The preparation of highly ordered single layer ZSM-5 coating on prefabricated stainless steel microchannels

• Published in: Applied catalysis. A, General General, 2001-01, Vol.206 (1), p.125-143
• Main Authors: Rebrov, E.V., Seijger, G.B.F., Calis, H.P.A., de Croon, M.H.J.M., van den Bleek, C.M., Schouten, J.C.
• Format: Article
• Language: English
• Subjects: Catalysis; Catalysts: preparations and properties; Chemistry; DeNO x; Exact sciences and technology; General and physical chemistry; Ion-exchange; Microreactor; Preparation; Surface physical chemistry; Theory of reactions, general kinetics. Catalysis. Nomenclature, chemical documentation, computer chemistry; XRD; Zeolite; Zeolites: preparations and properties; ZSM-5
• ISSN: 0926-860X; 1873-3875
• DOI: 10.1016/S0926-860X(00)00594-9

An elegant way to prepare catalytically active microreactors is by applying a coating of zeolite crystals onto a metal microchannel structure. In this study the hydrothermal formation of ZSM-5 zeolitic coatings on AISI 316 stainless steel plates with a microchannel structure has been investigated at different synthesis mixture compositions. The procedures of coating and thermal treatment have also been optimized. Obtaining a uniform thickness of the coating within 0.5 mm wide microchannels requires a careful control of various synthesis variables. The role of these factors and the problems in the synthesis of these zeolitic coatings are discussed. In general, the synthesis is most sensitive to the H 2O/Si ratio as well as to the orientation of the plates with respect to the gravity vector. Ratios of H 2O/Si=130 and Si/template=13 were found to be optimal for the formation of a zeolitic film with a thickness of one crystal at a temperature of 130°C and a synthesis time of about 35 h. At such conditions, ZSM-5 crystals were formed with a typical size of 1.5 μm×1.5 μm×1.0 μm and a very narrow (within 0.2 μm) crystal size distribution. The prepared samples proved to be active in the selective catalytic reduction (SCR) of NO with ammonia. The activity tests have been carried out in a plate-type microreactor. The microreactor shows no mass transfer limitations and a larger SCR reaction rate is observed in comparison with pelletized Ce-ZSM-5 catalysts.