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 8947
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
CHCl3 |
119.377 |
67-66-3 |
Chloroform |
| 2 |
C3H8O |
60.096 |
67-63-0 |
2-Propanol |
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Constant Value
Data Table
| T [K] |
x1 [mol/mol] |
y1 [mol/mol] |
| 355.55 |
0.00000 |
0.00000 |
| 354.15 |
0.03000 |
0.09100 |
| 353.15 |
0.05200 |
0.13000 |
| 351.65 |
0.09100 |
0.21700 |
| 348.85 |
0.13500 |
0.33400 |
| 347.15 |
0.19200 |
0.42000 |
| 345.75 |
0.23200 |
0.48500 |
| 343.95 |
0.31000 |
0.57100 |
| 341.65 |
0.39000 |
0.65000 |
| 340.35 |
0.45500 |
0.71000 |
| 339.25 |
0.50500 |
0.74500 |
| 338.65 |
0.55000 |
0.75500 |
| 337.75 |
0.61000 |
0.78000 |
| 336.65 |
0.68500 |
0.81100 |
| 335.95 |
0.73000 |
0.83000 |
| 335.15 |
0.79000 |
0.85000 |
| 334.85 |
0.81500 |
0.86500 |
| 334.35 |
0.87000 |
0.89000 |
| 333.95 |
0.92100 |
0.92100 |
| 334.05 |
0.98000 |
0.96000 |
| 334.25 |
1.00000 |
1.00000 |
(T - temperature, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Hanumantharao G.; Subbarao B.V.: Isobaric Vapor-Liquid Equilibria-Chloroform-Isopropanol, Tertiary Butanol-Toluene and Ternary Butanol-Trichloroethylene Systems. Indian J.Technol. 12 (1974) 292-295 |
Vapor-Liquid Equilibrium Data Set 9793
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
CHCl3 |
119.377 |
67-66-3 |
Chloroform |
| 2 |
C3H8O |
60.096 |
67-63-0 |
2-Propanol |
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Constant Value
Data Table
| T [K] |
x1 [mol/mol] |
y1 [mol/mol] |
| 353.65 |
0.03500 |
0.08900 |
| 352.05 |
0.06900 |
0.16700 |
| 350.85 |
0.09200 |
0.22200 |
| 349.15 |
0.13200 |
0.30400 |
| 347.15 |
0.18000 |
0.39300 |
| 346.15 |
0.20400 |
0.43200 |
| 345.15 |
0.23300 |
0.47200 |
| 343.35 |
0.29200 |
0.54400 |
| 341.75 |
0.34600 |
0.60000 |
| 341.05 |
0.36800 |
0.62100 |
| 339.75 |
0.42900 |
0.66800 |
| 338.05 |
0.51300 |
0.72400 |
| 336.55 |
0.63000 |
0.78200 |
| 336.35 |
0.64500 |
0.78900 |
| 335.35 |
0.75000 |
0.83700 |
| 334.85 |
0.82200 |
0.87000 |
| 334.45 |
0.90800 |
0.91900 |
| 334.45 |
0.93800 |
0.94000 |
| 334.25 |
0.95500 |
0.95400 |
| 334.25 |
0.97700 |
0.97500 |
(T - temperature, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Nagata I.: Isobaric Vapor-Liquid Equilibrium Data for Binary Systems. Can.J.Chem.Eng. 41 (1963) 21-23 |
Vapor-Liquid Equilibrium Data Set 11394
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
CHCl3 |
119.377 |
67-66-3 |
Chloroform |
| 2 |
C3H8O |
60.096 |
67-63-0 |
2-Propanol |
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Constant Value
Data Table
| P [kPa] |
x1 [mol/mol] |
y1 [mol/mol] |
| 33.077 |
0.09900 |
0.34200 |
| 39.757 |
0.17600 |
0.49200 |
| 47.263 |
0.28700 |
0.61700 |
| 52.756 |
0.38000 |
0.69400 |
| 57.889 |
0.48900 |
0.75700 |
| 61.248 |
0.58900 |
0.80100 |
| 62.395 |
0.62300 |
0.81200 |
| 66.288 |
0.77000 |
0.86500 |
| 67.861 |
0.83600 |
0.89500 |
| 68.874 |
0.93900 |
0.94700 |
| 69.088 |
0.95300 |
0.95700 |
(P - pressure, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Nagata I.: Vapor-Liquid Equilibria for the Ternary System 2-Propanol-Chloroform-Benzene. J.Chem.Eng.Data 30 (1985) 80-82 |
Diagrams
List of All References
| Source |
| Hanumantharao G.; Subbarao B.V.: Isobaric Vapor-Liquid Equilibria-Chloroform-Isopropanol, Tertiary Butanol-Toluene and Ternary Butanol-Trichloroethylene Systems. Indian J.Technol. 12 (1974) 292-295 |
| Nagata I.: Vapor-Liquid Equilibria for the Ternary System 2-Propanol-Chloroform-Benzene. J.Chem.Eng.Data 30 (1985) 80-82 |
| Nagata I.: Isobaric Vapor-Liquid Equilibrium Data for Binary Systems. Can.J.Chem.Eng. 41 (1963) 21-23 |
Vapor-Liquid Equilibrium Data Overview
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