Contents
Physical Properties
Temperature Dependent Properties
Datasets
Correlations
Similar Compounds
Mixtures
Sources
Physical Properties
Property
Value
Unit
Source
Δf G°
-24.22
kJ/mol
Joback Calculated Property
Δf H°gas
-198.65
kJ/mol
Joback Calculated Property
Δfus H°
19.69
kJ/mol
Joback Calculated Property
Δvap H°
37.72
kJ/mol
Joback Calculated Property
log 10 WS
-2.64
Crippen Calculated Property
log Poct/wat
3.024
Crippen Calculated Property
McVol
119.880
ml/mol
McGowan Calculated Property
Pc
2865.80
kPa
Joback Calculated Property
I
1536.00
NIST
Tboil
411.54
K
Joback Calculated Property
Tc
591.61
K
Joback Calculated Property
Tfus
217.22
K
Joback Calculated Property
Vc
0.469
m3 /kmol
Joback Calculated Property
Temperature Dependent Properties
Property
Value
Unit
Temperature (K)
Source
Cp,gas
[212.25; 266.73]
J/mol×K
[411.54; 591.61]
Cp,gas
212.25
J/mol×K
411.54
Joback Calculated Property
Cp,gas
222.36
J/mol×K
441.55
Joback Calculated Property
Cp,gas
232.05
J/mol×K
471.56
Joback Calculated Property
Cp,gas
241.32
J/mol×K
501.57
Joback Calculated Property
Cp,gas
250.18
J/mol×K
531.58
Joback Calculated Property
Cp,gas
258.64
J/mol×K
561.59
Joback Calculated Property
Cp,gas
266.73
J/mol×K
591.61
Joback Calculated Property
Cp,liquid
[236.59; 247.76]
J/mol×K
[283.15; 323.15]
Cp,liquid
236.59
J/mol×K
283.15
Heat Ca...
Cp,liquid
237.90
J/mol×K
288.15
Heat Ca...
Cp,liquid
239.26
J/mol×K
293.15
Heat Ca...
Cp,liquid
239.21
J/mol×K
293.15
Thermod...
Cp,liquid
239.50
J/mol×K
294.15
Thermod...
Cp,liquid
239.69
J/mol×K
295.15
Thermod...
Cp,liquid
240.02
J/mol×K
296.15
Thermod...
Cp,liquid
240.35
J/mol×K
297.15
Thermod...
Cp,liquid
240.64
J/mol×K
298.15
Thermod...
Cp,liquid
240.60
J/mol×K
298.15
Heat Ca...
Cp,liquid
240.85
J/mol×K
299.15
Thermod...
Cp,liquid
241.15
J/mol×K
300.15
Thermod...
Cp,liquid
241.46
J/mol×K
301.15
Thermod...
Cp,liquid
241.80
J/mol×K
302.15
Thermod...
Cp,liquid
242.06
J/mol×K
303.15
Thermod...
Cp,liquid
241.94
J/mol×K
303.15
Heat Ca...
Cp,liquid
242.34
J/mol×K
304.15
Thermod...
Cp,liquid
242.62
J/mol×K
305.15
Thermod...
Cp,liquid
242.83
J/mol×K
306.15
Thermod...
Cp,liquid
243.21
J/mol×K
307.15
Thermod...
Cp,liquid
243.49
J/mol×K
308.15
Thermod...
Cp,liquid
243.37
J/mol×K
308.15
Heat Ca...
Cp,liquid
243.73
J/mol×K
309.15
Thermod...
Cp,liquid
244.00
J/mol×K
310.15
Thermod...
Cp,liquid
244.35
J/mol×K
311.15
Thermod...
Cp,liquid
244.68
J/mol×K
312.15
Thermod...
Cp,liquid
244.91
J/mol×K
313.15
Thermod...
Cp,liquid
244.81
J/mol×K
313.15
Heat Ca...
Cp,liquid
246.28
J/mol×K
318.15
Heat Ca...
Cp,liquid
247.76
J/mol×K
323.15
Heat Ca...
η
[0.0003287; 0.0046414]
Pa×s
[217.22; 411.54]
η
0.0046414
Pa×s
217.22
Joback Calculated Property
η
0.0022422
Pa×s
249.61
Joback Calculated Property
η
0.0012802
Pa×s
281.99
Joback Calculated Property
η
0.0008204
Pa×s
314.38
Joback Calculated Property
η
0.0005713
Pa×s
346.77
Joback Calculated Property
η
0.0004232
Pa×s
379.15
Joback Calculated Property
η
0.0003287
Pa×s
411.54
Joback Calculated Property
n 0
1.45550
298.15
Thermod...
ρl
[1063.70; 1063.70]
kg/m3
[298.15; 298.15]
ρl
1063.70
kg/m3
298.15
Excess ...
ρl
1063.70
kg/m3
298.15
Excess ...
γ
[0.03; 0.04]
N/m
[293.15; 313.15]
γ
0.04
N/m
293.15
The add...
γ
0.03
N/m
298.15
The add...
γ
0.03
N/m
303.15
The add...
γ
0.03
N/m
308.15
The add...
γ
0.03
N/m
313.15
The add...
Datasets
Mass density, kg/m3
Fixed
Measured
Temperature, K - Liquid
Pressure, kPa - Liquid
Mass density, kg/m3 - Liquid
288.15
100.00
1073.7
288.15
500.00
1073.9
288.15
1000.00
1074.3
288.15
1600.00
1074.6
288.15
2000.00
1075.0
288.15
2500.00
1075.3
288.15
3100.00
1075.7
288.15
3600.00
1076.0
288.15
4100.00
1076.3
288.15
4600.00
1076.6
288.15
5100.00
1076.9
288.15
5600.00
1077.3
288.15
6100.00
1077.6
288.15
6500.00
1077.9
288.15
7100.00
1078.3
288.15
7600.00
1078.5
288.15
8100.00
1078.9
288.15
8600.00
1079.2
288.15
9100.00
1079.5
288.15
9600.00
1079.9
288.15
10100.00
1080.2
288.15
10600.00
1080.5
288.15
11100.00
1080.8
288.15
11600.00
1081.2
288.15
12100.00
1081.5
288.15
12600.00
1081.8
288.15
13100.00
1082.1
288.15
13600.00
1082.4
288.15
14200.00
1082.8
288.15
14700.00
1083.0
288.15
15200.00
1083.4
288.15
15700.00
1083.7
288.15
16300.00
1084.0
288.15
16800.00
1084.3
288.15
17300.00
1084.6
288.15
17800.00
1084.9
288.15
18300.00
1085.3
288.15
18800.00
1085.5
288.15
19200.00
1085.7
288.15
19700.00
1086.0
288.15
20200.00
1086.5
298.15
100.00
1063.8
298.15
500.00
1064.2
298.15
1000.00
1064.4
298.15
1500.00
1064.8
298.15
2000.00
1065.2
298.15
2500.00
1065.5
298.15
3100.00
1065.9
298.15
3600.00
1066.3
298.15
4100.00
1066.7
298.15
4500.00
1066.9
298.15
5000.00
1067.3
298.15
5600.00
1067.6
298.15
6100.00
1068.0
298.15
6600.00
1068.4
298.15
7100.00
1068.7
298.15
7600.00
1069.0
298.15
8100.00
1069.4
298.15
8600.00
1069.7
298.15
9200.00
1070.1
298.15
9600.00
1070.4
298.15
10100.00
1070.7
298.15
10600.00
1071.1
298.15
11000.00
1071.3
298.15
11700.00
1071.7
298.15
12100.00
1071.9
298.15
12600.00
1072.3
298.15
13100.00
1072.6
298.15
13600.00
1072.9
298.15
14200.00
1073.3
298.15
14700.00
1073.6
298.15
15200.00
1074.0
298.15
15700.00
1074.3
298.15
16400.00
1074.8
298.15
16800.00
1075.2
298.15
17300.00
1075.5
298.15
17800.00
1075.8
298.15
18300.00
1076.1
298.15
18700.00
1076.4
298.15
19200.00
1076.7
298.15
19700.00
1076.9
298.15
20200.00
1077.3
308.15
100.00
1054.6
308.15
500.00
1054.9
308.15
1000.00
1055.2
308.15
1500.00
1055.5
308.15
2000.00
1055.9
308.15
2500.00
1056.3
308.15
3100.00
1056.7
308.15
3600.00
1057.1
308.15
4100.00
1057.4
308.15
4600.00
1057.8
308.15
5100.00
1058.2
308.15
5600.00
1058.5
308.15
6100.00
1058.9
308.15
6600.00
1059.2
308.15
7100.00
1059.6
308.15
7600.00
1059.8
308.15
8100.00
1060.2
308.15
8600.00
1060.6
308.15
9200.00
1061.0
308.15
9600.00
1061.4
308.15
10100.00
1061.7
308.15
10600.00
1062.1
308.15
11100.00
1062.4
308.15
11600.00
1062.7
308.15
12100.00
1063.1
308.15
12600.00
1063.5
308.15
13100.00
1063.8
308.15
13600.00
1064.1
308.15
14100.00
1064.5
308.15
14800.00
1064.9
308.15
15100.00
1065.1
308.15
15700.00
1065.5
308.15
16200.00
1065.8
308.15
16700.00
1066.2
308.15
17300.00
1066.6
308.15
17800.00
1066.9
308.15
18300.00
1067.2
308.15
18700.00
1067.4
308.15
19200.00
1067.8
308.15
19700.00
1068.0
308.15
20300.00
1068.5
318.15
100.00
1045.1
318.15
500.00
1045.3
318.15
1000.00
1045.7
318.15
1500.00
1046.2
318.15
2000.00
1046.6
318.15
2500.00
1046.9
318.15
3100.00
1047.4
318.15
3600.00
1047.8
318.15
4100.00
1048.1
318.15
4600.00
1048.4
318.15
5100.00
1048.9
318.15
5600.00
1049.2
318.15
6100.00
1049.7
318.15
6600.00
1050.0
318.15
7100.00
1050.4
318.15
7600.00
1050.7
318.15
8100.00
1051.2
318.15
8500.00
1051.4
318.15
9100.00
1051.8
318.15
9600.00
1052.2
318.15
10100.00
1052.6
318.15
10700.00
1053.1
318.15
11100.00
1053.6
318.15
11600.00
1053.9
318.15
12100.00
1054.1
318.15
12600.00
1054.5
318.15
13100.00
1054.8
318.15
13600.00
1055.3
318.15
14200.00
1055.6
318.15
14700.00
1056.0
318.15
15200.00
1056.3
318.15
15600.00
1056.6
318.15
16300.00
1057.1
318.15
16800.00
1057.3
318.15
17300.00
1057.7
318.15
17800.00
1058.0
318.15
18300.00
1058.3
318.15
18900.00
1058.8
318.15
19200.00
1059.0
318.15
19700.00
1059.3
318.15
20200.00
1059.6
Reference
Fixed
Measured
Temperature, K - Liquid
Pressure, kPa - Liquid
Mass density, kg/m3 - Liquid
298.15
100.00
1063.8
Reference
Correlations
Property
Value
Unit
Temperature (K)
Source
Pvap
[1.33; 202.67]
kPa
[366.72; 503.12]
The Yaw...
Equation ln(Pvp) = A + B/(T + C) Coefficient A 1.61007e+01 Coefficient B -4.63200e+03 Coefficient C -7.37980e+01 Temperature range, min. 366.72
Temperature range, max. 503.12
Pvap
1.33
kPa
366.72
Calculated Property
Pvap
2.90
kPa
381.88
Calculated Property
Pvap
5.87
kPa
397.03
Calculated Property
Pvap
11.16
kPa
412.19
Calculated Property
Pvap
20.07
kPa
427.34
Calculated Property
Pvap
34.38
kPa
442.50
Calculated Property
Pvap
56.47
kPa
457.65
Calculated Property
Pvap
89.30
kPa
472.81
Calculated Property
Pvap
136.56
kPa
487.96
Calculated Property
Pvap
202.67
kPa
503.12
Calculated Property
Similar Compounds
Find more compounds similar to Hexane, 1,6-dichloro- .
Mixtures
Ethyl Acetate + Hexane, 1,6-dichloro-
Butanoic acid, ethyl ester + Hexane, 1,6-dichloro-
Pentanoic acid, ethyl ester + Hexane, 1,6-dichloro-
Ethyl formate + Hexane, 1,6-dichloro-
Propanoic acid, ethyl ester + Hexane, 1,6-dichloro-
Formic acid, butyl ester + Hexane, 1,6-dichloro-
Propanoic acid, butyl ester + Hexane, 1,6-dichloro-
Acetic acid, butyl ester + Hexane, 1,6-dichloro-
Butanoic acid, butyl ester + Hexane, 1,6-dichloro-
Formamide, N,N-dimethyl- + Hexane, 1,6-dichloro-
N,N-Dimethylacetamide + Hexane, 1,6-dichloro-
2-Pyrrolidinone, 1-methyl- + Hexane, 1,6-dichloro-
Formic acid, propyl ester + Hexane, 1,6-dichloro-
n-Propyl acetate + Hexane, 1,6-dichloro-
Propanoic acid, propyl ester + Hexane, 1,6-dichloro-
Butanoic acid, propyl ester + Hexane, 1,6-dichloro-
Dodecane + Hexane, 1,6-dichloro-
Heptane + Hexane, 1,6-dichloro-
Methyl formate + Hexane, 1,6-dichloro-
Formic acid, pentyl ester + Hexane, 1,6-dichloro-
Find more mixtures with Hexane, 1,6-dichloro- .
Sources
Crippen Method
Crippen Method
Thermodynamic study of (alkyl esters + a,x-alkyl dihalides) I: HE and V E for 25 binary mixtures {xCu-1H2u-1CO2C2H5 + (1-x)a,x-ClCH2(CH2)v-2CH2Cl}, where u = 1 to 5, a = 1 and v = x = 2 to 6
Thermodynamic study of (alkyl esters + a,x-alkyl dihalides)III. HE m and V E m for 20 binary mixtures {xCu-1H2u-1CO2C4H9 + (1 - x)a,x-ClCH2(CH2)v-2CH2Cl}, where u = 1 to 4, a = 1 and v = x = 2 to 6
Thermodynamic study of (alkyl esters + a,x-alkyl dihalides) V. Hex and Vex for 25 binary mixtures {xCu-1H2u-1CO2CH3 + (1-x)a,x-ClCH2(CH2)v-2CH2Cl}, where u = 1 to 5, a = 1 and v = x = 2 to 6
Excess molar enthalpies and (vapour + liquid) equilibria for mixtures containing N,N-dialkylamides and a,x-dichloroalkanes
Excess enthalpies and isothermal (vapour + liquid) equilibria of (1-methyl-2-pyrrolidone + 1-chloroalkane or +,?-dichloroalkane) mixtures
Thermodynamic study of (alkyl esters + a,x-alkyl dihalides) VII. HE m and VE m for 20 binary mixtures {xCu 1H2u 1CO2C3H7 + (1 x)a,x-ClCH2(CH2)v 2CH2Cl}, where u = 1 to 4, a = 1 and v = x = 2 to 6. An analysis of behavior using the COSMO-RS methodology
The additivity of surface and volumetric properties of alpha,omega-dihalogenoalkanes
Heat Capacities of alpha,omega-Dichloroalkanes at Temperatures from 284.15 K to 353.15 K and a Group Additivity Analysis
Heat Capacities, Densities, and Speeds of Sound for {(1,5-Dichloropentane or 1,6-Dichlorohexane) + Dodecane}
Thermodynamic and Acoustic Properties of Mixtures of 1,6-Dichlorohexane with Heptane from (293 to 313) K
Densities and Isothermal Compressibilities at Pressures up to 20 MPa of the Systems N,N-Dimethylformamide or N,N-Dimethylacetamide + r,o-Dichloroalkane
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
McGowan Method
NIST Webbook
The Yaws Handbook of Vapor Pressure
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