Page 356 - Pressure Swing Adsorption
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 332   PRESSURE SWING ADSORPTION   APPENDIX C                             333

 200c   •r----'i-1ooc
                                                      18 29
              related  disclosures  that  were  approved  in  1964.' ·  Their first  process  was
 Nz  RICH
 PRODUCT      also used for upgrading reformer recycle gas, m the range of 50% hvctrogen.
 112   412    with an ultimate purity of greater than 99% hydrbgen, u·sing activated ca_rbon
 123   411   423
 110   410    and activated alumma as the adsorbents. The ooeratmg conditions included a
 ID7b         pressure  range of from  200  to  650 osig for  ads0rot1on,  and 8  to  12  0s1a  for
 407,  407b
              desorPtIOn  and ourgmg. The cycle  mcluded  a  monthly  thermal  regeneration
 407
              at about 600°F, via an mert gas. The second patented process was apparently
              the first  that explicitly mentioned a  cocurrent blowctown  step  that was  used
              directly  partially  to  pressurize  a  parall"e!  column.  That  idea,  which  is  often
              referred to as  pressure eaualizatwn, has  been claimed  as  a vnal  nart of many
 I
              other patents, of which  only a  few  are cited  here as exampies:lfJ--i.i
 J'1
                C.2.9  Wilson
 317          Another early patent application concernmg the  actuai (versus  hypothetical)
 417
              separat10n  of oxygen  and  nitrogen  from  a1r  m  a  single  system  was  filed  by
 2.00CI   IOOo                                              7
              Wilson m 1959, although 1t  was not approved until 1965. It contained several
              novel ideas that recurred in later patents. For example, a three-step cycle was
              used:  pressunzatton  (with  orednect  air),  cocurrent  blowdown  (producing
              ennchect  oxygen,  at  70  to  90%),  and  countercurrent  blowdown  (producmg
 Figure· C.3  Flowsheet  of a second  PSA  apparatus  suggested by  Skarstrom  m  I 958,   enriched  nitrogen,  at subatmospheric  pressure).  He  suggested  an  option  of
 which appeared in  U.S. Patent No. 2,944,627 in  1960. This cqummcnt was apparently
 designed for cxtrncting two  nearly pure products from  a smgle  feed, such  as splitting   using heat to  achieve  a  higher degree of desorption  than  by  pressure aione.
 nitrogen and oxygen  from  air.   He also suggested usmg an oscillating ptston to dflve the pressure swmg, and
              that  idea  has  been  borrowed,  slightly  modified,  or  remvented  several
                   35 39
              ttmes.  -  He suggested that the same ideas could be used to remove carbon
 two  or  more  adsorbents  and  couoling  PSA  systems)  has  been  reinvented   dioxide  from  a!f (e.g.,  m  submarines) and  to  separate  helium  from  natural
 (with subtle  twists) or borrowed several timcs.  16 24   gas.
 -

                C.2.10  Stark
 C.2. 7  Skarstrom
              About  2  years  after  the  flurry  of  patent  applications  for  PSA  hydrogen
 Some  early  PSA  patents  concerned  with  hydrogen  ourificatton,  which  fol-
 lowed  up on much earlier suggestions by Perley ID  and Erdmann,  were filed   purification were  filed  by  Skarstrom  and  his  collbagues (see  C.2. 7),  another
 14
 by  Skarstrom  10  1960  and  awarded  m  1963-64_ 25 27   The  first  oatent 25   patent that extended the seoaration capability was filed  by the same company
 -
                                                 16
 described  upgrading reformer  recycle gases from various types of processes,   (Stark,  filed  m  1963  and  awarded  10  1966  ).  The  application  was  also  the
              upgrading of reformer recycle gas, m the range of 80% hydrogen, to attain an
 m the  range of 50  to 80%  hydrogen, with an ultimate purity of greater than
 95%  hydrogen,  using  activated  carbon  as·  the  adsorbent.  The  second  de~   ultimate  purity of 99.9%  hydrogen  at  a  recovery· of 75%.  usmg  silica  gel  as
 scribed specific ooeratmg conditions, but did not specify the resulting perfor-  the adSorbent.  The ooerating conditions  included  a  pressure  range  of from
              500 psig for adsorption and 0 os1g  for  desorotton  anct  ourgmg.
 mance.  The third  revealed  more  process  details,  and  mentioned a  potential
 recovery of 70%,  but did  not state the corresponding punty.
                C.2.11  Basmadjian and  Pogorski
 C.2.8  Hoke,  Marsh,  et al.   An  early  PSA  cycle  that  was  apparently  the  first  to  use  a  rmse  step  (see
              Section  4.4.5)  was  invented  by  Basmadjian  and  Pogorski.  Their  applicatmn
 Within  a  year  of  filing  of  Skarstrom·s  PSA  oatents  related  to  hydrogen   was filed  in  1963 and the oaten! issued m  1966. 411   This cycle was  mtended to
 I            recover helium and possibly other light comoonents from  nitrogen or natural
 purification,  his  colleagues,  Hoke,  Marsh,  Bernstem,  Pramuk,  and  he  filed
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