Page 78 - APPLIED PROCESS DESIGN FOR CHEMICAL AND PETROCHEMICAL PLANTS, Volume 1, 3rd Edition
P. 78

-


        64                        Applied Process Design for Chemical and Petrochemical Plants   IPS

                                                                       TUBE  OD
                                             -K
                  i                I                                     INDICATES           SIZE  INDICATES



                                                                                              NOMINAL
                                                                         OUISIDE
                                                                                              DIAMETER
                                                                         DIAMETER
                                             AE-
                                             .Ir                 How Tube OD Differs from IPS
              Dependable performance; fast, easy installation    In Tube OD the size specified indicates its outside diameter
              Uniformity  of  wall  thickness  and  geometric  accuracy  of   . . . whereas in Iron Pipe Size (I P S 1,  the size has reference
              ends  permit  precise  alignment  of  joints.     to a nominal diameter. See Table 2-1.
                   Figure 2-9. Dimension comparison of tubing and IPS (iron pipe size) steel piping. By permission, Tri-Clover,  Inc.


                                                        Table 2-1
                     Comparison of dimensions and flow area for Tubing and Iron Pipe Size (IPS) Steel Pipe.





















                 'Bawd on wet) s%k&nsn lkw on tollowlng p.oar.
                *'tndl~a wrt.r  lmintd. in deeting IIM  size wi%h ~.p.fity dolst to @ow muinnnmt.
                By permission Tri-Clover, Inc.


        Total Line Pressure Drop                              Background Information (Also see Chapter 3)

                                                                 Gas or vapor density following perfect gas law:
           The total piping system pressure drop for a particular
        pipe  installation is  the sum of  the friction drop in pipe   p  = 144 P'  (T) (1544/MW), lbs/cu  ft   (2-5)
        valves  and  fittings,  plus  other  pressure  losses  (drops)
         through control valves, plus drop through equipment in   Gas or vapor specific gravity referred to air:
         the system, plus static drop due to elevation or pressure
         level. For example, see Figure 2-2.                     S,  = MW of gas/MW of air = MW of gas/29   (2-6)

           This total pressure  loss is not necessarily required  in   Conversion between fluid head loss in feet and pres-
         determining the fictional losses in the system. It is neces-   sure drop in psi, any fluid:
         sary when establishing gravity flow or the pumping head
         requirements for a complete system.                     Pressure drop, pounds/sq in., AP  = hLp/144   (2-7)

           Design practice breaks the overall problem into small   For water, AP  = hL/2.31, psi            (2-8)
         component parts which allow for simple analysis and solu-
         tion.  This  is  the  recommended  approach  for  selection   Equivalent diameter and hydraulic radius for non-cir-
         and sizing of process piping.                        cular flow ducts or pipes
   73   74   75   76   77   78   79   80   81   82   83