Page 112 - APPLIED PROCESS DESIGN FOR CHEMICAL AND PETROCHEMICAL PLANTS, Volume 1, 3rd Edition
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98                        Applied Process Design for Chemical and Petrochemical Plants

                                                                     The pressure that can develop from the shock wave can
                                                                  be destructive to the containing system hardware, partic-
                                                                  ularly in long pipe. Examples of conditions that can devel-
                                                                  op water hammer are:

                                                                     1. start, stop, or an abrupt change in a pump's speed
                        Straight  pipe          90"  Elbow           2. power failure
                                                (Welding  Type)      3. rapid  closing  of  a  valve  (usually a  control  valve,
                          90" Elbow                                    which can slam shut in one or two seconds)
             Suction 3                                             [ 19, 201 :
                                     J.
                                                                     The magnitude  of  this shock wave  can  be  expressed
                         -6''  Gate  Valve
                           Full  Open
             Line
                    Centrifugal
                                                                                                               (2-69)
                      Pump
             Figure 2-27. Example 2-5, pipe system for pipe sizing calculations.
                                                                     For water:

               Total pressure  drop from face of discharge flange on   a,  4660/ (1 + Qs  B,)I/*,  ft/sec       (2-70)
             pump to nozzle connection on tank:
                                                                  where  h,h   = maximum pressure developed by hydraulic
                                                                             shock, ft of water
               AP = (125 + 67.5) [(0.720)/100] f 0
               AP = 1.386 psi                                            v,  = reduction in velocity, ft/sec  (actual flowing veloc-
                                                                             ity, ft/sec)
               AP = 1.386 psi (2.31 feet/psi)  = 3.20 feet water
                                                                          g = gravitational constant, 32.2 ft/sec
                                                                        Q, = ratio of elastic modulus of water to that of the
               Note  that  a  somewhat more  accurate  result  may  be       pipe material (See list below)
             obtained by  following the detailed loss coefficients given   B,  = ratio of pipe diameter (LD.) to wall thickness
             in Figures 2-12 through 2-16. However, most preliminary     a, = velocity of propagation of elastic vibration in the
             engineering design calculations for this type of water sys-     discharge pipe, ft/sec
             tem do not warrant the extra detail.
                                                                     Some typical &, values for water/metal  are [ 191 :
             Flow of Water from Open-End Horizontal Pipe

               The equation  of  Brooke  [36] is  useful in  estimating      Metal                    Khs
             water or similar fluids flow from the end of open pipes:        Copper                   0.017
                                                                             Steel                    0.010
               GPM = 1.04 a (1)                           (2-68)             Brass                    0.017
                                                                             Wrought iron             0.012
                                                                             Malleable cast iron      0.012
             where GPM = flow rate, gallons per minute
                     a = internal cross-sectional area for flow in pipe, sq in.   Aluminum            0.030
                      1 = horizontal distance from pipe opening to point
                         where flow stream has fallen one ft, in.    The time interval t,, required for the pressure wave to
                                                                   travel back and forth in the pipe is:
             Water Hammer [ 191
                                                                     ts = 2 L/qv, sec                           (2-71)
               Water hammer is an important problem that occurs in
             some  liquid  control  systems. It  is  defined  as  hydraulic   L = length of pipe, ft (not equivalent ft)
             shock that occurs when a non-viscous liquid flowing in a
             pipe experiences a sudden change in velocity, such as the
             fast closing of a valve. The kinetic energy of the moving   When the actual abrupt closing of a device to stop the
             mass of liquid upon sudden stoppage or abrupt change of   flow has a time shorter than t,,  then the maximum pres-
             direction  is  transformed  into  pressure  energy,  thereby   sure, hwh, will be exerted on the closed device and line.
             causing an abrupt pressure rise in the system, often result-   Note that the value of, hwh, is added to the existing static
             ing in severe mechanical damage [53].                 pressure in the system.
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