Experimental study on heat transfer of dense phase flow through a horizontal tube under constant wall flux conditions

被引:0
|
作者
Zhao, Ziwei [1 ,2 ,3 ,4 ]
Yu, Yupu [1 ,2 ,3 ,4 ]
Bai, Fengwu [1 ,2 ,3 ,4 ]
Wang, Zhifeng [1 ,2 ,3 ,4 ]
机构
[1] Chinese Acad Sci, Key Lab Solar Thermal Energy & Photovolta Syst, 6 Beiertiao, Beijing 100190, Peoples R China
[2] Chinese Acad Sci, Inst Elect Engn, 6 Beiertiao, Beijing 100190, Peoples R China
[3] Univ Chinese Acad Sci, 6 Beiertiao, Beijing 100190, Peoples R China
[4] Beijing Engn Res Ctr Solar Thermal Power, 6 Beiertiao, Beijing 100190, Peoples R China
关键词
Horizontal dense phase flow; Heat transfer coefficient; Constant wall heat flux; Multi-layer model; Experimental research; GAS-SOLID FLOW; SLUG FLOW; ELECTROMAGNETIC INDUCTION; TRANSFER COEFFICIENT; SEWAGE-SLUDGE; PLUG-FLOW; BED; PARTICLES; SIMULATION; SUSPENSION;
D O I
10.1016/j.ijthermalsci.2022.107728
中图分类号
O414.1 [热力学];
学科分类号
摘要
A novel application of particles is utilization as dense phase flow for heat capture, transportation and storage. The use of horizontal dense phase flow as heat transfer fluid in solar systems is discussed with respect to current technologies. The investigation aims to analyze the heat transfer behavior of a horizontal dense phase flow under the condition of uniform surface heat flux. The proposed technologies transport particles as semi-continuous plug flow with a bottom layer, particles at the bottom layer will regularly renew once plugs pass by. Tests were conducted in a self-pilot scale-up platform. The measured wall-to-mixture heat transfer coefficient varies from ~303 to 813 W/m2K in the particle mass flux range from 125 to 777 kg/m2s. Three heat transfer equations will be provided with the experimental data. A heat transfer equation describes the wall-to-mixture heat transfer coefficient linearly increases with particle mass flux. Then, a general empirical correlation in a dimensionless form predicted results well with experimental data of the present work and other data reported in the literature. Furthermore, a mechanistic heat transfer model is proposed according to a partial penetration mechanism and multi-layer flow model. The predicted results agree with experimental results within 12% of the average error. Considering the findings in this paper, researchers may have ideas to improve the heat transfer of horizontal dense phase flow to utilize this technology to the parabolic concentrator for the solar thermal industry.
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页数:17
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