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 Dortmund Data Bank
Thermophysical Data for Process Design
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DDB# Name CAS-RN Formula
31 Benzene 71-43-2 C6H6 Overview Details
50 Cyclohexane 110-82-7 C6H12 Overview Details
60 Decane 124-18-5 C10H22 Overview Details
78 Dodecane 112-40-3 C12H26 Overview Details
89 Hexane 110-54-3 C6H14 Overview Details
91 Heptane 142-82-5 C7H16 Overview Details
97 2,2,4-Trimethylpentane 540-84-1 C8H18 Overview Details
112 3-Methylpentane 96-14-0 C6H14 Overview Details
128 Octane 111-65-9 C8H18 Overview Details
154 Tetradecane 629-59-4 C14H30 Overview Details
161 Toluene 108-88-3 C7H8 Overview Details
367 2,3-Dimethylbutane 79-29-8 C6H14 Overview Details
370 2,2-Dimethylbutane 75-83-2 C6H14 Overview Details
388 Tridecane 629-50-5 C13H28 Overview Details
398 Nonane 111-84-2 C9H20 Overview Details
485 Eicosane 112-95-8 C20H42 Overview Details
516 Hexadecane 544-76-3 C16H34 Overview Details
553 Heptadecane 629-78-7 C17H36 Overview Details
651 Xylene (Isomer not specified) 1330-20-7 C8H10 Overview Details
724 n-Undecane 1120-21-4 C11H24 Overview Details
727 Pentadecane 629-62-9 C15H32 Overview Details
760 2-Methylhexane 591-76-4 C7H16 Overview Details
1130 Octadecane 593-45-3 C18H38 Overview Details
3443 2-Methyldecane 6975-98-0 C11H24 Overview Details
9847 2-Methylundecane 7045-71-8 C12H26 Overview Details
45290 C6+ fraction Overview Details
45326 Isohexanes 73513-42-5 C6H14 Overview Details
45327 Isoheptanes 31394-54-4 C7H16 Overview Details
45329 Isononanes C9H20 Overview Details
58546 Isodecanes C10H22 Overview Details
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Mixture Data

Databank Sets Points Temperature
Range		 Pressure
Range
Vapor-Liquid Equilibria VLE 31 767 283-384 K2-122 kPa
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 91 760
3
31 128 161
1
31 161 651
3
50 89 91
1
50 91 161
2
89 91 97
3
89 128 516
1
Heats of Mixing HE 43 975 293-298 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 60 154
1
31 89 161
1
31 91 154
1
31 91 161
1
31 154 161
1
50 78 89
1
50 78 97
1
50 78 370
1
50 89 91 161
1
50 89 128
1
50 89 161
1
50 91 161
7
50 97 128
1
50 128 370
1
78 89 97
1
78 89 370
3
89 97 128
1
89 128 370
3
(A)zeotropic Data AZD 11 11 283-343 K27-101 kPa
31 50 89
5
31 50 161
1
31 91 161
1
31 91 760
3
31 128 161
1
Solid-Liquid Equilibria SLE 24 283 180-311 K90-100300 kPa
50 91 1130
5
60 91 128
7
78 154 724
3
154 388 516 727
1
154 388 727
1
154 516 724 1130
1
154 516 727
1
154 516 1130
1
516 553 727
1
516 553 1130
2
516 724 1130
1
Densities and Volumes of Mixtures, Excess Volumes VE 141 1733 293-473 K97-101 kPa
31 50 89
22
31 50 91
7
31 50 161
9
31 89 516
1
50 60 91
1
50 60 97
7
50 89 91
1
50 89 161
1
50 91 128
1
50 91 161
2
50 91 398
1
60 78 91 128
3
60 78 154
1
60 89 91
1
60 89 128
1
60 89 154
1
60 91 128
3
60 91 388 516
2
60 112 154
1
60 128 724 727
2
60 154 367
1
60 154 370
1
60 388 516
1
60 388 1130
8
78 89 128
1
78 89 398
1
78 91 128 516
2
78 128 485 516
2
78 128 516
1
78 154 516
1
89 91 128
1
89 91 161
1
89 128 154
30
89 154 516
1
91 97 128
3
91 128 388 724
4
91 128 388 724 727
1
91 128 398
1
128 154 161
2
128 154 161 516
2
128 154 516
2
128 161 516
2
128 388 724 727
2
154 161 516
2
Critical Data of Mixtures CRI 2 46 508-569 K2496-3033 kPa
31 91 128
1
89 91 128
1
Mixture Viscosities VIS 112 1287 288-393 K100-100000 kPa
31 50 60 89
1
31 50 89
3
31 50 154
32
31 50 161
1
31 89 516
1
31 91 161
4
50 60 97
7
50 89 91
1
50 89 128 161
2
50 89 161
1
50 91 128 161
2
60 78 89 516
2
60 78 154 516
15
60 91 388 516
2
60 128 724 727
2
78 89 128 516
1
78 91 128 516
2
78 91 398 516
2
89 91 161
1
89 128 154
6
89 128 516
1
89 154 516
1
91 97 128
3
91 97 161
1
91 128 388 724
4
91 128 388 724 727
1
91 128 398
1
128 154 161
2
128 154 161 516
2
128 154 516
2
128 161 516
2
128 388 724 727
2
154 161 516
2
Mixture Surface Tensions MSFT 25 751 293-373 K101 kPa (const.)
31 50 89
2
31 50 161
1
50 60 97
7
50 91 161
1
89 128 154
6
91 516 724
8
Mixture Speeds of Sound MSOS 23 469 298-433 K100-100100 kPa
31 50 60 89
1
31 50 89
3
31 50 161
1
31 91 128
3
50 89 91
1
50 91 161
1
60 91 128 398
1
78 128 516
11
89 91 161
1
Mixture Thermal Conductivities MTCN 3 46 294-344 K101 kPa (const.)
31 50 97
2
91 516 724
1
Diffusion Coefficients DIF 4 42 298 K (const.)n.a.
31 50 60 89
1
31 50 89 91
1
31 89 91
1
89 91 161
1
Further Thermodynamic Properties X 23 269 243-493 K100-30000 kPa
31 50 60 78 89 91 97 112 128 154 161 367 370 388 398 485 516 553 651 724 727 760 1130 3443 9847 45290 45326 45327 45329 58546
1
31 50 78
1
31 50 89
1
31 50 91
3
31 50 128
1
31 50 161
3
31 91 161
3
60 78 89
1
78 89 161
1
78 516 1130
4
161 516 1130
4
Total 442 6679
31 50 60 78 89 91 97 112 128 154 161 367 370 388 398 485 516 553 651 724 727 760 1130 3443 9847 45290 45326 45327 45329 58546
1
31 50 60 89
3
31 50 78
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 97
2
31 50 128
1
31 50 154
32
31 50 161
19
31 60 154
1
31 89 91
1
31 89 161
3
31 89 516
2
31 91 128
4
31 91 154
1
31 91 161
10
31 91 760
6
31 128 161
2
31 154 161
1
31 161 651
3
50 60 91
1
50 60 97
21
50 78 89
1
50 78 97
1
50 78 370
1
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 91 398
1
50 91 1130
5
50 97 128
1
50 128 370
1
60 78 89
1
60 78 89 516
2
60 78 91 128
3
60 78 154
1
60 78 154 516
15
60 89 91
1
60 89 128
1
60 89 154
1
60 91 128
10
60 91 128 398
1
60 91 388 516
4
60 112 154
1
60 128 724 727
4
60 154 367
1
60 154 370
1
60 388 516
1
60 388 1130
8
78 89 97
1
78 89 128
1
78 89 128 516
1
78 89 161
1
78 89 370
3
78 89 398
1
78 91 128 516
4
78 91 398 516
2
78 128 485 516
2
78 128 516
12
78 154 516
1
78 154 724
3
78 516 1130
4
89 91 97
3
89 91 128
2
89 91 161
4
89 97 128
1
89 128 154
42
89 128 370
3
89 128 516
2
89 154 516
2
91 97 128
6
91 97 161
1
91 128 388 724
8
91 128 388 724 727
2
91 128 398
2
91 516 724
9
128 154 161
4
128 154 161 516
4
128 154 516
4
128 161 516
4
128 388 724 727
4
154 161 516
4
154 388 516 727
1
154 388 727
1
154 516 724 1130
1
154 516 727
1
154 516 1130
1
161 516 1130
4
516 553 727
1
516 553 1130
2
516 724 1130
1

Dortmund Data Bank Version: February 2024
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