Page 484 - Chemical process engineering design and economics
P. 484

Design of Flow Systems                                        461


            Table 8.4.1  Summary of Flow-System Design Computations.


                                             Suction    Discharge

                         Flow Rate (gal/min) a  100        100
                                  3 b
                         Density (Ib/ft )      62.3       62.3
                         Pipe ID (ft) c       0.336       0.256
                         Pipe Length (ft) c    12.0       60.0
                         Velocity (ft/s) d     2.84       4.34
                         Viscosity (lb M/ft-s) d  6.60x10-"  6.60x1 0- 4
                         Reynolds Number     S.OxlO 4    l.OSxlO 5
                         Relative Roughness  5.89x10"*  5.89x10^
                         Friction Factor, 4f  0.0205      0.021


                                 Suction (4 in pipe)     Discharge (3 in pipe)
              Fitting        No.     K      Total K   No.     K      Total K

              Gate Valves     1      0.16 0.16 3            0.20      0.60
              Check Valves                             1    2.00      2.00
              Tees, Branch    1      0.67          0.67
                                                       3
              Tees, Line      1      0.13          0.130.16           0.48
              90° Elbows                               1    0.33      0.33
              Flanges 6       2     0.04 0.08 4             0.04      0.16
              Entrance        1      0.23          0.23
              Exit                                     1    1.00      1.0
              Total  (IK)                    1.27                     4.57


                                             Suction   Discharge
                         1(4  f L/D)         0.732       4.92
                         l.l[I(4fL/D)]        8.05       5.41
                         1.25  IK             1.59       5.71
                          2
                         v /2g (ft) d        0.125       0.292
                         H F' (ft)"          0.299       3.25 f
                         H z(ft) d            7.0        49.0
                         H P(ft) d            34.0       115.0
                                     3
                                                          3
                        a) To convert to m /min multiply by 3.785xlO~ .
                                       3
                        b) To convert to kg/m  multiply by  16.019.
                        c) To convert to m multiply by 0.3048.
                        d) To convert to m/s multiply by 0.3048.
                        e) No data are available. Use a union to approximate a flanged connection.
                        f) Frictional losses do not include the control valve and heat exchanger.



         Copyright © 2003 by Taylor & Francis Group LLC
   479   480   481   482   483   484   485   486   487   488   489