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 12773
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C4H8O |
72.107 |
109-99-9 |
Tetrahydrofuran |
| 2 |
C4H8O2 |
88.106 |
141-78-6 |
Ethyl acetate |
Search the DDB for all data of this mixture
Constant Value
Data Table
| P [kPa] |
x1 [mol/mol] |
y1 [mol/mol] |
| 25.050 |
0.00000 |
0.00000 |
| 25.250 |
0.00790 |
0.01430 |
| 26.043 |
0.04680 |
0.08320 |
| 27.238 |
0.11180 |
0.17690 |
| 28.850 |
0.19740 |
0.28810 |
| 30.649 |
0.31330 |
0.42990 |
| 32.229 |
0.40580 |
0.52170 |
| 33.905 |
0.52330 |
0.63620 |
| 34.556 |
0.56600 |
0.67220 |
| 35.708 |
0.64740 |
0.74000 |
| 36.960 |
0.73390 |
0.80770 |
| 38.040 |
0.81940 |
0.87260 |
| 39.050 |
0.90500 |
0.93390 |
| 39.841 |
0.96140 |
0.97290 |
| 40.159 |
0.98980 |
0.99230 |
| 40.201 |
1.00000 |
1.00000 |
(P - pressure, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Wu H.S.; Sandler S.I.: Vapor-Liquid Equilibria of Tetrahydrofuran Systems. J.Chem.Eng.Data 33 (1988) 157-162 |
Vapor-Liquid Equilibrium Data Set 12774
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C4H8O |
72.107 |
109-99-9 |
Tetrahydrofuran |
| 2 |
C4H8O2 |
88.106 |
141-78-6 |
Ethyl acetate |
Search the DDB for all data of this mixture
Constant Value
Data Table
| P [kPa] |
x1 [mol/mol] |
y1 [mol/mol] |
| 55.858 |
0.00000 |
0.00000 |
| 56.159 |
0.00740 |
0.01230 |
| 57.493 |
0.04650 |
0.07370 |
| 59.500 |
0.10680 |
0.15890 |
| 62.400 |
0.19400 |
0.27360 |
| 65.115 |
0.28000 |
0.37760 |
| 67.754 |
0.38790 |
0.48460 |
| 70.509 |
0.47270 |
0.57420 |
| 71.881 |
0.52340 |
0.61840 |
| 74.053 |
0.60950 |
0.69490 |
| 76.462 |
0.70670 |
0.77580 |
| 78.631 |
0.79660 |
0.84640 |
| 80.365 |
0.87360 |
0.90610 |
| 81.571 |
0.92620 |
0.94550 |
| 82.211 |
0.95540 |
0.96610 |
| 83.100 |
1.00000 |
1.00000 |
(P - pressure, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Wu H.S.; Sandler S.I.: Vapor-Liquid Equilibria of Tetrahydrofuran Systems. J.Chem.Eng.Data 33 (1988) 157-162 |
Diagrams
List of All References
| Source |
| Wu H.S.; Sandler S.I.: Vapor-Liquid Equilibria of Tetrahydrofuran Systems. J.Chem.Eng.Data 33 (1988) 157-162 |
Vapor-Liquid Equilibrium Data Overview
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