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 3853
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C3H6O |
58.080 |
67-64-1 |
Acetone |
| 2 |
CH4O |
32.042 |
67-56-1 |
Methanol |
| 3 |
C6H12 |
84.161 |
110-82-7 |
Cyclohexane |
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Constant Value
Data Table
| P [kPa] |
x1 [mol/mol] |
x2 [mol/mol] |
y1 [mol/mol] |
y2 [mol/mol] |
| 50.103 |
0.11900 |
0.12800 |
0.29200 |
0.34700 |
| 50.343 |
0.12000 |
0.25000 |
0.23500 |
0.39100 |
| 50.249 |
0.11900 |
0.37800 |
0.20900 |
0.42000 |
| 49.689 |
0.12100 |
0.50100 |
0.18200 |
0.44700 |
| 49.396 |
0.12300 |
0.62900 |
0.18500 |
0.44800 |
| 47.783 |
0.12500 |
0.75000 |
0.18500 |
0.47800 |
| 52.196 |
0.25000 |
0.12300 |
0.42500 |
0.24000 |
| 52.489 |
0.25000 |
0.25500 |
0.36200 |
0.30500 |
| 51.929 |
0.25700 |
0.36500 |
0.32500 |
0.34200 |
| 51.716 |
0.25300 |
0.49700 |
0.30700 |
0.36600 |
| 50.316 |
0.25000 |
0.62500 |
0.32400 |
0.38700 |
| 52.329 |
0.36600 |
0.13500 |
0.49500 |
0.19400 |
| 53.316 |
0.38100 |
0.24200 |
0.44800 |
0.24700 |
| 53.169 |
0.40300 |
0.35700 |
0.43000 |
0.28200 |
| 51.822 |
0.37500 |
0.50000 |
0.43000 |
0.31700 |
| 53.262 |
0.52200 |
0.10200 |
0.57500 |
0.13500 |
| 53.836 |
0.53700 |
0.21400 |
0.53500 |
0.18900 |
| 52.529 |
0.50000 |
0.37500 |
0.52000 |
0.25300 |
| 52.982 |
0.66600 |
0.07800 |
0.64400 |
0.09500 |
| 52.769 |
0.64100 |
0.23800 |
0.60700 |
0.18800 |
| 52.076 |
0.81900 |
0.05600 |
0.73100 |
0.07800 |
(P - pressure, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Marinichev A.N.; Susarev M.P.: Investigation of Phase Equilibria in the System Acetone-Methanol-Cyclohexane. J.Appl.Chem.USSR 38 (1965) 1034-1037 |
Vapor-Liquid Equilibrium Data Set 3854
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C3H6O |
58.080 |
67-64-1 |
Acetone |
| 2 |
CH4O |
32.042 |
67-56-1 |
Methanol |
| 3 |
C6H12 |
84.161 |
110-82-7 |
Cyclohexane |
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Constant Value
Data Table
| P [kPa] |
x1 [mol/mol] |
x2 [mol/mol] |
y1 [mol/mol] |
y2 [mol/mol] |
| 74.661 |
0.11700 |
0.12700 |
0.27600 |
0.36700 |
| 75.514 |
0.11800 |
0.24800 |
0.21700 |
0.42400 |
| 75.674 |
0.11800 |
0.37900 |
0.19100 |
0.45200 |
| 75.074 |
0.12100 |
0.50100 |
0.17200 |
0.46600 |
| 74.767 |
0.12300 |
0.63100 |
0.17600 |
0.47100 |
| 71.327 |
0.12500 |
0.75200 |
0.17800 |
0.49700 |
| 79.167 |
0.24900 |
0.12000 |
0.41500 |
0.25200 |
| 78.074 |
0.24800 |
0.25400 |
0.35000 |
0.32200 |
| 77.954 |
0.25500 |
0.36900 |
0.31200 |
0.36700 |
| 77.594 |
0.25400 |
0.49700 |
0.29000 |
0.39100 |
| 75.460 |
0.25000 |
0.62600 |
0.31400 |
0.41200 |
| 78.274 |
0.37000 |
0.13100 |
0.48800 |
0.20000 |
| 79.087 |
0.38200 |
0.23900 |
0.43300 |
0.26700 |
| 79.153 |
0.40500 |
0.37500 |
0.41400 |
0.30300 |
| 77.234 |
0.37900 |
0.49700 |
0.41400 |
0.34300 |
| 78.327 |
0.52400 |
0.09800 |
0.57700 |
0.13400 |
| 79.647 |
0.53700 |
0.21400 |
0.52600 |
0.20200 |
| 77.807 |
0.51100 |
0.36900 |
0.50700 |
0.27500 |
| 77.807 |
0.66900 |
0.07600 |
0.65400 |
0.08800 |
| 76.540 |
0.64700 |
0.23200 |
0.60900 |
0.19300 |
| 76.487 |
0.82200 |
0.05400 |
0.74300 |
0.07600 |
(P - pressure, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Marinichev A.N.; Susarev M.P.: Investigation of Phase Equilibria in the System Acetone-Methanol-Cyclohexane. J.Appl.Chem.USSR 38 (1965) 1034-1037 |
Vapor-Liquid Equilibrium Data Set 3855
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C3H6O |
58.080 |
67-64-1 |
Acetone |
| 2 |
CH4O |
32.042 |
67-56-1 |
Methanol |
| 3 |
C6H12 |
84.161 |
110-82-7 |
Cyclohexane |
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] |
| 109.591 |
0.11300 |
0.12600 |
0.26100 |
0.38400 |
| 111.724 |
0.11600 |
0.24500 |
0.20300 |
0.44700 |
| 111.857 |
0.11600 |
0.37900 |
0.17700 |
0.47300 |
| 111.724 |
0.12100 |
0.50100 |
0.16200 |
0.48700 |
| 111.324 |
0.12400 |
0.63400 |
0.15900 |
0.49900 |
| 107.991 |
0.12400 |
0.75600 |
0.16500 |
0.53200 |
| 111.857 |
0.24800 |
0.11500 |
0.40200 |
0.27100 |
| 114.391 |
0.24400 |
0.25200 |
0.32000 |
0.36100 |
| 114.791 |
0.25200 |
0.37500 |
0.29200 |
0.39300 |
| 114.524 |
0.25600 |
0.49500 |
0.27900 |
0.41300 |
| 111.324 |
0.24900 |
0.63000 |
0.29600 |
0.44500 |
| 112.924 |
0.37600 |
0.12200 |
0.47500 |
0.21400 |
| 115.191 |
0.38400 |
0.23500 |
0.42700 |
0.27900 |
| 115.724 |
0.40700 |
0.37300 |
0.39600 |
0.32400 |
| 113.057 |
0.38000 |
0.50000 |
0.39200 |
0.38200 |
| 113.457 |
0.52800 |
0.09000 |
0.58000 |
0.13700 |
| 115.324 |
0.53700 |
0.21400 |
0.50900 |
0.22700 |
| 113.591 |
0.51500 |
0.36500 |
0.50800 |
0.27800 |
| 114.391 |
0.67500 |
0.07400 |
0.65500 |
0.09500 |
| 112.657 |
0.66100 |
0.21800 |
0.61700 |
0.18700 |
| 110.524 |
0.82600 |
0.05200 |
0.74800 |
0.07200 |
(P - pressure, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Marinichev A.N.; Susarev M.P.: Investigation of Phase Equilibria in the System Acetone-Methanol-Cyclohexane. J.Appl.Chem.USSR 38 (1965) 1034-1037 |
List of All References
Vapor-Liquid Equilibrium Data Overview
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