Page 456 - Design of Simple and Robust Process Plants
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11.4 Process Simplification and Intensification  443
                11.4
                Process Simplification and Intensification

                The technique for simplification and intensification cannot be generalized because
                each operation has its own solutions. However, it can be classified into categories to
                enable the thought process for development and application of simple designs. The
                simple design solutions for different units are ranked in sequential order of increas-
                ing complexity to support a designer in the design process.

                11.4.1
                Avoiding or Eliminating Functions

                No storage ± what you do not have cannot leak, and does not cost anything.
                  Transport of fluids can benefit from gravity forces and pressure differences.
                  Opportunities are process situations with repetitive actions called, do±undo±redo,
                like heating±cooling±re-heating, separation±mixing±separation, and pressurizing±
                depressurizing±pressurizing.

                11.4.2
                Combination of Functions

                Reaction and reaction; Reaction and separation; Separation and separation.
                  Integration of equipment. Most equipment has the possibility to integrate adja-
                cent equipment. This reduces not only equipment costs but also installation and
                piping costs.

                11.4.3
                Intensification of Functions

                High surface area per volume, as for heat and mass exchangers.
                  Increase mass and heat transfer (kA and UA).
                  Benefit from centrifugal forces for phase separation, eventually combined with
                mass transfer or reaction, as in rotating packed beds.

                11.4.4
                Overall Process Simplification

                Key elements are:

                  .   Operation at 100% conversion.
                  .   Adiabatic operations.
                  .   Prevention of waste.
                  .   Single train design and single component design.
                  .   Selection of optimal pressure levels.
                  .   Logistic strategy.
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