Page 126 - Chemical Process Equipment - Selection and Design
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98  FLOW  OF  FLUIDS
                                                                                            -
                                  TABLE 6.4.  Equivalent Lengths of Pipe Fittingsa

                                               ~~
                                                Q      Q      A      Q                       63n

                                   Pipe   Standard   Medium   Long-   45-deg   Tee   Gate   Globe   Swing
                                               radius   radius   ell         valve,   valve,   check,
                                                                                     open    open


                                     1    2.7    2.3    1.7    1.3     5.8    0.6      27     6.7
                                    2     5.5    4.6    3.5    2.5     11.0    1.2     57     13
                                    3     8.1    6.8    5.1    3.8    17.0    1.7      85    20
                                    4    11.0    9.1    7.0    5.0    22      2.3     110    27
                                    5    14.0   12.0    8.9    6.1    27      2.9     140    33

                                    6    16.0   14.0   11.0    7.7    33      3.5     160    40
                                    8    21     18.0   14.0   10.0    43      4.5     220    53
                                    10   26     22     17.0   13.0    56      5.7     290    67
                                    12   32     26     20.0   15.0    66      6.7     340    80
                                    14   36     31     23     17.0    76      8.0     390    93
                                    16   42     35     27     19.0    87      9.0     430    107
                                    18   46     40     30     21      100     10.2    500    120
                                   20    52     43     34     23      110     12.0    560    134
                                   24    63     53     40     28      140     14.0    680    160
                                   36    94     79     60     43      200     20.0   1,000   240

                                     a Length of straight pipe (ft) giving equivalent resistance.
                                     (Hicks and Edwards, Pump Application Engineering, McGraw-Hill,
                                  New York, 1971).


                 PO WE R REQUl RE M E NTS                           3.  The  friction  equation e. - 4 = (Sp/gcnz)~jLijQ~/D~ applies to
                                                                      the line connecting node i with j.
                 A  convenient  formula  in  common  engineering  units  for  power
                 consumption in the transfer of  liquids is            In the  usual  network  problem,  the  terminal  pressures,  line
                                                                    lengths, and line diameters are specified and the flow rates through-
                  p=  (volumetric flow rate)(pressure difference)   out  are  required  to  be  found.  The  solution  can  be  generalized,
                            (equipment efficiency)                  however, to determine  other unknown quantities equal in number
                                                                    to the  number of  independent  friction equations that describe the
                    -
                    -         (gals/min)(lb/sq in.)   horsepower.
                     1714(fractional pump eff)(fractional driver eff)   network. The procedure is illustrated with the network of  Example
                                                            (6.30a)   6.6.
                                                                       The  three  lines in  parallel  between  nodes 2  and  5  have  the
                 Efficiency data of  drivers are in Chapter 4 and of  pumps in Chapter   same pressure  drop Pz - Ps. In series lines such as 37  and 76 the
                 7. For example, with 500 gpm, a pressure difference of 75 psi, pump   flow rate is the same and a single equation represents friction in the
                 efficiency of  0.7, and driver efficiency of  0.9, the power requirement   series:
                 is 32.9 HP or 24.5 kw.

                 6.4.  PIPELINE  NETWORKS
                                                                        The number of flow rates involved is the same as the number of
                 A system for distribution of  fluids such as cooling water in a process   lines in  the  network,  which  is  9,  plus  the  number  of  supply and
                 plant  consists of  many interconnecting pipes in  series, parallel,  or   destination  lines,  which  is  5,  for  a  total  of  14.  The  number  of
                 branches.  For  purposes of  analysis, a point  at which  several lines   material  balances  equals  the  number  of  nodes  plus  one  for  the
                 meet is called a node and each is assigned a number as on the figure   overall balance, making a total of  7.
                 of  Example 6.6. A flow rate from node i to node j  is designated as   The solution of  the problem requires 14 - 7 = 7 more relations
                 Q,; the same subscript notation is used  for other characteristics of   to  be  established.  These  are  any  set  of  7 friction equations  that
                 the line such as f, L, D, and NRe.                 involve the  pressures at  all the  nodes.  The material balances and
                    Three  principles  are  applicable  to  establishing  flow  rates,   pressure drop equations for this example are tabulated.
                 pressures, and dimensions throughout the network:      From Eqs. (4)-(IO)  of  Example 6.6, any combination of  seven
                                                                    quantities Q, and/or L, and/or Dij can be found. Assuming that the
                 1. Each node i is characterized by a unique pressure 5.   Q, are to be found, estimates of  all seven are made to start, and the
                 2.  A material balance is preserved at each node: total flow in equals   corresponding  Reynolds  numbers  and  friction  factors  are  found
                   total flow out, or net flow equals zero.          from Eqs.  (2) and (3). Improved values of  the  Q, then  are found
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