Bifunctional alkane isomerization

In this section we present experimental evidence for a bifunctional alkane isomerization mechanism obtained by selective poisoning of the acidic sites of Pd-NiSMM with pyridine, which was pulse-injected into the liquid hydrocarbon feed stream. The possibility of additional poisoning of the metallic sites was checked by studying the hydrogenation of benzene and the isomerization and ring opening of methylcyclopentane (MCP). 

Recent results are presented illustrating principal mechanistic differences between alkane isomerization in liquid acids and over solid acids, including bifunctional catalysts. Isotopic labeling shows that butane isomerization over solid acids proceeds preferentially as a bimolecular process, i.e. via a Cg intermediate, which subsequently decomposes, preferentially into two iso-Cn structures. Bronsted acid sites in zeolites form chemical bonds with metal clusters. The resulting metal-proton adducts function as "collapsed bifunctional sites". 

Catalysts which contain reduced transition metal clusters besides acid sites are able to catalyze reactions that are not observed on catalysts exposing one type of site only. The reaction network is inadequately described by models which assume only additivity of catalytic functions and shuttling of intermediates between sites. There is strong evidence that metal clusters and Bronsted sites form metal-proton adducts. These act as "collapsed bifunctional sites" all alkane isomerization steps can take place on such sites during one single residence of the adsorbed molecule. At low temperature, adsorption in a mode reminiscent of a carbenium ion can suppress pure metal catalysis. 

To illustrate how a bifunctional catalyst operates, we discuss the kinetic scheme of the isomerization of pentane [R.A. van Santen and J.W. Niemantsverdriet, Chemical Kinetics and Catalysis (1995), Plenum, New York]. The first step is the dehydrogenation of the alkane on the metal ... 

Hence, the rate depends only on the ratio of the partial pressures of hydrogen and n-pentane. Support for the mechanism is provided by the fact that the rate of n-pentene isomerization on a platinum-free catalyst is very similar to that of the above reaction. The essence of the bifunctional mechanism is that the metal converts alkanes into alkenes and vice versa, enabling isomerization via the carbenium ion mechanism which allows a lower temperature than reactions involving a carbo-nium-ion formation step from an alkane. 

The three cycles have to turn over in the same range of temperature. This catalytic approach of the DeNOx reaction is not new. There is the same process for isomerization of alkanes, where there are also 3 catalytic cycles which have to turn over simultaneously (bifunctional catalysis). The kinetics of isomerization is given by only one cycle, the other two turning over very rapidly and are near equilibrium [13]. 

The hydroisomerization of heavy linear alkanes is of a great interest in petroleum industry. Indeed, the transformation of long chain n-alkanes into branched alkanes allows to improve the low temperature performances of diesel or lubricating oils [1-3]. On bifunctional Pt-exchanged zeolite catalysts, n-CK, transformed into monobranched isomers, multibranched isomers and cracking products [4], The HBEA zeolite based catalyst was more selective for isomerization than those containing MCM-22 or HZSM-5 zeolites [4], This was explained on one hand by a rapid diffusion of the reaction intermediates inside the large HBEA channels, and on the other hand by the very small crystallites size of this zeolite (0.02 pm). 

The platforming catalyst was the first example of a reforming catalyst having two functions.43 44 93 100-103 The functions of this bifunctional catalyst consist of platinum-catalyzed reactions (dehydrogenation of cycloalkanes to aromatics, hydrogenation of olefins, and dehydrocyclization) and acid-catalyzed reactions (isomerization of alkanes and cycloalkanes). Hyrocracking is usually an undesirable reaction since it produces gaseous products. However, it may contribute to octane enhancement. n-Decane, for example, can hydrocrack to C3 and C7 hydrocarbons the latter is further transformed to aromatics. 

When metal centers act in conjunction with acid sites on the zeolite, bifunctional catalysis can occur (e.g., Pd/HY). This type of catalysis is used mainly for the hydrocracking and isomerization of long-chain n-alkanes. For example, the rates of formation of 2- and 5-methylnonane isomers obtained from n-decane isomerization over bifunctional zeolite catalysts depend on the size and structure of the zeolites used. This reaction has been developed as a test reaction to characterize zeolite structures (17-19). 

With the aid of selective pyridine-poisoning experiments, we will show that isomerization of alkanes over NiSMM is a bifunction-ally catalyzed reaction. 

The isomerization of n-alkanes over NiSMM is a bifunctional reaction,... 

Isomerization reactions of alkanes and cycloalkanes occur very readily on bifunctional catalysts containing both metal and acidic sites (3,4), the latter being associated with the carrier employed for the metal. This mode of reaction is very important for the catalysts used in commercial reforming, which will be discussed in Chapter 5. In such bifunctional catalysts, the metal and acidic sites catalyze different steps in the reaction sequence. 

Investigations of the isomerization of alkanes in recent years have provided evidence that the reaction can occur on certain metals, notably platinum, in the absence of a separate acidic component in the catalyst (20-22). While it has been shown that a purely metal-catalyzed isomerization process can occur, the findings do not challenge the commonly accepted mode of action of bifunctional reforming catalysts in which separate metal and acidic sites participate in the reaction. The available data at conditions commonly employed with commercial reforming catalysts indicate that a purely metal-catalyzed process does not contribute appreciably to the overall isomerization reaction on a bifunctional catalyst. 

The most probable way of forming benzene is from a Cg oligomer, obtained from C3 condensation, but not through primary carbocations. The critical step would be the formation of the protonated cyclobutane ring, however, the four member ring cycloalkane has been claimed to occur as an intermediate during the isomerization of alkanes on bifunctional zeolite catalysts... 

The proposed mechanism for the isomerization of n-alkanes on bifunctional catalysts (60,61) is presented in Figure 14. From this mechanism an equilibrium between paraffins and olefins is established on the metal function. Then the olefins diffuse towards the Bronsted sites, where they become protonated and rearranged to give the branched carbenium ions. This, which is the rate controlling step, is followed by the desorption and hydrogenation, to yield the branched paraffins. 

Straight-run gasoline is composed primarily of alkanes and cycloalkanes with only a small fraction of aromatics, and has a low ON of about 50. The ON is improved by catalytic reforming of n-paraffins and cycloalkanes into branched alkanes and aromatics. The main reactions are isomerization (w- to iso-), cycli-zation, dehydrogenation, and dehydrocyclization. The bifunctional catalyst has an acidic function to catalyze isomerization and cyclization and a dehydrogenation function that requires an active metal site. Typically, platinum is used as the metal and AI2O3 for the acidity. 

The hydroconversion of -alkanes over noble metal-loaded zeolites follows a bifunctional mechanism, in which the reactant is dehydrogenated on the metal particles and the formed alkene is isomerized and/or cracked over the acid sites of the zeolite, followed by a subsequent hydrogenation of all unsaturated products on the metallic sites (see reaction Scheme 7). 

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