Application of Feasibility Diagram Column Feasible Split

Application of Feasibility Diagram Column Feasible Split 

The corresponding operating lines for the rectifying and stripping section are Rectifying  

Equation (44) can also be used to obtain a direct relationship between the feed, distillate and bottom compositions, i.e., 

Since the form of the transformed mass balances and the operating equations for the kinetically controlled reactive distillation are identical to the corresponding equations for conventional countercurrent distillation, we therefore can apply the same 

4 Thermodynamic and Kinetic Effects on the Feasible Products of Reactive Distillation 

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