Page 281 - Design of Simple and Robust Process Plants
P. 281

7.6 Optimization of Storage Capacity  267
                have an impact on the sizing of the storage tank. Planned plant shutdowns are
                excluded from this study as it is assumed that during that time period special meas-
                urements are taken to cope with storage provisions internal or external.

                7.6.2
                The Storage Tank


                A storage tank design study is limited in this example to an intermediate storage
                tank between process sections, as discussed in Section 6.4 in Chapter 6. The tank is
                placed between the upstream and downstream process, and is simulated as a vol-
                ume with a certain capacity. A clock is implemented in the flowsheet model, and a
                capacity set point for each process is determined. During the simulation in time we
                now calculate the inlet and outlet streams of the tank based on the actual capacity
                flow over a time interval. The tank hold-up is determined at time intervals by balan-
                cing the input and output streams of the tank. The tank is provided with a simple
                level controller which manipulates the capacities of the upstream and downstream
                processes to a definable algorithm. It functions in this example as follows.
                  The level of the tank is planned to be between 45 and 55% at balanced operation;
                say its set point range is 45±55%. The capacities of both processes are put at 100%
                at the start of the simulation, as the size of the tank is determined at design capacity.
                When the level of the tank is between 55 and 95%, the capacity of the downstream
                process is put at 105%, and that of the upstream process at 95%, to bring the tank
                level back to the 45±55% range. When the tank is between 5 and 45%, the capacity
                of the upstream process is put at 105%, and that of the downstream plant at 95%.
                Now, the level goes up to 45±55% range. When the tank is at 5% level (nearly
                empty), the downstream process is switched off (zero capacity); at 95%, the tank is




                  100 95  Storage level               Max. level


                   55 45
                                                    Set point range
                                                        Mim. level
                    5
                    0    % Flow in
                 105
                 100
                  95
                  60
                   0
                 105      % Flow out
                 100
                  95
                  60
                                                  Time

                Fig. 7.6. Histogram of feilures and effect on level and flows.
   276   277   278   279   280   281   282   283   284   285   286