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Setting up the Aspen Plus Simulation

Re clions Reactions R MIBE-U (RFAC DIST) Data Brovr.  [Pg.215]

0 SpMflcatkxK Q SmiaHoo Options Q Stream Class m Substreams m 2 Umts-Sets Custom Urrits Report Options [Pg.215]

DESIGN OF MTBE AND ETBE REACTIVE DISTILLATION COLUMNS [Pg.216]

Reactions Reactions R-MTBE4J (REAC DIST) - Data Browser [Pg.216]

0 Spec/Kebons Q Simiiation Options Q Streem Cass S Substreams S Units-Sets Q Custom Units Q Report Optior s Components Properties Flowsheet Streams Utitoes Btocks Reactions r 1 Chemistry Reactions o R-MTBE U Convergence Flowsheeting Options Model Analysts Tools EO Configurabon Resdts Summary [Pg.216]


The steps in setting up the Aspen Plus simulation are outlined below. The rigorous RCSTR model is used, which requires specifying reactions and kinetic parameters. An alternative, which is useful in some systems with reversible reactions, is the RGIBBS reactor module. Kinetic parameters are not required. Chemical equilibrium compositions are calculated for given feed and reactor temperature and pressure. If the forward and reverse reactions are known to be fast, so that the reactor effluent is at equilibrium conditions, the RGIBBS reactor provides a simple way to model a reactor. In Chapter 3 we will illustrate how this type of reactor can incorporate some approximate dynamics for developing control systems. [Pg.73]


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