Page 93 - Pressure Swing Adsorption
P. 93

68                                     PRESS II RE SWING ADSORPTION
                                                                                               PSA CYCLES:  BA51C  PRINCIPLES                                69
               Table 3.1.  Summary of the Elementary Steps Used in PSA Cycles
                                                                                               Table 3.1.  (Conmwed)
                  Elemenrnry step    Mo<le ot operatmn       Principal features                   Elementary steri   Mock of orierat1on      Princira! feature~
                   Pressunzat1on   i.  Press11nzu11on  with   Enrichment or the less               Pressure        The high- and low-    Comerves energy ;lnd
                                    fee<l  from the foed   selectively adsorbed                     egu&lization     pres,,ure bc<ls  are   separative work
                                    end                    species m the gas phase
                                                                                                                     either connected
                                                           at the product end
                                                                                                                     through their product
                                   2.  Pressurization with   Sharpens the concentration
                                                                                                                     ends or the  teed and
                                    raffinate product from   front, which improves the
                                                                                                                     product ends of the
                                    the product end pnor   purity and recoverv of
                                                                                                                     high-pressure hed are
                                    to feed pressunzat1on   raffinate product                                        connected lo the
                                                                                                                     respecuve ends ot  the
                   High-pressure   1.  Product (raffinate)   Raffinate produc1  1s
                                                                                                                     low-pressure bed
                     adsorption     withdrawal at constant   delivered at high pressure
                                    coiumn pressure                                                Rinse           The bed is  purged with   i'mprove~ extract product
                                   2.  The column r,ressure ·1s   Verv high recovery of  the                         the  preferentrnllv   purny when !he liRhler
                                    ;1llowed  to decrease   less sciectivliv adrnrhed
                                                                                                                     atl.'>orhcd  specie., ;1ftcr   spcoc~ <m.:  coachorhed in
                                    while  the  rullinuie   species rnav  be achieved.
                                                                                                                     high-pressurt:        large .imount with  heavier
                                    product 1s  drawn from   hut lhc product 1s                                      adsorption  at  fccU   components
                                    the product end        delivered at low pressure
                                                                                                                     pressure m I he
                                                                                                                     direc:tmn of the  feed
                   Blowdown        I.  Countercurrent     Usetl when onlv raltinaie
                                     blowdown  to a low    product 1s  reomred at high
                                     pressure              punty; prevents contammat1on
                                                           of the product end with more        4.  Desorption at  the  iower operating pressure;  this  mav be  accomplished  by
                                                           strongly adsorbed species
                                                                                                  evacuation,  purgmg the bed with  the  rnffinate  product  or,  m  a  kinetically
                                   2.  Cocurrent blowdown   Used when extract product
                                     to an mtermediate     ,s also reamred in  high               controlled  process, by  slow equilibration with consequent evoluuon of the
                                     pressure pnor to      punty; improves exlract                slower-diffusing sorbate;
                                     countercurrent        product purltV and mav also         5.  Pressure equalization (which  JS  used  in many cycles. pnor to the blowdown
                                     blowdown              mcrease raffinate recovery             step,  to conserve  energy and seoarative work);
                                                                                               6.  Rinse  (purging with  the  oreferentially adsorbect-soecies  at  high  pressure,
                    Desorption     I.  Couniercurre111    Improves raffinate product
                     at low          desorption with       at the expense ot decrease             following  the adsorotmn step).
                     pressure        product purge         m recover,,: purge at               The  processes  differ  from  one  another  111  the  sequence  of  the  elementary,
                                                           subatmmphcnc pressure
                                                                                                steps and  m  the way  in  which  these  steps arc earned ouL  Some  of the  mon;
                                                           reduces raflinate product
                                                           loss bm increases energy             important  vanants  and  the  benefits  derived  from  them  are  summarized  10
                                                           COSI                                Table 3.1.
                                   2.  Countercurreni     Recovery enhancement while
                                                                                                  To understand  a  PSA  cycle  properly  It  1s  necessary  to  know  the  way  m
                                     desorption without    mamrnmmg high product
                                     external purge        purity 1s  possible oniy m          which  the concentration profile  moves  and changes 'shape  during each of the
                                                                                                elementary steos.  Gas-phase concentratrnn  profiles  m  an  adsorotion  column
                                                           certain kinetic separation
                                   3.  Evacuation         High punty of both                    that  undergoes  m  sequence  oressunzatton,  high-ptessure  adsorot1on.  blow-
                                                            extract and raffinate               down, and low-pressure desorption are shown  m  Figure 3. i  for  both  equilib-
                                                            products; advantageous over         rium  and kinetic separations. The profiles were  calculated  for  pressurization
                                                            producl purge when the
                                                            allsorbei.l phase 1s  very          with  feed  gas  (from  the  feed  end  with  the  product 'end  closed),  reverse  flow
                                                            strongly hdd                        biowdown,  and  desorption  with  product  purge,  aiso  in  the  reverse  flow
                                                                                                direction.  It  1s  clear  that  the  movements  of  the  concentration  wave  are
                                                                        (Cml!mued)
                                                                                                similar  in  both  cases.  During  pressurization  the  initial  gas  in  the  hed  1s
                                                                                                pushed  toward  the  closed  product  end,  where  it  forms  a  plateau  that  1s
                                                                                                significantly enriched  in  the less strongiy adsorbed species. The region  before
                                                                                                the  plateau  shows  the  penetration  of  the  feed  gas.  This  behavior  1s  m
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