Page 94 - Pressure Swing Adsorption
P. 94

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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