Understanding transport phenomena in microreactors remains challenging owing to the peculiar transfer
features of microstructure devices and their interactions with chemistry. This paper, therefore,
theoretically investigates heat and mass transfer in microreactors consisting of porous microchannels
with thick walls, typical of real microreactors. To analyse the porous section of the microchannel the local
thermal non-equilibrium model of thermal transport in porous media is employed. A first order, catalytic
chemical reaction is implemented on the internal walls of the microchannel to establish the mass transfer
boundary conditions. The effects of thermal radiation and nanofluid flow within the microreactor are
then included within the governing equations. Further, the species concentration fields are coupled with
that of the nanofluid temperature through considering the Soret effect. A semi-analytical methodology is
used to tackle the resultant mathematical model with two different thermal boundary conditions.
Temperature and species concentration fields as well as Nusselt number for the hot wall are reported
versus various parameters such as porosity, radiation parameter and volumetric concentration of
nanoparticles. The results show that radiative heat transfer imparts noticeable effects upon the
temperature fields and consequently Nusselt number of the system. Importantly, it is observed that the
radiation effects can lead to the development of a bifurcation in the nanofluid and porous solid phases
and significantly influence the concentration field. This highlights the importance of including thermal
radiation in thermo-chemical simulations of microreactors.
History
School
Mechanical, Electrical and Manufacturing Engineering
This is a post-peer-review, pre-copyedit version of an article published in Journal of Thermal Analysis and Calorimetry. The final authenticated version is available online at: https://doi.org/10.1007/s10973-018-7027-z