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Else_AIEC-INGLE_cH005.qxd  7/12/2006  10:03 AM  Page 357
                  5.2 Basic Principles of Catalysis             357


                                                  Table 5.1

                                    Commercial catalysts and their uses (Gates, 1992)
                  Catalyst                        Reaction
                  Metals (e.g., Ni, Pd, and Pt as po wders  C=C bond hydrogenation,
                    or on supports) or metal oxides (e.g. Cr  2  O  3  )  olefin + H  2    paraf in f
                  Metals (e.g. Cu, Ni, Pt)  C=O bond hydrogenation,
                                                          acetone     H  2    isopropanol
                  Metal (e.g. Pd, Pt)       Complete oxidation of hydrocarbons,
                                                          oxidation of CO
                  Fe (supported and promoted with  3H      2    N  2    2NH  3
                    alkali metals)
                  Ni                                   CO     3H  2    CH  4    H  2  O (methanation)
                  Fe or Co (supported and promoted  CO         H  2    paraf ins  f    olef ins     H  2  O
                    with alkali metals)                     CO  2  (   other oxygen-containing or ganic
                                                          compounds) (Fischer–Tropsch reaction)
                  Cu (supported on ZnO, with other  CO       2H  2    CH  3  OH
                    components, e.g. Al  2  O  3  )
                  Re     Pt (supported on   n -Al  2  O  3  or  Paraffin dehydrogenation, isomerization,
                      -Al  2  O  3  promoted with chloride)  and dehydroc yclization
                  Solid acids (e.g., SiO  2  -Al  2  O  3  , zeolites)  Paraffin cracking and isomerization
                    -Al  2  O  3                        Alcohol     olef in     H  2  O
                  Pd supported on acidic zeolite  Paraffin hydrocracking
                  x Metal-oxide-supported complees of  Olefin polymerization,
                    Cr, Ti or Zr                  e.g. ethylene       polyethylene
                  Metal-oxide-supported oxides of  Olefin metathesis,
                    W or Re                         e.g. 2 prop ylene     ethylene     b utene
                  Ag (on inert support, promoted by   Ethylene     ½ O  2    ethylene oxide
                    alkali metals)              (with CO         2    H  2  O)
                  V  2  O  5  or Pt                  2 SO   2    O  2    2 SO  3
                  V  2  O  5  (on metal oxide support)  Naphthalene     9/2 O  2    phthalic anhydride
                                                            2 CO  2   2 H  2  O
                  Bismuth molybdate       Propylene               ½ O  2    acrolein
                  Mixed oxides of Fe and Mo  CH            3  OH     O  2    formaldehyde
                                                          (with CO  2    H  2  O)
                  Fe  3  O  4  or metal sulf ides  H      2  O    CO     H  2    CO  2


                                                  Table 5.2
                      olume,
                     Surface area, pore v and mean pore radii for typical solid catalysts (Wheeler 1950) ,
                  Catalyst             Surface area  olume Pore v  Mean pore radius
                                             (m  2  /g)    (cm  3  /g)     (Å)
                  Activated carbons  500        ∼ 1500    0.6   ∼ 0.8         10  ∼ 20
                  Silica gels         200       ∼ 600      0.4             15     ∼ 100
                  SiO  3  –Al  2  O  3  cracking catalysts  200  ∼ 500  0.2  ∼ 0.7  33  ∼ 150
                  Activated clays  150          ∼ 225      0.4  ∼ 0.52      100
                  Activated alumina  175     0.39            45
                  Celite (Kieselguhr)  4.2   1.1           11000
                  Synthetic ammonia catalysts, Fe  4  ∼ 11  0.12          200     ∼ 1000
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