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126   Cha p te r  S i x


                        Process              Dissolved           Pinch
                         stream             O  stream
                                              2
                       COD                 COD                I/COD   Substrate
                                                                     supply line
                              Dissolved            Process
                                                                 Slope = μ m /S
                              O  stream            stream        Intercept = I/S
                               2
                                     D                   I/D                 I/D
                          μ -Specific growth            Slope ~ growth rate, O  solubility,
                           m                                          2
                          S-Saturation                 residence time, oxidation energy load
                          D-Diluation
                     FIGURE 6.2  Oxygen Pinch method (after Zhelev, 2007).

                     energy required—a quality characteristic: the micro-organisms’
                     health as assessed by their rate of reproduction.

                6.3   Combined Analyses, I: Energy-Water, Oxygen-Water,
                      and Pinch-Emergy


                     6.3.1  Simultaneous Minimization of Energy and Water Use
                     Water savings can be achieved through the strategic implementation
                     of water reuse between water-using operations. Further minimization
                     of freshwater usage is possible by regenerating water, which is then
                     recycled. The design methodology developed by Smith and colleagues
                     (Wang and Smith, 1994; Kuo and Smith, 1997; Gunaratnam et al.,
                     2005) has proven to be effective in process industries because it
                     provides a systematic means of establishing realistic minimum water
                     requirements for a site as well as conceptual design guidelines for
                     de-bottlenecking water systems.
                        In some process industry sectors (e.g., the food industry), water
                     use is closely linked to energy systems. The diagram shown in
                     Figure 6.3 explains the basic concept and the importance of
                     considering water and energy systems concurrently. In Figure 6.3(a),
                     freshwater is supplied to two water-using operations and then is
                     discharged in a parallel arrangement. The necessary heating or
                     cooling (usually through a heat exchanger) is provided according to
                     process requirements. This conventional practice can be significantly
                     improved by implementing a design for simultaneous water reuse
                     and heat recovery, as shown in Figure 6.3(b). Water reuse between
                     operations reduces water consumption, and the proposed heat
                     recovery between streams will reduce the need for utilities (e.g.,
                     steam, cooling water).
                        When the problem is considered jointly, finding the best energy
                     recovery options and water reuse schemes is an extremely complex
                     task because there are strong design interactions between systems
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