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                                                        CHEMICAL ENGINEERING
                             3.9. Estimate the work required to compress ethylene from 32 MPa to 250 MPa in a
                                                                                          Ž
                                 two-stage reciprocating compressor where the gas is initially at 30 C and leaves
                                                   Ž
                                 the intercooler at 30 C. See Example 3.13.
                            3.10. Determine the pinch temperature and the minimum utility requirements for the
                                                                                            Ž
                                 process set out below. Take the minimum approach temperature as 15 C. Devise
                                 a heat exchanger network to achieve maximum energy recovery.
                                       Stream     Type     Heat capacity    Source       Target
                                                                 Ž
                                                                                              Ž
                                                                                 Ž
                                       number                 kW/ C        Temp. C      Temp. C
                                          1       hot          13.5           180          80
                                          2       hot          27.0           135          45
                                          3       cold         53.5            60         100
                                          4       cold         23.5            35         120
                            3.11. Determine the pinch temperature and the minimum utility requirements for the
                                                                                            Ž
                                 process set out below. Take the minimum approach temperature as 15 C. Devise
                                 a heat exchanger network to achieve maximum energy recovery.
                                       Stream     Type     Heat capacity    Source       Target
                                                                                 Ž
                                                                                              Ž
                                                                 Ž
                                       number                 kW/ C        Temp. C      Temp. C
                                          1       hot          10.0           200          80
                                          2       hot          20.0           155          50
                                          3       hot          40.0            90          35
                                          4       cold         30.0            60         100
                                          5       cold          8.0            35          90
                            3.12. To produce a high purity product two distillation columns are operated in series.
                                 The overhead stream from the first column is the feed to the second column.
                                 The overhead from the second column is the purified product. Both columns are
                                 conventional distillation columns fitted with reboilers and total condensers. The
                                 bottom products are passed to other processing units, which do not form part of this
                                 problem. The feed to the first column passes through a preheater. The condensate
                                 from the second column is passed through a product cooler. The duty for each
                                 stream is summarised below:
                                  No.         Stream         Type     Source      Target    Duty, kW
                                                                          Ž
                                                                                      Ž
                                                                     temp. C.    temp. C
                                  1       Feed preheater     cold       20         50          900
                                  2       First condenser    hot        70         60         1350
                                  3       Second condenser   hot        65         55         1100
                                  4       First reboiler     cold       85         87         1400
                                  5       Second reboiler    cold       75         77          900
                                  6       Product cooler     hot        55         25           30

                                 Find the minimum utility requirements for this process, for a minimum approach
                                                 Ž
                                 temperature of 10 C.
                                 Note: the stream heat capacity is given by dividing the exchanger duty by the
                                 temperature change.
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