Page 424 - Chemical process engineering design and economics
P. 424

404                                                      Chapter 7

           Rate Equation

           r A =  kf(p i )                                            (7.14.3)

           y ; = P i / P '                                            (7.14.4)

           Transport Equations
                                2
           (A p) B'  = 150 [n v s / (D p') ] (1 -  s') 2  / (s') 3  + 1.75  [ p (v sf  / D p' ] (1 -  e') / (e') 3
           —   0.11  psi/ft < (Ap) B < 0.2 psi/ft  [ 2470 < (Ap) B > 4490 Pa/m  ]  (7.14.5)

           Ap = [(Ap) B ](LB+3ft)                                    (7.14.6)


           V v = v sA B                                              (7.14.7)
           Geometric Relations
                   2
           A B = 7iD /  4  —  maximum D«  13.5  ft (4.llm)           (7.14.8)
           VB=W B /P B '                                             (7.14.9)

                                      1
           LB  =  V B / A B  —  L B minimum = A D
                       —  L Bmaximum* 25 ft (7.62m)                   (7.14.10)

           L R = L B +LI'  —  L! «3ft(0.914m)                        (7.14.11)

           System Properties
           k = A'exp(E'/R'T')                                        (7.14.12)

           Cp=Eyj'c P i'                                             (7.14.13)

            H = Iyi'Hi'                                               (7.14.14)

            P =  Zyi'pi'                                             (7.14.15)

           P'V v = m T 'R'T'                                         (7.14.16)

           Ah R = Ah 1' + AH° R'  +Ah 2'                             (7.14.17)

           Unknowns

              - W c - X A - Ah R - Ap -  C P -  ja    - D
           r A                      - p - k - A B  - V B  - W B  - L B - y j - v s  - V v



         Copyright © 2003 by Taylor & Francis Group LLC
   419   420   421   422   423   424   425   426   427   428   429