Mathematical Modeling and Simulation for Production of MTBE
Mathematical Modeling and Simulation for Production of MTBE
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 />
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