Page 206 - Design of Simple and Robust Process Plants
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5.7 Simplification and Ranking per Unit Operation  191
                The status of knowledge at any one time determines into which category the reactor
                 design will fall. Thus, the selection of category is seldom an option at the design
                 stage, but will be made at the research stage, when three general rules to simplify
                 the development must be followed:
                   1 ®Reactions within a gas phase should, preferably, be converted to liquid phase
                      reactions, the advantages of which include:
                   .  better mixing;
                   .  higher concentrations;
                   .  easier heat conditioning; and
                   .  smaller equipment dimensions.

                 An exception is that of reactions which take place inside the catalyst particle, where
                 diffusion plays an important role. In such cases, the high diffusion coefficients of
                 gases offer a major advantage.

                   2 ®Heterogeneous reactions should, preferably, be converted to one phase, either
                      liquid or gas. The advantages of homogenous reactions are:
                   .  no mass and heat transfer limitation between phases; and
                   .  flow conditions are more easily implemented.
                This also explains why reactor intensification concentrates on heterogeneous reactor
                 systems, to minimize these limitations (see Section 5.5).
                   3 ®Integration of multiple functions in one reactor system should also be con-
                      sidered as an option, especially for equilibrium reactions, where shifting of
                      the reaction will lead to higher conversions and selectivities (see Section
                      5.3.1)
                The reactor category is predetermined at the design stage, and will fall into one of the
                 above categories. The macro design of the reactor within the selected category will
                 be determined by:
                   .  catalyst selection;
                   .  energy household; and/or
                   .  mixing/flow distribution.
                 For priority ranking in terms of simplicity of the different categories, the chemistry
                 (as well as the catalyst selection) is beyond this discussion. However, the types of
                 reactor employed in the different categories will be discussed briefly, and a priority
                 ranking will be made. In the examples given, the related heat transfer is seen as
                 heat removal, although it is also applicable to heat addition (in which case the termi-
                 nology must be adapted).
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