Page 449 - Design and Operation of Heat Exchangers and their Networks
P. 449

432   Design and operation of heat exchangers and their networks


          9.1 Feasibility, flexibility, and controllability of heat
          exchanger networks

          9.1.1 Feasibility and flexibility
          A well-designed HEN or multistream heat exchanger should be a flexible
          one that is able to adapt to parameter deviations from nominal values and
          remain flexible when the parameters vary within a prespecified range. There
          is another word, feasibility, which is easily confounded with flexibility.
          Feasibility analysis gives us the information on whether or not a HEN
          can maintain the target temperatures after any possible disturbances within
          a prespecified range. However, flexibility analysis will tell us how the oper-
          ating cost changes over the specified range of uncertain parameters. Swaney
          and Grossmann (1985a,b) proposed a quantitative index, which they called
          “flexibility index” to measure the size of the parameter space over which
          feasible steady-state operation of the plant could be obtained by proper reg-
          ulation of controlling variables. Later, Roetzel and Luo (2002) defined a new
          flexibility factor to quantitatively address the flexibility of a HEN.
             Assume a HEN in a process, its thermal performance at the nominal
          operation point is described by
                                   hd, c N , u N Þ ¼ 0                 (9.1)
                                    ð
                                   gd, c N , u N Þ   0                 (9.2)
                                    ð
          where d is the vector of design variables and c N and u N are the vectors of
          controlling variables and uncontrolled operation variables at the nominal
          operation point, respectively. The set h contains the exit stream tempera-
          tures to be maintained at given targets, and the set g contains the exit stream
          temperatures to be limited in given regions. The total utility cost at the
          nominal operation point is calculated according to
                              X               X
                                                     ð
                                     ð
                         C N ¼   f HU Q HU,N Þ +  f CU Q CU,N Þ        (9.3)
          in which f HU and f CU are cost functions of corresponding hot and cold utility
          requirements, respectively.
             A HEN is feasible if for any deviations in uncontrolled operation vari-
          ables, Δu¼u u N (u2R u ), there exists c2R c such that the constraints
          h(d, c N , u N )¼0 and g(d, c N , u N ) 0 are satisfied. To specify the feasibility
          of a HEN quantitatively, the flexibility index D introduced by Swaney and
          Grossmann (1985a,b) is adopted, which is defined as

                                     D dðÞ ¼ maxδ                      (9.4)
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