Overview
FrançaisABSTRACT
Many industrial processes in oil refining and petrochemistry make use of the sustainable character of bifunctional catalysis. However, its role in light alkane conversion and in fine chemicals synthesis has so far been negligible. The set of study cases reported in this paper show that the bifunctional processes are similar, involving successive steps of molecular diffusion and chemical conversion catalyzed by two types of active sites. Conversely, the specific properties of the reactants, intermediates and products induce remarkable differences in their reactivity and in diffusional behavior along pores. The optimal features of the bifunctional catalysts are therefore different: support with meso- or macropores instead of micropores, etc. Some remarks on the main hurdles limiting their development and strategies to overcome them are also presented.
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Read the articleAUTHORS
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Michel GUISNET: University Professor - Catalysis in organic chemistry, Poitiers, France Centre for Biological and Chemical Engineering, Lisbon, Portugal
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Ludovic PINARD: Senior Lecturer - Institut de chimie des milieux et matériaux de Poitiers (IC2MP) École nationale supérieure d'ingénieurs de Poitiers (ENSIP), France
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Matteo GUIDOTTI: Researcher - National Research Council Institute for Molecular Science and Technology, Milan, Italy
INTRODUCTION
Article
hydrodehydrogenating sites originating either from noble metals Pt or Pd, or from mixed sulphides of metals from groups 6 (Mo or W) and 8 (Co, Ni);
protonic acid sites from inorganic oxides: chlorinated aluminas, acid zeolites and silica aluminas.
Reaction schemes for bifunctional hydrocarbon transformations involve multiple successive steps of catalysis at hydrodehydrogenating and protonic sites, and transport of reactant molecules, products and reaction intermediates. Despite this complexity, these transformations occur very rapidly and in an apparent single step, with the thermodynamically disadvantaged unsaturated intermediates appearing only in trace form in the final products. In addition, process optimization (catalyst and operating conditions) makes it possible to direct selectivity towards the desired products, while limiting catalyst deactivation.
These assets can be, and already are, partially valorized in the upgrading of light alkanes C 1 -C 4 and in the organic synthesis of high value-added products (Fine Chemicals). This article [J1 218] reviews the advances made in these fields, the choice to deal with them in a specific article being linked to the significant limitations imposed in the development of industrial processes by the peculiarities of most of the desired transformations.
– The first, which applies equally to the upgrading of light alkanes and to Fine Chemicals, is that the bond-cutting reactions that predominate in oil refining and petrochemical processes are naturally supplanted by condensation reactions.
– The second, specific to Fine Chemicals, is the very high reactivity of reagent molecules, intermediates and products (whether desired or not) conferred by the functional groups they contain.
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KEYWORDS
reaction mechanisms | catalyc active sites | light alkane conversion | fine chemicals synthesis
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Unit operations. Chemical reaction engineering
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Bifunctional catalysis
Bibliography
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ACS Catalysis, American Chemical Society
Advanced Synthesis and Catalysis, Wiley-VCH
Applied Catalysis-A: General; B: Environmental, Elsevier
Catalysis Communications, Elsevier
Catalysis Letters, Springer
Catalysis Science and Technology, Royal Society of Chemistry
Catalysis...
Patents
BELLUSSI (G.), GIUSTI (A.) and ZANIBELLI (L.). – Dehydroisomerisation catalyst and its use in the preparation of isobutene from N-butane. US Patent 5336830 assigned to Eniricerche SPA and Snamprogetti (1994).
FRITCH (J.R.), ASLAM (M.), RIOS (D.E.) and SMITH (J.C.). – Use of 4-substituted 2-butanones to prepare nabumetone. Patent WO 9640608 (1996).
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