Page 126 - Pressure Swing Adsorption
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 100   PRESSURE SWING ADSORPTION   EQUILIBRIUM THEORY                 101

 Inserting this  into  Eq. 4.1  yields:   altered form.  Since composit10n  can  be  determined  aiong  any  charactenst1c,
 ol'r;   auPy;   knowmg the initial composition, they provide an excellent means for perform-
 a("+ /3,a, - 0   (4.4)   mg steow1se material balances for PSA cvcles.
            The blowdown steo 1s  governed by Eas.  4. 7 and 458,  while  the subsequent
 where  /3,  - {l  + [(l  - e)Je]f;J-'.  which  1s  a  function  of  the  comoonent
          purge  step  can  be  analyzed  with  Eq.  4.7  alone.  These  steps  essentially
 partial  pressure.  Note  that  when  the  isotherms  of  both  components  are
          regenerate the adsorbent.  In  many convent1onal adsorption systems, regener-
 linear, this  oarameter is constant,  although here tt  1s  treated as  if it deoends
          ation  creates  a  wave  that  gradually  moves  through  the  bed,  which  1s  com-
 on oart1al  pressure,  Simply  adding the  appropnate forms  of Eo,  4.4  for  the
          monly  referred  to as  a  prooortwnate pattern  or  disoerstue  from  (see  Section
 respective components yields the overall matenal balance, which governs the   2.4).  In the remainder of this chapter, it 1s  referred to-as a  srmpie wave, partly
 interstitial  flow  m  the packed  bed.  Hence,  this exoression  may  be  empioyed   because it  contrasts with  the term  shock  wave  which.  ts  discussed beiow (see
 to  determine  the  Jocai  veioc1ty  in  terms  of  composition,  pressure,  and
          also  Section  2.4.1),  and  to  suggest  an  assoc1at1on  with  equilibrium  behavior
 adsorbent-adsorbate mteractions. The result is
          (as opposed to kinetic or dispersive effects).
 ",   (!''''   1 - /3   ·i   l  + (/3  - l)y,   To complete the analysis of even the simplest PSA cycle,  1t 1s  necessary to
 v, - exp'  YA,  l  + (/3  - l)yA  dyA  ='  l  + (/3  - l)y,   ( 4,5)   account for the uptake step(s). In particular, the feed step mvolves uptake of
          the  more  strongly adsorbed  component.  As  m conventional  adsorot,on  sys-
 where the approximation 1s  oniy exact for linear isotherms, and  f3  = (3A/f3 ,   tems, a sham concentration front 1s  created by this  uptake  that  1s  sometimes
 8
 which for nonlinear isotherms may depend on pressure and comoosition, but   called  a  constant  pattern  or self-sharpening  profile.  At  the  extreme  of local
 for  linear  isotherms  it  1s  constant.  During  pressurization  and  blowctown,  the   eauilibrium  behavior,  the  front  is  a  step change,  and  1s  called  a  shock  wave.
 composition,  pressure,  and  mterstitiai  velocity  vary  with  time  at  each  axml   Since  equilibrium  effects  are  emphasized  m  this  chapter,  the  term  shock
 position. The details are beyond  the· current scope (see Section 4.9),  but  the   wave  will  be  used,  even  though  m  reai  systems  diss1pat1ve  effects  may
 result for linear isotherms ts   dimm1sh  the  sharoness.  A  shock  wave  1s  shown  m  the  l)Ottom  portion  of
 -z   1  dP   Figure 4.1  m the feed  step. It appears as  a  thick line ,at  which charactensucs
 (4,6)    1ntersect, and it separates the shaded region (depicting presence of the heavy
 "  - f3.[1  + (/3  - l)yA]  P dt
          component)  from  the  plam  regmn  (depicting  the  pure  light  component).
 The  s1molic1ty  of eauilibrrnrn-based  theones  anses  because  the  couoled   Examples  of breakthrough  data  (from  expenments  rn  which  methane  was
 first-order oartiai  differential  eQuations governing the  matenal  balances can   admitted  to  a  bed  of activated  carbon  previously  pressunzect  with  mtrogcn)
 be  recast  as  two ordinary differential  eouat1ons  that  must  be  simultaneously   are  shown  m  Figure  4.2,  illustrating  the  sharpness  aua1nable  in  many  PSA
 satisfied.  The  mathematical  techmque  employed  1s  called  the  method  of   applicallons,
 characteristics.  A  bnef  explanation  is  given  in  Appendix  A.  The  resulting   It ts  the velocity of a shock wave  through !he packed bed that governs the
 equations are:   duration of the feed  and  nnse steps,  Simiiariy,  that velocity  1s  controlled  by
          the rate of flow into and out of the system: hence, the material baiance.1s also
 ( 4,7)   affected.  The  veloc1ty  of  the  shock  wave  depends  On  the  rnterstitial  fluid
          velocities at the leading and  trailing edges of the wave.  These are related  by
 and      equating the shock wave  velocities  based on  the  conditions  for  both  compo-
          nents  A  and .B  to get
 (/3  - 1)(1  - YA)YA
 ( 4,8)
 [l + (/3  - l)yA]P
                                                                      ( 4,9)
 Equation 4.7  defines charactenstic trajectories m  the  z, t  oiane.  First of all,
 Eq.  4.8  shows  that when  pressure  1s  constant, composition  ts  also  constant,
          where, m general,
 and  the  characteristics given  by  Ea.  4.7  are straight lines.  Conversely, when
 pressure  varies with  time.  the  composition  varies  according to Ea.  4.8,  and
 the characteristics are curved.  Examotes of characteristics are shown  m  the
 bottom portion of Figure 4.1, for example, as lines durmg feed and purge and
 as  curves  during  oressunzation  and  blowdown.  It  is  important  to  note  that   l  and  2 refer to the  leading and  trailing edges of the wave,  respectively, and
 charactenstics do  not enct  at  the  end  of a  step;  rather,  they continue  in  an   fi;  ts  given  by  Eo. 4.2  for component  1  at comoosition- J.


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