Please use this identifier to cite or link to this item: https://hdl.handle.net/20.500.14279/23792
Title: Continuous heterogeneously catalyzed oxidation of benzyl alcohol using a tube-in-tube membrane microreactor
Authors: Wu, Gaowei 
Constantinou, Achilleas 
Cao, Enhong 
Kuhn, Simon 
Morad, Moataz 
Sankar, Meenakshisundaram 
Bethell, Donald 
Hutchings, Graham J. 
Gavriilidis, Asterios 
Major Field of Science: Natural Sciences
Field Category: Chemical Sciences
Keywords: Alcohols;Catalysts;Oxygen;Microreactors;Pharmaceuticals
Issue Date: 29-Apr-2015
Source: Industrial & Engineering Chemistry, 2015, vol. 54, no. 16, pp. 4183–4189
Volume: 54
Issue: 16
Start page: 4183
End page: 4189
Journal: Industrial & Engineering Chemistry 
Abstract: A Teflon AF-2400 tube-in-tube microreactor is investigated for the continuous, solvent-free, catalytic oxidation of benzyl alcohol with oxygen. The semipermeable Teflon AF-2400 tube acts as the interface between the gaseous oxidant and the liquid substrate. Because of the inherent safety of this contacting method, the use of pure oxygen is possible. The semipermeable tube was packed with 1 wt % Au–Pd/TiO2 catalyst particles and placed inside a PTFE tube to provide an annular region which was pressurized with pure oxygen. This design allowed continuous penetration of oxygen through the inner tube during the reaction, resulting in higher oxygen concentration in the catalyst bed and significantly improved conversion compared to a reactor operating with an oxygen presaturated feed. The amount of oxygen available for reaction in the tube-in-tube microreactor was 2 orders of magnitude higher than that in a nonpermeable reactor with oxygen presaturated feed. The semipermeable tube reactor performance in terms of both conversion and selectivity was enhanced by increasing the gas pressure, the catalyst contact time and by dilution of the catalyst. The highest conversion of benzyl alcohol obtained for the range of conditions investigated was 44.1%, with 73.0% selectivity to benzaldehyde, at 120 °C; catalyst contact time, 115 gcat·s/galcohol; and catalyst dilution factor, 4.
URI: https://hdl.handle.net/20.500.14279/23792
ISSN: 15205045
DOI: 10.1021/ie5041176
Rights: © American Chemical Society
Type: Article
Affiliation : University College London 
KU Leuven 
Cardiff University 
University of Liverpool 
Appears in Collections:Άρθρα/Articles

CORE Recommender
Show full item record

SCOPUSTM   
Citations

44
checked on Mar 14, 2024

WEB OF SCIENCETM
Citations

42
Last Week
0
Last month
0
checked on Oct 29, 2023

Page view(s)

217
Last Week
1
Last month
12
checked on Jun 18, 2024

Google ScholarTM

Check

Altmetric


Items in KTISIS are protected by copyright, with all rights reserved, unless otherwise indicated.