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Forced Convective Heat Transfer in a Porous Plate Channel 被引量:1
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作者 Peixue Jiang Zhan Wang +1 位作者 zepei ren Buxuan Wang (Department of Thermal Engineering, Tsinghua University, Beijing 100084, China) 《Journal of Thermal Science》 SCIE EI CAS CSCD 1997年第3期197-206,共10页
Forced convective heat transfer in a plate channel filled with metallic spherical particles was investigated experimentally and numerically. The test section, 58 mm×80mm×5mm in size, was heated by a 0.4 mm t... Forced convective heat transfer in a plate channel filled with metallic spherical particles was investigated experimentally and numerically. The test section, 58 mm×80mm×5mm in size, was heated by a 0.4 mm thick plate electrical heater. The coolant water now rate ranged from 0.015 to 0.833 kg/s.The local wall temperature distribution was measured along with the inlet and outlet fluid temperatures and pressures. The results illustrate the heat transfer augmentation and increased pressure drop caused by the porous medium. The heat transfer coefficient was increased 5-12 times by the porous media although the hydraulic resistance was increased even more. The Nusselt number and the heat transfer coefficient increased with decreasing particIe diameter, while the pressure drop decreased as the particle diameter increased. It was found that, for the conditions studied (metallic packed bed),the effect of thermal dispersion did not need to be considered in the physical model, as opposed to a non-metallic packed bed, where thermal dispersion is important. 展开更多
关键词 convective heat transfer porous media plate channel heat transfer enhancement pressure drop
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