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 Dortmund Data Bank
Thermophysical Data for Process Design
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DDB# Name CAS-RN Formula
25 Ethylbenzene 100-41-4 C8H10 Overview Details
31 Benzene 71-43-2 C6H6 Overview Details
50 Cyclohexane 110-82-7 C6H12 Overview Details
89 Hexane 110-54-3 C6H14 Overview Details
91 Heptane 142-82-5 C7H16 Overview Details
128 Octane 111-65-9 C8H18 Overview Details
161 Toluene 108-88-3 C7H8 Overview Details
304 2,3-Dimethylpentane 565-59-3 C7H16 Overview Details
322 o-Xylene 95-47-6 C8H10 Overview Details
651 Xylene (Isomer not specified) 1330-20-7 C8H10 Overview Details
1713 Ethylene carbonate 96-49-1 C3H4O3 Overview Details
3501 N-Cyclohexyl-2-pyrrolidone 6837-24-7 C10H17NO Overview Details
59391 Petroleum naphtha reformate Overview Details
Search for mixtures containing this mixture as subsystem
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Mixture Data

Databank Sets Points Temperature
Range		 Pressure
Range
Vapor-Liquid Equilibria VLE 31 741 283-406 K4-122 kPa
25 31 161
3
25 31 161 322
1
25 31 322
1
25 128 161
1
31 50 89
9
31 50 89 161
2
31 50 91
1
31 50 161
2
31 89 161
2
31 91 161
1
31 128 161
1
31 161 322
1
31 161 651
3
50 89 91
1
50 91 161
2
Heats of Mixing HE 27 375 293-298 K80 kPa (const.)
31 50 89
5
31 50 89 91
1
31 50 89 91 161
1
31 50 91
7
31 50 161
1
31 89 161
1
31 91 161
1
50 89 91 161
1
50 89 128
1
50 89 161
1
50 91 161
7
Liquid-Liquid Equilibria (Miscibility Gaps) LLE 15 71 298-333 Kn.a.
25 91 1713
5
31 50 1713
2
31 91 1713
3
50 161 1713
1
91 161 1713
3
128 161 1713
1
(A)zeotropic Data AZD 10 10 283-343 K40-101 kPa
25 31 161
2
31 50 89
5
31 50 161
1
31 91 161
1
31 128 161
1
Solid-Liquid Equilibria SLE 4 15 276-278 Kn.a.
25 31 161
4
Densities and Volumes of Mixtures, Excess Volumes VE 49 757 293-473 K97-101 kPa
25 128 161
2
31 50 89
22
31 50 91
7
31 50 161
9
50 89 91
1
50 89 161
1
50 91 128
1
50 91 161
2
89 91 128
1
89 91 161
1
91 161 322
2
Critical Data of Mixtures CRI 2 46 508-569 K2496-3033 kPa
31 91 128
1
89 91 128
1
Mixture Viscosities VIS 53 658 293-313 K101 kPa (const.)
25 31 91
4
25 31 91 161
4
25 31 161
4
25 50 89 128
2
25 50 89 128 161
2
25 50 89 161
2
25 50 91 128
2
25 50 91 128 161
2
25 50 91 161
2
25 50 128 161
4
25 89 128 161
2
25 91 128 161
2
25 91 161
4
25 128 161
2
31 50 89
3
31 50 161
1
31 91 161
4
50 89 91
1
50 89 128 161
2
50 89 161
1
50 91 128 161
2
89 91 161
1
Mixture Surface Tensions MSFT 4 69 293-298 Kn.a.
31 50 89
2
31 50 161
1
50 91 161
1
Mixture Speeds of Sound MSOS 10 243 298-318 K100 kPa (const.)
31 50 89
3
31 50 161
1
31 91 128
3
50 89 91
1
50 91 161
1
89 91 161
1
Diffusion Coefficients DIF 4 43 298 K (const.)n.a.
25 89 91
1
31 50 89 91
1
31 89 91
1
89 91 161
1
Further Thermodynamic Properties X 13 111 273-493 K1-4000 kPa
25 31 50 89 91 128 161 304 322 651 1713 3501 59391
1
25 161 651
1
31 50 89
1
31 50 91
3
31 50 128
1
31 50 161
3
31 91 161
3
Total 222 3139
25 31 50 89 91 128 161 304 322 651 1713 3501 59391
1
25 31 91
4
25 31 91 161
4
25 31 161
13
25 31 161 322
1
25 31 322
1
25 50 89 128
2
25 50 89 128 161
2
25 50 89 161
2
25 50 91 128
2
25 50 91 128 161
2
25 50 91 161
2
25 50 128 161
4
25 89 91
1
25 89 128 161
2
25 91 128 161
2
25 91 161
4
25 91 1713
5
25 128 161
5
25 161 651
1
31 50 89
50
31 50 89 91
2
31 50 89 91 161
1
31 50 89 161
2
31 50 91
18
31 50 128
1
31 50 161
19
31 50 1713
2
31 89 91
1
31 89 161
3
31 91 128
4
31 91 161
10
31 91 1713
3
31 128 161
2
31 161 322
1
31 161 651
3
50 89 91
4
50 89 91 161
1
50 89 128
1
50 89 128 161
2
50 89 161
3
50 91 128
1
50 91 128 161
2
50 91 161
13
50 161 1713
1
89 91 128
2
89 91 161
4
91 161 322
2
91 161 1713
3
128 161 1713
1

Dortmund Data Bank Version: February 2024
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