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10.5 Process Development  239

               10.5
               Process Development
               Perhaps the first decision to be made in process development is the difficult decision
               of whether the enzymes to be used should be used in an integrated format. Such
               a question does not arise with conventional single biocatalytic steps but is highly
               important in multienzyme processes. One of the key criteria here is whether the
               enzymes can be operated together without compromise to any of the individual
               enzyme’s activity or stability. An interaction matrix (see Section 10.6) can be used to
               assist such decision making. In cases where the cost of one or more of the enzyme(s)
               is not critical, it will be possible to combine in a one-pot operation. In other cases,
               where the cost of an individual enzyme becomes critical, then it may be necessary
               to separate the catalysts, such that each can operate under optimal conditions.
               Likewise, selection of the biocatalyst format (immobilized enzyme, whole cell,
               cell-free extract, soluble enzyme, or combinations thereof) in combination with
               the basic reactor type (packed bed, stirred tank, or combinations thereof) and
               biocatalyst recovery (mesh, microfiltration, ultrafiltration, or combinations thereof)
               will determine the structure of the process flowsheet and therefore is an early
               consideration in the development of any bioprocess. The criterion for selection of
               the final type of biocatalyst and reactor combination is primarily economic and
               may best be evaluated by the four metrics in common use to assess the economic
               feasibility of biocatalytic processes [29]:

               • reaction yield (g product/g substrate);
               • biocatalyst yield (g product/g biocatalyst);
               • product concentration (g product/l);
               • space-time-yield (g product/l/h).

                The balance between the four metrics is dependent upon the relative costs
               in a process. For example, a process with a high cost of biocatalyst requires a
               high biocatalyst yield, whereas those with a high cost of process plant will require
               a high space-time-yield and those with a high downstream processing cost require
               a high product concentration to leave the reactor.
                Following these early decisions about catalyst integration, and selection of the
               appropriate biocatalyst and reactor combination, in the case of multienzyme pro-
               cesses it is then necessary to embark on a development program to improve
               the biocatalyst. One option is to consider the multitude of different forms and
               pretreatments of a biocatalyst (e.g., whole-cell options including display, permeabi-
               lized, washed permeabilized, intact). A complementary approach is to use genetic
               engineering, via expression of the desired enzymes over other proteins. Finally
               the third approach is to consider process strategies to overcome limitations and
               bottlenecks. In reality, all options should be considered in parallel, but for simplicity
               the possibilities of recombinant DNA technology and process engineering will be
               considered here.
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