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 5103
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C3H8O |
60.096 |
67-63-0 |
2-Propanol |
| 2 |
C8H10 |
106.167 |
106-42-3 |
p-Xylene |
Search the DDB for all data of this mixture
Constant Value
Data Table
| T [K] |
x1 [mol/mol] |
y1 [mol/mol] |
| 404.75 |
0.00600 |
0.08200 |
| 398.95 |
0.02000 |
0.20500 |
| 397.55 |
0.02500 |
0.24400 |
| 392.55 |
0.03800 |
0.36400 |
| 387.65 |
0.05200 |
0.46800 |
| 383.75 |
0.06800 |
0.53800 |
| 381.05 |
0.08200 |
0.56600 |
| 378.55 |
0.09600 |
0.62200 |
| 374.75 |
0.13400 |
0.66200 |
| 370.55 |
0.17400 |
0.71400 |
| 367.95 |
0.21400 |
0.75400 |
| 366.05 |
0.26400 |
0.78000 |
| 364.25 |
0.34100 |
0.80200 |
| 362.25 |
0.42800 |
0.82500 |
| 361.35 |
0.48800 |
0.83200 |
| 360.05 |
0.56600 |
0.84800 |
| 358.95 |
0.66800 |
0.86600 |
| 357.95 |
0.76200 |
0.89000 |
| 357.05 |
0.84800 |
0.91600 |
| 356.45 |
0.92800 |
0.95100 |
| 356.05 |
0.95800 |
0.97200 |
| 355.95 |
0.97500 |
0.98200 |
(T - temperature, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Kumar B.; Raju K.S.N.: Vapour-Liquid Equilibrium Data for the Systems 2-Propanol-Ethylbenzene & 2-Propanol-p-Xylene. Indian J.Technol. 14 (1976) 537-540 |
Vapor-Liquid Equilibrium Data Set 12013
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C3H8O |
60.096 |
67-63-0 |
2-Propanol |
| 2 |
C8H10 |
106.167 |
106-42-3 |
p-Xylene |
Search the DDB for all data of this mixture
Constant Value
Data Table
| T [K] |
x1 [mol/mol] |
y1 [mol/mol] |
| 411.55 |
0.00000 |
0.00000 |
| 407.55 |
0.00600 |
0.10300 |
| 404.55 |
0.01200 |
0.16500 |
| 403.85 |
0.01300 |
0.19400 |
| 401.55 |
0.01800 |
0.25000 |
| 397.75 |
0.02700 |
0.32300 |
| 393.75 |
0.04000 |
0.40300 |
| 391.35 |
0.05100 |
0.45200 |
| 387.15 |
0.06300 |
0.51700 |
| 385.25 |
0.06800 |
0.55000 |
| 382.95 |
0.07800 |
0.58600 |
| 380.45 |
0.09300 |
0.62700 |
| 377.45 |
0.10900 |
0.66100 |
| 375.20 |
0.12600 |
0.69100 |
| 373.70 |
0.13700 |
0.70600 |
| 370.05 |
0.19500 |
0.75950 |
| 367.50 |
0.22700 |
0.77850 |
| 365.90 |
0.26500 |
0.79250 |
| 365.15 |
0.29000 |
0.80250 |
| 364.65 |
0.31400 |
0.81300 |
| 364.00 |
0.34000 |
0.82050 |
| 362.30 |
0.40500 |
0.83850 |
| 361.40 |
0.46100 |
0.84550 |
| 360.75 |
0.50400 |
0.85300 |
| 360.20 |
0.53500 |
0.86250 |
| 359.80 |
0.57000 |
0.86900 |
| 359.20 |
0.62700 |
0.87600 |
| 358.70 |
0.66700 |
0.88300 |
| 358.30 |
0.69900 |
0.89150 |
| 357.95 |
0.73500 |
0.89800 |
| 357.90 |
0.74200 |
0.89950 |
| 357.60 |
0.76450 |
0.90550 |
| 357.10 |
0.81900 |
0.91850 |
| 356.60 |
0.86400 |
0.93200 |
| 356.20 |
0.90750 |
0.95350 |
| 355.85 |
0.95450 |
0.97100 |
| 355.70 |
0.97450 |
0.98400 |
| 355.55 |
1.00000 |
1.00000 |
(T - temperature, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| de Alfonso C.; Pintado M.; Saenz de la Torre A.F.: IV. Determination y estudio termodinamico en sistemas binarios de isopropanol con hidrocarburos aromaticos. An.Quim.Ser.A 79 (1983) 254-264 |
Vapor-Liquid Equilibrium Data Set 16800
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C3H8O |
60.096 |
67-63-0 |
2-Propanol |
| 2 |
C8H10 |
106.167 |
106-42-3 |
p-Xylene |
Search the DDB for all data of this mixture
Constant Value
Data Table
| P [kPa] |
x1 [mol/mol] |
| 1.1186 |
0.00000 |
| 3.936 |
0.07210 |
| 4.442 |
0.13710 |
| 4.721 |
0.18520 |
| 5.016 |
0.24900 |
| 5.213 |
0.32010 |
| 5.365 |
0.41020 |
| 5.469 |
0.49720 |
| 5.510 |
0.56130 |
| 5.605 |
0.67230 |
| 5.646 |
0.72540 |
| 5.721 |
0.79030 |
| 5.776 |
0.87820 |
| 5.846 |
0.93720 |
| 5.868 |
1.00000 |
(P - pressure, x - liquid mole fraction)
Reference
| Source |
| Gupta V.; Maken S.; Kalra K.C.; Singh K.C.: Molar Excess Gibbs Free Energy of 1-Propanol or 2-Propanol + Aromatic Hydrocarbons at 298.15 K in Terms of an Association Model with a Flory Contribution Term. Thermochim.Acta 277 (1996) 187-198 |
Diagrams
List of All References
| Source |
| Kumar B.; Raju K.S.N.: Vapour-Liquid Equilibrium Data for the Systems 2-Propanol-Ethylbenzene & 2-Propanol-p-Xylene. Indian J.Technol. 14 (1976) 537-540 |
| de Alfonso C.; Pintado M.; Saenz de la Torre A.F.: IV. Determination y estudio termodinamico en sistemas binarios de isopropanol con hidrocarburos aromaticos. An.Quim.Ser.A 79 (1983) 254-264 |
| Gupta V.; Maken S.; Kalra K.C.; Singh K.C.: Molar Excess Gibbs Free Energy of 1-Propanol or 2-Propanol + Aromatic Hydrocarbons at 298.15 K in Terms of an Association Model with a Flory Contribution Term. Thermochim.Acta 277 (1996) 187-198 |
Vapor-Liquid Equilibrium Data Overview
© DDBST GmbH
