Page 10 - Chemical process engineering design and economics
P. 10

Preface


           way  chemical  engineers  describe  a process  and  communicate.  This  chapter  con-
           tains some of the more common  flow-diagram  symbols. To reduce the complexity
           of  the  flow  diagram,  this  chapter  divides  a process  into  nine  process  operations.
           There  may be  more  than  one  process  operation  contained  in  a process  unit  (the
           equipment).  This  chapter  also  describes  the chemical-engineering  tasks  required
           in a project.
                Chapter 2, Production and Capital Cost Estimation,  only contains the essen-
           tials  of  chemical-engineering  economics.  Many  students  learn  other  aspects  of
           engineering  economics in a separate course. Rather than placing this chapter  later
           in  the book,  it  is  placed  here  to  show  the  student  how  equipment  influences  the
           production  cost.  Chapter  2 describes  cash  flow  and  working  capital  in  a corpora-
           tion. This chapter also describes the components  of  the production cost and how
           to calculate this cost. Finally, this chapter  describes the components of capital cost
           and  outlines  a procedure  for calculating  the  cost.  Most  of  the  other  chapters dis-
           cuss equipment selection and sizing needed for capital cost estimation.
                Chapter  3, Process-Circuit Analysis,  first  discusses the  strategy of  problem
           solving. Next,  the  chapter  summarizes  the  relationships  for  solving  design prob-
           lems. The approach to problem solving followed throughout most of the book is to
           first  list the appropriate design equations in a table for quick reference  and  check-
           ing.  The numbering system for equations appearing in the text is to show the chap-
           ter  number  followed  by  the  equation  number.  For  example,  Equation  5.7 means
           Equation 7 in Chapter 5. For equations listed in tables, the numbering system is to
           number the  chapter, then the table and the equation. Thus, 3.8.12 would be Equa-
           tion  12 in Table  8 and Chapter 3. Following this table another table outlines a cal-
           culating  procedure.  Then,  the  problem-sizing  method  is  applied  to  four  single-
           process units, and to a segment of a process consisting of  several units.
                Heat  transfer  is  one  of  the  more  frequently-occurring  process  operations.
           Chapter  4,  Process  Heat  Transfer,  discusses  shell-and-tube  heat  exchangers,  and
           Chapter  7,  Reactor  Design,  discusses jacket  and  coil  heat  exchangers.  Chapter  4
           describes  how  to  select  a  heat-transfer  fluid  and  a  shell-and-tube  heat-exchanger
           design. This chapter also shows how to make an estimate of  heat-exchanger  area
           and rate heat exchangers.
                Transferring  liquids and gases from  one process unit to another is also  a fre-
           quently  occurring  process  operation.  Heat  exchangers  and  pumps  are  the  most
           frequently  used  equipment  in  many processes.  Chapter  5,  Compressors, Pumps,
           and Turbines,  discusses the two general types of machines, positive  displacement
           and dynamic, for both liquids and gases. The  discussion of pumps also could logi-
           cally  be  included  in  Chapter  8,  Design  of  Flow  Systems.  Instead,  Chapter  5  in-
           cludes pumps to emphasize the similarities in the  design of  pumps and compres-
           sors. This chapter shows how to calculate the power required  for compressors and
           pumps.  Chapter  5  also  discusses  electric  motor  and  turbine  drives  for these  ma-
           chines.
                Chapter  6,  Separator  Design,  considers  only  the  most  common  phase  and
           component  separators. Because plates and column packings  are  contained  in ves-



       Copyright © 2003 by Taylor & Francis Group LLC
   5   6   7   8   9   10   11   12   13   14   15