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 30090
Components
| No. | Formula | Molar Mass | CAS Registry Number | Name |
|---|---|---|---|---|
| 1 | C6H12 | 84.161 | 110-82-7 | Cyclohexane |
| 2 | H2O | 18.015 | 7732-18-5 | Water |
Constant Value
| Temperature | 545.37 | K |
|---|
Data Table
| P [kPa] | y1 [mol/mol] |
|---|---|
| 9480.261 | 0.33522 |
(P - pressure, y - vapor mole fraction)
Reference
| Source |
|---|
| Guerrant R.P.: Hydrocarbon-Water Solubilities at High Temperatures under Vapor-Liquid-Liquid Equilibrium Conditions. Thesis (1964) |
Comment: vapor phase composition of VLLE
Vapor-Liquid Equilibrium Data Set 35330
Components
| No. | Formula | Molar Mass | CAS Registry Number | Name |
|---|---|---|---|---|
| 1 | C6H12 | 84.161 | 110-82-7 | Cyclohexane |
| 2 | H2O | 18.015 | 7732-18-5 | Water |
Data Table
| P [kPa] | T [K] | x1 [mol/mol] | y1 [mol/mol] |
|---|---|---|---|
| 172.368 | 369.26 | 0.99303 | 0.69465 |
| 344.737 | 394.26 | 0.98614 | 0.75030 |
| 344.737 | 399.82 | 0.99534 | 0.93358 |
| 689.473 | 416.48 | 0.77030 | 0.61086 |
| 689.473 | 422.04 | 0.98158 | 0.62924 |
| 689.473 | 427.59 | 0.99072 | 0.67483 |
| 689.473 | 433.15 | 0.99767 | 0.79438 |
| 1034.210 | 433.15 | 0.95494 | 0.60973 |
| 1034.210 | 444.26 | 0.97481 | 0.66585 |
| 1034.210 | 455.37 | 0.99627 | 0.82304 |
| 1378.940 | 444.26 | 0.93991 | 0.58891 |
| 1378.940 | 455.37 | 0.96590 | 0.63992 |
| 1378.940 | 466.48 | 0.98614 | 0.77030 |
| 1723.685 | 455.37 | 0.93358 | 0.62690 |
| 1723.685 | 466.48 | 0.96149 | 0.73985 |
| 1723.685 | 477.59 | 0.97932 | 0.86064 |
| 2068.417 | 466.48 | 0.93568 | 0.65209 |
| 2068.417 | 477.59 | 0.96590 | 0.75030 |
| 2068.417 | 488.70 | 0.98614 | 0.85511 |
| 2413.162 | 477.59 | 0.94204 | 0.67483 |
| 2413.162 | 488.70 | 0.97034 | 0.76562 |
| 2413.162 | 499.82 | 0.98843 | 0.86436 |
| 2757.893 | 477.59 | 0.90291 | 0.60084 |
| 2757.893 | 494.26 | 0.92318 | 0.71532 |
| 2757.893 | 510.93 | 0.98386 | 0.86436 |
| 151.684 | 366.48 | 0.99767 | 0.80936 |
| 344.737 | 394.26 | 0.98614 | 0.75944 |
| 586.052 | 422.04 | 0.99303 | 0.73985 |
| 689.473 | 422.04 | 0.97932 | 0.63633 |
| 792.893 | 422.04 | 0.96369 | 0.60638 |
| 1034.210 | 449.82 | 0.98386 | 0.72099 |
| 1172.105 | 449.82 | 0.97257 | 0.65955 |
| 1309.999 | 449.82 | 0.95930 | 0.62924 |
| 1447.894 | 449.82 | 0.94417 | 0.60749 |
| 1585.790 | 449.82 | 0.93149 | 0.58891 |
| 1723.685 | 477.59 | 0.97932 | 0.87756 |
| 2068.417 | 477.59 | 0.96590 | 0.76407 |
| 2413.162 | 477.59 | 0.94204 | 0.67483 |
| 2757.893 | 477.59 | 0.90491 | 0.60749 |
(P - pressure, T - temperature, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
|---|
| Burd S.D.; Braun W.G.: Vapor-Liquid Equilibrium of Some C6 Hydrocarbons with Water. Proc.Am.Petrol.Inst.Ref.Div. 48 (1968) 464-476 |
Diagrams
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List of All References
| Source |
|---|
| Burd S.D.; Braun W.G.: Vapor-Liquid Equilibrium of Some C6 Hydrocarbons with Water. Proc.Am.Petrol.Inst.Ref.Div. 48 (1968) 464-476 |
| Guerrant R.P.: Hydrocarbon-Water Solubilities at High Temperatures under Vapor-Liquid-Liquid Equilibrium Conditions. Thesis (1964) |
Vapor-Liquid Equilibrium Data Overview