Page 69 - Pressure Swing Adsorption
P. 69

44                                    PRESSURE SWING ADSORPTION                 FUNDAMENTALS OF ADSORPTION                                   45

                       i  • 0
                                                                                                                                 (1;1
                                                                                                   i. 0 ~-------------'-'--'--------------,
                       0.'                                                                                 'ca 3.65µm
                                                                                                      De/re  '3•10-'s·'                             0
                     '  •
                     -  0.6                                                                       0.8
                    .  o.,
                                                                                                l o.6
                       0.2
                                                                                                E
                                      '                                                                       D
                         0        q          10   12   111   16   ta   :rn                        0.4
                                           ti(mmi)
                                                                                                               0
                                                                                                   0.2


                                                                                                             5       10      15      20     25      30      35
                                                                                                                                Jt  isec )' 12
                                                                                                                    Figure 2.17  (Continued).



                                                                                              diffus10n  equation  takes the  form:
                                                                                                                                       2  iJ(J.,1  \
                                                                                                   iJ0A  _    [)_.Ju   [            + --J
                                                                                                    at  - ( I  - 8  - 0  )  ( I        r   (Ir          (2.4 I)
                                                                                                               A    H



                                                               b
                         -2
                        10
                           0   200   ,oo   600   800   1000   1200   lllOO
                                           Time  (min}
                                                                                              with a similar ex11ression  for component  /J.  These expressions arc  used  in  the
                                                                                              modeling  the  dvnam1c  behavior  of the  kincucally  sdect1ve  CMS  adsorhents
                                                                                              (see Secl!on  5.2).
                                                 Partial
                                                 pressure step
                          Curve   Sorbate   T (K)   {Torr)   Deir~  (s-')
                                                                                                 2.3.7  Macropore Diffusion
                           I     0,      193      6-225      2.6  K  10-s
                           2     N,      273     715-580     3.2  X  10- 6                     Locai  sorpt1on  raic:
                           3     o,      193     470- 750    1.ox10-~
                          4      0,      273     250----110   4.1  X  10- 4                          ac         \ aa  _    i  2  ac   a c  I
                                                                                                                                    2
                                                                                                   ',at+ (l  - ',,Tf - ,,D,\ R JR  + aR 2 )              (2.42)
               Figure  2.17  Expcnmcntai  uptake  curves  {a)  and  (b)  for  0  m  the  Bcrgbau-
                                                                2
               Forsclrnng  carbon  molecular  sieve  at  193  K  and  (c)  and  N.,  in  three  different  size
               fractions  ()!'  4A  zcolitc  crvstais.  showmg  conforniity with  thC  diffusion  model.  From   If the  equilibrium  is  linear (q*  = Kc),  this  reduces  to:
               Ruthven  14   and Yuccl  and  Ruthvcn.  44
                                                                                                                                                         ( 2 .43)
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