Optimizing of a metal foam-assisted solar air heater performance: a thermo-hydraulic analysis of porous insert placement
A numerical assessment of the heat transfer efficacy of a solar air heater (SAH) was carried out. The SAH is supplied with a porous metal foam layer to improve thermal mixing. Both the local thermal non-equilibrium (LTNE) and Darcy-extended Forchheimer (DEF) models were employed to forecast fluid an...
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Veröffentlicht in: | Environmental science and pollution research international 2024-05, Vol.31 (24), p.34995-35017 |
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Sprache: | eng |
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Zusammenfassung: | A numerical assessment of the heat transfer efficacy of a solar air heater (SAH) was carried out. The SAH is supplied with a porous metal foam layer to improve thermal mixing. Both the local thermal non-equilibrium (LTNE) and Darcy-extended Forchheimer (DEF) models were employed to forecast fluid and thermal transport within the partly filled SAH channel. The analysis was performed for various values of dimensionless foam layer lengths (
S
=
0
-
1
), pore densities (
ω
=
10
-
40
PPI
), and Reynolds numbers (
R
e
=
4000
-
1
6
,
000
) at a fixed value of layer thickness (
H
f
=
0.6
). Based on the position of the porous layer, three distinct arrangements, marked as Case 1, Case 2, and Case 3, were explored. Regarding the parameters examined, the findings indicate a definite improvement in the average Nusselt number (
Nu
), but unfortunately, the friction factor also increases unfavorably. By reducing the length of the porous layer, a reasonable reduction in heat transfer rate and a significant decrease in pressure drop were noticed. The results showed about 26.64%, 48.73%, and 70.74% reductions in pressure drop by reducing the dimensionless foam length from 1 to 0.25, 0.5, and 0.75 respectively for
ω
=
10
at
R
e
=
16
,
000
. On the other side, there are only about 11.05%, 23.11%, and 40.78% reductions in
Nu
. The exhaustive analysis of the thermal performance of SAH was conducted using the thermal performance factor (TPF), which considers the trade-off between the SAH channel’s potential for improved heat transmission and its cost for pressure loss. The TPF may reach a maximum of 2.82 compared to the empty channel when the metal foam layer is inserted with
S
=
1
, for
ω
=
10
, and
R
e
=
16
,
000
. |
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ISSN: | 1614-7499 0944-1344 1614-7499 |
DOI: | 10.1007/s11356-024-33593-3 |