Hac

MeOH

Fig. 2.6 Comparison simulation: experiment for an equilibrium stage model

MeAC h=1m,

Rombopak 9M

h=1.85m, ICVT-rings, Uni Clausthal 9x9x2

Rombopak 9M

Water

Our calculations using an equilibrium stage model agreed well with the experiments based on separation performance measurements using catalytic rings as internals (Fig. 2.6). On the basis of these results, we have to contradict various publications that attribute the decrease to reaction-kinetic effects. The primary effect is the saddle-point character of the products and the associated choice of a second feed point. The options for calculation and especially interpretation of RD lines, which have merely been outlined here are implemented in the program SYNTHESISER, a software product from the first EU-project.

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