Page 203 - Design of Simple and Robust Process Plants
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188  Chapter 5 Process Simplification and Intensification Techniques
                   ±  Do-undo-redo activities result in additional equipment that might be subject
                      to removal.
                   ±  Multiple trains and spare installed equipment offer major opportunities for
                      avoidance, and should receive close attention.
                   .  The combination of process functions offers major possibilities for simplifi-
                      cation.
                   ±  The combination of reaction and separation opens opportunities to increase
                      conversion by shifting the equilibrium and increasing selectivity, at lower
                      investment. Reactive separation examples include: reactive distillation, reac-
                      tive extrusion, reactive extraction, reactive absorption, reactive adsorption.
                   ±  The combination of distillation separations offers advantages through more
                      extensive application of dephlegmators, side streams, and divided wall col-
                      umns; this results in fewer separation columns.
                   ±  The direct coupling of distillation columns can also be exploited around reac-
                      tor system where the conversion is limited.
                   ±  The combination of different separations such as: extraction where more
                      extractions can be executed in one column as neutralization and washing;
                      absorption and stripping; devolatilization and evaporation; stripping and
                      blending extrusion.
                   .  Integration of equipment is another level of simplification. The benefits of
                      this are often less than derived from the integration of functions, but they
                      might be substantial on equipment costs and piping. Several examples are
                      given for the integration of reactor systems. The integration of distillation
                      equipment also receives wider application, resulting in lower capital costs;
                      similar opportunities are also exploitable with other units.
                   .  Intensification of process functions; progress made in this area can be
                      divided into three categories:
                   ±  Building more compact units by installing more area per unit volume. Com-
                      pact heat exchangers are well known in this area. Also, mass exchangers
                      based on separation membranes (e.g., reverse-osmosis and ultrafiltration), as
                      well as gas absorption through membranes are being developed.
                   ±  Increase heat, mass and impulse transport. In many heterogeneous reactions
                      the conversion rate is limited by mass and/or heat transport. In these situations,
                      intensification is highly beneficial. Different techniques are applied to enhance
                      transport, such as intensive mixing and re-mixing of liquid/liquid reaction me-
                      dium, intensified mixing of gas/liquid, application of pulsing flow techniques
                      to create large surface area, and surface renewal in trickle flow reactors.
                   ±  Benefits from centrifugal fields (ªHigeeº). The exploration of centrifugal
                      forces to improve phase separation and allow for higher processing velocities
                      was initially not successful, the development time being much longer than
                      expected. However, industrial applications of ªHigeeº technology are increas-
                      ing, and include: de-aeration (devolatilization) of liquid streams; rotational
                      particle separation for sizes >0.1 lm in dust and mist streams; reactive strip-
                      ping in a rotating packed bed; polymer de-volatilization and pelletization in
                      rotating packed beds.
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