TY - JOUR
T1 - Enhanced heat transfer in sandwich heat transfer unit with metal foam
T2 - A numerical investigation
AU - Duan, Xiuhui
AU - Pei, Jinchen
AU - Chen, Xueqing
AU - Wang, Yichun
AU - Ding, Chen
N1 - Publisher Copyright:
© 2024 Elsevier Ltd
PY - 2024/11/1
Y1 - 2024/11/1
N2 - In this study, a novel configuration of a sandwich heat transfer unit (SHTU) is proposed, characterized by the partial filling of metal foam on both sides of the fin. The thermal–hydraulic characteristics of the SHTU are investigated numerically using the local non-equilibrium method and Forchheimer-Brinkman extended Darcy model, and compared with those of traditional flat plate-fin heat transfer unit (PHTU). The effect of geometrical parameters, mass distribution of fin and metal foam, and morphological parameters of metal foam on the characteristic of SHTU was explored. Compared to PHTU the Nusselt number of SHTU increases by 13.1% and 27.6%, while the friction factor increases by 6.2% and 33.1% at Reynolds numbers of 100 and 900, respectively. At a Reynolds number of 500, as the filling ratio increases from 0 to 0.95, the Nusselt number, friction factor, and comprehensive thermal performance enhancement increase by factors of 10, 20, and 3, respectively. When the foam fraction increases from 0.30 to 0.90, the thermal performance enhancement improves by 4–5 times within the investigated range. The impact of porosity (ε) and pore density (ω) on the performance of SHTU is not monotonic. The optimal ω was observed to be in the range of 15–20 PPI, while the optimal ε was found between 0.90–0.92.
AB - In this study, a novel configuration of a sandwich heat transfer unit (SHTU) is proposed, characterized by the partial filling of metal foam on both sides of the fin. The thermal–hydraulic characteristics of the SHTU are investigated numerically using the local non-equilibrium method and Forchheimer-Brinkman extended Darcy model, and compared with those of traditional flat plate-fin heat transfer unit (PHTU). The effect of geometrical parameters, mass distribution of fin and metal foam, and morphological parameters of metal foam on the characteristic of SHTU was explored. Compared to PHTU the Nusselt number of SHTU increases by 13.1% and 27.6%, while the friction factor increases by 6.2% and 33.1% at Reynolds numbers of 100 and 900, respectively. At a Reynolds number of 500, as the filling ratio increases from 0 to 0.95, the Nusselt number, friction factor, and comprehensive thermal performance enhancement increase by factors of 10, 20, and 3, respectively. When the foam fraction increases from 0.30 to 0.90, the thermal performance enhancement improves by 4–5 times within the investigated range. The impact of porosity (ε) and pore density (ω) on the performance of SHTU is not monotonic. The optimal ω was observed to be in the range of 15–20 PPI, while the optimal ε was found between 0.90–0.92.
KW - Local thermal non-equilibrium
KW - Partial filled channel
KW - Plate-fin heat sink
KW - Sandwich heat transfer unit
KW - Thermal hydraulic performance
UR - http://www.scopus.com/inward/record.url?scp=85201082643&partnerID=8YFLogxK
U2 - 10.1016/j.applthermaleng.2024.124144
DO - 10.1016/j.applthermaleng.2024.124144
M3 - Article
AN - SCOPUS:85201082643
SN - 1359-4311
VL - 256
JO - Applied Thermal Engineering
JF - Applied Thermal Engineering
M1 - 124144
ER -