Page 128 - Process Equipment and Plant Design Principles and Practices by Subhabrata Ray Gargi Das
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5.3 Multi-stream problem    125






                                                      Hot composite
                                                      curve
                                                  ΔT   (original)
                                            Pinch   min
                                            ΔT
                            T (°C)            min

                                                          Cold composite
                                                           curve (original)

                                              Cold composite
                                              curve (shifted)
                                     q –               q rec               q +
                                                       H
               FIGURE 5.4
                             Using the hot and cold composite curves to determine energy targets.

                  We note that the range of ðDT min Þ is specified by maximum and minimum (zero) overlap of the two
               curves. A reduction of ðDT min Þ below the closest point of approach (minimum vertical distance be-
               tween the composites) does not increase the amount of heat recovery. At the other extreme, the point of
               zero overlap corresponds to zero heat recovery with all the heating and cooling provided by the
               utilities. Within this range, the correct setting of ðDT min Þ corresponds to an economic minimum
               temperature difference. Similar to the two-stream case, this is decided by economic trade-off between
               energy and capital cost.
                  Shifting the composite curves in the T-axis i.e. shifting up or down, is also possible. This would
               physically mean that the stream supply and target temperatures are being changed by the same amount
               and involves additional heating/cooling for the streams at the ends. Since the savings in utility is
               decided by the overlapping region of the curves, these shifts are carried out to increase the heat re-
               covery (q rec ) for the network.

               5.3.1 Optimal DT  min

               Designing the heat exchanger network is targeted at minimising (i) utility requirements (ii) total heat
               exchanger area and (iii) the number of heat exchangers to be provided. The first parameter relates to
                                                   the operating cost and the rest to the capital cost. Value of
                                                   these parameters in a heat exchanger network depends on
                     Capital-Energy Trade-off in new Design  the ‘pinch temperature’ as already illustrated and there
                                                   exists an economic optimum with respect to it. Calcula-
                                                   tion of these parameters is simple and a fair estimate can
               be obtained well ahead of the detailed design. The designer aims at minimising the stated parameters in
               order to approach the optimum design.
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