Page 284 - Pressure Swing Adsorption
P. 284

PRESSURE SWING ADSORPTION   PSA PROCESSES                           261
 260
 of  expans10n  of the  product  to  atmospheric  pressure.  For  a  vacuum  swi?g   without pressure equalization  there 1s  a shallow rnm11num  m the comoressor
 process· m  which  the  product  1s  produced  at  subatmosphenc  pr~ssure,  the   \   work curve at about  15  atm; while for  the process with  pressure equalization
 latter  quantity  will  be  negative.  Eauation  6.15  differs  from  the  normal   the  compressor work 1s  greatly  reduced  and  there  is  a  sharoer minimum  at
 definition  of the  First Law efficiency in that the seoarattve work  associated   l   about 4 atm. The exerget1c efficiency reaches a maximum  at aoout 5 atm for
 with  the  waste  product  1s  excluded  and  the  energy  of  compress10n  (or   I   the  process  with  pressure  eQualization  but  increases  monotomcally  for  the
 rations  were  considered:  the  two-bed  Skarstrom  cycle  with  and  without _a  I   grams for operation at their ootimal  pressures (in  terms of compressor work)
 expansion) of the product to atmosohenc pressure is allowed for.   process  without  oressure  equalization.  The  correspdnding  Grassman  dia-
 -A  detailed  exergy  analysis  of  PSA  air  separation  processes  has  been
        are  shown  in  Figure  6.26.  The  exerget1c  efficiency  is  about  17%  for  the
 40 41
 For oxygen  production tw?  process ~onfigu-
 reported by B·anerjee  et al.
 ,
 pressure  equalization step. The variation  of compressor work and exerget!c
 efficiency  with  operating  pressure  1s  shown  in  Figure  6.25.  For  the  cycle   COtfflGURATlON
                                    EXERGY
                                     OF
                           WO«K            lam
                          INPUT     FEED
 '•                 (a)    10•"            I
                          (100¼)

 PAOOl)Cl
 OHGE~  1014\
 1)1J<]   w,   t~•J•.1
 1100•1,1
 l)OOO  U•$'lol
 ••T~~c~l•O
 sOSHS  U\U              C0NFIGURAI10N  1          EXO 0-0t (0.5°/o)
 ""·~•,.)
                                     EX ERG¥
                           WORK       OF
                           INPUT     FEED
                            IHG     6•1J  ( 70¼)
 (a)
                           1100"/ol
                   (b)
                                               t'wJTV
                                               0,31 I l·6"/,)
 COMPRES
 f.XIT
 7113
 SlREAM   rsc'-"=~,  111•1•,.,
 )!178&                     3•56
 161"/ol                                            ly  1-76150"/.J
                                           y,:__.,~;.__E:X9  :0-0411•1"/ol
                  (c)                                O  0·01(0•3•1.1
 AFTERCOOlER
 l05S                                    •lO  ll•B'Vo)  0•1514•2•/•l
 COMPRESSOR   8657     FEED
 tOSSES   I 21•5 •/•l   EXERGY .. 0
 53.!9
 tu.,,.1                  -0-09
                          i-2-s.,-. J
 (b)
 Figure 6.26,  Grassman diagrams showmg losses of exergy for S~arstrom ~de (blo:,v-
 down  to  atmosohenc  pressure)  for  oxygen  production  (a)  without  .and  ~b)  with   Figure 6.27  Grassman  diagrams showing exergy losses for mtrogen  production  with
         three  different  cycles.  (a)  Skarstrom  cycle  and  (b)  SkarstrO:m  cvcJe  with  pressure
 pressure  eoualization.  Ooeratmg  pressures  are, ,resoect1vely,  15.b  and  3.9. b~r,  t.he
 Va1ues  for  Which  the  compressor  work  1s  m1mm1zed.  (From  Banenee  et  al.,   with   equalization  (PH)= 8  atm,  PL= 1  atm);  {c) vacuum  swing  cycle  (PH= 1  atm,  Pi.=
         0.2 atm). (From Banef]ee et ai., 41   with  pcrm1ss1on.)
 perm1ss1on.)
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