Physical Properties
Property
Value
Unit
Source
ω
0.6199
Relay (1.0) Calculated Property
Δf G°
9.46
kJ/mol
Joback Calculated Property
Δf H°gas
-305.25
kJ/mol
Relay (1.0) Calculated Property
Δfus H°
30.05
kJ/mol
Joback Calculated Property
Δvap H°
73.10
kJ/mol
NIST
IE
10.19
eV
Relay (1.0) Calculated Property
log 10 WS
-5.85
Relay (1.0) Calculated Property
log Poct/wat
4.585
Crippen Calculated Property
McVol
176.240
ml/mol
McGowan Calculated Property
Pc
1971.80
kPa
Joback Calculated Property
Inp
1526.00
NIST
I
[1916.00; 1918.00]
I
1918.00
NIST
I
1916.00
NIST
I
1916.00
NIST
Tboil
522.38
K
Relay (1.0) Calculated Property
Tc
725.17
K
Relay (1.0) Calculated Property
Tfus
288.75 ± 0.50
K
NIST
Vc
0.686
m3 /kmol
Relay (1.0) Calculated Property
Temperature Dependent Properties
Property
Value
Unit
Temperature (K)
Source
Δvap H
61.10
kJ/mol
480.50
NIST
Pressure Dependent Properties
Property
Value
Unit
Pressure (kPa)
Source
Tboilr
440.70
K
3.70
NIST
Correlations
Property
Value
Unit
Temperature (K)
Source
Cp,gas
[244.43; 551.78]
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 1.95800e+01
Coefficient B 9.67400e-01
Coefficient C -5.61000e-04
Coefficient D 1.25800e-07
Coefficient E 0.00000e+00
Temperature range, min. 273.00
Temperature range, max. 1000.00
Cp,gas
244.43
J/mol×K
273.00
Calculated Property
Cp,gas
297.18
J/mol×K
353.78
Calculated Property
Cp,gas
344.35
J/mol×K
434.56
Calculated Property
Cp,gas
386.35
J/mol×K
515.33
Calculated Property
Cp,gas
423.56
J/mol×K
596.11
Calculated Property
Cp,gas
456.38
J/mol×K
676.89
Calculated Property
Cp,gas
485.22
J/mol×K
757.67
Calculated Property
Cp,gas
510.46
J/mol×K
838.44
Calculated Property
Cp,gas
532.52
J/mol×K
919.22
Calculated Property
Cp,gas
551.78
J/mol×K
1000.00
Calculated Property
Property
Value
Unit
Temperature (K)
Source
η
[0.0026199; 0.0003017]
Pa×s
[288.75; 474.42]
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 -1.14673e+01
Coefficient B 1.59468e+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. 288.75
Temperature range, max. 474.42
η
0.0026199
Pa×s
288.75
Calculated Property
η
0.0018128
Pa×s
309.38
Calculated Property
η
0.0013135
Pa×s
330.01
Calculated Property
η
0.0009884
Pa×s
350.64
Calculated Property
η
0.0007677
Pa×s
371.27
Calculated Property
η
0.0006123
Pa×s
391.90
Calculated Property
η
0.0004996
Pa×s
412.53
Calculated Property
η
0.0004156
Pa×s
433.16
Calculated Property
η
0.0003515
Pa×s
453.79
Calculated Property
η
0.0003017
Pa×s
474.42
Calculated Property
Property
Value
Unit
Temperature (K)
Source
Pvap
[1.33; 202.66]
kPa
[403.32; 568.86]
The Yaws Handbook of Vapor Pressure
Equation ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A 1.48734e+01
Coefficient B -4.59549e+03
Coefficient C -8.82540e+01
Temperature range, min. 403.32
Temperature range, max. 568.86
Pvap
1.33
kPa
403.32
Calculated Property
Pvap
2.98
kPa
421.71
Calculated Property
Pvap
6.13
kPa
440.11
Calculated Property
Pvap
11.72
kPa
458.50
Calculated Property
Pvap
21.09
kPa
476.89
Calculated Property
Pvap
35.99
kPa
495.29
Calculated Property
Pvap
58.63
kPa
513.68
Calculated Property
Pvap
91.74
kPa
532.07
Calculated Property
Pvap
138.52
kPa
550.47
Calculated Property
Pvap
202.66
kPa
568.86
Calculated Property
Similar Compounds
Find more compounds similar to 1,10-Dichlorodecane .
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