Page 200 - Chemical process engineering design and economics
P. 200

182                                                      Chapter 4



                  UocU 0   3077(553.5)
                From Equation 4.7.9, the required fouling resistance for the condenser,

                                                 4
                                        4
                                4
                                                                     2
                                                                 5
                                                    2
               = Rfi +R fo = 2.5xlO" +  1.0xlO-  = 3.5xlO- m -K/W(6.16xlO~ h-ft -°F/Btu)
                Therefore,
           Thus, the condenser will be  adequate for the  service.  Because the available  foul-
           ing resistance is greater than the required fouling resistance, the condenser will last
           longer than the specified time before cleaning.


           Table 4.7  Summary of Equations for Rating a Heat Exchanger ______

           First subscript: Process stream = 1,2,3 or 4
           Second subscript: Component =1 or 2

           Mass Balance

           m 3 '=m4                                                    (4.7.1)

           Energy Equation

           Q = h 3, 2m3'-h4, 2m                                        (4.7.2)

           Rate Equation

                                                                       (4.7.3)
           Q = U 0  A 0 F(At) LM
           F = f(tj', , t 3', t 4')  —  Equation 4.10                  (4.7.4)
                  t 2
           (At) LM = f(ti', t 2, t 3', V)  —  Equation 4.2             (4.7.5)

           Economic Relations

           1  3' -  1 2 = approach At —  Table 4.5                     (4.7.6)

           Thermodynamic Properties

           h 3j2 = f(t 3')                                             (4.7.7)






         Copyright © 2003 by Taylor & Francis Group LLC
   195   196   197   198   199   200   201   202   203   204   205