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 11527
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C2H6O |
46.069 |
64-17-5 |
Ethanol |
| 2 |
H2O |
18.015 |
7732-18-5 |
Water |
| 3 |
C6H12 |
84.161 |
110-82-7 |
Cyclohexane |
Search the DDB for all data of this mixture
Constant Value
Data Table
| P [kPa] |
x1 [mol/mol] |
x2 [mol/mol] |
| 755.932 |
1.00000 |
0.00000 |
| 361.352 |
0.00000 |
1.00000 |
| 452.271 |
0.00000 |
0.00000 |
| 593.854 |
0.04760 |
0.00010 |
| 670.420 |
0.09090 |
0.00020 |
| 778.861 |
0.18390 |
0.00040 |
| 827.103 |
0.24630 |
0.00050 |
| 855.347 |
0.29710 |
0.00060 |
| 876.289 |
0.34510 |
0.00070 |
| 894.162 |
0.40280 |
0.00090 |
| 905.757 |
0.45060 |
0.00100 |
| 914.171 |
0.49480 |
0.00120 |
| 919.764 |
0.54950 |
0.00130 |
| 924.256 |
0.60190 |
0.00150 |
| 926.130 |
0.65230 |
0.00160 |
| 927.365 |
0.70140 |
0.00180 |
| 924.020 |
0.75120 |
0.00190 |
| 913.562 |
0.80000 |
0.00200 |
| 901.321 |
0.84010 |
0.00210 |
| 923.873 |
0.79680 |
0.05360 |
| 941.373 |
0.75690 |
0.10090 |
| 957.716 |
0.71240 |
0.15370 |
| 970.067 |
0.67580 |
0.19720 |
| 982.554 |
0.63300 |
0.24800 |
| 960.460 |
0.67040 |
0.04980 |
| 991.154 |
0.63010 |
0.10850 |
| 1008.717 |
0.59710 |
0.15620 |
| 1023.080 |
0.56630 |
0.20070 |
| 996.954 |
0.63290 |
0.17010 |
| 1010.558 |
0.59730 |
0.21730 |
| 1020.884 |
0.56280 |
0.26310 |
| 1033.759 |
0.52690 |
0.31060 |
| 851.431 |
0.81000 |
0.14800 |
| 915.543 |
0.76910 |
0.14000 |
| 951.831 |
0.72730 |
0.13190 |
| 974.256 |
0.68520 |
0.12390 |
| 987.403 |
0.64890 |
0.11710 |
| 1001.715 |
0.55400 |
0.09950 |
| 1004.875 |
0.50920 |
0.09140 |
| 1006.044 |
0.46690 |
0.08390 |
| 1005.932 |
0.42480 |
0.07650 |
| 1004.368 |
0.38250 |
0.06920 |
| 1001.975 |
0.34180 |
0.06220 |
| 963.375 |
0.63250 |
0.27340 |
| 1003.580 |
0.59880 |
0.25800 |
| 1036.859 |
0.55740 |
0.23940 |
| 1043.479 |
0.51730 |
0.22170 |
| 1049.927 |
0.47810 |
0.20470 |
| 1053.779 |
0.43940 |
0.18800 |
| 1057.098 |
0.40110 |
0.17170 |
| 1058.973 |
0.36210 |
0.15530 |
| 1061.362 |
0.32580 |
0.14020 |
| 1061.434 |
0.31040 |
0.13380 |
| 868.970 |
0.90330 |
0.00230 |
| 886.551 |
0.84900 |
0.06300 |
| 898.706 |
0.80540 |
0.11160 |
| 908.927 |
0.76260 |
0.15940 |
| 916.538 |
0.72480 |
0.20150 |
| 924.728 |
0.68150 |
0.24990 |
| 933.130 |
0.64140 |
0.29450 |
| 940.211 |
0.59200 |
0.34960 |
| 949.065 |
0.54720 |
0.39950 |
| 959.313 |
0.50400 |
0.44750 |
| 973.692 |
0.45360 |
0.50340 |
| 990.938 |
0.40740 |
0.55470 |
| 1012.370 |
0.36300 |
0.60380 |
| 1043.149 |
0.31630 |
0.65540 |
| 1066.642 |
0.27100 |
0.70500 |
(P - pressure, x - liquid mole fraction)
Reference
| Source |
| Gmehling J.: unpublished data. Unpublished Data (2011) 1-43 |
Vapor-Liquid Equilibrium Data Set 12077
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C2H6O |
46.069 |
64-17-5 |
Ethanol |
| 2 |
H2O |
18.015 |
7732-18-5 |
Water |
| 3 |
C6H12 |
84.161 |
110-82-7 |
Cyclohexane |
Search the DDB for all data of this mixture
Constant Value
Data Table
| P [kPa] |
x1 [mol/mol] |
x2 [mol/mol] |
| 114.860 |
0.00000 |
0.00000 |
| 130.740 |
1.00000 |
0.00000 |
| 57.510 |
0.00000 |
1.00000 |
| 174.428 |
0.90272 |
0.00069 |
| 192.016 |
0.80473 |
0.00061 |
| 199.514 |
0.70026 |
0.00053 |
| 202.074 |
0.60111 |
0.00046 |
| 202.870 |
0.49711 |
0.00038 |
| 146.089 |
0.04670 |
0.00003 |
| 182.548 |
0.09078 |
0.00006 |
| 192.143 |
0.15172 |
0.00011 |
| 195.755 |
0.19680 |
0.00014 |
| 198.246 |
0.24552 |
0.00018 |
| 199.966 |
0.29837 |
0.00022 |
| 201.099 |
0.34801 |
0.00026 |
| 201.881 |
0.40159 |
0.00030 |
| 202.502 |
0.50065 |
0.00038 |
| 177.116 |
0.76711 |
0.18120 |
| 195.871 |
0.73191 |
0.17278 |
| 206.919 |
0.69259 |
0.16341 |
| 213.172 |
0.65136 |
0.15363 |
| 216.544 |
0.61161 |
0.14421 |
| 218.517 |
0.57102 |
0.13461 |
| 219.978 |
0.52996 |
0.12492 |
| 220.974 |
0.49026 |
0.11557 |
| 221.788 |
0.44982 |
0.10605 |
| 222.642 |
0.40959 |
0.09660 |
| 223.282 |
0.37416 |
0.08829 |
| 199.001 |
0.57611 |
0.37580 |
| 219.494 |
0.54582 |
0.35582 |
| 224.987 |
0.51572 |
0.33607 |
| 226.151 |
0.49334 |
0.32142 |
| 225.943 |
0.49531 |
0.31199 |
| 225.973 |
0.48048 |
0.27910 |
| 192.048 |
0.80244 |
0.00061 |
| 198.020 |
0.76372 |
0.04905 |
| 203.561 |
0.72680 |
0.09522 |
| 212.762 |
0.64460 |
0.19790 |
| 216.572 |
0.60599 |
0.24609 |
| 220.341 |
0.56686 |
0.29490 |
| 225.149 |
0.50837 |
0.37478 |
| 212.007 |
0.19917 |
0.79859 |
| 190.236 |
0.29946 |
0.69499 |
| 171.718 |
0.39907 |
0.59270 |
| 206.684 |
0.45478 |
0.51723 |
| 185.501 |
0.67084 |
0.27798 |
| 206.786 |
0.63096 |
0.26129 |
| 220.245 |
0.56528 |
0.23395 |
| 222.596 |
0.53010 |
0.21934 |
| 223.852 |
0.49460 |
0.20463 |
| 224.599 |
0.45811 |
0.18952 |
| 225.229 |
0.42257 |
0.17482 |
| 225.761 |
0.38775 |
0.16043 |
| 226.229 |
0.35192 |
0.14565 |
| 165.512 |
0.85414 |
0.09653 |
| 185.177 |
0.80995 |
0.09146 |
| 196.918 |
0.76405 |
0.08622 |
| 207.170 |
0.67523 |
0.07612 |
| 209.911 |
0.63031 |
0.07104 |
| 211.780 |
0.58543 |
0.06598 |
| 213.100 |
0.54073 |
0.06094 |
| 213.822 |
0.49529 |
0.05584 |
| 214.808 |
0.43212 |
0.04875 |
| 215.373 |
0.38035 |
0.04297 |
| 157.946 |
0.94872 |
0.00073 |
| 185.409 |
0.85115 |
0.00065 |
| 196.704 |
0.74873 |
0.00057 |
| 200.833 |
0.65024 |
0.00050 |
| 202.317 |
0.55377 |
0.00042 |
| 202.570 |
0.49835 |
0.00038 |
(P - pressure, x - liquid mole fraction)
Reference
| Source |
| Gmehling J.: unpublished data. Unpublished Data (2011) 1-43 |
Vapor-Liquid Equilibrium Data Set 12660
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C2H6O |
46.069 |
64-17-5 |
Ethanol |
| 2 |
H2O |
18.015 |
7732-18-5 |
Water |
| 3 |
C6H12 |
84.161 |
110-82-7 |
Cyclohexane |
Search the DDB for all data of this mixture
Constant Value
Data Table
| P [kPa] |
x1 [mol/mol] |
x2 [mol/mol] |
| 428.390 |
1.00000 |
0.00000 |
| 198.530 |
0.00000 |
1.00000 |
| 288.240 |
0.00000 |
0.00000 |
| 533.296 |
0.66080 |
0.29200 |
| 586.564 |
0.62530 |
0.27550 |
| 610.307 |
0.59120 |
0.26000 |
| 621.389 |
0.56040 |
0.24620 |
| 630.052 |
0.51820 |
0.22730 |
| 635.841 |
0.48290 |
0.21170 |
| 638.117 |
0.44760 |
0.19620 |
| 640.297 |
0.41480 |
0.18180 |
| 642.276 |
0.37620 |
0.16490 |
| 643.799 |
0.34140 |
0.14980 |
| 645.291 |
0.30460 |
0.13390 |
| 576.067 |
0.52110 |
0.43100 |
| 624.986 |
0.49540 |
0.40890 |
| 638.002 |
0.46830 |
0.38610 |
| 643.066 |
0.44100 |
0.36330 |
| 647.716 |
0.41450 |
0.34120 |
| 577.328 |
0.53940 |
0.04660 |
| 603.876 |
0.50750 |
0.10380 |
| 621.044 |
0.47990 |
0.15310 |
| 632.692 |
0.45250 |
0.20190 |
| 640.813 |
0.42370 |
0.25310 |
| 645.392 |
0.39210 |
0.30910 |
| 391.546 |
0.04490 |
0.00010 |
| 465.180 |
0.10150 |
0.00030 |
| 501.559 |
0.16230 |
0.00040 |
| 520.280 |
0.21710 |
0.00050 |
| 534.991 |
0.27560 |
0.00060 |
| 543.257 |
0.32100 |
0.00070 |
| 549.429 |
0.33950 |
0.00080 |
| 555.632 |
0.44120 |
0.00110 |
| 558.261 |
0.49570 |
0.00120 |
| 560.793 |
0.54720 |
0.00140 |
| 561.095 |
0.59590 |
0.00150 |
| 562.070 |
0.64530 |
0.00160 |
| 560.065 |
0.69280 |
0.00180 |
| 556.788 |
0.73870 |
0.00190 |
| 550.425 |
0.78520 |
0.00200 |
| 541.398 |
0.82640 |
0.00210 |
| 534.681 |
0.84880 |
0.00220 |
| 582.672 |
0.67050 |
0.05780 |
| 598.263 |
0.63550 |
0.10740 |
| 616.852 |
0.57720 |
0.18960 |
| 619.673 |
0.54970 |
0.22840 |
| 628.851 |
0.52580 |
0.26210 |
| 634.972 |
0.49300 |
0.30830 |
| 640.927 |
0.45180 |
0.36620 |
| 598.345 |
0.42330 |
0.05020 |
| 620.662 |
0.40390 |
0.09430 |
| 634.024 |
0.38560 |
0.13550 |
| 640.722 |
0.36860 |
0.17390 |
| 611.295 |
0.32830 |
0.06470 |
| 633.931 |
0.31410 |
0.10600 |
| 634.012 |
0.30190 |
0.14130 |
| 561.534 |
0.43840 |
0.53630 |
| 620.688 |
0.42630 |
0.52130 |
| 640.991 |
0.41460 |
0.50670 |
| 506.164 |
0.82820 |
0.11760 |
| 542.939 |
0.78840 |
0.11170 |
| 568.540 |
0.73640 |
0.10400 |
| 582.092 |
0.70670 |
0.09970 |
| 593.089 |
0.65760 |
0.09260 |
| 597.464 |
0.61570 |
0.08660 |
| 598.611 |
0.57440 |
0.08080 |
| 601.240 |
0.52760 |
0.07420 |
| 603.852 |
0.48430 |
0.06810 |
| 604.641 |
0.43930 |
0.06190 |
| 604.754 |
0.39750 |
0.05610 |
| 604.217 |
0.34910 |
0.04950 |
(P - pressure, x - liquid mole fraction)
Reference
| Source |
| Gmehling J.: unpublished data. Unpublished Data (2011) 1-43 |
List of All References
Vapor-Liquid Equilibrium Data Overview
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