Page 109 - Pressure Vessel Design Manual
P. 109

90    Pressure Vessel Design Manual

            An  economic  UD ratio  is between  1 and  10. L/D ratios   Given
          greater  than  10  may  produce  the  lowest  surface-area-to-
          volume ratio but should be considered impractical for most   V, volume
          applications. Obviously plot space is also a consideration  in   P, pressure
          ultimate  cost. In general, the higher the pressure the larger   C, corrosion allowance
          the ratio, and the lower the pressure  the lower the ratio. As   S, allowable stress
          previously  stated,  the  optimum  UD  ratio  for  an   E, joint efficiency
          atmospheric drum is 1. Average pressure  vessels will range
          between  3 and 5.                                     Method 1
            Two procedures  are included here and are called Method
          1 and  Method  2.  The  two  procedures,  though  similar  in   1. Calculate F1.
          execution,  yield  different  results.  Both  methods  take  into   2.  From Fig. 2-58, using F1 and vessel volume, V, deter-
          account  pressure,  corrosion, joint  efficiency, and  allowable   mine the vessel diameter, D.
          stress. Even with this much detail, it is impossible to deter-   3.  Use D and V to calculate the required  length, L.
          mine  exactly what  proportions  will yield  the  lowest overall
          cost, since there are many more variables that enter into the
          ultimate  cost of a vessel. However, determining  the  lowest
          weight is probably the best parameter in achieving the lowest   Method 2
          cost.
            The procedure  for determining  the  optimum  WD  ratios   1. Calculate Fz.
          for the two methods is as  follows:                     2.  From Fig. 2-59 determine WD ratio.
                                                                  3.  From the UD ratio, calculate the diameter,  D.
                                                                  4.  Use D and V to calculate the required  length, L.












           v (cu. ft.)     P (PSIG)     Method'       D (ft)       L (ft)       t (in.)      w (Ib)       UD
           1500              150    I     1      I     7.5    I    34      I   0.5625   I    20,365   I    4.5    I
                                    I     2      I     8.5    I    23.6    I    0.625   I    20,086  I     2.8    I

                             300           1           6           53           0.8125       35,703        8.8
                                          2            7.5         31.5         0.8125       28.668        4.2





















          'Methods are as follows, based on graphs: Method 1: K. Abakians, Hydrocarbon Processing, June 1963. Method 2: S.P. Jawadekar, Chemical Engineering, Dec. 15, 1980.
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