Page 133 - Pressure Swing Adsorption
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108                                   PRESSURE SWING ADSORPTION                  EQUILIBRIUM THEORY                                           109

                The moles of the  oure,  light product withdrawn  during the feed  step may
              be  determined from  Eqs.  4.10  and  4.22,  as  follows
                                                                                                              1.0
                                                                        ( 4.24)
              where  8 A  has the same value as  m Eqs.  4.20 and 4.22.                                     R  o.5
                The pressunzation with  product step  m this cycle  follows  the  purge step;
              so  the bed 1s  presumed to contain only the pure, light component. Thus, Eq.
              4.17 yields                                                                                       0
                                                                                                                0
                                                                        ( 4.25)
              Consequently,  the  rate  of pressunzauon  ts  immaterial;  only  the  initial  and
              final  pressllres matter.
                The definition of recouery  of the light component for  this four•step  cycle,
              with  pressurization by product 1s:                                                                             (a)
                    .-
                     _  :0::tlF - Q;;;tlPR  - O:tlru
                  R                                                     ( 4.26)
                               Qiu'IFY8F
              Thus,  by  combining Eas. 4.22  through 4.26 and rearrangmg, one obtains:

                                                                                                               0.1
                                                                        ( 4.27)
                                                                                                            R o.o5
              where/;= 1/[1 + (gPHYF/3A.,)/(1  - /3 )] is  a factor that deviates from  umty
                                              0
              only  for  nonlinear  isotherms.  For · examole,  when  component  A  follows  a
              auadratic  isotherm,  qA  =  KAcA  + MAc~  and  component  B  follows  a  linear                   0
              isotherm,  q = K»c  ,  one gets
                       8       8                                                                                 0
                       l  - e  MA
                   t= -,-R
                Some  specific results of Ea. 4.27  are shown  m  Figure 4.4  for  the case of                               '-o  '
              linear  isotherms  (MA  =  0  and  { =  1).  This  figure  illustrates  the  effects  of
              feed  composition and pressure  ratio on product recovery, for  two  adsorbent                                  (b)
              selectivities,  -{3  =  0.1  and 0.9. These selectivities span  the  range of very easy
                                                                                                Figure  4.4  The  effeci  on  recovery  of  feed  composition  and  pressure  ratio,  for  ~
              (e.g.,  hydrogen  purificatmn) to qmte difficult (e.g.,  separation of argon from
                                                                                                (a)  = 0.1  and (b) 0.9,  for pressurizatton with  product.  13
              oxygen),  respectively.  The  resuits  are  shown  as  three-dimensional  surfaces
              that  nave  qmte  similar  shapes,  despite  the  large  difference  m  selectiviues.
              Both surfaces approach an asymotote at high oressure ratios and, to a lesser
              extent,  as  the  oercentage  of the  heavy  component  m  the  feed  approaches
              zero.  Conversely,  recovery  of the  light  comoonent  always  decreases  as  the
               amount of the heavy component m the feed  mcreases.  Later, m Secllon 4.6,
               additional comparisons are made that focus  on  the  effect of isotherm curva-
               ture.
                 Another  measure  of overall  PSA  performance  is  the  ennchment  of the
               byproduct,  EA  = Y AwlYAF- This  may  be  of interest  when  the  more  strongly
               adsorbed  component  1s  valuable.  If  that  component  is  very  valuable,  the
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