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 One Introduction<br />
1. Pressure swing distillation.<br />
2. Salted distillation.<br />
3. Extractive distillation.<br />
4. Azeotropic distillation.<br />
5. Reactive distillation.<br />
As shown above the presence <strong>of</strong> the azeotrope in a mixture makes<br />
separation by conventional distillation difficult. Azeotropes can <strong>for</strong>m distillation<br />
regions, which limit the separation. When reacive distillation process is used,<br />
improvements can be obtained by really integrating the tasks, on the following<br />
items:<br />
• On the reaction: because there is an equilibrium displacement, since the<br />
products are being withdrawn.<br />
• On the separation: because <strong>of</strong> the changes in the driving <strong>for</strong>ce <strong>for</strong> mass<br />
transfer due to the reaction.<br />
There are several applications <strong>of</strong> reactive distillation to separate azeotropic<br />
mixtures in industry, <strong>for</strong> example production <strong>of</strong> octane boosters (<strong>MTBE</strong>,<br />
TAME, <strong>and</strong> ETBE)<br />
2