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              Membranes, Synthetic, Applications                                                          301




































                            FIGURE 12  Illustration of mixed matrix strategy to exceed best available polymer performance.

                While such strategies are extremely attractive, signif-  mentation, each major application is discussed separately
              icant  hurdles  remain  to  be  overcome  in  all  cases.  The  below.
              crosslinking scheme needs to be tested on hollow fibers,
              since all reported literature is on flat-sheet membranes.
                                                                  1.  Hydrogen Separations
              Development of alternative crosslinking mechanisms is
              also  required,  as  this  will  provide  greater  flexibility  in  The first large-scale applications of membranes for gas
              implementation of this scheme. The mixed matrix work  separation were for hydrogen recovery. Hydrogen is im-
              needs to be extended to polymers that are currently use-  portant both as an energy resource and as a chemical feed-
              ful for gas separation. These materials are rigid and have  stock. Its major uses include the synthesis of ammonia and
              issues with poor adhesion between the polymeric phase  methanol, hydrogenation of oils and fats, as reducing at-
              and the molecular sieving phase (Mahajan, Zimmerman,  mospheres in ovens, and potentially as a nonpolluting fuel.
              and Koros, 1999). The extension of composite spinning to  Hydrogen is produced by steam reforming of natural gas,
              spinning with sieve materials is another significant chal-  petroleumhydrocarbons,orbyelectrolysis.Asoilreserves
              lenge to the implementation of this scheme. The polymeric  become “heavier,” or lower in hydrogen-to-carbon ratio
              materials used to mimic molecular sieves are currently  with continued depletion of reserves, the overall hydrogen
              processed  at  temperatures  that  would  make  large-scale  balance in refineries and petrochemical complexes gradu-
              commercialization  less  attractive.  The  development  of  ally becomes increasingly deficient. Recycling hydrogen
              chemistries  where  these  materials  can  be  produced  at  from  purge  streams  helps  reduce  the  load  of  catalytic
              lower temperatures is, therefore, highly desirable.  reformers and hydrogen plants; it also minimizes supple-
                                                                mental purchases of hydrogen to maintain an acceptable
                                                                hydrogen-to-carbon balance in petroleum refining. Some
              D.  Applications
                                                                applications in the petroleum refining industry are shown
              The major membrane-based gas separation applications  in Fig. 13.
              are shown in Table V. The diverse needs of these sep-  In the chemical process industry, an important appli-
              arations call for a somewhat wider range of membrane  cation of hydrogen recovery is in ammonia synthesis
              properties and module designs than is the case with liq-  purge streams. Ammonia is produced by combining hy-
              uid separations. To reflect this market and technical seg-  drogen and nitrogen at high pressure and temperature in
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