Page 213 - Design of Simple and Robust Process Plants
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198  Chapter 5 Process Simplification and Intensification Techniques
                Table 5.8. Summary of heterogeneous reactor systems G/S and L/S, G/L, G/L/S the ranking of
                 reactor selection in order of increasing complexity.

                 G/S and G/L      G/L             G/L             G/L/S
                                  Liquid phase    Interfacial controlled
                                  controlled
                 1) Adiabatic packed  1) Bubble column  1) Spray column  1) Trickle flow packed
                  bed                                              bed
                 2) Packed bed(s) with  2) CSTR, jet mixer  2) Packed column  2) Spray column packed
                  cooling                                          bed
                  a) recycle
                  b) cold injection
                  c) inter-stage cooling
                 3) Fluidized bed  3) CSTR with agitator          3) Packed bubble/
                                                                   multi-stage, column
                 4) Multi-stage fluidized 4) Multi-tray bubble    4) Slurry
                  beds             column
                 5) Multi-tubular reactor 5) Tray column          5) Multi tubular
                                  6) Membrane
                                   separation

                The general rules for the design of reactor systems to obtain less complex systems
                 are:
                   1.  Design for homogeneous liquid phase reactor systems, the liquid phase is
                      preferred above the gas phase.
                   2.  Heterogeneous reactor systems are preferably converted to homogeneous
                      systems.
                   3.  Integrate reaction with other process functions like: other reactions, distilla-
                      tion, extrusion, heat exchange (reverse flow reactor).
                   4.  Reactor systems are preferably operated adiabatic (no heat transfer provi-
                      sions), with larger solid particles (easily captured/separated), flow distribu-
                      tion/mixing by static devices.
                The ranked reactor types with an increase in complexity did not take into account
                 any thermodynamic or reaction kinetics information which might force the designer
                 from an economical perspective to a more complex reactor design. The results of
                 the reactor discussion are summarized in Tables 5.7 and 5.8.

                 5.7.2
                 Distillation and Absorption

                 Distillation and absorption is one of the oldest ± and certainly one of the most
                 applied ± separation techniques used for homogeneous mixtures. The advantage is
                 that it can easily be designed based on vapor liquid equilibrium data that are readily
                 available in public databanks, or can be determined at laboratory scale at relative low
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