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11.2 Examples of Reactors for Illustration of Process Design Considerations 283

       11.1.2 Mechanical Design
                            The distinction between process design (as outlined in Section 11.1.1) and “mechanical”
                            design (most other aspects!) is somewhat arbitrary. However, in the latter we include
                            the following, which, although important, are outside our scope in this book (see Perry,
                            et al., 1984; Peters and Timmerhaus, 1991):
                            impeller or agitator design (as in a stirred tank)
                            power requirement (for above)
                            reactor-as-pressure-vessel  design
                               wall  thickness
                               over-pressure  relief
                               fabrication
                            support-structure  design
                            maintenance  features



       11.2  EXAMPLES OF REACTORS FOR ILLUSTRATION OF PROCESS
             DESIGN     CONSIDERATIONS

                            Reactors exist in a variety of types with differing modes of operation for various pro-
                            cesses and reacting systems. Figures 11.1 to 11.8 illustrate a number of these, some in a
                            schematic, generic sense, and some for specific processes.


       11.2.1 Batch Reactors
                            A schematic representation of a batch reactor in Figure ll.l(a) shows some of the es-
                            sential features. A cylindrical vessel is provided with nozzles for adding and removing
                            reactor contents. To ensure adequate mixing, the vessel has a stirrer (turbine) equipped
                            with an external drive, and several vertical baffles to break up vortices around the im-
                            peller tips. Temperature control may be achieved with internal heating/cooling coils, as
                            shown, or with an external heat exchanger or jacket. The vessel may be designed as a
                            pressure vessel, in which case a pressure-relief device (e.g., a rupture disc) is required
                            in case over-pressure develops, or as an “atmospheric” vessel, in which case a vent is
                            used. Batch reactors are discussed in Chapter 12.




                             Vent or  pressure-
                             relief-device nozzle


                                                           Mixing
                                                           turbine
                                                           Baffle
                                  Heating/  _
                                cooling coils






                                                 (a)                       (b)
                            Figure 11.1  Batch reactors: (a) schematic representation showing some fea-
                            tures; (b) pilot plant reactor for production of sodium aluminosilicate (Cour-
                            tesy of National Silicates Ltd.)
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