Intensification of ultra-lean catalytic combustion of methane in microreactors by boundary layer interruptions- A computational study
Intensification of ultra-lean catalytic combustion of methane in microreactors by boundary layer interruptions- A computational study
Oxidation of an ultra-lean mixture of methane and air over a platinum catalyst at the constant temperature of 1000 K is investigated numerically in several microreactor configurations featuring different hydrodynamics. These include a straight microchannel with the catalyst coated on the walls and a few wavy microchannels with continuous and discretised catalytic coating. The surface generated CO2 is selected as the indicator of catalytic activity and is evaluated along the catalytic surfaces and the outlet of reactor. It is shown that separation and reattachment of the boundary layer significantly alters the catalytic activity by modifying the structure of concentration boundary layer. Comparison of a strategically coated wavy microchannel with a straight microchannel, with accounting for the residence time, yields an increase of up to 400% in the production rate of CO2. It is argued that the observed hydrodynamic effects upon catalytic activities could help designing highly improved catalytic microreactors.
Hunt, Graeme
261ea6ee-17c1-4f50-8596-fbed762d6fac
Karimi, Nader
620646d6-27c9-4e1e-948f-f23e4a1e773a
Mehdiadeh, Amirfarhang
61aa31bd-9367-437c-995e-a889d8746513
12 October 2021
Hunt, Graeme
261ea6ee-17c1-4f50-8596-fbed762d6fac
Karimi, Nader
620646d6-27c9-4e1e-948f-f23e4a1e773a
Mehdiadeh, Amirfarhang
61aa31bd-9367-437c-995e-a889d8746513
Hunt, Graeme, Karimi, Nader and Mehdiadeh, Amirfarhang
(2021)
Intensification of ultra-lean catalytic combustion of methane in microreactors by boundary layer interruptions- A computational study.
Chemical Engineering Science, 242, [116730].
(doi:10.1016/j.ces.2021.116730).
Abstract
Oxidation of an ultra-lean mixture of methane and air over a platinum catalyst at the constant temperature of 1000 K is investigated numerically in several microreactor configurations featuring different hydrodynamics. These include a straight microchannel with the catalyst coated on the walls and a few wavy microchannels with continuous and discretised catalytic coating. The surface generated CO2 is selected as the indicator of catalytic activity and is evaluated along the catalytic surfaces and the outlet of reactor. It is shown that separation and reattachment of the boundary layer significantly alters the catalytic activity by modifying the structure of concentration boundary layer. Comparison of a strategically coated wavy microchannel with a straight microchannel, with accounting for the residence time, yields an increase of up to 400% in the production rate of CO2. It is argued that the observed hydrodynamic effects upon catalytic activities could help designing highly improved catalytic microreactors.
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Published date: 12 October 2021
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Local EPrints ID: 509128
URI: http://eprints.soton.ac.uk/id/eprint/509128
ISSN: 0009-2509
PURE UUID: 71c75b65-1b7a-4eae-bbb2-54ea560efb82
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Date deposited: 11 Feb 2026 17:52
Last modified: 12 Feb 2026 03:31
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Author:
Graeme Hunt
Author:
Nader Karimi
Author:
Amirfarhang Mehdiadeh
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