Page 28 - Design of Simple and Robust Process Plants
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1.3 Design Philosophies  11
                      certain percentage of product recycle, which results in a need for more capi-
                      tal. The concept of ªprevent versus cureº attempts to avoid all these additional
                      provisions. The solution is consistent operation, which can only be realized
                      by a certain level of automation and much more attention to feed-forward
                      control to avoid off-spec situations. Do not build a plant for all types of mis-
                      haps (excluding safety provisions) ± do it right the first time.
                   2.  Design for first-pass prime. This is a specific case of ªprevent versus cureº. Dur-
                      ing start-up of a plant, it is often necessary to deal with off-spec situations.
                      The challenge is how to prevent these and thus avoid all the rework and/or
                      losses. The answer is to design for first-pass prime, and this often involves
                      designed start-up procedures. Start a continuous process from the back end,
                      and put the finishing sections of a plant in hot stand by condition. This
                      means that the finishing section is at operational and specification condition
                      (e.g., distillations are at total reflux, compressors run in recycle mode) and
                      ready to process the feed from the reactor section. In addition, it is necessary
                      to prepare the reactor for a flying start. This requires a good understanding
                      of the reactor operation that can be obtained from dynamic simulations, lead-
                      ing to start-up procedures to achieve first-pass prime. The hardware modifi-
                      cations to achieve this are limited, and mostly result in minor piping modifi-
                      cations. A leading article on this subject was produced by Verwijs et al.
                      (1995). An example of minimization of components by total quality control
                      and no redundancy is shown in Figure 1.3.



                                               Q
                    RAW MATERIAL                  CHECK TANKS   PRODUCT TANKS
                                        PLANT










                                                                     CUSTOMERS

                           DISTURBANCES
                                         MODEL BASED
                 RAW MATERIAL                         Q        PRODUCT TANK
                                      Q    CONTROL

                                                  PLANT                CUSTOMERS

                 Fig. 1.3. Minimize components by total quality control and no redundancy.
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