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               330                                                                         Membranes, Synthetic, Applications


               TABLE X  Catalytic Membrane Reactor Concepts for Chemical Synthesis
                Reaction type       Example           Conditions       Limitations         Membrane concept
                                                         ◦
               Dehydrogenation  Ethyl benzene to styrene  500−600 C; Fe-Cr-K  Equilibrium limited
                                                     oxide catalyst   conversion
                                                                                             CH 2 CH 3
                                                                      Costly separations
                                      CH 2 CH 3
                                                                                                           H 2
                                                                      Endothermic
                                                                                             CH  CH 2
                                      CHCH 2      H 2
                                                     ◦
               Hydrogenation  Carbon monoxide to   250 C; 50–100 bar;  Equilibrium limited      Catalyst
                                methanol             Cu-Al-Zn oxide   conversion
                                                                                     CO   H 2   CO   H 2
                                                     catalyst         (12–15%)
                              CO   2H 2
                                                                    Catalyst poisoning  H 2 S
                                                                      (by S, Cl)                 CH 3 OH
                               CH 3 OH                              Exothermic
                                                                                                         CH 3 OH
                                                        ◦
               Olefin metathesis  RCH  CH(CH 2 ) n COOR  25−400 C; W, Re  Equilibrium     Catalyst
                                                     (homogeneous,    mixtures require  A  A
                                                     heterogeneous)   product-feed
                                                                      separations
                                    RCH  CHR
                                                                    Catalyst poisoned      B      B
                                  CH(CH 2 ) n COOR′                   by water
                                                                                           C      C
                                  CH(CH 2 ) n COOR′
                                                                                                  Acid
                                                     ◦
               Hydration      Ethylene to ethanol  300 C; 70 bar;   Equilibrium limited
                                                                                                 Catalyst
                                                     H 2 PO 4  catalyst  conversion (<5%)
                                   CH 2    H 2 O                                     CH 2  CH 2
                              CH 2
                                                                    Large recycle
                                                                                        H 2 O
                                                                                                CH 2 CH 2 OH
                               CH 3 CH 2 OH
                                                         ◦
               Hydroformylation  RCH  CH 2    CO   H 2  100−200 C; 200–450  Catalyst recovery  RCH  CH 2
                                                     bar; Co, Ru, Rh  Product separation           ML n
                                                     homogeneous
                                  RCH 2 CH 2 CHO     complex catalysts                 CO   H 2
                                                                                                RCH 2 CH 2 CHO




               in genomes, and proteomics, the comprehensive study of  creating a miniature bioreactor chamber. If an ultrafiltra-
               proteins. Some examples are (1) increased automation,  tion membrane is used instead, proteins expressed by the
               through the use of robotic systems and powerful comput-  cells could be retained and subsequently desalted and puri-
               ers, to conduct massive screening of candidates to identify  fied by successive buffer exchange. Biochemical reactions
               those showing an expected response; (2) miniaturization  may be conducted in situ and monitored instrumentally
               of “classical” membrane processes; and (3) improved ana-  by fluorescence, luminescence, or absorbance measure-
               lytical sensitivity and specificity such as those associated  ments. In response to the ever-increasing pace of drug
               with  PCR  (polymerase  chain  reaction)  or  special  mass  discovery driven by pharmacogenomics, new designs of
               spectrometry techniques. With respect to membrane sys-  membrane microplates containing 384 or even 1536 wells
               tems, 96 individual assays may be performed systemati-  have been introduced to support rapid parallel processing.
               cally in as many cavities built into a multiwell form factor  There is little doubt that traditional laboratory membrane
               (Fig. 6). The bottom of each cavity may be sealed with a  operations will be adapted to this large-scale integration
               microfiltration membrane, for example, to retain cells but  strategy, analogous to the evolution of integrated circuits
               permit nutrients or reagents to perfuse through, thereby  in the microelectronics industry.
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