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 13155
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C4H6 |
54.092 |
106-99-0 |
1,3-Butadiene |
| 2 |
C2H3N |
41.053 |
75-05-8 |
Acetonitrile |
| 3 |
H2O |
18.015 |
7732-18-5 |
Water |
Search the DDB for all data of this mixture
Constant Value
Data Table
| P [kPa] |
x1 [mol/mol] |
x2 [mol/mol] |
| 199.317 |
0.03830 |
0.89640 |
| 199.317 |
0.04100 |
0.87580 |
| 248.380 |
0.05110 |
0.89660 |
| 248.380 |
0.05180 |
0.87790 |
| 297.309 |
0.06050 |
0.87780 |
| 297.309 |
0.06680 |
0.86800 |
| 297.309 |
0.06980 |
0.86120 |
| 346.372 |
0.07870 |
0.85300 |
| 346.372 |
0.08210 |
0.82700 |
| 346.372 |
0.09310 |
0.84510 |
| 395.301 |
0.09960 |
0.82990 |
| 395.301 |
0.10490 |
0.83950 |
| 395.301 |
0.11610 |
0.81810 |
| 444.363 |
0.12510 |
0.81180 |
| 444.363 |
0.13110 |
0.79530 |
| 493.293 |
0.16590 |
0.79350 |
| 542.355 |
0.16310 |
0.78710 |
| 542.355 |
0.18260 |
0.75510 |
| 542.355 |
0.18470 |
0.76510 |
| 542.355 |
0.19080 |
0.76980 |
| 199.317 |
0.02380 |
0.77030 |
| 199.317 |
0.02360 |
0.79490 |
| 199.317 |
0.02320 |
0.76210 |
| 199.317 |
0.02970 |
0.82230 |
| 209.183 |
0.02140 |
0.78170 |
| 248.380 |
0.02910 |
0.76140 |
| 248.380 |
0.02920 |
0.76780 |
| 248.380 |
0.03920 |
0.80190 |
| 248.380 |
0.03950 |
0.78770 |
| 248.380 |
0.03950 |
0.78390 |
| 248.380 |
0.03040 |
0.73030 |
| 248.380 |
0.04180 |
0.80770 |
| 248.380 |
0.04290 |
0.77920 |
| 292.509 |
0.05370 |
0.79400 |
| 297.309 |
0.04380 |
0.76980 |
| 297.309 |
0.04680 |
0.80130 |
| 297.309 |
0.05000 |
0.78020 |
| 297.309 |
0.05050 |
0.77560 |
| 297.309 |
0.05440 |
0.76800 |
| 346.372 |
0.06270 |
0.79090 |
| 346.372 |
0.07030 |
0.78000 |
| 346.372 |
0.07100 |
0.75150 |
| 346.372 |
0.07450 |
0.79030 |
| 351.438 |
0.06700 |
0.81810 |
| 356.371 |
0.06010 |
0.75070 |
| 359.304 |
0.07180 |
0.78020 |
| 395.567 |
0.08750 |
0.76750 |
| 400.500 |
0.08280 |
0.76830 |
| 400.500 |
0.08950 |
0.79910 |
| 444.630 |
0.09840 |
0.73150 |
| 444.630 |
0.10080 |
0.72740 |
| 444.630 |
0.11000 |
0.72670 |
| 493.293 |
0.12120 |
0.73540 |
| 493.293 |
0.14010 |
0.70640 |
| 591.285 |
0.15870 |
0.68760 |
| 199.317 |
0.02010 |
0.68210 |
| 199.317 |
0.02650 |
0.70430 |
| 248.380 |
0.03050 |
0.69340 |
| 248.380 |
0.03200 |
0.68580 |
| 297.309 |
0.04070 |
0.66280 |
| 297.309 |
0.05100 |
0.70040 |
| 297.309 |
0.03850 |
0.69330 |
| 346.372 |
0.04120 |
0.68730 |
| 346.372 |
0.05370 |
0.70320 |
| 346.372 |
0.05540 |
0.66800 |
| 395.301 |
0.06460 |
0.66720 |
| 395.301 |
0.06520 |
0.65520 |
| 395.301 |
0.07500 |
0.67960 |
| 444.363 |
0.07090 |
0.66150 |
| 444.363 |
0.08860 |
0.65920 |
| 493.293 |
0.09340 |
0.65400 |
| 493.293 |
0.10070 |
0.65050 |
| 493.293 |
0.10370 |
0.63950 |
| 542.355 |
0.12000 |
0.63880 |
| 591.285 |
0.14120 |
0.62090 |
| 591.285 |
0.16970 |
0.61980 |
(P - pressure, x - liquid mole fraction)
Reference
| Source |
| Jingzhou H.; Zhejiang Univ.: A Study on the Vapor-Liquid Equilibrium for the Mixture of C4 Hydrocarbon Components and Acetonitrile Containing Water. Huaxue-gongcheng (1975) 27-54 |
List of All References
Vapor-Liquid Equilibrium Data Overview
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