Physical Properties
Property
Value
Unit
Source
ω
0.3641
Relay (1.0) Calculated Property
Δc H°liquid
-6766.80
kJ/mol
NIST
Δf G°
269.03
kJ/mol
Joback Calculated Property
Δf H°gas
127.13
kJ/mol
Relay (1.0) Calculated Property
Δf H°liquid
56.10
kJ/mol
NIST
Δfus H°
18.18
kJ/mol
Joback Calculated Property
Δvap H°
70.74
kJ/mol
Relay (1.0) Calculated Property
IE
8.90
eV
Relay (1.0) Calculated Property
log 10 WS
-4.21
Relay (1.0) Calculated Property
log Poct/wat
4.015
Crippen Calculated Property
McVol
158.750
ml/mol
McGowan Calculated Property
Pc
2976.29
kPa
Joback Calculated Property
Inp
[1595.70; 1595.70]
Inp
1595.70
NIST
Inp
1595.70
NIST
Tboil
551.86
K
Relay (1.0) Calculated Property
Tc
817.60
K
Relay (1.0) Calculated Property
Tfus
[290.15; 290.15]
K
Tfus
290.15 ± 0.40
K
NIST
Tfus
290.15 ± 0.40
K
NIST
Vc
0.577
m3 /kmol
Relay (1.0) Calculated Property
Temperature Dependent Properties
Property
Value
Unit
Temperature (K)
Source
Cp,gas
[352.58; 431.02]
J/mol×K
[587.39; 841.80]
Cp,gas
352.58
J/mol×K
587.39
Joback Calculated Property
Cp,gas
368.81
J/mol×K
629.79
Joback Calculated Property
Cp,gas
383.66
J/mol×K
672.19
Joback Calculated Property
Cp,gas
397.21
J/mol×K
714.59
Joback Calculated Property
Cp,gas
409.56
J/mol×K
756.99
Joback Calculated Property
Cp,gas
420.80
J/mol×K
799.40
Joback Calculated Property
Cp,gas
431.02
J/mol×K
841.80
Joback Calculated Property
Cp,liquid
[290.40; 295.00]
J/mol×K
[298.50; 310.00]
Cp,liquid
290.40
J/mol×K
298.50
NIST
Cp,liquid
291.00
J/mol×K
300.00
Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid
295.00
J/mol×K
310.00
Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
η
[0.0001785; 0.0031563]
Pa×s
[304.03; 587.39]
η
0.0031563
Pa×s
304.03
Joback Calculated Property
η
0.0014173
Pa×s
351.26
Joback Calculated Property
η
0.0007694
Pa×s
398.48
Joback Calculated Property
η
0.0004754
Pa×s
445.71
Joback Calculated Property
η
0.0003222
Pa×s
492.94
Joback Calculated Property
η
0.0002337
Pa×s
540.16
Joback Calculated Property
η
0.0001785
Pa×s
587.39
Joback Calculated Property
Δvap H
70.40
kJ/mol
415.50
NIST
Pressure Dependent Properties
Property
Value
Unit
Pressure (kPa)
Source
Tboilr
413.20
K
0.40
NIST
Correlations
Property
Value
Unit
Temperature (K)
Source
Pvap
[1.33; 202.63]
kPa
[435.78; 630.88]
The Yaws Handbook of Vapor Pressure
Equation ln(Pvp) = A + B/(T + C) Coefficient A 1.65327e+01 Coefficient B -7.07929e+03 Temperature range, min. 435.78
Temperature range, max. 630.88
Pvap
1.33
kPa
435.78
Calculated Property
Pvap
2.88
kPa
457.46
Calculated Property
Pvap
5.80
kPa
479.14
Calculated Property
Pvap
10.99
kPa
500.81
Calculated Property
Pvap
19.76
kPa
522.49
Calculated Property
Pvap
33.90
kPa
544.17
Calculated Property
Pvap
55.80
kPa
565.85
Calculated Property
Pvap
88.53
kPa
587.52
Calculated Property
Pvap
135.93
kPa
609.20
Calculated Property
Pvap
202.63
kPa
630.88
Calculated Property
Similar Compounds
Find more compounds similar to Benzene, 1,1'-(chloromethylene)bis- .
Sources
Cheméo Relay (1.0)
Crippen Method
Crippen Method
Joback Method
McGowan Method
NIST Webbook
The Yaws Handbook of Vapor Pressure
Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
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