Contents
Physical Properties
Temperature Dependent Properties
Pressure Dependent Properties
Datasets
Correlations
Similar Compounds
Mixtures
Sources
Physical Properties
Property
Value
Unit
Source
Δc H°liquid
-5310.00 ± 1.80
kJ/mol
NIST
Δf G°
4.55
kJ/mol
Joback Calculated Property
Δf H°gas
-238.90 ± 1.90
kJ/mol
NIST
Δf H°liquid
-291.30 ± 1.90
kJ/mol
NIST
Δfus H°
20.67
kJ/mol
Joback Calculated Property
Δvap H°
[51.40; 52.42]
kJ/mol
Δvap H°
52.42
kJ/mol
NIST
Δvap H°
51.40
kJ/mol
NIST
Δvap H°
52.40 ± 0.10
kJ/mol
NIST
Δvap H°
52.42 ± 0.12
kJ/mol
NIST
IE
[9.99; 10.10]
eV
IE
9.99
eV
NIST
IE
10.10 ± 0.05
eV
NIST
log 10 WS
-3.32
Crippen Calculated Property
log Poct/wat
3.586
Crippen Calculated Property
McVol
135.820
ml/mol
McGowan Calculated Property
Pc
2443.48
kPa
Joback Calculated Property
Inp
[1043.80; 1066.00]
Inp
1046.00
NIST
Inp
1059.00
NIST
Inp
1064.00
NIST
Inp
1043.80
NIST
Inp
1047.00
NIST
Inp
1051.00
NIST
Inp
1059.00
NIST
Inp
1066.00
NIST
Inp
1051.00
NIST
Inp
1052.00
NIST
Inp
1048.00
NIST
Inp
1059.00
NIST
Inp
1066.00
NIST
Inp
1052.00
NIST
I
[1232.00; 1262.00]
I
1247.00
NIST
I
Outlier 1232.00
NIST
I
1242.00
NIST
I
1251.00
NIST
I
1257.00
NIST
I
1260.00
NIST
I
1262.00
NIST
I
1262.00
NIST
I
1257.00
NIST
Tboil
[451.00; 456.95]
K
Tboil
456.95
K
KDB
Tboil
455.20
K
NIST
Tboil
456.95 ± 0.30
K
NIST
Tboil
451.00 ± 1.50
K
NIST
Tc
590.71
K
Joback Calculated Property
Tfus
209.84
K
Joback Calculated Property
Vc
0.532
m3 /kmol
Joback Calculated Property
Temperature Dependent Properties
Property
Value
Unit
Temperature (K)
Source
Cp,gas
[262.83; 332.22]
J/mol×K
[419.87; 590.71]
Cp,gas
262.83
J/mol×K
419.87
Joback Calculated Property
Cp,gas
275.59
J/mol×K
448.34
Joback Calculated Property
Cp,gas
287.86
J/mol×K
476.82
Joback Calculated Property
Cp,gas
299.64
J/mol×K
505.29
Joback Calculated Property
Cp,gas
310.96
J/mol×K
533.76
Joback Calculated Property
Cp,gas
321.81
J/mol×K
562.24
Joback Calculated Property
Cp,gas
332.22
J/mol×K
590.71
Joback Calculated Property
Cp,liquid
[269.76; 298.14]
J/mol×K
[284.15; 353.15]
Cp,liquid
269.76
J/mol×K
284.15
Heat Ca...
Cp,liquid
270.79
J/mol×K
286.65
Heat Ca...
Cp,liquid
271.83
J/mol×K
289.15
Heat Ca...
Cp,liquid
272.66
J/mol×K
291.65
Heat Ca...
Cp,liquid
273.66
J/mol×K
294.15
Heat Ca...
Cp,liquid
274.53
J/mol×K
296.65
Heat Ca...
Cp,liquid
274.70
J/mol×K
298.15
NIST
Cp,liquid
275.61
J/mol×K
299.15
Heat Ca...
Cp,liquid
276.52
J/mol×K
301.65
Heat Ca...
Cp,liquid
277.29
J/mol×K
304.15
Heat Ca...
Cp,liquid
278.37
J/mol×K
306.65
Heat Ca...
Cp,liquid
279.28
J/mol×K
309.15
Heat Ca...
Cp,liquid
280.50
J/mol×K
311.65
Heat Ca...
Cp,liquid
281.58
J/mol×K
314.15
Heat Ca...
Cp,liquid
282.47
J/mol×K
316.65
Heat Ca...
Cp,liquid
283.79
J/mol×K
319.15
Heat Ca...
Cp,liquid
284.92
J/mol×K
321.65
Heat Ca...
Cp,liquid
285.45
J/mol×K
324.15
Heat Ca...
Cp,liquid
286.81
J/mol×K
326.65
Heat Ca...
Cp,liquid
288.43
J/mol×K
329.15
Heat Ca...
Cp,liquid
289.95
J/mol×K
331.65
Heat Ca...
Cp,liquid
290.13
J/mol×K
334.15
Heat Ca...
Cp,liquid
291.34
J/mol×K
336.65
Heat Ca...
Cp,liquid
291.91
J/mol×K
339.15
Heat Ca...
Cp,liquid
293.56
J/mol×K
341.65
Heat Ca...
Cp,liquid
294.16
J/mol×K
344.15
Heat Ca...
Cp,liquid
294.82
J/mol×K
346.65
Heat Ca...
Cp,liquid
295.79
J/mol×K
349.15
Heat Ca...
Cp,liquid
297.21
J/mol×K
351.65
Heat Ca...
Cp,liquid
298.14
J/mol×K
353.15
Heat Ca...
η
[0.0002789; 0.0052971]
Pa×s
[209.84; 419.87]
η
0.0052971
Pa×s
209.84
Joback Calculated Property
η
0.0022835
Pa×s
244.84
Joback Calculated Property
η
0.0012150
Pa×s
279.85
Joback Calculated Property
η
0.0007439
Pa×s
314.86
Joback Calculated Property
η
0.0005024
Pa×s
349.86
Joback Calculated Property
η
0.0003644
Pa×s
384.87
Joback Calculated Property
η
0.0002789
Pa×s
419.87
Joback Calculated Property
Δvap H
50.30
kJ/mol
392.00
NIST
n 0
1.42820
298.15
Densiti...
ρl
[786.80; 905.50]
kg/m3
[253.15; 393.15]
ρl
905.50
kg/m3
253.15
Density...
ρl
897.10
kg/m3
263.15
Density...
ρl
889.00
kg/m3
273.15
Density...
ρl
880.60
kg/m3
283.15
Density...
ρl
872.30
kg/m3
293.15
Density...
ρl
868.98
kg/m3
298.15
Excess ...
ρl
868.98
kg/m3
298.15
(Vapour...
ρl
868.30
kg/m3
298.15
Density...
ρl
847.40
kg/m3
323.15
Density...
ρl
830.50
kg/m3
343.15
Density...
ρl
813.20
kg/m3
363.15
Density...
ρl
786.80
kg/m3
393.15
Density...
Pressure Dependent Properties
Property
Value
Unit
Pressure (kPa)
Source
Tboilr
351.20
K
2.00
NIST
Datasets
Mass density, kg/m3
Fixed
Measured
Temperature, K - Liquid
Pressure, kPa - Liquid
Mass density, kg/m3 - Liquid
288.15
100.00
877.3
288.15
2000.00
878.8
288.15
4000.00
880.2
288.15
6000.00
881.6
288.15
8000.00
883.0
288.15
10000.00
884.4
288.15
11900.00
885.8
288.15
13900.00
887.1
288.15
16000.00
888.4
288.15
18000.00
889.7
288.15
20100.00
891.2
298.15
100.00
868.8
298.15
2000.00
870.2
298.15
4100.00
871.8
298.15
6100.00
873.3
298.15
8100.00
874.8
298.15
10000.00
876.2
298.15
12100.00
877.8
298.15
14200.00
879.3
298.15
16300.00
880.7
298.15
18300.00
882.1
298.15
20200.00
883.4
308.15
100.00
861.4
308.15
2000.00
862.8
308.15
4000.00
864.4
308.15
6000.00
865.9
308.15
7900.00
867.5
308.15
10100.00
869.1
308.15
12000.00
870.5
308.15
14000.00
872.0
308.15
15900.00
873.3
308.15
18000.00
874.8
308.15
20000.00
876.5
318.15
100.00
852.9
318.15
2000.00
854.5
318.15
4000.00
856.2
318.15
6000.00
857.9
318.15
8000.00
859.5
318.15
10000.00
861.2
318.15
12000.00
862.8
318.15
14000.00
864.3
318.15
16000.00
865.8
318.15
18000.00
867.3
318.15
20100.00
868.9
Reference
Fixed
Measured
Temperature, K - Liquid
Pressure, kPa - Liquid
Mass density, kg/m3 - Liquid
298.15
100.00
868.8
Reference
Correlations
Similar Compounds
Find more compounds similar to Octane, 1-chloro- .
Mixtures
Octane, 1-chloro- + Acetic acid, butyl ester
Octane, 1-chloro- + Formamide, N,N-dimethyl-
Octane, 1-chloro- + N,N-Dimethylacetamide
Octane, 1-chloro- + 2-Pyrrolidinone, 1-methyl-
Octane, 1-chloro- + Octadecane
Octane, 1-chloro- + Nonadecane
Octane, 1-chloro- + Eicosane
Tetracosane + Octane, 1-chloro-
Sources
KDB Vapor Pressure Data
Crippen Method
Crippen Method
Densities, Excess Molar Volumes, Viscosities, and Refractive Indices of Binary Mixtures of n-Butyl Acetate with 1-Chloroalkanes (C4 C8) at 298.15 K
(Vapour + liquid) equilibria and excess molar enthalpies for binary mixtures containing N,N-dialkylamides and 1-chloroalkanes
Excess enthalpies and isothermal (vapour + liquid) equilibria of (1-methyl-2-pyrrolidone + 1-chloroalkane or +,?-dichloroalkane) mixtures
Does Alkyl Chain Length Really Matter? Structure-Property Relationships in Thermochemistry of Ionic Liquids.
Solubilities of Some Long-Chain n-Alkanes in Dipropyl Ether, Dibutyl Ether, 1-Chlorobutane, and 1-Chlorooctane as Functions of Temperature
Heat Capacities of 1-chloroalkanes and 1-bromoalkanes within the temperature range from 284.15 K to 353.15 K. A group additivity and molecular connectivity analysis
Densities and Isothermal Compressibilities at Pressures up to 20 MPa of the Systems N,N-Dimethylformamide or N,N-Dimethylacetamide + 1-Chloroalkane
Density of Some 1-Chloroalkanes within the Temperature Range from (253.15 to 423.15) K
Densities and Isothermal Compressibilities at Pressures up to 20 MPa of the Systems 1-Methyl-2-pyrrolidone + 1-Chloroalkane or + r,u-Dichloroalkane
Joback Method
KDB
McGowan Method
NIST Webbook
The Yaws Handbook of Vapor Pressure
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