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Mathematical Modeling and Simulation for Production of MTBE

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Chapter Two Literature Survey<br />

2 C ↔ F<br />

(2.3)<br />

This reaction can be carried out in a conventional process setup as<br />

sketched on the left side <strong>of</strong> Figure (2.1), the objective is to produce C out <strong>of</strong><br />

reactants A <strong>and</strong> B, thereby making byproduct D. In addition, there are undesired<br />

side <strong>and</strong> consecutive reactions, so that the exit stream <strong>of</strong> the reactor will be a<br />

mixture <strong>of</strong> all components.<br />

A <strong>and</strong> B have to be separated <strong>and</strong> recycled, C has to be separated <strong>and</strong><br />

purified to separation, <strong>and</strong> D, E, <strong>and</strong> F have to be disposed <strong>of</strong>. Normally, this<br />

will require more than the single distillation column that is given in Figure (2.1).<br />

Shown on the right h<strong>and</strong> side <strong>of</strong> Figure (2.1) is a typical setup <strong>for</strong> reactive<br />

distillation column. The reactions will take place in the reactive section.<br />

Figure 2.1 Schematic representation <strong>of</strong> a conventional<br />

<strong>and</strong> reactive distillation process(Around, 1999)<br />

6

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