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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products are being withdrawn.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

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