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 2072
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C3H8O |
60.096 |
67-63-0 |
2-Propanol |
| 2 |
C6H6 |
78.114 |
71-43-2 |
Benzene |
| 3 |
H2O |
18.015 |
7732-18-5 |
Water |
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Constant Value
Data Table
| T [K] |
x1 [mol/mol] |
x2 [mol/mol] |
y1 [mol/mol] |
y2 [mol/mol] |
| 339.66 |
0.20000 |
0.64000 |
0.16500 |
0.50000 |
| 340.81 |
0.40000 |
0.48000 |
0.27000 |
0.50000 |
| 343.60 |
0.60000 |
0.32000 |
0.38500 |
0.48000 |
| 347.92 |
0.80000 |
0.16000 |
0.59500 |
0.32500 |
| 339.55 |
0.20000 |
0.48000 |
0.18300 |
0.47500 |
| 340.46 |
0.40000 |
0.36000 |
0.24500 |
0.47500 |
| 343.58 |
0.60000 |
0.24000 |
0.34500 |
0.44500 |
| 348.21 |
0.80000 |
0.12000 |
0.60500 |
0.27000 |
| 339.60 |
0.20000 |
0.32000 |
0.19200 |
0.46500 |
| 340.65 |
0.40000 |
0.24000 |
0.24000 |
0.45000 |
| 344.30 |
0.60000 |
0.16000 |
0.35000 |
0.40000 |
| 349.33 |
0.80000 |
0.08000 |
0.64000 |
0.20000 |
| 339.91 |
0.20000 |
0.16000 |
0.19500 |
0.46000 |
| 342.15 |
0.40000 |
0.12000 |
0.32000 |
0.33000 |
| 346.65 |
0.60000 |
0.08000 |
0.43500 |
0.27000 |
| 350.89 |
0.80000 |
0.04000 |
0.70000 |
0.10000 |
(T - temperature, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Mitropolskaya V.A.; Kazaz M.S.; Mozzhukhin A.S.; Serafimov L.A.: Flüssig-Flüssig- und Dampf-Flüssig-Gleichgewichte in System Benzol-Isopropanol-Wasser bei 760 mmHg. Tr.Mosk.Inst.Tonkoj Khim.Tekhnol. 2 (1972) 207-213 |
Vapor-Liquid Equilibrium Data Set 7222
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C3H8O |
60.096 |
67-63-0 |
2-Propanol |
| 2 |
H2O |
18.015 |
7732-18-5 |
Water |
| 3 |
C6H6 |
78.114 |
71-43-2 |
Benzene |
Search the DDB for all data of this mixture
Constant Value
Data Table
| T [K] |
x1 [mol/mol] |
x2 [mol/mol] |
y1 [mol/mol] |
y2 [mol/mol] |
| 352.15 |
0.79920 |
0.13300 |
0.78200 |
0.13040 |
| 351.35 |
0.79650 |
0.12410 |
0.77710 |
0.04440 |
| 351.65 |
0.79310 |
0.13870 |
0.78700 |
0.04420 |
| 351.95 |
0.74700 |
0.24410 |
0.63600 |
0.24270 |
| 349.05 |
0.72390 |
0.21890 |
0.51460 |
0.24600 |
| 349.65 |
0.71260 |
0.26340 |
0.56040 |
0.23370 |
| 349.45 |
0.70920 |
0.19760 |
0.64360 |
0.07120 |
| 346.95 |
0.65130 |
0.15690 |
0.36290 |
0.25090 |
| 347.15 |
0.65710 |
0.16720 |
0.35800 |
0.23760 |
| 346.15 |
0.64250 |
0.26850 |
0.40430 |
0.23830 |
| 350.35 |
0.61470 |
0.37850 |
0.56670 |
0.27400 |
| 345.35 |
0.56830 |
0.13320 |
0.34510 |
0.21050 |
| 351.65 |
0.56130 |
0.40630 |
0.51230 |
0.26910 |
| 350.15 |
0.55590 |
0.37780 |
0.42520 |
0.29750 |
| 350.65 |
0.55140 |
0.44000 |
0.55450 |
0.32870 |
| 348.35 |
0.52280 |
0.40890 |
0.46530 |
0.27240 |
| 351.15 |
0.51710 |
0.46070 |
0.54510 |
0.29260 |
| 343.05 |
0.51640 |
0.02250 |
0.33880 |
0.16540 |
| 352.15 |
0.43150 |
0.56100 |
0.56880 |
0.33040 |
| 343.55 |
0.43120 |
0.05930 |
0.31840 |
0.15710 |
| 342.85 |
0.42040 |
0.40670 |
0.27760 |
0.31550 |
| 352.95 |
0.41150 |
0.56590 |
0.54950 |
0.34330 |
| 341.05 |
0.39390 |
0.28660 |
0.25510 |
0.17780 |
| 342.65 |
0.37450 |
0.48640 |
0.27650 |
0.24350 |
| 340.85 |
0.36840 |
0.27880 |
0.24210 |
0.22690 |
| 343.95 |
0.34530 |
0.06060 |
0.20100 |
0.12260 |
| 344.15 |
0.28850 |
0.62450 |
0.25990 |
0.25220 |
| 341.25 |
0.26440 |
0.61550 |
0.22270 |
0.26480 |
| 340.05 |
0.25120 |
0.49860 |
0.24020 |
0.26860 |
| 354.55 |
0.25120 |
0.74510 |
0.56640 |
0.37680 |
| 339.85 |
0.24580 |
0.28780 |
0.19130 |
0.24590 |
| 348.45 |
0.22100 |
0.75310 |
0.37970 |
0.28700 |
| 343.45 |
0.20150 |
0.76650 |
0.28960 |
0.24940 |
| 340.85 |
0.19590 |
0.62880 |
0.21820 |
0.23360 |
| 341.05 |
0.18360 |
0.77400 |
0.24430 |
0.24540 |
| 340.25 |
0.18060 |
0.55630 |
0.15080 |
0.30050 |
| 340.15 |
0.17860 |
0.69330 |
0.21470 |
0.36960 |
| 339.85 |
0.17350 |
0.57840 |
0.19790 |
0.25080 |
| 355.45 |
0.15810 |
0.84060 |
0.58480 |
0.38800 |
| 339.85 |
0.15730 |
0.28170 |
0.17920 |
0.21630 |
| 343.85 |
0.12670 |
0.69410 |
0.17610 |
0.24680 |
| 354.15 |
0.12470 |
0.82320 |
0.07700 |
0.17620 |
| 345.15 |
0.12460 |
0.86560 |
0.35110 |
0.29420 |
| 341.15 |
0.11950 |
0.84930 |
0.21320 |
0.26280 |
| 340.15 |
0.11610 |
0.76450 |
0.20650 |
0.24500 |
| 340.15 |
0.10700 |
0.71020 |
0.20990 |
0.23330 |
| 345.15 |
0.10410 |
0.87270 |
0.27990 |
0.28310 |
| 343.65 |
0.10090 |
0.82680 |
0.12690 |
0.25520 |
| 356.45 |
0.09390 |
0.90500 |
0.56770 |
0.42470 |
| 341.15 |
0.09220 |
0.85900 |
0.18950 |
0.22440 |
| 342.15 |
0.08880 |
0.89060 |
0.23720 |
0.24060 |
| 340.35 |
0.08750 |
0.89320 |
0.20200 |
0.22910 |
| 353.45 |
0.07460 |
0.92210 |
0.37280 |
0.44250 |
| 354.15 |
0.06310 |
0.93420 |
0.34010 |
0.51220 |
| 358.35 |
0.06040 |
0.93880 |
0.55220 |
0.43710 |
| 347.85 |
0.06010 |
0.85280 |
0.18030 |
0.22750 |
| 340.15 |
0.05930 |
0.88650 |
0.17540 |
0.20200 |
| 354.45 |
0.05600 |
0.94130 |
0.35770 |
0.44740 |
| 340.75 |
0.04510 |
0.76210 |
0.15040 |
0.20340 |
| 346.65 |
0.04450 |
0.27620 |
0.15100 |
0.05600 |
| 348.75 |
0.04300 |
0.84840 |
0.15990 |
0.15700 |
| 359.15 |
0.03790 |
0.96160 |
0.30260 |
0.59650 |
| 345.05 |
0.03270 |
0.40660 |
0.10890 |
0.05650 |
| 361.65 |
0.03160 |
0.96790 |
0.24600 |
0.69470 |
| 363.55 |
0.02950 |
0.97000 |
0.18420 |
0.63770 |
| 362.75 |
0.02920 |
0.97050 |
0.45440 |
0.54370 |
| 366.65 |
0.02650 |
0.97280 |
0.06690 |
0.64850 |
| 343.45 |
0.02360 |
0.55560 |
0.07980 |
0.02910 |
| 367.95 |
0.02340 |
0.97630 |
0.39150 |
0.60670 |
| 363.25 |
0.01890 |
0.98020 |
0.16410 |
0.64760 |
| 363.35 |
0.01880 |
0.98090 |
0.25490 |
0.68460 |
| 360.45 |
0.01880 |
0.98090 |
0.12970 |
0.57460 |
| 368.15 |
0.01750 |
0.98200 |
0.11900 |
0.78070 |
| 365.05 |
0.01670 |
0.98260 |
0.31170 |
0.59520 |
| 345.55 |
0.01140 |
0.69450 |
0.03340 |
0.41050 |
| 370.15 |
0.01050 |
0.98880 |
0.06680 |
0.90430 |
(T - temperature, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Yorizane M.; Yoshimura S.: Measurement and Prediction of Vapor-Liquid Equilibrium of the Ternary System. Hiroshima Daigaku Kogakubu Kenkyu Hokoku 13 (1965) 41-50 |
Vapor-Liquid Equilibrium Data Set 7386
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C6H6 |
78.114 |
71-43-2 |
Benzene |
| 2 |
C3H8O |
60.096 |
67-63-0 |
2-Propanol |
| 3 |
H2O |
18.015 |
7732-18-5 |
Water |
Search the DDB for all data of this mixture
Constant Value
Data Table
| T [K] |
x1 [mol/mol] |
x2 [mol/mol] |
y1 [mol/mol] |
y2 [mol/mol] |
| 307.47 |
0.91272 |
0.07462 |
0.67754 |
0.12688 |
| 307.47 |
0.00103 |
0.04930 |
0.67754 |
0.12688 |
| 307.20 |
0.77224 |
0.18371 |
0.65171 |
0.15711 |
| 307.20 |
0.00133 |
0.06361 |
0.65171 |
0.15711 |
| 307.41 |
0.61004 |
0.26908 |
0.64746 |
0.16471 |
| 307.41 |
0.00191 |
0.07512 |
0.64746 |
0.16471 |
| 307.67 |
0.30527 |
0.36245 |
0.63287 |
0.17998 |
| 307.67 |
0.00459 |
0.09814 |
0.63287 |
0.17998 |
(T - temperature, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Morachevskii A.G.; Legochkina L.A.: Three-Phase Equilibria Liquid-Liquid-Vapor in the System Isopropanol-Benzene-Water. J.Appl.Chem.USSR 38 (1965) 1751-1754 |
List of All References
Vapor-Liquid Equilibrium Data Overview
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