Hydrocracking, zeolite-supported catalysts

Hydrocracking, 30 48-52 behavior, thermal, 29 269 catalytic, 26 383 deethylation, 30 50 demethylation, 30 50 metallocarbene formation, 30 51-52 of f -decane, 35 332-333 primary coal liquids, 40 57 procedure, 40 66-67 product distribution, 30 49 reactions, over perovskites, 36 311 suppression by sulfur, 31 229 zeolite-supported catalysts, 39 181-188... 

Schutz and Weitkamp (15) show product distributions for the hydrocracking of dodecane on several noble metals on zeolite catalysts. Product distributions are in general similar to those distributions previously reported for noble metals on ambrphous supports. These results show no major unexpected effect of the zeolitic support differences among the catalysts tested are related to changes in hydrogenation ability or acidity. 

Several explanations have been advanced for the unique performance of Pt/LTL zeolite catalysts. There is a consensus that dehydrocyclization is catalyzed by the platinum clusters alone, with the support providing no catalytic sites [23,38,40]. The support must be nonacidic to prevent acid-catalyzed isomerization and hydrocracking as side reactions [41-43] The aromatic selectivity increases with the basicity of the LTL zeolite support. The interaction of the platinum clusters with the basic support has been suggested to result in an increase in the... 

Naphtha reforming catalysts are mostly based on metals (Pt, Pt-Re, Pt-lr, Pt-Sn, Pt-Re-Sn) supported on chlorinated-ALOs or on a KL zeolite. Non-acidic KL zeolite in combination with Pt has been applied in a new reforming process. The non-acidic zeolite support inhibits undcsircd isomerization and hydrocracking reactions leading to enhanced aromalization selectivities [69]. Besides the absence of acidity, the presence of highly dispersed Pt clusters inside the zeolite channels and the shape-selective effects imposed by the monodirectional channel structure (0.71 nm diameter) of the zeolite may also contribute to the excellent aromatization performance of Pt/KL catalysts. 

Metals catalyze many reactions of practical importance, and the most conunon form of an industrial metal catalyst is a supported metal consisting of dusters or particles on a high surface area support such as a metal oxide. The support may also be a zeolite as in the Pd supported in faujasite catalyst used for hydrocracking. For the most part, zeolite supported metals are structurally complex and are beyond the scope of this chapter. They have been reviewed elsewhere. [105]... 

The acid component of a hydrocracking catalyst can be an amorphous oxide, e.g., a silica-alumina ora zeolite, eg., USY. This component usually serves as a support for the metal compound responsible for the hydrogenation function. The metal compound can be a noble metal, e.g., Pt or Pd, or a mixture of sulfides, e.g., of Ni/Mo, NiAV, or Co/Mo. The relative amounts of the respective compounds have to be thoroughly balanced to achieve an optimum performance. 

Figure 16.7 Influence of support type on product distribution in hydrocracking hydrotreated light Arabian gasoil feed hydrocracked over amorphous and high zeolite catalysts differential yields measured in 50°F (10°C) increments.

Recently, we reported that an Fe supported zeolite (FeHY-1) shows high activity for acidic reactions such as toluene disproportionation and resid hydrocracking in the presence of H2S [1,2]. Investigations using electron spin resonance (ESR), Fourier transform infrared spectroscopy (FT-IR), MiJssbauer and transmission electron microscopy (TEM) revealed that superfine ferric oxide cluster interacts with the zeolite framework in the super-cage of Y-type zeolites [3,4]. Furthermore, we reported change in physicochemical properties and catalytic activities for toluene disproportionation during the sample preparation period[5]. It was revealed that the activation of the catalyst was closely related with interaction between the iron cluster and the zeolite framework. In this work, we will report the effect of preparation conditions on the physicochemical properties and activity for toluene disproportionation in the presence of 82. ... 

The acid function of the catalyst is supplied by the support. Among the supports mentioned in the literature are silica-alumina, silica-zirconia, silica-magnesia, alumina-boria, silica-titania, acid-treated clays, acidic metal phosphates, alumina, and other such solid acids. The acidic properties of these amorphous catalysts can be further activated by the addition of small proportions of acidic halides such as HF, BF3, SiFit, and the like (3.). Zeolites such as the faujasites and mordenites are also important supports for hydrocracking catalysts (2). 

On the other hand, it was proposed that acid catalyzed reactions such as skeletal isomerization of paraffin [2], hydrocracking of hydrocarbons [3] or methanol conversion to hydrocarbon [4] over metal supported acid catalysts were promoted by spillover hydrogen (proton) on the acid catalysts. Hydrogen spillover phenomenon from noble metal to other component at room temperature has been reported in many cases [5]. Recently Masai et al. [6] and Steinberg et al. [7] showed that the physical mixtures of protonated zeolite and R/AI2O3 showed high hydrocracking activities of paraffins and skeletal isomerization to some extent. 

HYDROCRACKING OF PARAFFHNIC HYDROCARBONS OVER HYBRH) CATALYSTS CONTAINING H-ZSM-5 ZEOLITE AND SUPPORTED HYDROGENATION CATALYST... 

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