Page 45 - Pressure Swing Adsorption
P. 45

,Ii

               20                                    PRESSURE SWING ADSORPTION                   FUNDAMENTALS OF ADSORPTION                                    21

               Table 2.3.  Physical Properties of Some Common Adsorbents
                                                                                                 rcsultmg  surface  is  no  longer  hydrophilic.  Despite  ns  widespread  use  as  u
                              Sp. pore   Av.  pore   Pore     Sp.      Particle                  desiccant  silica  gel  ,s  not  commoniy  used  in  PSA  orocesses  as  its  physical
                               vol.      diam.      size      area     density                   strength 1s  mfenor to that of alumma or zeolite  based  desiccants.
                  Adsnrhcnt   (cm·; g- 1 )   (A>   distrih.   (m2 g-1)   (gem   • T\
                                                                            '
                 Silica gel (I)   0.43   22       Ununodal   800       l.09                         2. 1.8  Activated Alumina
                 Silica )?el (2)   1.15   140     Unimodal   340       0.62
                                                                                                                                                              2
                 An. alumw,i   0.50     JO-· ,ooo   U111m11d11I   :no   1.21-1                   Activated  alum ma  1s  essentially  a  m1croporous  (amorphous)  form  of A 1 0~
                 Acl. carh1m   0.15-0.5   Wide    Bim11dal   200-      0.6~-0. 1 )               and  1s  made  hy  several  different  methods.  The -most  common  route  1s  hy
                                          range                2000                              controlled  dchvdrat1on  of the  trihvdrate A1 0::  3H 0  formed  m  the  Baver
                                                                                                                                             2
                                                                                                                                     2
                 CMS          0.25                Dimodal    400       0.98                      process but some  alummas are made by  orec101tat1on  from  a soluble salt in  a
                                                                                                 manner similar to  the  production of silica  gel.
                                                                                                    2.1.9  Zeolites
               removal  step.  Bnef details  of  two  representative  matenals  are  mciuded  111
               Table  2.3.  The large-pore matenal is  used  in  many liquid-phase applications.   In  contrast  to  the  other  adsorbents  so  far  considered,  the  zeolites  are
               whiie  the small-pore  matenal  ts  widely  used  as  a  desiccant  in  vaoor-ohase   crystalline rather than  amorphous. and  the  m1cro@ores  are  actuallv mtracrvs-
               systems.                                                                           talline  channels  with  dimr:ns1ons  precisely  deten:nmcd  by  the  crvstai  struc-
                  Adsorption  isotherms for  waicr vapor on  silica gci, acuvaicd alumina, and    ture. There  is  therefore virtually  no disirihution  of microporc size, and  these
               4A zeolite are compared  m  Figure 2.5.  Silica gci docs not  retam water vapor    adsorbents  show  well~dcfined  s1ze~selcct1ve  mo·lecular  sieve  properties-
               as  strongly  as  the  other  adsorbents,  but  Jl  has  a  higher  ultimate  capacity.   exclusion  of molecules  larger  than  a  certam  cnttcal  size  and  strong  stenc
               Furthermore,  1t  can  be  regenerated  at moderate  temoeratures (150-200°C).     restnct1on of diffusion  for  molecules with  dimensions approaching  this  limit.
               It  JS  therefore a  useful desiccant where the moisture load is  high and the dew   The framework  structures of three  of the most  important zeolites  are  shown
               pomt  required  is  not too low.  If silica gei  is  heated above about 300°C,  most   schematically  m  Figure  2.6.  The  frameworks  consist  of  tetrahedrally  con-
               of  the  hydroxyls  arc  removed.  The  adsorhcnt  loses  surface  area  and  the   nected  assemblages  of  Si0 1  and  A\0 1  units.  To  translate  the  schematic
                                                                                                  diagrams into aciual structur~s one musi-consider that the  iines  represent the
                                                                                                  diameters of oxygen  atoms (or  ions), while  the  m:uch  smaller  Si  or Al  atoms
                              40~--------------~                                                  are located at the ap1ces  of the  ooiyhedra. Within  rather broad  iimits Si  and
                                                                                                  Al  atoms  are  interchangeable  in  the  lattice,  hut  each  Al  introduces  u  net
                                                                                                  negative  charge  that  must  be  balanced  tw  an  exchangeable  catwn.  In  many
                              30                                                                  structures,  notably  zeolite  A,  the  exchangeable  cations  oart1ally  (or  totally)
                                                                                                  obstruct  the  mrcrooores.  The  eouilibnum  distribution  of  the  exchangeable
                                                                                                  catmns among the various  possible  cat10n  "sites"  has  been  extensively stud-
                                                                                                                                                   9
                                                                                                  ied and is well  established for  most of the common zeolites. For example, 10
                                                               4A                                 zeolite A  there are three types of site, as  indicated in  Figure 2.6(a). The most
                                                                                                                                                 2
                                                                                                  favorable are the type I sites (eight per cage) so in  the Ca +  form  (s,x cations
                                                                                                  per cage) all cat10ns  can  be  accommodated. m  the  type  I  sites where  thev do
                                                                                                  not  obstruct  the  channels.  The  effective  ditnens:1on  of  the  channei  1s  then
                                                                                                  limited by the aperture of the  eight-membered oxygen  nng (wmdow),  which
                                                                                                  has  a  free  diameter  of about  4.3  A.  Since  moiecules  with  diameters  up  to
                                                           80                                     about 5.0 A can penetrate these windows,  this 1s  referred to as a "5A" sieve.
                                            Relative  humidity,%                                    The Na+  form contains 12 cat10ns per cage; so not only are all  eight type  I
                Figure  2.5  Comparative  isotherms  showmg  the  adsorpuon  of water vapor  on  silica   sites  filled,  but  all  wmdow  sites  (3.0  per cage)  are  also  filled.  (The  twelfth
                gei,  aclivated  a\umma,  and  4A  zcolitc.  (When  plotted  in  terms of rciat1vc  humidity,   Na+  catmn 1s  accommodated  in  the  relat1vcly  unfavorable  type  III  site.) The
                the  isotherms are  approx1mateiv  independent  of temperature.)                  Na+  cation partially obstructs the wmdows,  reducmg the effective  size  cutoff
   40   41   42   43   44   45   46   47   48   49   50