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Catalyst testing in multiphase micro-packed-bed reactors; criterion for radial mass transport

Paper ID Volume ID Publish Year Pages File Format Full-Text
53495 46972 2016 6 PDF Available
Title
Catalyst testing in multiphase micro-packed-bed reactors; criterion for radial mass transport
Abstract

•For multiphase flow in micro-packed-beds, particle sizes 50–200 μm, capillary forces dominate.•In such systems, thick liquid layers are present, causing relatively slow radial mass transport.•We derived a criterion to probe radial dispersion limitations that can corrupt reaction rate data.•We observed radial dispersion limitations in cases where this is no issue in large trickle beds.•Even for HDS of dibenzothiophene, a slow reaction, radial dispersion limitations surfaced.

In catalyst activity testing, micro-packed-bed reactors are the most commonly used devices. However, the small particle sizes (typically 0.05–0.2 mm) inherent with these microreactors in multiphase systems do exhibit special hydrodynamics characteristics, that are not generally recognized.Cold three-phase model investigations show that in micro-packed-bed reactors segregated flows of gas and liquid occur in a broad range of conditions. This situation is dramatically different from the hydrodynamics in industrial-scale trickle-bed reactors. Since in a broad range of conditions the gas flow follows preferential pathways through the micro-packed bed, the average thickness of the liquid layers is relatively large. Because the transport through these layers occurs mainly by molecular diffusion, the observed reaction rate potentially will be limited, resulting in poor radial dispersion. Even for a rather slow reaction as the hydrodesulfurization of dibenzothiophene (HDS), radial mass-transfer limitations were observed. This counterintuitive result is due to the combination of (i) the presence of apparent stagnant liquid layers with several particle diameters thickness, (ii) the low rate of radial transport, and (iii) the strong inhibition by the reaction product H2S. A general criterion, analogous to the Weisz–Prater criterion for internal diffusion limitations, is proposed for the estimation of the influence of poor radial dispersion in catalyst performance testing in micro-packed-bed reactors. For use in practice, it is advised to start with a worst-case scenario and dependent on the outcome to relax this strict criterion.

Graphical abstractRadial transport limitations negligible in multiphase reactors? Criterion.Figure optionsDownload full-size imageDownload high-quality image (97 K)Download as PowerPoint slide

Keywords
HDS; Reaction kinetics; Radial dispersion; Micro-packed bed reactor
First Page Preview
Catalyst testing in multiphase micro-packed-bed reactors; criterion for radial mass transport
Publisher
Database: Elsevier - ScienceDirect
Journal: Catalysis Today - Volume 259, Part 2, 1 January 2016, Pages 354–359
Authors
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Subjects
Physical Sciences and Engineering Chemical Engineering Catalysis