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142    Chapter 5 Heat exchanger network analysis




             5.8.4 True utility streams
             A true utility stream i.e., steam, cooling water, refrigerant, etc., is one that can in principle be replaced
             by any other stream (process or utility) for heat exchange purposes. Some streams like the live stream
             used for stripping in strippers that provide energy as well as reduce the partial pressure in the column
             are to be treated as process streams. Live stripping stream is not considered as ‘true’ utility as it cannot
             be replaced with any other thermal fluid supplying the heat.


             5.9 Applications
             In a nutshell, the applications of pinch technology are

             (a) Improvement of energy efficiency of a system/process
             (b) Process debottlenecking where utility system is the main bottleneck by reducing utility
                 consumption and providing additional scope for increasing production.
                                          (c) Significant reduction in process water demand and waste
                                             water generation via improved re-use of water within the
                   Importance of Pinch Analysis  process
                                          (d) For low temperature processes, pinch technology in
                                             combination with energy analysis allows the designer to
                 assess the impact of various design changes on refrigerator power consumption


             5.10 Design illustration

             Problem 5.1. A chemical process involves 4 streams, the details of which are provided in Table P5.1A
             (the last column in the Table refers to heat Transfer Coefficient).
                Design the optimum heat exchanger network when (a) hot utility, high pressure steam and cold
             utility, refrigerated brine are available at 220 and 12 C, respectively. (b) Utilisation of utilities at

             multiple levels is suggested to reduce operating cost. Consider that the cheaper utilities e MP steam
                                                                 o
                                                       o
             and cooling water are additionally available at 170 C and at 35 C.
               Table P5.1A Stream details.
               Stream no.    Type        TS ( C)    TT ( C)     CP ¼ mC p (kW/ C)   h (kW/m C)


                                                                                          2

               1           Hot           180        40          2.0                 h1
               2           Hot           150        40          4.0                 h2
               3           Cold          60         180         3.0                 h3
               4           Cold          30         105         2.6                 h4
               HU          Hot utility   220        e           e                   hh
               CU          Cold utility  12         20          e                   hc
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