A new
design method for determining the structure of a fully thermally
coupled distillation column is proposed. The method involves approximate
group method and the Fenske equation. To design the prefractionator,
an approximate calculation procedure that relates compositions of
multicomponent vapor and liquid streams is developed to formulate
the expressions used to compute the number of stages. To investigate
the usability and performance of this design method, different feed
mixtures are tried. The results indicate that the method works well
for a variety of process conditions; the results show that the structure
design from group method leads to a process similar to a feasible
actual process. The structure design results and operating conditions
for the whole column system enable the examination of the optimal
internal flows and their effects on the structure design equations.
The results show that the proposed design method provides good initial
values for rigorous simulation.