Page 266 - Design and Operation of Heat Exchangers and their Networks
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Optimal design of heat exchanger networks  255


              in transferred from the system to the cold utility, but no heat flows into the
              system. If there is a heat flow across the pinch, the excess external cooling
              and excess external heating for the same amount of heat are required, which
              increases both the hot and cold utility costs. The pinch principle allows the
              designer to keep the level of heat recovery optimized by simply making sure
              that the heat crossing the pinch is minimized.
                 Because any network design that transfers heat across the pinch will cause
              both heating and cooling duties larger than their minimum, there are three
              principles:
              (1) Do not use cold utilities above the pinch.
              (2) Do not use hot utilities below the pinch.
              (3) Do not transfer heat across the pinch.
              For the network design, there are therefore three consequences:
              (1) Divide the network at the pinch into two parts.
              (2) Design each part separately.
              (3) Do not use heaters in the part above the pinch (hot end part); do not use
                 coolers in the part below the pinch (cold end part).
              For the matching of streams, two rules should be followed:
              (1) In the part above the pinch, the number of the hot streams (including
                 their branches) should be less than or equal to that of the cold streams
                 (including their branches), that is,
                                  N h   N c above the pinchð  Þ          (6.74)
                    Otherwise, the stream splitting is necessary to ensure that Eq. (6.74)
                 is fulfilled. Similarly, in the part below the pinch, the inequality is
                 inversed:
                                  N h   N c below the pinchÞ             (6.75)
                                          ð
              (2) For a match in the part above the pinch, the thermal capacity rate of a
                 hot stream (or the branch of a hot stream) should be less than or equal to
                 that of the cold stream (or the branch of a cold stream) to be matched,
                 that is,
                                   _    _
                                  C h   C c above the pinchð  Þ          (6.76)
                 Otherwise, the stream splitting is necessary. For a match in the part
              below the pinch, the inequality is inversed:
                                   _    _
                                  C h   C c below the pinchð  Þ          (6.77)
                 The pinch design method is illustrated in detail in Example 6.4.
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