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                             The procedures to follow in the design of threshold problems are discussed by Smith
                           (1995) and IChemE (1994).    CHEMICAL ENGINEERING
                           3.17.6. Multiple pinches and multiple utilities
                           The use of multiple utilities can lead to more than one pinch in a problem. In intro-
                           ducing multiple utilities the best strategy is to generate at the highest level and use at the
                           lowest level. For a detailed discussion of this type of problem refer to Smith (1995) and
                           IChemE (1994).


                           3.17.7. Process integration: integration of other process operations
                           The use of the pinch technology method in the design of heat exchanger networks has been
                           outlined in Sections 3.17.1 to 3.17.6. The method can also be applied to the integration
                           of other process units; such as, separation column, reactors, compressors and expanders,
                           boilers and heat pumps. The wider applications of pinch technology are discussed in the
                           Institution of Chemical Engineers Guide, IChemE (1994) and by Linnhoff et al. (1983),
                           and Townsend and Linnhoff (1982), (1983), (1993).
                             Some guide rules for process integration:
                             1. Install combined heat and power (co-generation) systems across the pinch; see
                                Chapter 14.
                             2. Install heat engines either above or below the pinch.
                             3. Install distillation columns above or below the pinch.
                             4. Install heat pumps across the pinch; see Section 3.16.7.
                             The techniques of process integration have been expanded for use in optimising mass
                           transfer operations, and have been applied in waste reduction, water conservation, and
                           pollution control, see Dunn and El-Halwagi (2003).

                           Example 3.18
                           Determine the pinch temperatures and the minimum utility requirements for the streams
                           set out in the table below, for a minimum temperature difference between the streams of
                             Ž
                           20 C. Devise a heat exchanger network to achieve the maximum energy recovery.
                               Stream             Heat capacity    Source       Target       Heat
                                                         Ž
                                                                                    Ž
                                                                        Ž
                               number     Type       kW/ C         temp. C     temp. C     load kW
                                 1        hot         40.0           180          40         5600
                                 2        hot         30.0           150          60         2700
                                 3        cold        60.0            30         180         9000
                                 4        cold        20.0            80         160         1600

                           Solution
                           The construction of the problem table to find the minimum utility requirement and the
                           pinch temperature is facilitated by using a spreadsheet. The calculations in each cell are
                           repetitive and the formula can be copied from cell to cell using the cell copy commands.
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