Page 324 - Applied Process Design For Chemical And Petrochemical Plants Volume II
P. 324

Packed Towers                                           31 3




                                        -A   :Wire  Screen, also  Weir-  ,Type(Steell
                                        --- B :Plain  Melai Plate
                                        Wire  Screen  Plate ~92% Fres  Space
                                        with  3/8"Square Openings




                                        L: Water  Rate, Ib./Hr.(sq.ft.)
                Air Mass Velocity, Ib../Hr.(sq.ft.)
           Figure 957. Comparison effect of  pressure drop across support     u
           plate and bed of 1% in.  lntalox@ saddles.  Used by permission of
           Leva, M.,  Lucas, J. M.,  and Frahme, H. H.,  Ind, Eng Chem. V. 46, No.   500  1,000
           6 (1 954); all rights reserved.
                                                                               Gas  Mass Velocity, Ib./Hr.(sq.  f t.)
                                                                            Pressure  Drop Through Fused Raschig
                                                                            Ring Plate,wi!h  Plate Covered  with
                                                                            One  inch of  I  Size  lntalox  Saddles
                                                                            (L:Liquid  Mass  Rate Parameter)

                                                                           Plate = 58 % Free Area

                                                                 Figure 9-39. Pressure drop through fused ceramic Raschig ring plate
                                                                 with plate covered with 1 in. of 1 -in.-size Intalox@ saddles. Used by
                                                                 permission of Leva, M.,  Lucas,  J.  M.,  and Frahme, H.  H.,  Ind.  Eng.
                                                                 Chem.,  V.  46, No. 6 (1 954); all rights reserved.




                        Pocked  40" High with
                        I"  lntolox  Saddles

                          2     4      6     8     10    12
                 Ratio of  Liquid Mass Velocity -Air  Mass Velocity through Tower   5.0
                                                                                     L 3,570

           Figure 9-38. Effect of choice of support plate on flooding rate. Used
           by permission  of U.S.  Stoneware Co. (now, Norton Chemical Process
           Equipment Corp.).





           In general the dumped saddle type packing should give less
           blocking to support openings than ring type.
                                                                              500  1,000
           Example 9-2: Evaluation of Tower                                  Gas  Mass Velocity> I b./Hr.(sq.f  t.)
           Condition and Pressure Drop                                   Pressure  Drop  through Plain Ceramic
                                                                                       Plate
             Check the design of a 4ft, Gin. I.D. tower packed with      (LE Liquid Mass  Rate Parameter)
           43 ft of 1-in. x  Xiin. thick steel Raschig rings if the service   Curve A also  Represents Weir-Type
           requires a liquid rate of 2,250 lb/hr  (ft2) of  10% caustic   Plate Covered  With One  inch of  I"
           solution (sp. gr. = 1.22) and 4,540 Ib/hr  (ft2) of 110°F air   lntalox  Saddles
           containing C02 to be scrubbed at 363 psia.                    Plate-20 O/O  Free Area  Plain Ceramic
                                                                              ~60 ?h Free Area  Weir- Type
             1. Determine the operating range for the tower by ref-   Figure 9-40. Pressure drop through plain ceramic plate. Used by per-
               erencing to Figure 9-21B or 9-21C. Use 9-21C for this   mission of  Leva,  M.,  Lucas,  J.  M., and  Frahme,  H. H.,  Ind.  Eng.
               example.                                           Chem.,  V.  46, No. 6 (1 954); all rights reserved.
   319   320   321   322   323   324   325   326   327   328   329