Research Article
Feasibility of Batch Reactive Distillation with Equilibrium-Limited Consecutive Reactions in Rectifier, Stripper, or Middle-Vessel Column
Table 4
Parameters of the
Wilson model (cal/mol) [
7].
| | (-) | () |
| | MeOH-EtOH | 135.8113 | −132.0576 | | MeOH-DMC | 771.98 | 202.44 | | MeOH-MEC | 684.591 | 203.922 | | MeOH-DEC | 364.177 | 411.055 | | EtOH-DMC | 522.235 | 450.581 | | EtOH-MEC | 709.523 | 164.462 | | EtOH-DEC | 626.606 | 331.781 | | DMC-MEC | 323.814 | −311.777 | | DMC-DEC | −474.659 | 1000.0 | | MEC-DEC | 80.9023 | −83.1232 |
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