Page 347 - Design of Simple and Robust Process Plants
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8.4 Control Design  333

                           TC








                                              LC





                Fig. 8.16. Flash unit with basic control loops.



                This expression is the constitutive part of the balance equation. The expression elim-
                inates all the terms of the balance equation like the components terms, and only
                leaves the essential terms for the operation. It shows for a flash that only three vari-
                ables affect the rate of energy transfer between the entropy current and the flash
                temperatures; these are the considered potential dominant variables. The I s flow
                term can be manipulated, while the temperatures are the intensive variables. In this
                example the temperature in the flash is dominant, as the up-front temperature is
                not available for control in this scheme. The control scheme with the dominant vari-
                ables is shown in Figure 8.16.
                  The following loop pairing rule was presented by evaluation of the power release
                term for a unit:

                  Whenever a flow appears as an important energy carrier pair this flow with the corre-
                  sponding intensity belonging to the unit.

                When this rule is applied to other thermal processes like a distillation column, the
                energy carrier (heat duty of the reboiler) is paired with a corresponding intensity
                (selected column temperature). Identical expressions for thermal processes can be
                generated that are also applicable for single component irreversible reactions such
                as A ® B that can easily be expressed as a thermal process (e.g., a fired heater). In a
                fired heater, the loop pairing is the energy flow and a (intensity) process tempera-
                ture.
                  For multi-component reactions the component production terms must be includ-
                ed in the equation. This has been described extensively in the referred article of Tyr-
                Øus with several general conclusions for irreversible and equilibrium reaction sys-
                tems.
                  The methodology has demonstrated its usefulness by its application to a coupled
                reactor system as a FCC unit. An entire process (Tennessee Eastman process) was
                successfully studied with this methodology to design the dominant pairings.
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