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 2578
Components
No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
1 |
CHCl3 |
119.377 |
67-66-3 |
Chloroform |
2 |
CH4O |
32.042 |
67-56-1 |
Methanol |
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] |
334.65 |
0.10000 |
0.10000 |
0.11000 |
0.42000 |
332.15 |
0.10000 |
0.20000 |
0.09000 |
0.49000 |
331.65 |
0.10000 |
0.30000 |
0.10500 |
0.50500 |
331.25 |
0.10000 |
0.40000 |
0.11500 |
0.49500 |
331.15 |
0.10000 |
0.50000 |
0.11000 |
0.56000 |
330.15 |
0.10000 |
0.60000 |
0.12000 |
0.57000 |
330.65 |
0.10000 |
0.70000 |
0.18000 |
0.59000 |
331.15 |
0.10000 |
0.80000 |
0.19000 |
0.64500 |
333.95 |
0.20000 |
0.10000 |
0.18000 |
0.39500 |
331.35 |
0.20000 |
0.20000 |
0.18000 |
0.47500 |
331.15 |
0.20000 |
0.30000 |
0.19000 |
0.50400 |
330.95 |
0.20000 |
0.40000 |
0.19000 |
0.51000 |
330.15 |
0.20000 |
0.50000 |
0.15000 |
0.55500 |
329.15 |
0.20000 |
0.60000 |
0.28000 |
0.52000 |
329.45 |
0.20000 |
0.70000 |
0.33000 |
0.55000 |
334.15 |
0.30000 |
0.10000 |
0.29000 |
0.38500 |
331.35 |
0.30000 |
0.20000 |
0.27000 |
0.45000 |
331.45 |
0.30000 |
0.30000 |
0.28000 |
0.47000 |
331.15 |
0.30000 |
0.40000 |
0.28000 |
0.48000 |
329.15 |
0.30000 |
0.50000 |
0.35500 |
0.47500 |
328.65 |
0.30000 |
0.60000 |
0.42500 |
0.49500 |
333.15 |
0.40000 |
0.10000 |
0.37500 |
0.36500 |
332.15 |
0.40000 |
0.20000 |
0.38500 |
0.38000 |
331.15 |
0.40000 |
0.30000 |
0.36000 |
0.42000 |
329.15 |
0.40000 |
0.40000 |
0.34500 |
0.46500 |
328.65 |
0.40000 |
0.50000 |
0.48000 |
0.44000 |
332.65 |
0.50000 |
0.10000 |
0.47200 |
0.34000 |
331.15 |
0.50000 |
0.20000 |
0.45500 |
0.39000 |
330.65 |
0.50000 |
0.30000 |
0.47000 |
0.39000 |
328.65 |
0.50000 |
0.40000 |
0.53000 |
0.39500 |
331.55 |
0.60000 |
0.10000 |
0.56000 |
0.30500 |
328.55 |
0.60000 |
0.30000 |
0.56000 |
0.36000 |
331.35 |
0.70000 |
0.10000 |
0.64000 |
0.26000 |
330.15 |
0.70000 |
0.20000 |
0.64000 |
0.28500 |
330.65 |
0.80000 |
0.10000 |
0.72500 |
0.20000 |
(T - temperature, x - liquid mole fraction, y - vapor mole fraction)
Reference
Source |
Shishkin K.N.; Kotsyuba A.A.: Investigation in the area of rectification of binary and ternary azeotropic mixtures. II. Tr.Dnepropetr.Khim.Tekhnol.Inst. 4 (1955) 11-17 |
Vapor-Liquid Equilibrium Data Set 6481
Components
No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
1 |
CHCl3 |
119.377 |
67-66-3 |
Chloroform |
2 |
CH4O |
32.042 |
67-56-1 |
Methanol |
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] |
327.52 |
0.52800 |
0.40100 |
0.38000 |
0.58800 |
327.90 |
0.62500 |
0.28100 |
0.57700 |
0.37700 |
328.00 |
0.45400 |
0.45100 |
0.49100 |
0.44100 |
328.25 |
0.52600 |
0.41100 |
0.42100 |
0.54300 |
328.31 |
0.33900 |
0.55600 |
0.33100 |
0.61400 |
328.39 |
0.54200 |
0.37700 |
0.43700 |
0.53000 |
328.44 |
0.45500 |
0.46400 |
0.37700 |
0.57900 |
328.47 |
0.29000 |
0.60300 |
0.29800 |
0.63300 |
328.50 |
0.57900 |
0.34200 |
0.45600 |
0.51300 |
328.51 |
0.43900 |
0.45600 |
0.37500 |
0.57600 |
328.62 |
0.26900 |
0.62200 |
0.28800 |
0.64100 |
328.65 |
0.32000 |
0.64400 |
0.35300 |
0.62500 |
328.80 |
0.29800 |
0.59100 |
0.29900 |
0.63600 |
328.90 |
0.22100 |
0.66300 |
0.25000 |
0.66700 |
328.92 |
0.64600 |
0.28600 |
0.50000 |
0.47500 |
329.04 |
0.42500 |
0.43300 |
0.35000 |
0.58000 |
329.21 |
0.58800 |
0.17700 |
0.52800 |
0.35000 |
329.35 |
0.57000 |
0.21000 |
0.51600 |
0.36600 |
329.41 |
0.43600 |
0.30700 |
0.41500 |
0.43100 |
329.52 |
0.71800 |
0.21900 |
0.55200 |
0.42600 |
329.60 |
0.28100 |
0.62000 |
0.38200 |
0.51000 |
329.62 |
0.34300 |
0.58600 |
0.34100 |
0.57700 |
329.65 |
0.47700 |
0.34300 |
0.37700 |
0.54700 |
329.70 |
0.25500 |
0.53100 |
0.29700 |
0.51100 |
329.70 |
0.36300 |
0.36100 |
0.36300 |
0.45100 |
329.95 |
0.29100 |
0.42800 |
0.30200 |
0.49000 |
329.97 |
0.22600 |
0.52500 |
0.20400 |
0.61300 |
330.05 |
0.61900 |
0.22400 |
0.46500 |
0.45300 |
330.10 |
0.21100 |
0.56500 |
0.25400 |
0.53300 |
330.15 |
0.23400 |
0.55300 |
0.27600 |
0.52900 |
330.30 |
0.24500 |
0.50600 |
0.18600 |
0.65900 |
330.31 |
0.14400 |
0.58800 |
0.13900 |
0.68500 |
330.32 |
0.20000 |
0.47800 |
0.17400 |
0.64500 |
330.50 |
0.16600 |
0.63600 |
0.21100 |
0.57100 |
330.55 |
0.16500 |
0.50900 |
0.17600 |
0.54300 |
330.62 |
0.16000 |
0.52900 |
0.17600 |
0.54500 |
330.65 |
0.52500 |
0.14800 |
0.47200 |
0.34400 |
330.65 |
0.11900 |
0.64700 |
0.15200 |
0.58400 |
330.70 |
0.12400 |
0.62600 |
0.15200 |
0.57900 |
330.72 |
0.20000 |
0.37300 |
0.18600 |
0.51500 |
330.75 |
0.11700 |
0.56100 |
0.13000 |
0.56800 |
330.80 |
0.22000 |
0.34100 |
0.20300 |
0.50200 |
330.80 |
0.15100 |
0.43400 |
0.14800 |
0.53100 |
330.82 |
0.11300 |
0.56600 |
0.12500 |
0.56800 |
330.88 |
0.78400 |
0.14000 |
0.62900 |
0.34400 |
330.92 |
0.10200 |
0.47100 |
0.10100 |
0.55700 |
331.00 |
0.10900 |
0.53900 |
0.11700 |
0.56100 |
331.03 |
0.17700 |
0.70800 |
0.26100 |
0.57600 |
331.05 |
0.33600 |
0.27300 |
0.22700 |
0.59200 |
331.15 |
0.08600 |
0.74400 |
0.12600 |
0.63000 |
331.16 |
0.00600 |
0.59500 |
0.00700 |
0.61000 |
331.16 |
0.23600 |
0.32200 |
0.16900 |
0.61100 |
331.18 |
0.02100 |
0.73100 |
0.03900 |
0.61100 |
331.18 |
0.03300 |
0.68500 |
0.04100 |
0.62700 |
331.20 |
0.02300 |
0.57600 |
0.02400 |
0.60300 |
331.20 |
0.01000 |
0.59200 |
0.01100 |
0.60800 |
331.20 |
0.01900 |
0.58300 |
0.02100 |
0.60200 |
331.20 |
0.03200 |
0.63200 |
0.03700 |
0.61000 |
331.22 |
0.01600 |
0.58400 |
0.01700 |
0.60500 |
331.23 |
0.01700 |
0.65400 |
0.01900 |
0.62200 |
331.24 |
0.01100 |
0.65300 |
0.01200 |
0.62300 |
331.25 |
0.27700 |
0.31300 |
0.21500 |
0.61500 |
331.25 |
0.01700 |
0.69100 |
0.02100 |
0.53300 |
331.25 |
0.13500 |
0.33800 |
0.11900 |
0.52600 |
331.25 |
0.19300 |
0.27900 |
0.16700 |
0.50200 |
331.26 |
0.00700 |
0.68200 |
0.00800 |
0.62700 |
331.27 |
0.08600 |
0.42300 |
0.08000 |
0.54000 |
331.30 |
0.05300 |
0.72000 |
0.06100 |
0.63700 |
331.31 |
0.03400 |
0.71100 |
0.04300 |
0.63600 |
331.34 |
0.09000 |
0.30800 |
0.06800 |
0.54600 |
331.37 |
0.02300 |
0.74400 |
0.03000 |
0.65300 |
331.37 |
0.02800 |
0.74000 |
0.03800 |
0.65200 |
331.37 |
0.04200 |
0.40000 |
0.03700 |
0.56800 |
331.43 |
0.03600 |
0.45500 |
0.05000 |
0.54200 |
331.45 |
0.01200 |
0.75100 |
0.01500 |
0.66100 |
331.47 |
0.02700 |
0.73000 |
0.03500 |
0.64900 |
331.48 |
0.00700 |
0.75800 |
0.00800 |
0.66000 |
331.49 |
0.05400 |
0.37600 |
0.04600 |
0.55700 |
331.50 |
0.06800 |
0.33400 |
0.05900 |
0.52000 |
331.51 |
0.08000 |
0.33400 |
0.06800 |
0.53900 |
331.53 |
0.11300 |
0.83700 |
0.18900 |
0.74900 |
331.56 |
0.05900 |
0.49500 |
0.05300 |
0.59100 |
331.57 |
0.08600 |
0.34800 |
0.07500 |
0.53500 |
331.63 |
0.17300 |
0.27400 |
0.14800 |
0.50400 |
331.65 |
0.04700 |
0.35900 |
0.04000 |
0.54100 |
331.75 |
0.04900 |
0.35600 |
0.04200 |
0.51000 |
331.76 |
0.02600 |
0.80500 |
0.04000 |
0.68100 |
331.77 |
0.11200 |
0.34400 |
0.09900 |
0.52900 |
331.82 |
0.09200 |
0.82400 |
0.16300 |
0.68100 |
331.83 |
0.54600 |
0.21300 |
0.42900 |
0.43400 |
331.85 |
0.07000 |
0.27500 |
0.05600 |
0.53900 |
331.90 |
0.03300 |
0.33200 |
0.02800 |
0.55500 |
331.98 |
0.22300 |
0.27500 |
0.18000 |
0.56900 |
332.00 |
0.02900 |
0.69900 |
0.03500 |
0.63500 |
332.00 |
0.06600 |
0.43600 |
0.06000 |
0.56600 |
332.05 |
0.06000 |
0.25200 |
0.04900 |
0.52500 |
332.09 |
0.10600 |
0.30000 |
0.09200 |
0.52200 |
332.11 |
0.05300 |
0.26000 |
0.03500 |
0.52200 |
332.11 |
0.12000 |
0.22900 |
0.09800 |
0.51100 |
332.05 |
0.04400 |
0.31300 |
0.03700 |
0.53200 |
332.15 |
0.09600 |
0.33300 |
0.09300 |
0.39900 |
332.15 |
0.28000 |
0.16200 |
0.24200 |
0.43700 |
332.18 |
0.62500 |
0.17900 |
0.51500 |
0.40200 |
332.20 |
0.84000 |
0.09800 |
0.72300 |
0.25500 |
332.25 |
0.09000 |
0.35700 |
0.07900 |
0.53600 |
332.30 |
0.15800 |
0.21700 |
0.13000 |
0.49700 |
332.35 |
0.07600 |
0.85700 |
0.14200 |
0.71800 |
332.45 |
0.06400 |
0.33100 |
0.05400 |
0.54600 |
332.53 |
0.11000 |
0.20200 |
0.08900 |
0.49600 |
332.60 |
0.10000 |
0.26300 |
0.08500 |
0.50900 |
332.73 |
0.86500 |
0.08200 |
0.77800 |
0.20100 |
332.77 |
0.06600 |
0.30800 |
0.06000 |
0.45100 |
332.80 |
0.02200 |
0.87900 |
0.03900 |
0.74700 |
332.81 |
0.11000 |
0.17700 |
0.08900 |
0.49000 |
333.12 |
0.09300 |
0.22200 |
0.07600 |
0.50000 |
333.20 |
0.08400 |
0.22200 |
0.06700 |
0.51800 |
333.34 |
0.05300 |
0.90200 |
0.11200 |
0.77400 |
333.35 |
0.08100 |
0.20500 |
0.06600 |
0.49800 |
333.47 |
0.14800 |
0.15000 |
0.12300 |
0.46000 |
333.60 |
0.03100 |
0.95600 |
0.07300 |
0.89200 |
333.80 |
0.70700 |
0.10200 |
0.63400 |
0.28500 |
334.28 |
0.28200 |
0.19000 |
0.22300 |
0.52900 |
334.45 |
0.73300 |
0.08800 |
0.69400 |
0.22600 |
334.47 |
0.03800 |
0.93000 |
0.08300 |
0.83300 |
334.52 |
0.45700 |
0.19400 |
0.42300 |
0.39000 |
334.55 |
0.85300 |
0.03800 |
0.82800 |
0.11800 |
334.55 |
0.12800 |
0.11500 |
0.10400 |
0.44700 |
334.81 |
0.76400 |
0.07300 |
0.74400 |
0.18100 |
334.90 |
0.43600 |
0.13200 |
0.38500 |
0.41000 |
334.93 |
0.35000 |
0.16000 |
0.28900 |
0.47800 |
335.15 |
0.18900 |
0.17700 |
0.14500 |
0.55000 |
335.30 |
0.02900 |
0.94800 |
0.06300 |
0.87400 |
335.45 |
0.11100 |
0.10900 |
0.09100 |
0.43400 |
335.81 |
0.02200 |
0.96000 |
0.05000 |
0.90200 |
335.92 |
0.16200 |
0.08800 |
0.14400 |
0.40100 |
338.65 |
0.24300 |
0.05300 |
0.24300 |
0.28000 |
339.65 |
0.47700 |
0.04200 |
0.53800 |
0.18600 |
342.45 |
0.20400 |
0.06500 |
0.21900 |
0.27600 |
342.85 |
0.24100 |
0.05100 |
0.28700 |
0.22600 |
344.65 |
0.26400 |
0.02200 |
0.34200 |
0.13000 |
344.75 |
0.07700 |
0.02500 |
0.08600 |
0.20300 |
(T - temperature, x - liquid mole fraction, y - vapor mole fraction)
Reference
Source |
Wisniak J.; Tamir A.: Vapor-Liquid Equilibria of the Ternary System Chloroform-Methanol Benzene. J.Chem.Eng.Data 23 (1978) 287-292 |
Vapor-Liquid Equilibrium Data Set 18035
Components
No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
1 |
CHCl3 |
119.377 |
67-66-3 |
Chloroform |
2 |
CH4O |
32.042 |
67-56-1 |
Methanol |
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] |
353.24 |
0.00000 |
0.00000 |
0.00000 |
0.00000 |
337.70 |
0.00000 |
1.00000 |
0.00000 |
1.00000 |
334.33 |
1.00000 |
0.00000 |
1.00000 |
0.00000 |
331.79 |
0.00800 |
0.81500 |
0.01200 |
0.68900 |
331.25 |
0.01100 |
0.73300 |
0.01500 |
0.64600 |
331.05 |
0.01600 |
0.61800 |
0.01800 |
0.61000 |
333.97 |
0.02800 |
0.91900 |
0.06000 |
0.80200 |
331.66 |
0.03600 |
0.80000 |
0.05700 |
0.67400 |
331.18 |
0.04400 |
0.45200 |
0.04200 |
0.57100 |
331.90 |
0.05300 |
0.82400 |
0.09100 |
0.68700 |
331.03 |
0.05300 |
0.70200 |
0.07100 |
0.62200 |
330.92 |
0.06200 |
0.56400 |
0.06700 |
0.58500 |
333.12 |
0.06400 |
0.88600 |
0.13000 |
0.75200 |
330.89 |
0.06500 |
0.59800 |
0.07400 |
0.59100 |
331.02 |
0.06600 |
0.48400 |
0.06600 |
0.57000 |
332.73 |
0.06600 |
0.18100 |
0.05400 |
0.51200 |
330.87 |
0.06900 |
0.63200 |
0.08200 |
0.59700 |
330.83 |
0.07800 |
0.58100 |
0.08800 |
0.58300 |
330.86 |
0.08400 |
0.53700 |
0.09000 |
0.57500 |
330.77 |
0.09100 |
0.58400 |
0.10400 |
0.58000 |
330.75 |
0.10000 |
0.67100 |
0.13100 |
0.59700 |
332.68 |
0.10100 |
0.17600 |
0.08300 |
0.50100 |
330.77 |
0.11000 |
0.52100 |
0.11800 |
0.56500 |
330.64 |
0.12100 |
0.56300 |
0.13800 |
0.56700 |
330.47 |
0.13600 |
0.61200 |
0.16700 |
0.57200 |
330.44 |
0.14200 |
0.63900 |
0.18400 |
0.57400 |
331.36 |
0.14800 |
0.29900 |
0.13000 |
0.51900 |
330.38 |
0.14900 |
0.67000 |
0.20400 |
0.57900 |
330.38 |
0.15600 |
0.70100 |
0.22800 |
0.58600 |
330.57 |
0.15700 |
0.49400 |
0.16700 |
0.54400 |
330.42 |
0.16300 |
0.73400 |
0.25700 |
0.59600 |
331.05 |
0.16500 |
0.34300 |
0.15000 |
0.52200 |
330.55 |
0.17200 |
0.76400 |
0.29200 |
0.60700 |
330.28 |
0.17300 |
0.58200 |
0.20900 |
0.55200 |
330.72 |
0.17700 |
0.79400 |
0.32600 |
0.61900 |
330.40 |
0.19800 |
0.46600 |
0.20700 |
0.52800 |
335.08 |
0.20200 |
0.08700 |
0.17900 |
0.40600 |
331.04 |
0.21200 |
0.30500 |
0.19200 |
0.50100 |
329.90 |
0.21900 |
0.57600 |
0.26900 |
0.53400 |
329.64 |
0.23700 |
0.60900 |
0.31200 |
0.53100 |
329.53 |
0.24000 |
0.69100 |
0.36500 |
0.54600 |
330.11 |
0.25100 |
0.44900 |
0.26800 |
0.50300 |
329.62 |
0.25900 |
0.54600 |
0.31200 |
0.51300 |
335.42 |
0.26200 |
0.06800 |
0.24000 |
0.37300 |
329.30 |
0.28000 |
0.57500 |
0.36000 |
0.50800 |
330.15 |
0.28300 |
0.37300 |
0.28200 |
0.48300 |
332.48 |
0.30200 |
0.13600 |
0.26100 |
0.42900 |
328.99 |
0.31800 |
0.54700 |
0.39100 |
0.48900 |
329.49 |
0.32500 |
0.43100 |
0.34800 |
0.47400 |
331.57 |
0.34400 |
0.17100 |
0.30100 |
0.43200 |
329.63 |
0.34500 |
0.38900 |
0.35500 |
0.46300 |
328.94 |
0.35900 |
0.47000 |
0.40500 |
0.46500 |
328.68 |
0.37000 |
0.48100 |
0.42800 |
0.45900 |
333.35 |
0.38100 |
0.09200 |
0.34000 |
0.37500 |
328.16 |
0.39700 |
0.50700 |
0.47500 |
0.44800 |
329.02 |
0.41000 |
0.38200 |
0.42500 |
0.44200 |
332.68 |
0.41400 |
0.09800 |
0.37100 |
0.36800 |
330.34 |
0.41500 |
0.22300 |
0.37400 |
0.42600 |
331.93 |
0.44300 |
0.11500 |
0.39400 |
0.37400 |
327.60 |
0.45300 |
0.48900 |
0.52100 |
0.43600 |
328.56 |
0.47200 |
0.35700 |
0.47800 |
0.41800 |
329.19 |
0.48200 |
0.27900 |
0.45700 |
0.41000 |
330.71 |
0.50300 |
0.14400 |
0.44700 |
0.37200 |
327.32 |
0.51000 |
0.43700 |
0.56600 |
0.39900 |
328.74 |
0.53900 |
0.26700 |
0.50700 |
0.39100 |
332.85 |
0.55000 |
0.07000 |
0.50500 |
0.30300 |
327.82 |
0.59000 |
0.30000 |
0.57000 |
0.37400 |
328.97 |
0.60800 |
0.18800 |
0.54500 |
0.35800 |
331.86 |
0.64700 |
0.06900 |
0.59100 |
0.27500 |
327.73 |
0.69300 |
0.21900 |
0.62200 |
0.33900 |
330.79 |
0.69500 |
0.07900 |
0.62100 |
0.27700 |
332.64 |
0.72900 |
0.04300 |
0.68900 |
0.20900 |
330.41 |
0.82900 |
0.05500 |
0.73700 |
0.21700 |
(T - temperature, x - liquid mole fraction, y - vapor mole fraction)
Reference
Source |
Kurihara K.; Hori H.; Kojima K.: Vapor-Liquid Equilibrium Data for Acetone + Methanol + Benzene, Chloroform + Methanol + Benzene, and Constituent Binary Systems at 101.3 kPa. J.Chem.Eng.Data 43 (1998) 264-268 |
List of All References
Vapor-Liquid Equilibrium Data Overview
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