Page 122 - Academic Press Encyclopedia of Physical Science and Technology 3rd Chemical Engineering
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 Encyclopedia of Physical Science and Technology  EN002G-87  May 19, 2001  20:3






               520                                                                               Catalyst Characterization


               the active sites exist and where chemisorption, chemical
               reaction, and desorption take place.
                 Most commonly a freshly reduced metal or metal-
               supported catalyst will have a layer of oxygen, either
               strongly chemisorbed or fully oxidized, on its surface. Be-
               cause of this it is common practice in hydrogenation reac-
               tions to pretreat the catalyst in a stream of H 2 in the reactor
               to remove all traces of surface oxygen before performing
               the catalytic reactions. Also, throughout the years catalytic
               scientists have dealt with the problem of pyrophoric met-
               als by intentionally blanketing the catalyst with a carefully
               controlled amount of O 2 or CO 2 after reduction to prevent
               bulk oxidation. These protective layers are removed by re-
               duction and/or heat treatment in order to permit catalysis
               to occur.
                 Platinum–rhodium alloys in the form of wires woven
               into screens or gauzes are catalysts for the production of
               hydrogen cyanide by the reaction of ammonia, methane,
               and oxygen. The surface of these wires may contain impu-
               rities from the manufacturing operations, and thus surface
               analysis as opposed to bulk analysis is more important for
               predicting reaction rates. During ammonia oxidation, the
               platinum–rhodium alloy becomes surface enriched with
                                                                 FIGURE 21 ESCA spectrum of a palladium-on-carbon catalyst.
               less active rhodium due to the volatility of the platinum
                                                                 A, Survey scan locating the carbon 1s and the palladium 3pand 3d
               oxide, causing the reaction rate to diminish gradually.  peaks; B, scale expansion around the palladium 3d doublet. The
                 Sulfur compounds adsorb onto surface-active metal (or  small shoulder at the oxide location is assigned to a chemisorbed
               metal oxide) sites, causing deactivation in a large num-  oxygen state.
               ber of petroleum, petrochemical, and chemical catalytic
               applications. Acidic catalysts such as zeolites and pro-
                                                                 oxide support, changes in oxidation state on activation of
               moted aluminas are poisoned by nitrogen compounds by
                                                                 the catalyst, and deactivation of the catalyst by poisons.
               chemisorption onto active sites also located on the surface.
                                                                   Figure 21 provides an example of the use of ESCA to
                                                                 define an oxidation state of a freshly reduced palladium-
                 2. Surface Techniques                           on-carbon hydrogenation catalyst exposed to the air. The
                                                                 metallic palladium peaks (Fig. 21a) are quite evident, indi-
               The tools available for surface composition characteri-
                                                                 cating no bulk oxidation occurred. There is a strong peak
               zation are electron spectroscopy for chemical analysis
                                                                 for carbon, probably due to adsorbed CO 2 from the air.
               (ESCA), Auger spectroscopy (AES), ion scattering spec-  The presence of a small amount of PdO is suggested at
               troscopy (ISS), and secondary ion mass spectroscopy  337 eV in Fig. 21B. This peak is a shoulder on the palla-
               (SIMS). ESCA spectroscopy is used more widely than the  dium 3d 5/2 peak and most likely represents a surface layer
               others for studying the surface composition and oxidation  of oxide on the palladium. This information could not be
               states of industrial catalysts, and thus its application will  conveniently obtained by XRD because small palladium
               be discussed in limited detail.                   (or PdO) crystallites cannot diffract X rays. Furthermore,
                 The acronym ESCA refers to the technique of bombard-  XRD measures bulk properties and would not “see” sur-
               ing the surface with X-ray photons, which produce the  face oxides even if the crystallite sizes were sufficiently
               emission of characteristic electrons measured as a func-  large to be XRD sensitive. We can therefore expect to
               tion of electron energy. Because of the low energy of the
                                                                 see more frequent use of ESCA or other surface sensitive
               characteristic electrons, the depth to which the analysis is  techniques to monitor the surface of catalytic materials.
                               ˚
               made is only ∼20 A. The composition of this thin layer
               as a function of depth can be determined by sputtering
               away layers of the surface and analyzing the underly-  IV. COMPLEMENTARY TECHNIQUES
               ing surfaces. A number of important catalytic properties
               have been studied by this technique, including oxidation  Characterization techniques described in this section are
               state of the active species, interaction of a metal with an  used primarily to support the more routine methods used
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