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 16248
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
CHCl3 |
119.377 |
67-66-3 |
Chloroform |
| 2 |
C6H6 |
78.114 |
71-43-2 |
Benzene |
| 3 |
C4H10O |
74.123 |
71-36-3 |
1-Butanol |
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] |
| 391.61 |
0.00000 |
0.00000 |
0.00000 |
0.00000 |
| 354.41 |
0.00000 |
1.00000 |
0.00000 |
1.00000 |
| 335.37 |
1.00000 |
0.00000 |
1.00000 |
0.00000 |
| 348.60 |
0.39830 |
0.42650 |
0.58120 |
0.40110 |
| 349.75 |
0.35980 |
0.43420 |
0.55170 |
0.40660 |
| 350.97 |
0.32860 |
0.39860 |
0.49110 |
0.41580 |
| 351.76 |
0.30940 |
0.34680 |
0.49680 |
0.41660 |
| 352.08 |
0.35030 |
0.18670 |
0.66430 |
0.23640 |
| 352.72 |
0.28520 |
0.30300 |
0.52300 |
0.37670 |
| 352.80 |
0.28650 |
0.35090 |
0.51000 |
0.40700 |
| 353.14 |
0.36720 |
0.14240 |
0.69240 |
0.18510 |
| 353.30 |
0.33950 |
0.15290 |
0.68160 |
0.21380 |
| 353.62 |
0.30890 |
0.25700 |
0.58160 |
0.31670 |
| 354.42 |
0.26610 |
0.32950 |
0.47810 |
0.41040 |
| 355.00 |
0.30560 |
0.16340 |
0.65000 |
0.22960 |
| 355.18 |
0.22520 |
0.37930 |
0.39090 |
0.48400 |
| 355.21 |
0.17380 |
0.47570 |
0.28500 |
0.59000 |
| 355.26 |
0.25710 |
0.34190 |
0.45620 |
0.43360 |
| 356.30 |
0.23600 |
0.31320 |
0.43750 |
0.41710 |
| 356.72 |
0.20220 |
0.41040 |
0.34740 |
0.52350 |
| 357.56 |
0.22320 |
0.28000 |
0.43500 |
0.41920 |
| 358.05 |
0.25920 |
0.17540 |
0.55250 |
0.27890 |
| 361.09 |
0.18820 |
0.19710 |
0.43690 |
0.35320 |
| 362.45 |
0.13640 |
0.21410 |
0.34420 |
0.41410 |
| 363.05 |
0.16520 |
0.22190 |
0.36550 |
0.41710 |
| 364.91 |
0.09450 |
0.24080 |
0.25190 |
0.48930 |
| 366.09 |
0.12610 |
0.17460 |
0.32550 |
0.39910 |
| 366.75 |
0.06100 |
0.24020 |
0.16570 |
0.55160 |
| 369.63 |
0.09900 |
0.14040 |
0.32030 |
0.36030 |
| 371.81 |
0.08240 |
0.12070 |
0.27980 |
0.34110 |
(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 16249
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
CHCl3 |
119.377 |
67-66-3 |
Chloroform |
| 2 |
C6H6 |
78.114 |
71-43-2 |
Benzene |
| 3 |
C4H10O |
74.123 |
71-36-3 |
1-Butanol |
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] |
| 411.93 |
0.00000 |
0.00000 |
0.00000 |
0.00000 |
| 378.01 |
0.00000 |
1.00000 |
0.00000 |
1.00000 |
| 357.53 |
1.00000 |
0.00000 |
1.00000 |
0.00000 |
| 369.26 |
0.48110 |
0.49420 |
0.60970 |
0.36970 |
| 370.68 |
0.44630 |
0.41070 |
0.60960 |
0.34270 |
| 372.15 |
0.49360 |
0.12280 |
0.78760 |
0.09330 |
| 372.41 |
0.39510 |
0.38750 |
0.58590 |
0.34390 |
| 372.86 |
0.46600 |
0.18730 |
0.73610 |
0.15040 |
| 373.57 |
0.40950 |
0.25980 |
0.65960 |
0.24340 |
| 374.04 |
0.45020 |
0.14720 |
0.74050 |
0.14640 |
| 374.49 |
0.38050 |
0.32250 |
0.59550 |
0.31800 |
| 374.83 |
0.35560 |
0.34630 |
0.51790 |
0.35800 |
| 375.12 |
0.34680 |
0.37800 |
0.54470 |
0.37310 |
| 375.43 |
0.34190 |
0.43150 |
0.52680 |
0.41580 |
| 376.20 |
0.27100 |
0.48660 |
0.38450 |
0.49830 |
| 376.35 |
0.32120 |
0.31630 |
0.53620 |
0.34800 |
| 376.43 |
0.24080 |
0.53580 |
0.34000 |
0.54370 |
| 376.77 |
0.39550 |
0.16970 |
0.67000 |
0.16310 |
| 378.19 |
0.34860 |
0.19270 |
0.65840 |
0.19340 |
| 379.21 |
0.28830 |
0.28320 |
0.50210 |
0.34630 |
| 379.30 |
0.30800 |
0.20860 |
0.54980 |
0.25860 |
| 380.43 |
0.25330 |
0.23250 |
0.47380 |
0.31000 |
| 381.06 |
0.25640 |
0.25390 |
0.47660 |
0.34020 |
| 382.90 |
0.20880 |
0.26170 |
0.40710 |
0.36590 |
| 383.14 |
0.22560 |
0.22210 |
0.45410 |
0.33410 |
| 385.22 |
0.19760 |
0.19700 |
0.39610 |
0.32570 |
| 385.48 |
0.14700 |
0.28360 |
0.28770 |
0.45340 |
| 386.17 |
0.12500 |
0.25910 |
0.27510 |
0.43540 |
| 387.38 |
0.15860 |
0.15770 |
0.37370 |
0.29700 |
| 388.22 |
0.07810 |
0.26420 |
0.16460 |
0.49390 |
| 389.73 |
0.12270 |
0.13630 |
0.32540 |
0.28990 |
| 392.34 |
0.11410 |
0.11420 |
0.31560 |
0.25790 |
| 394.95 |
0.09540 |
0.09870 |
0.27770 |
0.22710 |
(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 16250
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
CHCl3 |
119.377 |
67-66-3 |
Chloroform |
| 2 |
C6H6 |
78.114 |
71-43-2 |
Benzene |
| 3 |
C4H10O |
74.123 |
71-36-3 |
1-Butanol |
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] |
| 425.25 |
0.00000 |
0.00000 |
0.00000 |
0.00000 |
| 393.58 |
0.00000 |
1.00000 |
0.00000 |
1.00000 |
| 372.35 |
1.00000 |
0.00000 |
1.00000 |
0.00000 |
| 380.80 |
0.68360 |
0.30890 |
0.78230 |
0.21530 |
| 382.32 |
0.63440 |
0.29360 |
0.74540 |
0.21740 |
| 384.21 |
0.58070 |
0.27430 |
0.76030 |
0.20530 |
| 385.80 |
0.53240 |
0.25630 |
0.73830 |
0.21630 |
| 387.35 |
0.48650 |
0.23470 |
0.70560 |
0.21100 |
| 389.51 |
0.43050 |
0.21260 |
0.66310 |
0.21280 |
| 393.08 |
0.38200 |
0.19050 |
0.60370 |
0.21840 |
| 395.19 |
0.27830 |
0.33780 |
0.45100 |
0.38040 |
| 397.48 |
0.24500 |
0.30280 |
0.38660 |
0.38280 |
| 400.75 |
0.18900 |
0.25950 |
0.34350 |
0.37180 |
| 401.93 |
0.21590 |
0.15490 |
0.44730 |
0.23850 |
| 402.99 |
0.16270 |
0.22200 |
0.30180 |
0.34950 |
| 403.02 |
0.23010 |
0.09250 |
0.49660 |
0.15700 |
| 405.08 |
0.14210 |
0.16930 |
0.26820 |
0.30170 |
| 405.10 |
0.18540 |
0.09350 |
0.40140 |
0.19680 |
| 406.45 |
0.12100 |
0.16710 |
0.22850 |
0.32600 |
| 408.15 |
0.17100 |
0.03270 |
0.41860 |
0.09720 |
| 408.76 |
0.09540 |
0.13440 |
0.21630 |
0.27080 |
| 410.70 |
0.08210 |
0.11530 |
0.20460 |
0.25530 |
| 413.99 |
0.06090 |
0.08440 |
0.16440 |
0.21260 |
| 416.51 |
0.04440 |
0.06340 |
0.12900 |
0.17320 |
| 418.50 |
0.03380 |
0.04840 |
0.09870 |
0.12840 |
(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 |
List of All References
Vapor-Liquid Equilibrium Data Overview
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