Page 408 - Book Hosokawa Nanoparticle Technology Handbook
P. 408

FUNDAMENTALS                           CH. 6 EVALUATION METHODS FOR PROPERTIES OF NANOSTRUCTURED BODY
                  Table 6.9.1
                  Gas-separation efficiencies of various polymer membranes.
                    10
                         3
                  10 , P cm -cm   Polysulfone   Acetylcellulose  Polyimide  Poly                Silicon rubber
                    –2
                      –1
                  cm s cmHg                                                 (4-methylpentene-1)
                  H 2                13            12               9             136               550
                  CO 2                6             6               –              93               270
                  O 2                 1             1               0.5            32               501
                  
 ij
                  H /CO              40            40              76               –                 –
                   2
                  H /CH 4            60            60             200               –                 0.7
                   2
                  H /N 2             72            70             200              17                 2
                   2
                  CO /CH 4           25            30               –               –                 0.3
                    2
                  O /N 2              6             5.5                             4                 2
                   2
                  Note: Temperature 25–30, constant pressure.
                            Alloy membranes  Amorphous alloy membrane  (a) Hydrogen pump
                                                                                  Direct-current
                                                                                   electricity
                                                                            e −               e −

                                                                                     H +      H
                                                                             H 2               2
                                                                           	 (H ,I)         	 (H ,I)
                                                                                               2
                                                                              2
                                                                 (b) Hydrogen separation by proton-electron mixed electroconductive membrane

                                                                                      +
                                                                                     H
                                                                             H 2              H 2
                                                                          	 (H ,feed)  e   	 (H ,feed)
                                                                             2
                                                                                              2
                  Figure 6.9.3
                  The mechanism of gas permeation and separation of alloy  Figure 6.9.4
                  and amorphous alloy membranes.
                                                                 The permeation mechanisms of proton-electroconductive
                                                                 material and oxygen ion-electroconductive material.
                                                                 (a) Hydrogen pump. (b) Hydrogen separation by
                  method, the intermediate layer and the porous sup-  proton–electron mixed electroconductive membrane.
                  porting plate made by the sol–gel method. By control-
                  ling the pore sizes in these structural layers at about
                  0.3 nm, about 4 nm and 80–150 nm respectively, high  but cannot attain high gas purity. In contrast, it is pos-
                  separation and permeability coefficients have been  sible to realize 100% gas purification using the alloy
                  obtained with the ceramic membranes.           and amorphous membranes, although it is only
                    On the other hand, the mechanism of permeation  achievable for some gases.
                  and separation of alloy membrane and amorphous one  Besides the polymer, alloy and amorphous mem-
                  is completely different from that of the polymer mem-  branes, the research and development of separation
                  brane, as shown schematically in Fig. 6.9.3. At the  membranes for hydrogen or oxygen using proton-
                  surface of the alloy and amorphous membranes, the  electroconductive oxides or oxygen ion-electro con-
                  hydrogen molecules are decomposed by the catalytic  ductive oxide has also been actively carried out. These
                  effect to generate hydrogen atoms.  The hydrogen  separation mechanisms include using hydrogen pump
                  atoms are then absorbed through the membrane sur-  to transfer and separate hydrogen with the electric
                  face and diffuse towards its opposite side and finally  current as shown in Fig. 6.9.4a and separating hydro-
                  leave the membrane as hydrogen molecules.      gen by spontaneous permeation based on the differ-
                    Due to such differences in the permeation and sep-  ence in the partial pressure of hydrogen as shown in
                  aration mechanism, the polymer membranes are able  Fig. 6.9.4b. The latter is regarded as a hydrogen per-
                  to enrich the gas molecules at a relatively high speed,  meation membrane [7]. However, no report has been

                  382
   403   404   405   406   407   408   409   410   411   412   413