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 15344
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
CHCl3 |
119.377 |
67-66-3 |
Chloroform |
| 2 |
C2H6O |
46.069 |
64-17-5 |
Ethanol |
| 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] |
| 353.26 |
0.00000 |
0.00000 |
0.00000 |
0.00000 |
| 351.30 |
0.00000 |
1.00000 |
0.00000 |
1.00000 |
| 334.28 |
1.00000 |
0.00000 |
1.00000 |
0.00000 |
| 336.32 |
0.53480 |
0.23300 |
0.60210 |
0.24720 |
| 336.45 |
0.58240 |
0.16740 |
0.62980 |
0.21400 |
| 336.74 |
0.44590 |
0.36140 |
0.56160 |
0.29410 |
| 336.94 |
0.36890 |
0.56330 |
0.58110 |
0.34790 |
| 337.05 |
0.39740 |
0.43080 |
0.53030 |
0.32580 |
| 337.22 |
0.36210 |
0.52630 |
0.53460 |
0.34850 |
| 337.45 |
0.66810 |
0.05140 |
0.72490 |
0.10920 |
| 338.23 |
0.30340 |
0.60070 |
0.48630 |
0.39430 |
| 338.99 |
0.69460 |
0.01450 |
0.79170 |
0.03740 |
| 339.74 |
0.64930 |
0.01540 |
0.75230 |
0.04480 |
| 340.12 |
0.26870 |
0.29450 |
0.31070 |
0.33520 |
| 340.20 |
0.61630 |
0.01730 |
0.72260 |
0.05010 |
| 340.90 |
0.04660 |
0.41750 |
0.05560 |
0.42790 |
| 341.08 |
0.03540 |
0.56440 |
0.04860 |
0.47660 |
| 341.13 |
0.05710 |
0.28700 |
0.06370 |
0.39340 |
| 341.77 |
0.06400 |
0.19390 |
0.07000 |
0.34820 |
| 341.70 |
0.02670 |
0.67980 |
0.04260 |
0.52090 |
| 342.29 |
0.16110 |
0.79050 |
0.33240 |
0.57240 |
| 342.54 |
0.42240 |
0.03290 |
0.51110 |
0.09650 |
| 342.57 |
0.01990 |
0.75540 |
0.03560 |
0.56860 |
| 342.79 |
0.07100 |
0.11820 |
0.06720 |
0.29080 |
| 343.44 |
0.32180 |
0.04080 |
0.39190 |
0.12700 |
| 343.60 |
0.01590 |
0.81270 |
0.03110 |
0.61620 |
| 344.61 |
0.07600 |
0.06260 |
0.08810 |
0.21910 |
| 344.73 |
0.01170 |
0.85680 |
0.02640 |
0.66480 |
| 344.78 |
0.27470 |
0.04410 |
0.34190 |
0.13440 |
| 345.39 |
0.04240 |
0.88360 |
0.10240 |
0.71280 |
| 345.84 |
0.00760 |
0.89400 |
0.02110 |
0.71570 |
| 347.06 |
0.03990 |
0.03770 |
0.04980 |
0.17990 |
| 348.93 |
0.05990 |
0.01420 |
0.08320 |
0.08380 |
(T - temperature, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Chen G.-H.; Wang Q.; Ma Z.M.; Yan X.-H.; Han S.-J.: Phase Equilibria at Superatmospheric Pressures for Systems Containing Halohydrocarbon, Aromatic Hydrocarbon, and Alcohol. J.Chem.Eng.Data 40 (1995) 361-366 |
Vapor-Liquid Equilibrium Data Set 16216
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
CHCl3 |
119.377 |
67-66-3 |
Chloroform |
| 2 |
C2H6O |
46.069 |
64-17-5 |
Ethanol |
| 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] |
| 369.82 |
0.48110 |
0.45980 |
0.56010 |
0.39120 |
| 370.22 |
0.49820 |
0.37670 |
0.54280 |
0.36110 |
| 370.46 |
0.43370 |
0.46470 |
0.50480 |
0.40890 |
| 370.72 |
0.51190 |
0.30750 |
0.53630 |
0.33560 |
| 371.68 |
0.33100 |
0.50780 |
0.40190 |
0.45200 |
| 371.83 |
0.32140 |
0.55390 |
0.40390 |
0.47540 |
| 372.51 |
0.25430 |
0.55870 |
0.31610 |
0.50000 |
| 372.74 |
0.22780 |
0.58500 |
0.28750 |
0.51680 |
| 372.87 |
0.40160 |
0.27920 |
0.41520 |
0.35430 |
| 372.99 |
0.34850 |
0.34590 |
0.34850 |
0.39590 |
| 373.01 |
0.23150 |
0.66590 |
0.32250 |
0.55150 |
| 373.37 |
0.17210 |
0.60330 |
0.21900 |
0.54180 |
| 373.54 |
0.88660 |
0.01750 |
0.91020 |
0.03490 |
| 373.82 |
0.13470 |
0.49910 |
0.15360 |
0.50730 |
| 373.90 |
0.82170 |
0.02970 |
0.85400 |
0.06170 |
| 374.09 |
0.10320 |
0.61310 |
0.12870 |
0.56480 |
| 374.30 |
0.13200 |
0.44900 |
0.14380 |
0.48960 |
| 374.79 |
0.07730 |
0.71150 |
0.10510 |
0.63030 |
| 374.80 |
0.07060 |
0.44870 |
0.07510 |
0.50370 |
| 374.97 |
0.26320 |
0.35780 |
0.28240 |
0.42220 |
| 374.97 |
0.63740 |
0.06600 |
0.67090 |
0.14120 |
| 375.00 |
0.47850 |
0.18710 |
0.51390 |
0.26240 |
| 375.23 |
0.12730 |
0.78460 |
0.20270 |
0.66780 |
| 376.05 |
0.05010 |
0.81250 |
0.07910 |
0.71190 |
| 377.10 |
0.03560 |
0.86810 |
0.06920 |
0.76690 |
| 378.46 |
0.02360 |
0.91440 |
0.04290 |
0.83340 |
| 379.62 |
0.19090 |
0.15630 |
0.19440 |
0.31710 |
| 381.83 |
0.12170 |
0.08030 |
0.13440 |
0.22870 |
(T - temperature, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Chen G.-H.; Wang Q.; Ma Z.M.; Yan X.-H.; Han S.-J.: Phase Equilibria at Superatmospheric Pressures for Systems Containing Halohydrocarbon, Aromatic Hydrocarbon, and Alcohol. J.Chem.Eng.Data 40 (1995) 361-366 |
Vapor-Liquid Equilibrium Data Set 16561
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
CHCl3 |
119.377 |
67-66-3 |
Chloroform |
| 2 |
C2H6O |
46.069 |
64-17-5 |
Ethanol |
| 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] |
| 353.26 |
0.00000 |
0.00000 |
| 351.30 |
0.00000 |
1.00000 |
| 334.28 |
1.00000 |
0.00000 |
| 344.96 |
0.07260 |
0.86310 |
| 343.32 |
0.10520 |
0.81460 |
| 342.25 |
0.13900 |
0.78380 |
| 341.06 |
0.16970 |
0.75590 |
| 340.18 |
0.20060 |
0.72780 |
| 339.47 |
0.22930 |
0.70160 |
| 334.16 |
0.63800 |
0.26960 |
| 334.39 |
0.59780 |
0.31560 |
| 334.59 |
0.56150 |
0.35710 |
| 334.87 |
0.52180 |
0.40270 |
| 335.09 |
0.48730 |
0.44210 |
| 335.43 |
0.45720 |
0.47660 |
| 335.99 |
0.41850 |
0.49870 |
| 340.62 |
0.08810 |
0.27890 |
| 340.50 |
0.08040 |
0.34190 |
| 340.26 |
0.10210 |
0.38240 |
| 340.06 |
0.12220 |
0.41760 |
| 340.13 |
0.11350 |
0.45890 |
| 339.96 |
0.13680 |
0.48560 |
| 340.09 |
0.12680 |
0.52320 |
| 340.25 |
0.11800 |
0.55620 |
| 338.26 |
0.28390 |
0.55690 |
| 337.81 |
0.30930 |
0.49850 |
| 337.60 |
0.33010 |
0.45240 |
| 338.03 |
0.31140 |
0.42690 |
| 338.31 |
0.29480 |
0.40410 |
| 338.52 |
0.27640 |
0.37890 |
| 338.80 |
0.26090 |
0.35760 |
| 339.08 |
0.24690 |
0.33840 |
| 339.23 |
0.23260 |
0.31890 |
| 339.42 |
0.22020 |
0.30180 |
(T - temperature, x - liquid mole fraction)
Reference
| Source |
| Li H.; Han S.; Teng Y.: Bubble points measurements for system chloroform-ethanol-benzene by inclined ebulliometer. Fluid Phase Equilib. 113 (1995) 185-195 |
List of All References
Vapor-Liquid Equilibrium Data Overview
© DDBST GmbH