Dortmund Data Bank
Vapor-Liquid Equilibrium Data
The experimental data shown in these pages are freely available and have been published already in the DDB Explorer Edition. The data represent a small sub list of all available data in the Dortmund Data Bank. For more data or any further information please search the DDB or contact DDBST.
Vapor-Liquid Equilibrium Data Set 17556
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C2H6O |
46.069 |
64-17-5 |
Ethanol |
| 2 |
C3H6O |
58.080 |
67-64-1 |
Acetone |
| 3 |
C6H6 |
78.114 |
71-43-2 |
Benzene |
| 4 |
C6H14 |
86.177 |
110-54-3 |
Hexane |
Search the DDB for all data of this mixture
Constant Value
Data Table
| T [K] |
x1 [mol/mol] |
x2 [mol/mol] |
x3 [mol/mol] |
| 330.40 |
0.33200 |
0.26480 |
0.22130 |
| 330.04 |
0.30290 |
0.35960 |
0.20230 |
| 329.78 |
0.30000 |
0.51880 |
0.10880 |
| 328.04 |
0.10240 |
0.71430 |
0.10520 |
| 331.17 |
0.46550 |
0.37080 |
0.08920 |
| 333.61 |
0.60340 |
0.23990 |
0.09180 |
| 330.97 |
0.10490 |
0.50230 |
0.31170 |
| 332.62 |
0.29470 |
0.34070 |
0.28750 |
| 334.85 |
0.47970 |
0.18400 |
0.26820 |
| 334.23 |
0.11490 |
0.32110 |
0.48450 |
| 336.23 |
0.30680 |
0.14580 |
0.47760 |
| 337.48 |
0.11310 |
0.14170 |
0.66190 |
| 330.38 |
0.09990 |
0.33280 |
0.34030 |
| 333.83 |
0.11090 |
0.14330 |
0.48980 |
| 326.04 |
0.10060 |
0.53450 |
0.11210 |
| 328.35 |
0.12590 |
0.15340 |
0.12310 |
| 326.01 |
0.09830 |
0.38100 |
0.11090 |
| 330.76 |
0.11290 |
0.15470 |
0.29630 |
| 326.31 |
0.11340 |
0.31490 |
0.11310 |
| 331.19 |
0.09650 |
0.14830 |
0.33000 |
| 330.44 |
0.10180 |
0.24050 |
0.35000 |
| 335.09 |
0.10820 |
0.08720 |
0.53380 |
| 351.30 |
1.00000 |
0.00000 |
0.00000 |
| 329.34 |
0.00000 |
1.00000 |
0.00000 |
| 353.26 |
0.00000 |
0.00000 |
1.00000 |
| 341.95 |
0.00000 |
0.00000 |
0.00000 |
(T - temperature, x - liquid mole fraction)
Reference
| Source |
| Li H.; Han S.: Vapor-Liquid Equilibria for the Quaternary System Ethanol + Acetone + Benzene + Hexane. J.Chem.Eng.Data 42 (1997) 655-657 |
Vapor-Liquid Equilibrium Data Set 17557
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C2H6O |
46.069 |
64-17-5 |
Ethanol |
| 2 |
C3H6O |
58.080 |
67-64-1 |
Acetone |
| 3 |
C6H6 |
78.114 |
71-43-2 |
Benzene |
| 4 |
C6H14 |
86.177 |
110-54-3 |
Hexane |
Search the DDB for all data of this mixture
Constant Value
Data Table
| P [kPa] |
x1 [mol/mol] |
x2 [mol/mol] |
x3 [mol/mol] |
| 43.830 |
0.33200 |
0.26480 |
0.22130 |
| 44.710 |
0.30290 |
0.35960 |
0.20230 |
| 44.990 |
0.30000 |
0.51880 |
0.10880 |
| 48.900 |
0.10240 |
0.71430 |
0.10520 |
| 42.650 |
0.46550 |
0.37080 |
0.08920 |
| 38.260 |
0.60340 |
0.23990 |
0.09180 |
| 43.530 |
0.10490 |
0.50230 |
0.31170 |
| 40.319 |
0.29470 |
0.34070 |
0.28750 |
| 36.190 |
0.47970 |
0.18400 |
0.26820 |
| 38.410 |
0.11490 |
0.32110 |
0.48450 |
| 34.131 |
0.30680 |
0.14580 |
0.47760 |
| 33.580 |
0.11310 |
0.14170 |
0.66190 |
| 44.600 |
0.09990 |
0.33280 |
0.34030 |
| 39.079 |
0.11090 |
0.14330 |
0.48980 |
| 52.580 |
0.10060 |
0.53450 |
0.11210 |
| 47.549 |
0.12590 |
0.15340 |
0.12310 |
| 52.480 |
0.09830 |
0.38100 |
0.11090 |
| 43.660 |
0.11290 |
0.15470 |
0.29630 |
| 51.800 |
0.11340 |
0.31490 |
0.11310 |
| 43.040 |
0.09650 |
0.14830 |
0.33000 |
| 44.240 |
0.10180 |
0.24050 |
0.35000 |
| 36.940 |
0.10820 |
0.08720 |
0.53380 |
(P - pressure, x - liquid mole fraction)
Reference
| Source |
| Li H.; Han S.: Vapor-Liquid Equilibria for the Quaternary System Ethanol + Acetone + Benzene + Hexane. J.Chem.Eng.Data 42 (1997) 655-657 |
Vapor-Liquid Equilibrium Data Set 17558
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C2H6O |
46.069 |
64-17-5 |
Ethanol |
| 2 |
C3H6O |
58.080 |
67-64-1 |
Acetone |
| 3 |
C6H6 |
78.114 |
71-43-2 |
Benzene |
| 4 |
C6H14 |
86.177 |
110-54-3 |
Hexane |
Search the DDB for all data of this mixture
Constant Value
Data Table
| P [kPa] |
x1 [mol/mol] |
x2 [mol/mol] |
x3 [mol/mol] |
| 64.851 |
0.33200 |
0.26480 |
0.22130 |
| 65.920 |
0.30290 |
0.35960 |
0.20230 |
| 66.631 |
0.30000 |
0.51880 |
0.10880 |
| 71.539 |
0.10240 |
0.71430 |
0.10520 |
| 63.109 |
0.46550 |
0.37080 |
0.08920 |
| 57.210 |
0.60340 |
0.23990 |
0.09180 |
| 64.109 |
0.10490 |
0.50230 |
0.31170 |
| 59.840 |
0.29470 |
0.34070 |
0.28750 |
| 54.400 |
0.47970 |
0.18400 |
0.26820 |
| 56.950 |
0.11490 |
0.32110 |
0.48450 |
| 51.600 |
0.30680 |
0.14580 |
0.47760 |
| 50.271 |
0.11310 |
0.14170 |
0.66190 |
| 65.631 |
0.09990 |
0.33280 |
0.34030 |
| 57.681 |
0.11090 |
0.14330 |
0.48980 |
| 76.680 |
0.10060 |
0.53450 |
0.11210 |
| 70.050 |
0.12590 |
0.15340 |
0.12310 |
| 76.590 |
0.09830 |
0.38100 |
0.11090 |
| 64.389 |
0.11290 |
0.15470 |
0.29630 |
| 75.690 |
0.11340 |
0.31490 |
0.11310 |
| 63.509 |
0.09650 |
0.14830 |
0.33000 |
| 65.240 |
0.10180 |
0.24050 |
0.35000 |
| 54.979 |
0.10820 |
0.08720 |
0.53380 |
(P - pressure, x - liquid mole fraction)
Reference
| Source |
| Li H.; Han S.: Vapor-Liquid Equilibria for the Quaternary System Ethanol + Acetone + Benzene + Hexane. J.Chem.Eng.Data 42 (1997) 655-657 |
List of All References
Vapor-Liquid Equilibrium Data Overview
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