Contents
Physical Properties
Temperature Dependent Properties
Pressure Dependent Properties
Datasets
Correlations
Similar Compounds
Mixtures
Sources
Physical Properties
Property
Value
Unit
Source
ω
0.4683
Relay (1.0) Calculated Property
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
-4.73
Relay (1.0) 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
1051.00
NIST
Inp
1052.00
NIST
Inp
1059.00
NIST
Inp
1066.00
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
1257.00
NIST
I
1262.00
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
640.32
K
Relay (1.0) Calculated Property
Tfus
228.17
K
Relay (1.0) Calculated Property
Vc
0.534
m3 /kmol
Relay (1.0) Calculated Property
Temperature Dependent Properties
Property
Value
Unit
Temperature (K)
Source
Cp,liquid
[269.76; 298.14]
J/mol×K
[284.15; 353.15]
Cp,liquid
269.76
J/mol×K
284.15
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
Cp,liquid
270.79
J/mol×K
286.65
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
Cp,liquid
271.83
J/mol×K
289.15
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
Cp,liquid
272.66
J/mol×K
291.65
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
Cp,liquid
273.66
J/mol×K
294.15
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
Cp,liquid
274.53
J/mol×K
296.65
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
Cp,liquid
274.70
J/mol×K
298.15
NIST
Cp,liquid
275.61
J/mol×K
299.15
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
Cp,liquid
276.52
J/mol×K
301.65
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
Cp,liquid
277.29
J/mol×K
304.15
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
Cp,liquid
278.37
J/mol×K
306.65
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
Cp,liquid
279.28
J/mol×K
309.15
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
Cp,liquid
280.50
J/mol×K
311.65
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
Cp,liquid
281.58
J/mol×K
314.15
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
Cp,liquid
282.47
J/mol×K
316.65
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
Cp,liquid
283.79
J/mol×K
319.15
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
Cp,liquid
284.92
J/mol×K
321.65
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
Cp,liquid
285.45
J/mol×K
324.15
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
Cp,liquid
286.81
J/mol×K
326.65
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
Cp,liquid
288.43
J/mol×K
329.15
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
Cp,liquid
289.95
J/mol×K
331.65
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
Cp,liquid
290.13
J/mol×K
334.15
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
Cp,liquid
291.34
J/mol×K
336.65
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
Cp,liquid
291.91
J/mol×K
339.15
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
Cp,liquid
293.56
J/mol×K
341.65
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
Cp,liquid
294.16
J/mol×K
344.15
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
Cp,liquid
294.82
J/mol×K
346.65
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
Cp,liquid
295.79
J/mol×K
349.15
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
Cp,liquid
297.21
J/mol×K
351.65
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
Cp,liquid
298.14
J/mol×K
353.15
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
Δvap H
50.30
kJ/mol
392.00
NIST
n 0
1.42820
298.15
Densities, Excess Molar Volumes, Viscosities, and Refractive Indices of Binary Mixtures of n-Butyl Acetate with 1-Chloroalkanes (C4 C8) at 298.15 K
ρl
[786.80; 905.50]
kg/m3
[253.15; 393.15]
ρl
905.50
kg/m3
253.15
Density of Some 1-Chloroalkanes within the Temperature Range from (253.15 to 423.15) K
ρl
897.10
kg/m3
263.15
Density of Some 1-Chloroalkanes within the Temperature Range from (253.15 to 423.15) K
ρl
889.00
kg/m3
273.15
Density of Some 1-Chloroalkanes within the Temperature Range from (253.15 to 423.15) K
ρl
880.60
kg/m3
283.15
Density of Some 1-Chloroalkanes within the Temperature Range from (253.15 to 423.15) K
ρl
872.30
kg/m3
293.15
Density of Some 1-Chloroalkanes within the Temperature Range from (253.15 to 423.15) K
ρl
868.98
kg/m3
298.15
(Vapour + liquid) equilibria and excess molar enthalpies for binary mixtures containing N,N-dialkylamides and 1-chloroalkanes
ρl
868.98
kg/m3
298.15
Excess enthalpies and isothermal (vapour + liquid) equilibria of (1-methyl-2-pyrrolidone + 1-chloroalkane or +,?-dichloroalkane) mixtures
ρl
868.30
kg/m3
298.15
Density of Some 1-Chloroalkanes within the Temperature Range from (253.15 to 423.15) K
ρl
847.40
kg/m3
323.15
Density of Some 1-Chloroalkanes within the Temperature Range from (253.15 to 423.15) K
ρl
830.50
kg/m3
343.15
Density of Some 1-Chloroalkanes within the Temperature Range from (253.15 to 423.15) K
ρl
813.20
kg/m3
363.15
Density of Some 1-Chloroalkanes within the Temperature Range from (253.15 to 423.15) K
ρl
786.80
kg/m3
393.15
Density of Some 1-Chloroalkanes within the Temperature Range from (253.15 to 423.15) K
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
Property
Value
Unit
Temperature (K)
Source
Cp,gas
[188.60; 440.33]
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 8.50700e+00
Coefficient B 7.70620e-01
Coefficient C -4.31800e-04
Coefficient D 9.30000e-08
Coefficient E 0.00000e+00
Temperature range, min. 273.00
Temperature range, max. 1000.00
Cp,gas
188.60
J/mol×K
273.00
Calculated Property
Cp,gas
231.21
J/mol×K
353.78
Calculated Property
Cp,gas
269.48
J/mol×K
434.56
Calculated Property
Cp,gas
303.69
J/mol×K
515.33
Calculated Property
Cp,gas
334.14
J/mol×K
596.11
Calculated Property
Cp,gas
361.13
J/mol×K
676.89
Calculated Property
Cp,gas
384.95
J/mol×K
757.67
Calculated Property
Cp,gas
405.89
J/mol×K
838.44
Calculated Property
Cp,gas
424.25
J/mol×K
919.22
Calculated Property
Cp,gas
440.33
J/mol×K
1000.00
Calculated Property
Property
Value
Unit
Temperature (K)
Source
η
[0.0052971; 0.0002914]
Pa×s
[209.84; 413.69]
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 -1.11262e+01
Coefficient B 1.23504e+03
Coefficient C 0.00000e+00
Coefficient D 0.00000e+00
Coefficient E 0.00000e+00
Temperature range, min. 209.84
Temperature range, max. 413.69
η
0.0052971
Pa×s
209.84
Calculated Property
η
0.0029855
Pa×s
232.49
Calculated Property
η
0.0018629
Pa×s
255.14
Calculated Property
η
0.0012554
Pa×s
277.79
Calculated Property
η
0.0008979
Pa×s
300.44
Calculated Property
η
0.0006731
Pa×s
323.09
Calculated Property
η
0.0005240
Pa×s
345.74
Calculated Property
η
0.0004207
Pa×s
368.39
Calculated Property
η
0.0003464
Pa×s
391.04
Calculated Property
η
0.0002914
Pa×s
413.69
Calculated Property
Property
Value
Unit
Temperature (K)
Source
Pvap
[1.33; 202.64]
kPa
[346.30; 476.61]
The Yaws Handbook of Vapor Pressure
Equation ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A 1.60368e+01
Coefficient B -4.38150e+03
Coefficient C -6.80900e+01
Temperature range, min. 346.30
Temperature range, max. 476.61
Pvap
1.33
kPa
346.30
Calculated Property
Pvap
2.91
kPa
360.78
Calculated Property
Pvap
5.89
kPa
375.26
Calculated Property
Pvap
11.19
kPa
389.74
Calculated Property
Pvap
20.11
kPa
404.22
Calculated Property
Pvap
34.46
kPa
418.69
Calculated Property
Pvap
56.56
kPa
433.17
Calculated Property
Pvap
89.41
kPa
447.65
Calculated Property
Pvap
136.64
kPa
462.13
Calculated Property
Pvap
202.64
kPa
476.61
Calculated Property
Pvap
[0.75; 102.47]
kPa
[327.15; 457.15]
KDB Vapor Pressure Data
Equation ln(Y) = A + B/T + C·ln(T) + D·T² + E/T² Y is Pvap in kPa, T in K
Coefficient A 1.42325e+02
Coefficient B -1.14740e+04
Coefficient C -1.87950e+01
Coefficient D 1.20730e-05
Coefficient E 0.00000e+00
Temperature range, min. 327.15
Temperature range, max. 457.15
Pvap
0.75
kPa
327.15
Calculated Property
Pvap
1.65
kPa
341.59
Calculated Property
Pvap
3.34
kPa
356.04
Calculated Property
Pvap
6.32
kPa
370.48
Calculated Property
Pvap
11.22
kPa
384.93
Calculated Property
Pvap
18.93
kPa
399.37
Calculated Property
Pvap
30.49
kPa
413.82
Calculated Property
Pvap
47.21
kPa
428.26
Calculated Property
Pvap
70.61
kPa
442.71
Calculated Property
Pvap
102.47
kPa
457.15
Calculated Property
Pvap
[0.75; 102.21]
kPa
[327.30; 457.30]
NIST
Equation ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A 1.37418e+01
Coefficient B -3.38441e+03
Coefficient C -8.59930e+01
Reference Kemme and Kreps, 1969
Temperature range, min. 327.30
Temperature range, max. 457.30
Pvap
0.75
kPa
327.30
Calculated Property
Pvap
1.66
kPa
341.74
Calculated Property
Pvap
3.37
kPa
356.19
Calculated Property
Pvap
6.37
kPa
370.63
Calculated Property
Pvap
11.31
kPa
385.08
Calculated Property
Pvap
19.05
kPa
399.52
Calculated Property
Pvap
30.65
kPa
413.97
Calculated Property
Pvap
47.37
kPa
428.41
Calculated Property
Pvap
70.67
kPa
442.86
Calculated Property
Pvap
102.21
kPa
457.30
Calculated Property
Similar Compounds
Find more compounds similar to Octane, 1-chloro- .
Mixtures
Octane, 1-chloro- + 2-Pyrrolidinone, 1-methyl-
Octane, 1-chloro- + Formamide, N,N-dimethyl-
Octane, 1-chloro- + N,N-Dimethylacetamide
Octane, 1-chloro- + Acetic acid, butyl ester
Octane, 1-chloro- + Octadecane
Octane, 1-chloro- + Nonadecane
Octane, 1-chloro- + Eicosane
Tetracosane + Octane, 1-chloro-
Sources
KDB Vapor Pressure Data
Cheméo Relay (1.0)
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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