Author/Authors :
B.S. Akpa، نويسنده , , C. D’Agostino، نويسنده , , L.F. Gladden، نويسنده , , K. Hindle، نويسنده , , H. Manyar، نويسنده , , J. McGregor، نويسنده , , R. Li، نويسنده , , M. Neurock، نويسنده , , N. Sinha، نويسنده , , E.H. Stitt، نويسنده , , D. Weber، نويسنده , , J.A. Zeitler، نويسنده , , D.W. Rooney، نويسنده ,
Abstract :
In liquid-phase reaction systems, the role of the solvent is often limited to the simple requirement of dissolving and/or diluting substrates. However, the correct choice, either pure or mixed, can significantly influence both reaction rate and selectivity. For multi-phase heterogeneously catalysed reactions observed variations may be due to changes in mass transfer rates, reaction mechanism, reaction kinetics, adsorption properties and combinations thereof. The liquid-phase hydrogenation of 2-butanone to 2-butanol over a Ru/SiO2 catalyst, for example, shows such complex rate behaviour when varying water/isopropyl alcohol (IPA) solvent ratios. In this paper, we outline a strategy which combines measured rate data with physical property measurements and molecular simulation in order to gain a more fundamental understanding of mixed solvent effects for this heterogeneously catalysed reaction. By combining these techniques, the observed complex behaviour of rate against water fraction is shown to be a combination of both mass transfer and chemical effects.
Keywords :
NH3-SCR , Copper , SAPO-34 , Cu species , Active Sites