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The effects of exothermic catalytic reactions upon combined transport of heat and mass in porous microreactors

The effects of exothermic catalytic reactions upon combined transport of heat and mass in porous microreactors
The effects of exothermic catalytic reactions upon combined transport of heat and mass in porous microreactors
Microreactors for chemical synthesis and combustion have already attracted significant attention. Exothermic catalytic activity features heavily in these devices and thus advective-diffusive transport is of key importance in their analyses. Yet, thermal modelling of the heat generated by catalytic reactions on the internal surfaces of porous microreactors has remained as an important unresolved issue. To address this, the diffusion of heat of catalytic reactions into three phases including fluid, porous solid and solid walls is investigated by extending an existing interface model of porous media under local thermal non-equilibrium. This is applied to a microchannel fully filled with a porous material, subject to a heat flux generated by a catalytic layer coated on the porous-wall boundary. The finite wall thickness and viscous dissipation of the flow kinetic energy are considered, and a two-dimensional analytical model is developed, examining the combined heat and mass transfer and thermodynamic irreversibilities of the system. The analytical solution is validated against the existing theoretical studies on simpler configurations as well as a computational model of the microreactor in the limit of very large porosity. In keeping with the recent findings, the wall thickness is shown to strongly influence the heat and mass transport within the system. This remains unchanged when the symmetricity of the microchannel is broken through placing walls of unequal thicknesses, while deviation from local thermal equilibrium is significantly intensified in this case. Importantly, the Nusselt number is shown to have a singular point, which remains fixed under various conditions.
0017-9310
1227-1249
Hunt, G.
c61092e6-cb33-48f4-bfcc-08227d385bad
Karimi, N.
620646d6-27c9-4e1e-948f-f23e4a1e773a
Yadollahi, B.
edeae402-db71-454e-98ed-1a94e46fd72a
Torabi, M.
cca46013-f51a-4d5d-b8d0-7d54bcff33d0
Hunt, G.
c61092e6-cb33-48f4-bfcc-08227d385bad
Karimi, N.
620646d6-27c9-4e1e-948f-f23e4a1e773a
Yadollahi, B.
edeae402-db71-454e-98ed-1a94e46fd72a
Torabi, M.
cca46013-f51a-4d5d-b8d0-7d54bcff33d0

Hunt, G., Karimi, N., Yadollahi, B. and Torabi, M. (2019) The effects of exothermic catalytic reactions upon combined transport of heat and mass in porous microreactors. International Journal of Heat and Mass Transfer, 134, 1227-1249. (doi:10.1016/j.ijheatmasstransfer.2019.02.015).

Record type: Article

Abstract

Microreactors for chemical synthesis and combustion have already attracted significant attention. Exothermic catalytic activity features heavily in these devices and thus advective-diffusive transport is of key importance in their analyses. Yet, thermal modelling of the heat generated by catalytic reactions on the internal surfaces of porous microreactors has remained as an important unresolved issue. To address this, the diffusion of heat of catalytic reactions into three phases including fluid, porous solid and solid walls is investigated by extending an existing interface model of porous media under local thermal non-equilibrium. This is applied to a microchannel fully filled with a porous material, subject to a heat flux generated by a catalytic layer coated on the porous-wall boundary. The finite wall thickness and viscous dissipation of the flow kinetic energy are considered, and a two-dimensional analytical model is developed, examining the combined heat and mass transfer and thermodynamic irreversibilities of the system. The analytical solution is validated against the existing theoretical studies on simpler configurations as well as a computational model of the microreactor in the limit of very large porosity. In keeping with the recent findings, the wall thickness is shown to strongly influence the heat and mass transport within the system. This remains unchanged when the symmetricity of the microchannel is broken through placing walls of unequal thicknesses, while deviation from local thermal equilibrium is significantly intensified in this case. Importantly, the Nusselt number is shown to have a singular point, which remains fixed under various conditions.

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Published date: 1 May 2019

Identifiers

Local EPrints ID: 509072
URI: http://eprints.soton.ac.uk/id/eprint/509072
ISSN: 0017-9310
PURE UUID: d009e24a-a60c-4d9c-9dbd-1821c0fd7c68
ORCID for N. Karimi: ORCID iD orcid.org/0000-0002-4559-6245

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Date deposited: 10 Feb 2026 18:10
Last modified: 11 Feb 2026 03:18

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Contributors

Author: G. Hunt
Author: N. Karimi ORCID iD
Author: B. Yadollahi
Author: M. Torabi

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