Gas-liquid hydrogenation in continuous flow - The effect of mass transfer and residence time in powder packed-bed and catalyst-coated reactors
- 1 January 2020
- journal article
- research article
- Published by Elsevier BV in Chemical Engineering Journal
- Vol. 379, 122292
- https://doi.org/10.1016/j.cej.2019.122292
Abstract
No abstract availableKeywords
Funding Information
- InnovateUK (900041)
This publication has 65 references indexed in Scilit:
- Formation and Characterization of PdZn Alloy: A Very Selective Catalyst for Alkyne SemihydrogenationThe Journal of Physical Chemistry C, 2011
- Transient Behavior and Stability in Miniaturized Multiphase Packed Bed ReactorsIndustrial & Engineering Chemistry Research, 2010
- Kinetics of the solvent-free hydrogenation of 2-methyl-3-butyn-2-ol over a structured Pd-based catalystCatalysis Today, 2009
- Catalyst testing in a multiple-parallel, gas–liquid, powder-packed bed microreactorApplied Catalysis A: General, 2009
- Pd catalysed hexyne hydrogenation modified by Bi and by PbJournal of Catalysis, 2009
- Microreactor Technology: A Revolution for the Fine Chemical and Pharmaceutical Industries?Chemical Engineering & Technology, 2005
- Transport and reaction in microscale segmented gas–liquid flowLab on a Chip, 2004
- Kinetics of liquid-phase hydrogenation reactions over supported metal catalysts — a reviewApplied Catalysis A: General, 2001
- Process Development and Scale Up: III. Scale-up and scale-down of trickle bed processesReviews in Chemical Engineering, 1998
- Selective Hydrogenation of Phenylacetylene on Pumice-Supported Palladium CatalystsJournal of Catalysis, 1995