Page 22 - APPLIED PROCESS DESIGN FOR CHEMICAL AND PETROCHEMICAL PLANTS, Volume 1, 3rd Edition
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Process Planning, Scheduling and Flowsheet Design                      11


















































                                            Figure 1-10, Piping detail isometric flow diagram.


           given to the relative weights and styles of lines to aid in the   offs, tie-ins to existing or known points, etc. Only in this
          readability of the sheets.                            way can all the decisions as well as specifications be delin-
             Figure 3-1 k suggests an approach to standardization of   eated for the various parts contributing to the entire pro-
          form for general use. It can be rearranged in several ways   ject.  The master  process or  mechanical  flowsheet must
           to provide  a format suitable for any one of  several pur-   contain specific references to the other sheets for contin-
          poses. Of particular importance is the flexibility of adding   uation of the details and complete coordination.
          or  deleting  data  without  changing  other  details. Some
           companies prefer to place the process data on a separate   Flowsheet size may  vary  depending upon  the  prefer-
           sheet, although the same basic form for the table can be   ences of  the  individuals using  them.  The  most popular
          retained as shown in Figure 1-11. The layout principles of   system uses one size sheet about 24 x 36 inches for  all
          Figure 1-8 are also standardized by some companies.   flowsheets. The use of miscellaneous large and small sizes
                                                                to represent the entire project is often awkward when col-
                                                                lected, and increases the possibilities of  sheets becoming
                                                                misplaced. Some groups use sheets from a roll and these
             Each phase of the process is best represented  on indi-   are sized to length by  systems, becoming 24 x 60 inches,
          vidual flowsheets. Electric power, fuel gas, drainage and   24 x 72 inches or longer. These are fine for initial study
           the  many  other  auxiliary system  requirements  are  also   but become  tedious to handle on the usual desk. These
          best  defined  bj7  separate  individual  flowsheets.  These   sheets can be reduce to 11 x 36 inches 01-  11 by 48 inches
           should  be  complete including all headers, branch  take-                             (text continued on page 151
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