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 2580
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C2H6O |
46.069 |
64-17-5 |
Ethanol |
| 2 |
CHCl3 |
119.377 |
67-66-3 |
Chloroform |
| 3 |
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] |
y1 [mol/mol] |
y2 [mol/mol] |
| 331.77 |
0.09900 |
0.80200 |
0.13900 |
0.74300 |
| 331.48 |
0.20400 |
0.70000 |
0.18200 |
0.68500 |
| 331.19 |
0.09900 |
0.70200 |
0.16600 |
0.62800 |
| 331.58 |
0.30600 |
0.59800 |
0.21700 |
0.63300 |
| 330.83 |
0.20200 |
0.60100 |
0.18700 |
0.58400 |
| 330.87 |
0.09800 |
0.60200 |
0.16600 |
0.55600 |
| 331.97 |
0.40600 |
0.49700 |
0.24600 |
0.58000 |
| 330.86 |
0.30200 |
0.49900 |
0.22000 |
0.52000 |
| 330.61 |
0.20200 |
0.49900 |
0.19700 |
0.49000 |
| 330.93 |
0.09200 |
0.50100 |
0.16500 |
0.48400 |
| 332.70 |
0.51000 |
0.39100 |
0.27900 |
0.51200 |
| 331.31 |
0.40400 |
0.39900 |
0.24000 |
0.45700 |
| 330.66 |
0.30300 |
0.39800 |
0.21900 |
0.42200 |
| 330.51 |
0.20000 |
0.39800 |
0.20200 |
0.40300 |
| 330.98 |
0.09800 |
0.40000 |
0.17600 |
0.40100 |
| 333.43 |
0.61000 |
0.29400 |
0.31600 |
0.43000 |
| 331.42 |
0.51000 |
0.29400 |
0.24900 |
0.38800 |
| 330.95 |
0.41100 |
0.29700 |
0.26700 |
0.33600 |
| 330.66 |
0.30200 |
0.29900 |
0.24800 |
0.31700 |
| 330.73 |
0.20000 |
0.29900 |
0.23200 |
0.30900 |
| 331.31 |
0.09600 |
0.29500 |
0.20600 |
0.31300 |
| 334.64 |
0.71000 |
0.19200 |
0.35100 |
0.32500 |
| 332.35 |
0.60600 |
0.19900 |
0.30300 |
0.27600 |
| 331.46 |
0.50900 |
0.19600 |
0.29300 |
0.24900 |
| 330.99 |
0.40500 |
0.19900 |
0.29600 |
0.22300 |
| 330.88 |
0.30400 |
0.19900 |
0.28100 |
0.21600 |
| 330.95 |
0.19200 |
0.19900 |
0.27300 |
0.21000 |
| 331.58 |
0.09200 |
0.19900 |
0.25100 |
0.21500 |
| 336.86 |
0.81500 |
0.09500 |
0.40600 |
0.17300 |
| 333.37 |
0.70500 |
0.09800 |
0.35700 |
0.13900 |
| 331.98 |
0.60900 |
0.10000 |
0.32500 |
0.12100 |
| 331.49 |
0.50500 |
0.10000 |
0.32800 |
0.11200 |
| 331.29 |
0.41000 |
0.09900 |
0.30700 |
0.10900 |
| 331.12 |
0.30100 |
0.10000 |
0.30000 |
0.10700 |
| 331.34 |
0.19900 |
0.09900 |
0.29900 |
0.10700 |
| 331.94 |
0.09000 |
0.09800 |
0.27700 |
0.11300 |
(T - temperature, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Kudryavtseva L.S.; Susarev M.P.: Dampf-Flüssig-Gleichgewicht im System Ethanol - Chloroform - Hexan bei Temperaturen 55, 45, 35°C und Drucken 760 mmHg. Zh.Prikl.Khim. 36 (1963) 2025-2031 |
Vapor-Liquid Equilibrium Data Set 2581
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C2H6O |
46.069 |
64-17-5 |
Ethanol |
| 2 |
CHCl3 |
119.377 |
67-66-3 |
Chloroform |
| 3 |
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] |
y1 [mol/mol] |
y2 [mol/mol] |
| 42.636 |
0.10000 |
0.80100 |
0.10000 |
0.77400 |
| 42.557 |
0.20200 |
0.70000 |
0.13100 |
0.72700 |
| 43.623 |
0.09000 |
0.70200 |
0.11700 |
0.66500 |
| 42.010 |
0.30400 |
0.59900 |
0.16200 |
0.67500 |
| 43.343 |
0.20100 |
0.60100 |
0.14200 |
0.61400 |
| 43.850 |
0.09900 |
0.60100 |
0.13000 |
0.58000 |
| 41.183 |
0.40400 |
0.49800 |
0.18800 |
0.62000 |
| 43.010 |
0.30100 |
0.49900 |
0.16700 |
0.55600 |
| 43.650 |
0.20100 |
0.49900 |
0.15000 |
0.52000 |
| 43.690 |
0.09400 |
0.50100 |
0.13500 |
0.50000 |
| 40.237 |
0.50700 |
0.39400 |
0.20100 |
0.56200 |
| 42.197 |
0.40300 |
0.39900 |
0.18400 |
0.49000 |
| 43.156 |
0.30200 |
0.39900 |
0.17300 |
0.45100 |
| 43.423 |
0.20000 |
0.39900 |
0.16200 |
0.43100 |
| 43.396 |
0.09800 |
0.40000 |
0.13700 |
0.42200 |
| 38.237 |
0.60700 |
0.29600 |
0.24100 |
0.47100 |
| 41.397 |
0.50700 |
0.29600 |
0.20800 |
0.40200 |
| 42.157 |
0.40800 |
0.29800 |
0.20300 |
0.37000 |
| 42.916 |
0.30100 |
0.30000 |
0.18700 |
0.34500 |
| 42.557 |
0.20000 |
0.30000 |
0.19200 |
0.33100 |
| 42.330 |
0.09800 |
0.29600 |
0.15900 |
0.33700 |
| 35.770 |
0.70700 |
0.19400 |
0.29300 |
0.35300 |
| 39.437 |
0.60500 |
0.19900 |
0.24500 |
0.29700 |
| 41.077 |
0.50600 |
0.19800 |
0.23800 |
0.25800 |
| 41.917 |
0.40400 |
0.19900 |
0.23800 |
0.24100 |
| 42.117 |
0.30300 |
0.19900 |
0.22200 |
0.23700 |
| 42.197 |
0.19500 |
0.19900 |
0.19800 |
0.23500 |
| 41.943 |
0.09500 |
0.19900 |
0.18800 |
0.23500 |
| 31.931 |
0.81100 |
0.09600 |
0.36800 |
0.19500 |
| 37.557 |
0.70400 |
0.09900 |
0.29100 |
0.14900 |
| 39.783 |
0.60600 |
0.10000 |
0.26700 |
0.13100 |
| 40.397 |
0.50400 |
0.10000 |
0.26300 |
0.12200 |
| 40.970 |
0.40700 |
0.09900 |
0.25600 |
0.11800 |
| 41.117 |
0.30100 |
0.10000 |
0.22600 |
0.11900 |
| 41.117 |
0.19900 |
0.10000 |
0.21700 |
0.12000 |
| 40.703 |
0.09200 |
0.09900 |
0.21000 |
0.12400 |
(P - pressure, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Kudryavtseva L.S.; Susarev M.P.: Dampf-Flüssig-Gleichgewicht im System Ethanol - Chloroform - Hexan bei Temperaturen 55, 45, 35°C und Drucken 760 mmHg. Zh.Prikl.Khim. 36 (1963) 2025-2031 |
Vapor-Liquid Equilibrium Data Set 2582
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C2H6O |
46.069 |
64-17-5 |
Ethanol |
| 2 |
CHCl3 |
119.377 |
67-66-3 |
Chloroform |
| 3 |
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] |
y1 [mol/mol] |
y2 [mol/mol] |
| 63.155 |
0.10000 |
0.80000 |
0.12000 |
0.75800 |
| 63.261 |
0.20100 |
0.70000 |
0.15000 |
0.71000 |
| 64.568 |
0.10000 |
0.70100 |
0.12700 |
0.65600 |
| 62.755 |
0.30300 |
0.59900 |
0.18100 |
0.65900 |
| 64.395 |
0.20100 |
0.60000 |
0.17000 |
0.59500 |
| 64.995 |
0.09900 |
0.60100 |
0.14600 |
0.57000 |
| 61.662 |
0.40300 |
0.49800 |
0.20800 |
0.60500 |
| 64.128 |
0.30100 |
0.49900 |
0.18800 |
0.54100 |
| 64.688 |
0.20100 |
0.49900 |
0.17300 |
0.50600 |
| 64.915 |
0.09700 |
0.50000 |
0.15000 |
0.49300 |
| 60.382 |
0.50400 |
0.39600 |
0.23600 |
0.54000 |
| 63.195 |
0.40200 |
0.39900 |
0.20300 |
0.47900 |
| 64.741 |
0.30100 |
0.39900 |
0.19500 |
0.44000 |
| 64.981 |
0.20000 |
0.40000 |
0.18100 |
0.41900 |
| 64.621 |
0.09900 |
0.40000 |
0.15900 |
0.41100 |
| 57.849 |
0.60400 |
0.29700 |
0.26800 |
0.45700 |
| 63.248 |
0.50400 |
0.29700 |
0.24000 |
0.38500 |
| 63.835 |
0.40400 |
0.29900 |
0.23100 |
0.35200 |
| 64.475 |
0.30100 |
0.30000 |
0.22000 |
0.33000 |
| 63.728 |
0.20000 |
0.30000 |
0.20900 |
0.32400 |
| 63.328 |
0.09800 |
0.29800 |
0.18000 |
0.32600 |
| 54.822 |
0.70400 |
0.19700 |
0.31300 |
0.34400 |
| 59.875 |
0.60300 |
0.19900 |
0.26700 |
0.28800 |
| 62.035 |
0.50400 |
0.19800 |
0.25800 |
0.25000 |
| 62.928 |
0.40200 |
0.20000 |
0.25400 |
0.23600 |
| 63.528 |
0.30100 |
0.20000 |
0.24100 |
0.22900 |
| 63.568 |
0.19700 |
0.19900 |
0.23200 |
0.22600 |
| 62.755 |
0.09700 |
0.19900 |
0.22200 |
0.22600 |
| 50.356 |
0.80600 |
0.09800 |
0.38300 |
0.18300 |
| 57.435 |
0.70200 |
0.09900 |
0.31000 |
0.14400 |
| 60.328 |
0.60400 |
0.10000 |
0.29100 |
0.12800 |
| 61.395 |
0.50200 |
0.10000 |
0.28200 |
0.11900 |
| 62.075 |
0.40400 |
0.10000 |
0.27000 |
0.11600 |
| 62.368 |
0.30000 |
0.10000 |
0.26200 |
0.11400 |
| 62.195 |
0.19900 |
0.10000 |
0.25800 |
0.11400 |
| 61.595 |
0.09600 |
0.09900 |
0.23700 |
0.12000 |
(P - pressure, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Kudryavtseva L.S.; Susarev M.P.: Dampf-Flüssig-Gleichgewicht im System Ethanol - Chloroform - Hexan bei Temperaturen 55, 45, 35°C und Drucken 760 mmHg. Zh.Prikl.Khim. 36 (1963) 2025-2031 |
List of All References
Vapor-Liquid Equilibrium Data Overview
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