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Two-dimensional analytical investigation of coupled heat and mass transfer and entropy generation in a porous, catalytic microreactor

Two-dimensional analytical investigation of coupled heat and mass transfer and entropy generation in a porous, catalytic microreactor
Two-dimensional analytical investigation of coupled heat and mass transfer and entropy generation in a porous, catalytic microreactor
Influences of the solid body of microreactors (or the microstructure) upon the transfer processes and hence on the performance of microreactors have been recently emphasised. Nonetheless, the subtle connections between microstructure design and micro-transport phenomena are still largely unknown. To resolve this, the current paper presents an analytical study of the advective-diffusive transport phenomena in a microreactor filled with porous media and with catalytic surfaces. The system under investigation includes the fluid and porous solid phases inside a microchannel with thick walls and subject to uneven thermal loads. The thermal diffusion of mass, viscous dissipation of the flow momentum and local thermal non-equilibrium in the porous medium are considered. The axial variations of heat and mass transfer processes are also taken into account and two-dimensional solutions of the temperature and concentration fields are provided. The local and total entropy generation within the system are further calculated. The results clearly demonstrate the major influences of thick walls on the thermal behaviour and subsequently on the mass transfer and entropy generation of the microreactor. In particular, the Nusselt number is shown to be strongly dependent upon the configuration of microstructure such that it decreases significantly by thickening the walls. The results also demonstrate that for finite Soret numbers the total irreversibility of the system is dominated by the Soret effect. The analytical results of this work can be further used for the validation of future numerical analyses of microreactors.
0017-9310
372-391
Hunt, G.
c61092e6-cb33-48f4-bfcc-08227d385bad
Karimi, N.
620646d6-27c9-4e1e-948f-f23e4a1e773a
Torabi, M.
cca46013-f51a-4d5d-b8d0-7d54bcff33d0
Hunt, G.
c61092e6-cb33-48f4-bfcc-08227d385bad
Karimi, N.
620646d6-27c9-4e1e-948f-f23e4a1e773a
Torabi, M.
cca46013-f51a-4d5d-b8d0-7d54bcff33d0

Hunt, G., Karimi, N. and Torabi, M. (2018) Two-dimensional analytical investigation of coupled heat and mass transfer and entropy generation in a porous, catalytic microreactor. International Journal of Heat and Mass Transfer, 119, 372-391. (doi:10.1016/j.ijheatmasstransfer.2017.11.118).

Record type: Article

Abstract

Influences of the solid body of microreactors (or the microstructure) upon the transfer processes and hence on the performance of microreactors have been recently emphasised. Nonetheless, the subtle connections between microstructure design and micro-transport phenomena are still largely unknown. To resolve this, the current paper presents an analytical study of the advective-diffusive transport phenomena in a microreactor filled with porous media and with catalytic surfaces. The system under investigation includes the fluid and porous solid phases inside a microchannel with thick walls and subject to uneven thermal loads. The thermal diffusion of mass, viscous dissipation of the flow momentum and local thermal non-equilibrium in the porous medium are considered. The axial variations of heat and mass transfer processes are also taken into account and two-dimensional solutions of the temperature and concentration fields are provided. The local and total entropy generation within the system are further calculated. The results clearly demonstrate the major influences of thick walls on the thermal behaviour and subsequently on the mass transfer and entropy generation of the microreactor. In particular, the Nusselt number is shown to be strongly dependent upon the configuration of microstructure such that it decreases significantly by thickening the walls. The results also demonstrate that for finite Soret numbers the total irreversibility of the system is dominated by the Soret effect. The analytical results of this work can be further used for the validation of future numerical analyses of microreactors.

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Published date: 1 April 2018

Identifiers

Local EPrints ID: 509051
URI: http://eprints.soton.ac.uk/id/eprint/509051
ISSN: 0017-9310
PURE UUID: 9342366c-8e42-4781-98c8-6912965c3fbb
ORCID for N. Karimi: ORCID iD orcid.org/0000-0002-4559-6245

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Date deposited: 10 Feb 2026 17:51
Last modified: 11 Feb 2026 03:18

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Contributors

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

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