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Catalysis of Organic..

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Ardizzi et al. 7710. The Control <strong>of</strong> Regio- and Chemo-Selectivity in the Gas-phase, Acid-CatalyzedMethylation <strong>of</strong> 1,2-Diphenol (Catechol)Mattia Ardizzi, Nicola Ballarini, Fabrizio Cavani, Luca Dal Pozzo,Luca Maselli, Tiziana Monti and Sara RovinettiUniversity <strong>of</strong> Bologna, Dipartimento di Chimica Industriale e dei Materiali, VialeRisorgimento 4, 40136 Bologna, Italy. INSTM, Research Unit <strong>of</strong> Bologna. A member<strong>of</strong> Concorde CA and <strong>of</strong> Idecat NoE (6FP <strong>of</strong> the EU).Abstractfabrizio.cavani@unibo.itThe catalytic properties <strong>of</strong> materials having either (i) Brønsted-type acidity (Hmordeniteand Al phosphate), or (ii) Lewis-type acidity (Al trifluoride), wereinvestigated in the reaction <strong>of</strong> gas-phase catechol methylation with methanol. H-mordenite and AlF 3 gave high selectivity to guaiacol (the product <strong>of</strong> O-methylation)only under mild reaction conditions, that is for very low catechol conversion. In fact,the increase <strong>of</strong> temperature led to the transformation <strong>of</strong> guaiacol to phenol andcresols, and to considerable catalyst deactivation. The use <strong>of</strong> a mildly acidic catalyst,AlPO 4 , instead made it possible to obtain a stable catalytic performance, with highselectivity to guaiacol at 42% catechol conversion.IntroductionPhenol and diphenols (catechol, resorcinol and hydroquinone, the ortho, meta andpara isomers, respectively), are versatile starting material for the synthesis <strong>of</strong> manycompounds. However, most <strong>of</strong> the corresponding industrial transformations still havedrawbacks that make the processes environmentally unfriendly, such as:(1) The use <strong>of</strong> alkylhalides, or dimethylsulphate or acylhalides as co-reactants, withco-production <strong>of</strong> waste effluents containing inorganic salts, which have to bedisposed.(2) The high number <strong>of</strong> synthetic steps that sometimes are necessary, withconsequent low overall yield, due to the by-products formed in each step.(3) The use <strong>of</strong> stoichiometric conditions instead than catalytic, or <strong>of</strong> such largeamounts <strong>of</strong> catalyst, <strong>of</strong>ten not recoverable, that the process can be regarded as astoichiometric one. Moreover, the use <strong>of</strong> homogeneous catalysts <strong>of</strong>ten impliesthe development <strong>of</strong> corrosive reaction media, and problems in the purification <strong>of</strong>the product.(4) The use <strong>of</strong> solvents that may have themselves unfriendly characteristics.Therefore, the development <strong>of</strong> new processes having lower environmentalimpact represents one important target (1,2). In the present work we report about

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