Page 364 - APPLIED PROCESS DESIGN FOR CHEMICAL AND PETROCHEMICAL PLANTS, Volume 1, 3rd Edition
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332                      Applied  Process Design for Chemical and Petrochemical  Plants

                                  Table 5-7                                            Table 5-8
                 Example Scale-Up of Two, D 2 /D 1, For Varying      Order of Magnitude of Outside Film Coefficients, h
                               Mixing Slopes  16                                    Turbulent Range

            Mixing Slope, x   N2/N1   P2/P1   V2/V1   (P/V)2/(P/V)1                   Helical Coils  I   Vertical Coils
                                                                  Fluid             BTU/(Hr.)  (sq. ft.)  (°F.  between tank
              0.5 ...............   1.0   32.0   8     4.0                                  fluid and coil fluid)
              0.6 ...............   0.8   16.0   8     2.0
              0.75 ..............   0.63   8.0   8     1.0        Water,  0.38 cp   .   500-1100         500-1100
              0.9 ...............   0.54   5.0   8     0.62       Oil,  10 cp    .                        20--70
                                                   I
              1.0 ...............   0.50   4.0   8     0.50       Oil,  52 cp    .      40-70             10-30
             By permission; Rushton.]. H., Chem. Eng. Prog. V 47,  (1951), pg. 485  [16].

                                                                     4.Jackel [35][29]
                 For NRe  > 4  X  10 in fluid bulk in tank
                                3
                                                 2  0.658                   � 0.85( D'tp r  [ ':µ J" [:. J" (;  r
                                             (  ND  p  )
                 h (plate coil)  (Ppcw  /k)  =  0.0317   - µ -
                  0
                                      [ �  )0.33  [..!:...)0.50   (5- 77)     (  TD   )0.13                    (5- 78)
                                        kw       µf
                                                                  Design Application
                 Some scale-up heat transfer relationships  [29]:
                                                                         A few  typical overall heat transfer coefficients,  U 0,
                 a)  Laminar flow,  R,, <  100                         are presented in Table 5-9  [27]  [29].
                    h., p  HP  (horsepower at the impeller shaft)        Figure 5-41  indicates the mixing correlation expo-
                 b)  For a constant impeller diameter,  turbulent flow:
                                                                       nent, x, as related to power per unit volume ratio for
                    ho p  (HP) o.22                                    heal  transfer  scale-up.  The  exponent x  is  given  in
                 c)  For constant speed,  same impeller type  (family)   Table 5-6 for the systems shown, and is the exponent
                    ho  P  (HP)  o.29                                  of the  Reynolds  number  term,  or  the  slope  of the


                                                             Table 5-9
                               Approximate Overall Heat Transfer Coefficients for  Jacketed Mixing Vessels

                                                    U Expressed in BTU/hr/sq ft/°F
             FLUID INSIDE         FLUID IN
             JACKET               VESSEL                 WALL MATERIAL              AGITATION               u
             Steam                'Nater                 Enameled C.l.*              0-400 R.P.M.          96-120  [25]
             Steam                Milk                   Enameled C.l.               None                 200
             Steam                Milk                   Enameled C.l.               Stirring             300
             Steam                Milk boiling           Enameled C.l.               None                 500
             Steam                Boiling water          Steel                       None                 187
             Hot water            \Va.rm water           Enameled C.l.               None                  70
             Cold water           Cold water             Enameled C.I.               None                  43
             Steam                Water                  Copper                      None                 148
             Steam                Water                  Copper                      Simple               244
                                                                                       stirring
             Steam                Boiling water          Copper                      None                 250
             Stearn               Paraffin wax           Copper                      None                  27.4
             Steam                Paraffin wax           Cast iron                   Scraper              107
             ,vater               Paraffin wax           Copper                      None                  24.4
             'Nater               Paraffin wax           Cast iron                   Scraper               72.3
              "C.I.  =  Cast Iron
             "*= or Glass-lined on steel
             Adapted  by  permission:  Lightnin/Unit of General Signal  (27].
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