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 23537
Components
| No. |
Formula |
Molar Mass |
CAS Registry Number |
Name |
| 1 |
C2H3N |
41.053 |
75-05-8 |
Acetonitrile |
| 2 |
H2O |
18.015 |
7732-18-5 |
Water |
| 3 |
C6H12O2 |
116.160 |
123-86-4 |
Acetic acid butyl ester |
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] |
| 354.72 |
1.00000 |
0.00000 |
1.00000 |
0.00000 |
| 373.15 |
0.00000 |
1.00000 |
0.00000 |
1.00000 |
| 399.00 |
0.00000 |
0.00000 |
0.00000 |
0.00000 |
| 349.90 |
0.70430 |
0.27320 |
0.68090 |
0.30620 |
| 349.98 |
0.61480 |
0.36100 |
0.64800 |
0.33590 |
| 350.07 |
0.76520 |
0.21620 |
0.71280 |
0.27830 |
| 350.15 |
0.53720 |
0.44420 |
0.62400 |
0.35710 |
| 350.35 |
0.81330 |
0.17140 |
0.74710 |
0.24590 |
| 350.39 |
0.44880 |
0.53950 |
0.60730 |
0.37070 |
| 350.49 |
0.63250 |
0.28140 |
0.61810 |
0.33930 |
| 350.51 |
0.57670 |
0.34540 |
0.59060 |
0.36300 |
| 350.59 |
0.65700 |
0.25370 |
0.63020 |
0.32740 |
| 350.67 |
0.69810 |
0.21980 |
0.65670 |
0.30520 |
| 350.81 |
0.74610 |
0.18310 |
0.69460 |
0.27620 |
| 350.89 |
0.87420 |
0.11880 |
0.79620 |
0.20040 |
| 351.15 |
0.78460 |
0.14850 |
0.72620 |
0.24660 |
| 351.74 |
0.90900 |
0.08020 |
0.83370 |
0.15990 |
| 352.02 |
0.89250 |
0.08030 |
0.83290 |
0.15310 |
| 352.26 |
0.84930 |
0.08940 |
0.79930 |
0.17550 |
| 352.38 |
0.87170 |
0.07840 |
0.81560 |
0.16150 |
| 352.76 |
0.85080 |
0.07710 |
0.80930 |
0.15960 |
| 353.20 |
0.94880 |
0.05000 |
0.91050 |
0.08930 |
| 353.36 |
0.94940 |
0.04710 |
0.92880 |
0.06950 |
| 353.56 |
0.81160 |
0.07030 |
0.79550 |
0.15900 |
| 353.60 |
0.94490 |
0.04310 |
0.91430 |
0.08160 |
| 353.70 |
0.96280 |
0.03590 |
0.93550 |
0.06350 |
| 353.82 |
0.95610 |
0.02670 |
0.93240 |
0.06080 |
| 354.00 |
0.79080 |
0.06910 |
0.79030 |
0.15670 |
| 354.02 |
0.92280 |
0.04300 |
0.90760 |
0.07760 |
| 354.16 |
0.93790 |
0.02560 |
0.92300 |
0.06120 |
| 354.32 |
0.98600 |
0.01140 |
0.97370 |
0.02500 |
| 354.46 |
0.89910 |
0.04350 |
0.89840 |
0.07800 |
| 354.50 |
0.92170 |
0.02430 |
0.91780 |
0.05960 |
| 354.90 |
0.89220 |
0.02450 |
0.90530 |
0.06080 |
| 355.36 |
0.86810 |
0.02630 |
0.89770 |
0.06060 |
| 355.44 |
0.72200 |
0.06040 |
0.77030 |
0.15570 |
| 355.81 |
0.65160 |
0.07070 |
0.71680 |
0.19400 |
| 355.89 |
0.83770 |
0.03590 |
0.89140 |
0.05880 |
| 356.51 |
0.81420 |
0.02310 |
0.88250 |
0.05780 |
| 356.59 |
0.60140 |
0.07350 |
0.69370 |
0.20370 |
| 357.07 |
0.78670 |
0.02380 |
0.87730 |
0.05400 |
| 357.71 |
0.75980 |
0.02130 |
0.86410 |
0.06400 |
| 358.36 |
0.71760 |
0.03240 |
0.86790 |
0.04740 |
| 358.44 |
0.50960 |
0.06640 |
0.65150 |
0.21840 |
| 359.06 |
0.70010 |
0.01600 |
0.86070 |
0.04490 |
| 359.78 |
0.66900 |
0.01790 |
0.85010 |
0.04550 |
| 360.17 |
0.43530 |
0.06310 |
0.61160 |
0.23400 |
| 360.49 |
0.64040 |
0.01720 |
0.84240 |
0.04510 |
| 361.34 |
0.61130 |
0.01390 |
0.83240 |
0.04230 |
| 362.52 |
0.56640 |
0.01500 |
0.82100 |
0.03780 |
| 362.74 |
0.50020 |
0.02260 |
0.74770 |
0.10510 |
| 363.47 |
0.53530 |
0.01380 |
0.80900 |
0.03710 |
| 364.28 |
0.46250 |
0.01690 |
0.73740 |
0.09570 |
| 364.67 |
0.35090 |
0.03780 |
0.60110 |
0.19220 |
| 365.00 |
0.40180 |
0.02970 |
0.67700 |
0.13180 |
| 365.39 |
0.43560 |
0.01780 |
0.72880 |
0.07910 |
| 366.02 |
0.38990 |
0.02190 |
0.67950 |
0.11840 |
| 366.65 |
0.32460 |
0.03200 |
0.59920 |
0.17150 |
| 368.33 |
0.30260 |
0.03080 |
0.59390 |
0.15530 |
| 372.34 |
0.22130 |
0.03010 |
0.51480 |
0.16470 |
| 372.63 |
0.24990 |
0.01540 |
0.57880 |
0.11280 |
| 374.67 |
0.19720 |
0.01920 |
0.52150 |
0.14360 |
| 383.40 |
0.12240 |
0.00870 |
0.41010 |
0.06410 |
(T - temperature, x - liquid mole fraction, y - vapor mole fraction)
Reference
| Source |
| Acosta J.; Arce A.; Rodil E.; Soto A.: A Thermodynamic Study on Binary and Ternary Mixtures of Acetonitrile, Water and Butyl Acetate. Fluid Phase Equilib. 203 (2002) 83-98 |
List of All References
Vapor-Liquid Equilibrium Data Overview
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