Simultaneous Measurement of In-Situ Bubble Size and Reaction Rates with Heterogeneous Catalytic Hydrogenation Reaction

Binjie Hu, Robert Fishwick, Alvin Nienow, Andrzej Pacek, John Winterbottom, Joseph Wood, EH Stitt

Research output: Contribution to journalArticle

18 Citations (Scopus)

Abstract

The effect of solvent composition (water, 2-propanol and mixtures of the two) on the three phase, heterogeneously catalysed, two-step hydrogenation of 2-butyne-1,4-diol on Pd/alumina was investigated in a stirred reactor and for the first time, bubble sizes were measured in situ simultaneously with reaction rates. The first step forming the alkene is slow and gas-liquid mass transfer limitation is unlikely whilst the second step to alkane is much faster and may be mass transfer dominated. Overall, reaction rates displayed a complex relationship with solvent composition. The smallest bubbles where observed with 5%v/v 2-propanol in water and under gas-liquid mass transfer limited conditions (energy dissipation rates <4 W/kg), the overall reaction closely follows the ratio of mean bubble diameter to hydrogen solubility, both of which are a function of solvent. Overall, the solvent 5%v/v 2-propanol/water gave faster reactions combined with pod selectivity compared to the others and is therefore recommended. (c) 2007 Elsevier Ltd. All rights reserved.
Original languageEnglish
Pages (from-to)5392-5396
Number of pages5
JournalChemical Engineering Science
Volume62
Issue number18-20
DOIs
Publication statusPublished - 1 Sept 2007

Keywords

  • multiphase reactions
  • catalysis
  • reaction engineering
  • stirred tank reactor
  • mass transfer

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