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 7565
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C3H6O |
58.080 |
67-64-1 |
Acetone |
| 2 |
CHCl3 |
119.377 |
67-66-3 |
Chloroform |
| 3 |
CH4O |
32.042 |
67-56-1 |
Methanol |
| 4 |
C2H6O |
46.069 |
64-17-5 |
Ethanol |
Search the DDB for all data of this mixture
Constant Value
Data Table
| T [K] |
x1 [mol/mol] |
x2 [mol/mol] |
x3 [mol/mol] |
y1 [mol/mol] |
y2 [mol/mol] |
y3 [mol/mol] |
| 333.31 |
0.20000 |
0.51200 |
0.12800 |
0.15100 |
0.55400 |
0.18300 |
| 337.05 |
0.20000 |
0.25600 |
0.06400 |
0.27700 |
0.39800 |
0.09000 |
| 339.76 |
0.20000 |
0.12800 |
0.03200 |
0.33900 |
0.20100 |
0.03400 |
| 334.02 |
0.40000 |
0.38400 |
0.09600 |
0.40600 |
0.35700 |
0.14500 |
| 334.95 |
0.40000 |
0.28800 |
0.07200 |
0.45300 |
0.28400 |
0.09300 |
| 335.86 |
0.40000 |
0.19200 |
0.04800 |
0.51100 |
0.19000 |
0.05800 |
| 336.28 |
0.40000 |
0.09600 |
0.02400 |
0.57500 |
0.09800 |
0.02500 |
| 333.00 |
0.60000 |
0.25600 |
0.06400 |
0.65000 |
0.19200 |
0.09300 |
| 333.27 |
0.60000 |
0.19200 |
0.04800 |
0.67400 |
0.14700 |
0.06200 |
| 333.27 |
0.60000 |
0.12800 |
0.03200 |
0.70300 |
0.09700 |
0.03700 |
| 334.02 |
0.60000 |
0.06400 |
0.01600 |
0.72600 |
0.05000 |
0.01700 |
| 331.81 |
0.80000 |
0.12800 |
0.03200 |
0.85200 |
0.07800 |
0.04100 |
| 331.62 |
0.80000 |
0.09600 |
0.02400 |
0.85700 |
0.05600 |
0.03000 |
| 331.61 |
0.80000 |
0.06400 |
0.01600 |
0.86100 |
0.03700 |
0.01800 |
| 331.46 |
0.80000 |
0.03200 |
0.00800 |
0.86900 |
0.01700 |
0.00900 |
| 332.51 |
0.20000 |
0.38400 |
0.25600 |
0.17300 |
0.43700 |
0.30000 |
| 335.38 |
0.20000 |
0.28800 |
0.19200 |
0.22500 |
0.36600 |
0.21400 |
| 338.30 |
0.20000 |
0.19200 |
0.12800 |
0.26800 |
0.25600 |
0.14300 |
| 340.97 |
0.20000 |
0.09600 |
0.06400 |
0.34300 |
0.14700 |
0.07300 |
| 334.07 |
0.40000 |
0.28800 |
0.19200 |
0.41200 |
0.27200 |
0.27300 |
| 334.52 |
0.40000 |
0.21600 |
0.14400 |
0.46600 |
0.21100 |
0.16800 |
| 336.08 |
0.40000 |
0.14400 |
0.09600 |
0.47400 |
0.15900 |
0.10300 |
| 337.19 |
0.40000 |
0.07200 |
0.04800 |
0.57600 |
0.05100 |
0.07400 |
| 332.96 |
0.60000 |
0.19200 |
0.12800 |
0.64300 |
0.14300 |
0.15900 |
| 333.26 |
0.60000 |
0.14400 |
0.09600 |
0.66830 |
0.11030 |
0.11130 |
| 333.30 |
0.60000 |
0.09600 |
0.06400 |
0.70200 |
0.07650 |
0.06950 |
| 333.64 |
0.60000 |
0.04800 |
0.03200 |
0.73100 |
0.03550 |
0.03350 |
| 331.00 |
0.80000 |
0.09600 |
0.06400 |
0.83500 |
0.05800 |
0.07900 |
| 331.15 |
0.80000 |
0.07200 |
0.04800 |
0.84600 |
0.04300 |
0.05000 |
| 331.96 |
0.80000 |
0.04800 |
0.03200 |
0.85000 |
0.02900 |
0.03800 |
| 331.76 |
0.80000 |
0.02400 |
0.01600 |
0.86300 |
0.01300 |
0.01800 |
| 333.42 |
0.20000 |
0.25600 |
0.38400 |
0.21100 |
0.31700 |
0.38800 |
| 336.19 |
0.20000 |
0.19200 |
0.28800 |
0.25300 |
0.25700 |
0.30400 |
| 338.00 |
0.20000 |
0.12800 |
0.19200 |
0.31200 |
0.18400 |
0.20600 |
| 340.98 |
0.20000 |
0.06400 |
0.09600 |
0.36300 |
0.10000 |
0.10900 |
| 333.15 |
0.40000 |
0.19200 |
0.28800 |
0.43800 |
0.18300 |
0.31200 |
| 334.24 |
0.40000 |
0.14400 |
0.21600 |
0.49400 |
0.13900 |
0.22700 |
| 335.46 |
0.40000 |
0.09600 |
0.14400 |
0.53700 |
0.09500 |
0.15400 |
| 336.34 |
0.40000 |
0.04800 |
0.07200 |
0.58500 |
0.04980 |
0.07200 |
| 331.66 |
0.60000 |
0.12800 |
0.19200 |
0.64800 |
0.09000 |
0.21500 |
| 332.34 |
0.60000 |
0.09600 |
0.14400 |
0.67400 |
0.07100 |
0.15900 |
| 332.63 |
0.60000 |
0.06400 |
0.09600 |
0.70400 |
0.04600 |
0.10300 |
| 333.50 |
0.60000 |
0.03200 |
0.04800 |
0.72800 |
0.02440 |
0.05020 |
| 330.30 |
0.80000 |
0.06400 |
0.09600 |
0.82080 |
0.03770 |
0.11530 |
| 330.60 |
0.80000 |
0.04800 |
0.07200 |
0.83960 |
0.02830 |
0.08030 |
| 331.00 |
0.80000 |
0.03200 |
0.04800 |
0.85270 |
0.01860 |
0.05400 |
| 331.10 |
0.80000 |
0.01600 |
0.02400 |
0.86100 |
0.00890 |
0.02600 |
| 334.02 |
0.20000 |
0.12800 |
0.51200 |
0.24700 |
0.18400 |
0.48300 |
| 336.17 |
0.20000 |
0.09600 |
0.38400 |
0.28400 |
0.04100 |
0.38800 |
| 338.36 |
0.20000 |
0.06400 |
0.25600 |
0.33400 |
0.09800 |
0.26700 |
| 340.71 |
0.20000 |
0.03200 |
0.12800 |
0.38200 |
0.05200 |
0.14300 |
| 332.29 |
0.40000 |
0.09600 |
0.38400 |
0.48700 |
0.09600 |
0.35500 |
| 333.70 |
0.40000 |
0.07200 |
0.28800 |
0.51800 |
0.07500 |
0.27800 |
| 336.18 |
0.40000 |
0.02400 |
0.09600 |
0.59300 |
0.02700 |
0.09400 |
| 330.83 |
0.60000 |
0.06400 |
0.25600 |
0.66700 |
0.04600 |
0.23900 |
| 331.65 |
0.60000 |
0.04800 |
0.19200 |
0.68820 |
0.03620 |
0.18720 |
| 332.40 |
0.60000 |
0.03200 |
0.12800 |
0.71200 |
0.02600 |
0.12400 |
| 333.17 |
0.60000 |
0.01600 |
0.06400 |
0.73900 |
0.01300 |
0.06100 |
| 329.80 |
0.80000 |
0.03200 |
0.12800 |
0.82900 |
0.01850 |
0.12850 |
| 330.19 |
0.80000 |
0.02400 |
0.09600 |
0.84200 |
0.01400 |
0.09500 |
| 331.06 |
0.80000 |
0.00800 |
0.03200 |
0.86410 |
0.00550 |
0.03190 |
(T - temperature, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Pavlova A.A.; Obukhova L.Yu.; Nikolaev E.S.; Mitropolskaya V.A.; Mozzhukhin A.S.: Experimentelle Uhtersuchung und matematische Modelierung des Dampf-Flüssig-Gleichgewichtes im System Aceton-Chloroform-Methanol-Ethanol. Osnovnoi Organ.Sintez.Neftekhim. 4 (1975) 115-119 |
List of All References
Vapor-Liquid Equilibrium Data Overview
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