Page 473 - Advanced thermodynamics for engineers
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464    CHAPTER 19 PINCH TECHNOLOGY




              P19.3 Figure P19.3 shows a network design using steam, cooling water and some heat recovery.
                    (a) Does this design achieve the minimum energy target for DT min ¼ 20 C?

                    (b) If the current network does not achieve the targets, show a network design that does.
                                                 +
                                  +        ¼ 170 C; Q C ¼ 480 kW; Q H ¼ 380 kW;
                    [(a) T C pinch  ¼ 150 C; T H pinch
                                           ¼ 260 kW]
                    (b) Q C min  ¼ 360 kW; Q H min
                                        mC = 20         mC = 10
                                               o
                                                              o
                                            155 C           180 C
                                                                    o
                                      o
                                    250 C                        100 C
                                 1                                       mC = 10
                               Hot streams  150 C                 140 C
                                      o
                                                                    o
                                  2
                                               o
                                                             o
                                            130 C          30 C         mC = 50
                                           3              4
                                              Cold streams
             FIGURE P19.4
             Network for problem P19.4.


              P19.4 Figure P19.4 shows two hot streams and two cold streams for heat integration (subject to
                    DT min ¼ 20 C).

                     (i) What are the energy targets?
                    (ii) Show a network design achieving these targets.
                                   ¼ 0]
                    [Q H min  ¼ 0; Q C min
                                    Steam,
                           o        ΔH = 480 kW
                         110
                                                  o
                                               170
                         50 o         165 o         200 o  90 o         180 o  60 o
                                            Process              Process
                         Heat exchanger
                         ΔH = 460 kW                                        Cooling water
                                                                            ΔH = 360 kW



                                                Cooling water
                                                ΔH = 200 kW
             FIGURE P19.5
             Network for problem P19.5.
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