Page 385 - Design of Simple and Robust Process Plants
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372  Chapter 9 Operation Optimization
                  .   The application of suboptimizations is to be decided during the control strat-
                      egy design as it has an impact on the model.
                  .   Constraints to be modeled ± constraints are either handled in constraint con-
                      trollers often based on direct plant measurements, or they are modeled. This
                      differentiation must be made during the design of the control structure.
                Process units have, for most of the time, more than one constraint. Although it
                should be noted that in general there are only a few process units that are limiting
                for the operation, these often have more than one active constraint. The number of
                potential constraints of a simple distillation tower is listed in Table 9.1. The poten-
                tial constraints for a furnace are illustrated in Figure 9.10. It is clear from these lists
                that different constraints might be restrictive under variable conditions (White,
                1999). For the example of the distillation, the actual operational constraint list may
                seem much shorter. Often, the pressure in the column is a limiting factor as a result
                of limited capacity of the reboiler/condenser next to flooding or weeping limitations
                in the column. A representation of the constraints of a column itself is shown in
                Figure 9.11. However, be aware that during optimization the column might run into
                different constraints at different operational conditions. Flooding in the bottom,
                feed or top section based on gas and liquid loads may be practical limits, but weep-
                ing may also be a constraint:
                  .   Feed slate, product slate ranges, feed and product and utility specifications.
                  .   DOFs for the optimization.
                  .   Parameters to be estimated or calculated during operation.
                  .   Price range projection.
                  .   Robustness over the entire operational range.




                Constraints:
                Air supply;
                Air Blower
                Air temp
                Fuel supply;
                             T1
                Fuel pressure
                                               T2
                Fuel valve
                Environment
                CO / NO x    T3                 T4
                Burner
                Design Temp
                                                        AIR intake
                Skin T coil
                Skin T conv
                Arch temp
                Furn.temp
                Design Tconv     Fuel
                Design Trad


                Fig. 9.10. Furnace constraints.
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