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280  Chapter 11: Preliminary Considerations in Chemical Reaction Engineering

                            relate to technical feasibility (e.g., can the required fractional conversion be achieved in
                            the size specified?), and to socio-economic feasibility (cost, safety, and environmental
                            considerations). The factors to be taken into account are listed in more detail in the
                            next section.
                              The design problem usually fits into the spectrum ranging from (1) the rational design
                            of a completely new reactor for a new process, to (2) the analysis of performance of an
                            existing reactor for an existing process. A common situation, between these extremes,
                            even for a new plant, is the modification of an existing type of reactor, the design of
                            which has evolved over time.


                            11.1.1.2  Matters  for  Consideration
                            Process design involves making decisions about a series of matters, on as rational and
                            quantitative a basis as possible, given the information available. The following is an
                            illustrative list of such matters but not an exhaustive one; the items are not all mutually
                            exclusive.
                               (1)  type of processing
                                     batch
                                     continuous
                                     semibatch or semicontinuous
                                       batch with respect to (specified phase or phases)
                                       continuous with respect to (specified phase or phases)
                               (2) type and nature of reacting system
                                     reactant(s) and product(s)
                                     simple
                                     complex (desirable, undesirable products)
                                     stoichiometry
                                     phases, number of phases
                                     catalytic (choice of catalyst) or noncatalytic
                                     endothermic or exothermic
                                     possibility of equilibrium limitation
                               (3) type and size of reactor
                                     batch
                                     continuous
                                       stirred tank
                                       tubular, multitubular
                                       tower/column
                                         spray
                                         packed, plate
                                         bubble
                                       bed
                                         fixed
                                         fluidized
                                         spouted
                                         trickle
                                       furnace
                                (4) mode of operation
                                     configurational
                                       single-stage or multistage (number of)
                                       parallel (e.g., multitubular)
                                       axial or radial flow (through fixed bed)
                                       arrangement of heat transfer surface (if any)
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