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174   Cha p te r  E i g h t


                       Operating unit    Acronym   Operating unit      Acronym
                       Mobile press      MP        Central converter, juice  CCJ
                       Central press     CP        Local converter, rest of   LCRF
                                                   fibers
                       Local fibers      LF        Central converter, rest   CCRF
                       production                  of fibers
                       Central fibers    CF        Central converter, rest   CCRJ
                       production                  of juice
                       Green biorefinery  GBR      Local transport, silage  LTrS
                       Local biogas      LBG       Central transport,   CTrS
                                                   silage
                       Central biogas    CBG       Local transport, cake  LTrC
                       Local converter,   LCS      Central transport, cake  CTrC
                       silage
                       Central converter,   CCS    Local transport, juice  LTrJ
                       silage
                       Local converter, cake  LCC  Central transport, juice  CTrJ
                       Central converter,   CCC    Central transport, rest   CTrRF
                       cake                        of fibers
                       Local converter, juice  LCJ


                     TABLE 8.2  List of Process Steps Incorporated into the Synthesis of the Base
                     Case


                     system. Such information can be represented by a residue curve map
                     (RCM). The RCM of an ethanol-water-toluene system is shown in
                     Figure 8.7. The points E, W, and T represent the pure components
                     ethanol (product), water (by-product), and the entrainer, respectively,
                     while points F and H denote the feed and the ternary azeotrope,
                     respectively. The whole RCM is partitioned into materials
                     corresponding to these points; then the lines L1, . . . , L13 demarcate
                     the areas A1, . . . , A6.
                        A set of operating units for this process can be represented in a
                     P-graph; see Figure 8.8. The maximal structure and each solution
                     structure can be generated by algorithms MSG and SSG, respectively.
                     The Mathematical Programming model of a process network includes
                     constraints on operating units (i.e., mathematical models of those
                     units) as well as constraints on materials (e.g., mass balance
                     constraints). Mathematical models of mixers, separators, and decanters
                     are linear, including their mass balances, because they are based on
                     component flow rates. Thus, the Mathematical Programming model
                     of process networks involving mixers, separators, and decanters
                     gives rise to an LPR problem. Each solution structure satisfying
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