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 2598
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C6H6 |
78.114 |
71-43-2 |
Benzene |
| 2 |
C2H6O |
46.069 |
64-17-5 |
Ethanol |
| 3 |
C6H14 |
86.177 |
110-54-3 |
Hexane |
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Constant Value
Data Table
| T [K] |
x1 [mol/mol] |
x2 [mol/mol] |
y1 [mol/mol] |
y2 [mol/mol] |
| 334.05 |
0.10800 |
0.05200 |
0.07700 |
0.24000 |
| 334.95 |
0.22100 |
0.04600 |
0.15900 |
0.23000 |
| 333.05 |
0.21800 |
0.18500 |
0.15400 |
0.30000 |
| 334.85 |
0.32700 |
0.07300 |
0.22400 |
0.24900 |
| 333.85 |
0.30300 |
0.30700 |
0.22900 |
0.33300 |
| 337.85 |
0.62500 |
0.07900 |
0.42100 |
0.24500 |
| 339.35 |
0.71900 |
0.18300 |
0.52000 |
0.32500 |
(T - temperature, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Waldo R.A.; Weber J.H.: Vapor-Liquid Equilibrium at Atmospheric Pressure: The Ternary System Benzene-Ethanol-n-Hexane. J.Chem.Eng.Data 8 (1963) 349-354 |
Vapor-Liquid Equilibrium Data Set 2599
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C6H14 |
86.177 |
110-54-3 |
Hexane |
| 2 |
C2H6O |
46.069 |
64-17-5 |
Ethanol |
| 3 |
C6H6 |
78.114 |
71-43-2 |
Benzene |
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Constant Value
Data Table
| P [kPa] |
x1 [mol/mol] |
x2 [mol/mol] |
y1 [mol/mol] |
y2 [mol/mol] |
| 64.461 |
0.02300 |
0.54800 |
0.06100 |
0.44700 |
| 62.728 |
0.02800 |
0.75900 |
0.12400 |
0.52500 |
| 54.182 |
0.03000 |
0.92800 |
0.19800 |
0.67700 |
| 62.795 |
0.04000 |
0.14100 |
0.06800 |
0.30600 |
| 54.902 |
0.04600 |
0.03800 |
0.08100 |
0.18900 |
| 69.034 |
0.05900 |
0.52600 |
0.14500 |
0.39900 |
| 72.114 |
0.07400 |
0.64000 |
0.20100 |
0.44100 |
| 72.181 |
0.08300 |
0.72600 |
0.27000 |
0.44400 |
| 73.114 |
0.08700 |
0.79300 |
0.33800 |
0.47700 |
| 70.661 |
0.08900 |
0.34500 |
0.15800 |
0.36700 |
| 74.674 |
0.09500 |
0.84300 |
0.37100 |
0.43700 |
| 67.514 |
0.10500 |
0.11900 |
0.17000 |
0.30600 |
| 69.928 |
0.10700 |
0.23400 |
0.16400 |
0.33800 |
| 74.461 |
0.11600 |
0.45900 |
0.23800 |
0.38500 |
| 58.515 |
0.11800 |
0.01400 |
0.20500 |
0.14300 |
| 73.127 |
0.16800 |
0.20100 |
0.23700 |
0.31500 |
| 80.127 |
0.17400 |
0.63000 |
0.37200 |
0.40600 |
| 77.994 |
0.18300 |
0.43400 |
0.31000 |
0.37100 |
| 82.487 |
0.19600 |
0.69400 |
0.43500 |
0.42900 |
| 71.754 |
0.22300 |
0.10400 |
0.27000 |
0.26600 |
| 81.593 |
0.22400 |
0.52300 |
0.37800 |
0.37300 |
| 77.314 |
0.22700 |
0.28100 |
0.23000 |
0.37500 |
| 84.753 |
0.25300 |
0.63300 |
0.46500 |
0.40300 |
| 81.060 |
0.27200 |
0.37200 |
0.36900 |
0.34900 |
| 83.980 |
0.29900 |
0.46100 |
0.43700 |
0.35000 |
| 73.874 |
0.31400 |
0.09900 |
0.32300 |
0.25300 |
| 86.180 |
0.33500 |
0.48700 |
0.50000 |
0.34100 |
| 81.287 |
0.38100 |
0.20700 |
0.41600 |
0.30300 |
| 88.179 |
0.39600 |
0.52800 |
0.55300 |
0.36700 |
| 79.900 |
0.40000 |
0.13800 |
0.41800 |
0.27300 |
| 77.420 |
0.43700 |
0.07900 |
0.41600 |
0.27200 |
| 89.313 |
0.44300 |
0.53500 |
0.59400 |
0.38100 |
| 85.006 |
0.46000 |
0.27100 |
0.47600 |
0.33000 |
| 67.088 |
0.47300 |
0.01500 |
0.52300 |
0.09200 |
| 88.473 |
0.54600 |
0.33800 |
0.55800 |
0.34600 |
| 85.326 |
0.56100 |
0.21300 |
0.51400 |
0.32500 |
| 82.913 |
0.58700 |
0.11700 |
0.48000 |
0.28000 |
| 84.380 |
0.62500 |
0.14300 |
0.53200 |
0.29500 |
| 87.526 |
0.63700 |
0.23300 |
0.59400 |
0.32300 |
| 86.393 |
0.71800 |
0.14500 |
0.60900 |
0.30000 |
| 75.020 |
0.73800 |
0.02600 |
0.65700 |
0.15600 |
| 87.659 |
0.75800 |
0.18600 |
0.63100 |
0.32400 |
| 80.140 |
0.89500 |
0.04200 |
0.73700 |
0.21900 |
(P - pressure, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Yuan K.S.; Lu B.C-Y.; Deshpande A.K.; Ho J.C.K.: Part III. System Ethanol - Cyclohexane at Atmospheric Pressure. J.Chem.Eng.Data 8 (1963) 549-559 |
Vapor-Liquid Equilibrium Data Set 12433
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C6H14 |
86.177 |
110-54-3 |
Hexane |
| 2 |
C2H6O |
46.069 |
64-17-5 |
Ethanol |
| 3 |
C6H6 |
78.114 |
71-43-2 |
Benzene |
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Constant Value
Data Table
| T [K] |
x1 [mol/mol] |
x2 [mol/mol] |
y1 [mol/mol] |
y2 [mol/mol] |
| 343.15 |
0.03800 |
0.11800 |
0.07000 |
0.29600 |
| 340.25 |
0.03200 |
0.29800 |
0.07600 |
0.41400 |
| 339.85 |
0.02200 |
0.44900 |
0.02500 |
0.45600 |
| 340.05 |
0.02000 |
0.54800 |
0.07000 |
0.46700 |
| 340.65 |
0.01900 |
0.62500 |
0.07400 |
0.49800 |
| 342.95 |
0.03100 |
0.70400 |
0.08100 |
0.56800 |
| 344.25 |
0.02200 |
0.83200 |
0.08200 |
0.66600 |
| 347.05 |
0.01800 |
0.91600 |
0.07500 |
0.77500 |
| 341.45 |
0.08200 |
0.11500 |
0.12600 |
0.32800 |
| 338.15 |
0.05200 |
0.45600 |
0.12400 |
0.43100 |
| 338.15 |
0.05300 |
0.59100 |
0.15300 |
0.46900 |
| 339.65 |
0.06100 |
0.67500 |
0.21000 |
0.48100 |
| 340.45 |
0.04600 |
0.79900 |
0.24800 |
0.52100 |
| 342.65 |
0.03200 |
0.89600 |
0.24200 |
0.63100 |
| 339.65 |
0.16100 |
0.13800 |
0.26100 |
0.31100 |
| 337.35 |
0.12600 |
0.33700 |
0.26200 |
0.37000 |
| 336.65 |
0.13600 |
0.47400 |
0.28900 |
0.39000 |
| 336.65 |
0.14900 |
0.57200 |
0.31400 |
0.42000 |
| 339.65 |
0.07500 |
0.77700 |
0.27900 |
0.53600 |
| 340.35 |
0.29000 |
0.13700 |
0.34800 |
0.31000 |
| 337.95 |
0.29300 |
0.12100 |
0.36600 |
0.30300 |
| 335.65 |
0.22300 |
0.36700 |
0.35000 |
0.35500 |
| 335.35 |
0.21500 |
0.48100 |
0.36600 |
0.35100 |
| 335.65 |
0.20900 |
0.61300 |
0.46600 |
0.36400 |
| 336.65 |
0.15500 |
0.76100 |
0.46800 |
0.43900 |
| 336.15 |
0.40000 |
0.10700 |
0.42200 |
0.30000 |
| 334.65 |
0.31200 |
0.36900 |
0.43300 |
0.34900 |
| 334.15 |
0.26200 |
0.55000 |
0.49700 |
0.34800 |
| 333.95 |
0.29100 |
0.62500 |
0.55700 |
0.36300 |
| 335.15 |
0.53800 |
0.15300 |
0.48800 |
0.27500 |
| 333.35 |
0.45600 |
0.34400 |
0.53400 |
0.32500 |
| 333.65 |
0.64700 |
0.14100 |
0.57600 |
0.28100 |
| 333.65 |
0.63300 |
0.18200 |
0.57900 |
0.28600 |
| 332.35 |
0.59900 |
0.32300 |
0.63500 |
0.30800 |
| 333.15 |
0.76200 |
0.15900 |
0.65800 |
0.27500 |
| 335.85 |
0.93200 |
0.03400 |
0.79200 |
0.17600 |
| 349.15 |
0.01300 |
0.95900 |
0.05600 |
0.86500 |
| 348.15 |
0.01600 |
0.05600 |
0.03100 |
0.20900 |
(T - temperature, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Park J.O.; Nam S.J.: (Vapor-Liquid Equilibria of Benzene(1)-n-Heptane(2)-Toluene(3) and n-Hexane(1)-Ethanol(2)-Benzene(3) Systems). Hwahak Konghak 24 (1986) 311-319 |
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Vapor-Liquid Equilibrium Data Overview
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