Reynders, FritzNicol, Willie2012-02-162012-08-312011Reynders, F & Nicol, W 2011, 'Gas-limited hydrogenation of 1-Octene in a fixed bed : upflow versus downflow', Industrial and Engineering Chemistry Research, vol. 50, no. 18, pp.10476-10479.0888-5885 (print)1520-5045 (online)10.1021/ie200738chttp://hdl.handle.net/2263/18132Two downflow operational modes with different hydrodynamic states were compared to upflow operation. Various gas limited conditions (γ = 15 - 60) were employed. The downflow mode with the higher wetting efficiency consistently outperformed the downflow mode with the lower wetting efficiency. Both the downflow modes outperformed the upflow mode at high gas mass fluxes and underachieved against upflow at lower gas mass fluxes. The results stand in contradiction to the theory on direct gas-solid mass transfer under trickle flow conditions. The switching behavior of the upflow mode performance was attributed to hydrodynamic regime shifts, hinting that the perceived ‘poor’ performance of upflow reactors under gas limited conditions might be linked to slugging in laboratory scale reactors.en© 2011 American Chemical Society. This document is the Accepted Manuscript version of a Published Work that appeared in final form in Industrial and Engineering Chemistry Research, copyright © American Chemical Society after peer review and technical editing by the publisher. To access the final edited and published work see http://pubs.acs.org/journals/iecred/index.html. This article is embargoed by the publisher until August 2012.CatalysisHydrodynamicsMass transferMultiphase reactorsPacked bedPostprint Article