Page 287 - Pressure Swing Adsorption
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              264                                   PRESSURE SWING ADSORPTION
                                                                                     i                                CHAPTER
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              16.  S.  Sircar and J,  W.  Zondlo,  U.S.  Patent 4,013,429 (1977)  to Air Products.   I
              17.  S.  Sircar. m  Adsorp11on: Science and Technology,  p. 285, NATO ASI  E158 A. E. Rodrigues,             7
                 M.  D.  Le Van, and D. Tondeur, eds., Kluwer,  Dordrecht (1989).
                                                                                     I
              18.  J. L.  Wagner, U.S.  Patent 3,430,418  to Umon Carbide (1969).
              19.  L.  B.  Balta, U.S.  Patent 3,564,816 to Unton Carbide (1971).             Extensions of the PSA Concept
              20.  R. W. Alexis, Chem.  Eng.  Prag.  Symp.  Ser.  63(74),  50 0968).
                                                                                     I
              21.  H. A.  Stewart ani J.  L.  Heck, Chem.  Eng.  Prog. 65(9),  78  (1969).
               22.  K.  J. Doshi, C.H. Kahro, and  H.  A. Stewart, AlChE Symp.  Ser. 67017) (1971).
               23.  T.  Tomita, T. ·sakamoto,  U.  Ohkamo,  and  M.  Suzuki,  in  Fundamentals  of Adsorpt,on  II,
                  p.  89,  A.  I.  Liapis, ed.,  Eng. Foundation, NY (I 987).
               24.  J,  L.  Heck and T.  Johansen,  Hvdmcarbon  Processmg,  p.  175 Oan.  1978).
               25.  A. Fuderer and E. Rudelstorfer, U.S. Patent 3,846,849  to Union Carbide (1976).
               26.  R.  T.  Cassidy,  "Polybed  Pressure  Swmg  Hvdrogen  Processes,"  in  Adsorption  and  Jon
                  Exchange with Svnthettc Zeoli/es, W,  H. Flanck, ed.,  ACS Symp. Ser. 13S, p. 247, Am. Chem.
                  Soc.,  Waf>hington  D.C. (1980).
               27.  R. T. Cassidy and  E. S.  Ho1nies,  AIChE Symp.  Ser. 80(233), 68 (1984),
               28.  G.  Keller, "Gas Adsorption Processes: State of the Art in Industrial Gas Separations," Am.
                  Chem.  Soc.  Symp.  Ser. (223) (1983).
               29.  M.  Suzuki,  Adsorprwn Engineermg,  p. 247, Kodansha Elsevier, Tokyo 0990).
               30.  0. J. Smith and A. W.  Westerberg, Chem.  Eng.  Sci. 46, 2961 (1991).     The  basic  pressure  and  vacuum  swing  processes  have  been  developed  in  a
                                                                                              vanety of ways  by  making  use  of ingenious  multiole~bed  cycles  to  conserve
               31.  J.  Izumi. Mitsubishi Heavy tndustnes Ltd., personai commumcat1on (1992).
                                                                                              energy anct  separative work. The processes described in  Chapter 6 give some
               32.  J.  Grebbell, Oil and Gas Journal,  p.  85,  April  14 (1985).
                                                                                              mdicat10n  of the range of such solutions.  In  all  these 'Processes the reiat1on~
               33.  W.  C.  Kratz, D.  L,  Rarig, and  J.  M.  Pietrantonm,  A!ChE Symp.  Ser.  84(264) (1988).   shio with  the onginal PSA concept ts  ciuue  clear. However, the  PSA concept
                34.  R.  Kumar,  W.  c.  Kratz,  D.  E.  Guro.  D.  L.  Rarig,  and  W.  P.  Schmidt,  "Gas  Mixture   has  also  been  developed  m  other  ways,  leading  to  processes -m  which  the
                   Fractionation  to  Produce Two  High  Puritv  Products by  PSA,"  Sep. Sci.  and  Technoi.  27,   relationship to  the  parent process  1s  less  obvwus.  Three such  develooments,
                   509 (1992).                                                                none of which has so far been developed on an mdustnal scale, are described
                35.  S.  K.  Sood,  C.  Fong,  K.  M.  Kaivanam,  A.  Bus1gm,  0.  V.  Kveton,  and   in  this chapter.
                   D.  M.  Ruthven,  Fu.non  Technology  24,299 (1992).
                36.  D.  M.  Ruthven and S. Farooq, Chem.  Eng.  Sci. On  press).
                                                                                              7.1  The Pressure Swing Parametric Pump
                37.  J.  A.  Ritter and  R. T. Yang,  J and E.C.  Research  30,  1023 (1991).
                38.  E.  S.  Rikkinides and R.  T. Yang,  J and E.C.  Research  30,  1981  (1991).   The  term  parametric  pumpmg  was  coined  by  Wilhelm  in  the  l 960s  to
                                                                                              describe  a  novel  class of liquid-phase separation  processes in  which  separa-
                39.  S.  Sircar,  Fourth  International  Conferences  on  Adsorption,  Kyoto,  Japan,  May,  1992,
                   plenary lecture, "Novei Applications of Adsorption Technology."            tion ts achieved in an oscillating flow system subjected to a periodic change m
                                                                                                                                               1
                                                                                              temperature  and  other  intensive  thermodynamic  variable.  He  and  his  co-
                40.  R.  Banenee, K.  G.  Naravankhedkar, and  S.  P.  Sukhatine, Chem.  Eng.  Sci.  45,467 (1990).
                                                                                              workers  focused  on  temperature  swmgs,  but  they  contemplated  also  the
                41.  R.  Baner_,ee,  K.  G.  Naravankhedkar, and S.  P. Sukhatine, Chem.  Eng.  Sci.  47,  1307 (1992).
                                                                                              synchronous cycJe of pressure, pH, and electrical and magnetic fields.  In fact,
                                                                                              he cited  the earliest patent of Skarstrom (PSA aJr dryer) as  an example of a
                                                                                              pressure parametnc pump.
                                                                                                The  essential  features  of a  thermally  driven  system  are  shown  m  Figure
                                                                                              7.1.  During  the  heating  half-cycle  liquid  flows  upwards,  while  the  flow  1s
                                                                                              reversed  ctunng  the  cooling  half-cycle.  The  basts  of the  separation  can  be
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