Value
Unit
Temperature (K)
Source
Cp,gas
[131.03; 322.34]
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 -2.70800e+01
Coefficient B 6.97620e-01
Coefficient C -4.66200e-04
Coefficient D 1.18000e-07
Coefficient E 0.00000e+00
Temperature range, min. 273.00
Temperature range, max. 1000.00
Cp,gas
131.03
J/mol×K
273.00
Calculated Property
Cp,gas
166.60
J/mol×K
353.78
Calculated Property
Cp,gas
197.72
J/mol×K
434.56
Calculated Property
Cp,gas
224.77
J/mol×K
515.33
Calculated Property
Cp,gas
248.11
J/mol×K
596.11
Calculated Property
Cp,gas
268.12
J/mol×K
676.89
Calculated Property
Cp,gas
285.18
J/mol×K
757.67
Calculated Property
Cp,gas
299.65
J/mol×K
838.44
Calculated Property
Cp,gas
311.92
J/mol×K
919.22
Calculated Property
Cp,gas
322.34
J/mol×K
1000.00
Calculated Property
Property
Value
Unit
Temperature (K)
Source
η
[0.0050108; 0.0002230]
Pa×s
[221.26; 467.93]
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 -1.12000e+01
Coefficient B 1.30628e+03
Coefficient C 0.00000e+00
Coefficient D 0.00000e+00
Coefficient E 0.00000e+00
Temperature range, min. 221.26
Temperature range, max. 467.93
η
0.0050108
Pa×s
221.26
Calculated Property
η
0.0026140
Pa×s
248.67
Calculated Property
η
0.0015517
Pa×s
276.08
Calculated Property
η
0.0010121
Pa×s
303.48
Calculated Property
η
0.0007086
Pa×s
330.89
Calculated Property
η
0.0005239
Pa×s
358.30
Calculated Property
η
0.0004043
Pa×s
385.71
Calculated Property
η
0.0003230
Pa×s
413.12
Calculated Property
η
0.0002653
Pa×s
440.52
Calculated Property
η
0.0002230
Pa×s
467.93
Calculated Property
Property
Value
Unit
Temperature (K)
Source
Pvap
[1.33; 202.63]
kPa
[340.36; 492.32]
The Yaws Handbook of Vapor Pressure
Equation ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A 1.42544e+01
Coefficient B -3.77816e+03
Coefficient C -6.98500e+01
Temperature range, min. 340.36
Temperature range, max. 492.32
Pvap
1.33
kPa
340.36
Calculated Property
Pvap
3.03
kPa
357.24
Calculated Property
Pvap
6.28
kPa
374.13
Calculated Property
Pvap
12.07
kPa
391.01
Calculated Property
Pvap
21.71
kPa
407.90
Calculated Property
Pvap
36.95
kPa
424.78
Calculated Property
Pvap
59.92
kPa
441.67
Calculated Property
Pvap
93.17
kPa
458.55
Calculated Property
Pvap
139.64
kPa
475.44
Calculated Property
Pvap
202.63
kPa
492.32
Calculated Property
Similar Compounds
Find more compounds similar to Benzene, (1-chloroethyl)- .
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