Page 97 - Analysis, Synthesis and Design of Chemical Processes, Third Edition
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that chapter, considerable emphasis is placed on the sequencing of distillation columns, and some of the
                    problems associated with azeotropic systems are covered.


                    2.6 Step 5—Heat-Exchanger Network or Process Energy Recovery System





                    The main objective of process energy recovery is to optimize the energy that a process exchanges with the
                    utilities. At the expense of capital investment, the utility usage can be decreased by exchanging energy
                    between  process  streams.  The  amount  of  energy  integration  is  a  function  of  the  relative  costs  of  the
                    utilities.  In  addition,  the  process  becomes  more  complex  and  more  difficult  to  control.  This  loss  in
                    flexibility must be weighed against the savings in operating costs. These and other issues are covered in
                    more detail in Chapter 15.


                    2.7 Information Required and Sources





                    In formulating a process flow diagram, one of the most important tasks is the collection and synthesis of
                    data.  These  data  are  available  in  a  wide  variety  of  publications.  As  a  guide,  a  summary  of  useful

                    resources is presented in Table 2.3. The data in this table are partitioned into information pertaining to
                    new and existing processes and data on new and existing chemical pathways.

                    Table 2.3 Summary of Resources for Obtaining Information on Chemical Processes
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