Experimental investigation of flow and exergy transfer characteristics in the air-cooled randomly packed particle bed based on second law analysis

被引:6
作者
Zhang, Sheng [1 ]
Zhao, Liang [1 ]
Zhang, Menghui [1 ]
Feng, Junsheng [2 ]
Dong, Hui [1 ]
机构
[1] Northeastern Univ, SEP Key Lab Ecoind, Shenyang 110819, Liaoning, Peoples R China
[2] Anhui Jianzhu Univ, Sch Environm & Energy Engn, Hefei 230601, Peoples R China
基金
中国国家自然科学基金;
关键词
Forced convection heat transfer; Exergy analysis; Randomly packed bed; Experimental approach; Internal heat generation; CONVECTIVE HEAT-TRANSFER; PRESSURE-DROP; TRANSFER COEFFICIENT; THERMAL-ANALYSIS; ENERGY-STORAGE; DRYING PROCESS; FLUID-FLOW; PERFORMANCE; RECOVERY; SYSTEM;
D O I
10.1016/j.ijheatmasstransfer.2021.122360
中图分类号
O414.1 [热力学];
学科分类号
摘要
Randomly packed particle beds (RPPB) are widely used in industry, and their internal flow and heat trans-fer characteristics have a significant impact on the energy efficiency of the overall system. Based on the second law of thermodynamics theory, the correlation equation to predict the exergy transfer coefficient (ETC), exergy transfer Nusselt number (Nu(ex)) within the RPPB is developed, which can reflect temperature and pressure exergy transfer. It effectively reveals the relationship between the role of heat transfer and pressure loss. The experiments are then carried out using stainless-steel particles packed bed with an electric induction heating system to provide a uniform internal heat source. The ambient air is used as the test fluid to cool the heated particles. The pressure drops and forced convection heat transfer char-acteristics of air-cooled high-temperature particles are investigated. The experiments are performed for flows with modified Reynolds number Redh in the range of 811-6810. The effects of cooling air inlet veloc-ity (u(a,in)) and electromagnetic induction heating power (Q(e)) on the experimental results are investigated under different particle sizes (d(p) = 6 and 8 mm). The results show that when d(p) and Q(e) are constant, the overall Nu(ex) decreases exponentially with increasing Redh, and even becomes negative. It means that the heat gain of the air through the RPPB is lower than the pressure loss. The critical Re-dh are 2650 and 5300 when d(p) = 6 and 8 mm, respectively. At fixed d(p) and u(a,i)n, Nu(ex),T decrease linearly with the in-crease of Re-dh. In the case of low Q(e), the exergy transfer between the particles and air is mainly based on pressure exergy transfer. As the Q(e) increases, the temperature exergy transfer gradually increases and dominates, and Nuex shifts from negative to positive. This study delves deeper into the forced convective heat transfer process in RPPB, comprehensively considering the effects of heat transfer and pressure loss. (c) 2021 Elsevier Ltd. All rights reserved.
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页数:17
相关论文
共 54 条
[1]   Exergy transfer analysis of an aluminum holding furnace [J].
Acevedo, Luis ;
Uson, Sergio ;
Uche, Javier .
ENERGY CONVERSION AND MANAGEMENT, 2015, 89 :484-496
[2]  
Al-Mubaddel F.S., 2021, CASE STUD THERM ENG, V26, P1
[3]   Experimental results and modeling of energy storage and recovery in a packed bed of alumina particles [J].
Anderson, Ryan ;
Shiri, Samira ;
Bindra, Hitesh ;
Morris, Jeffrey F. .
APPLIED ENERGY, 2014, 119 :521-529
[4]   Adiabatic Compressed Air Energy Storage with packed bed thermal energy storage [J].
Barbour, Edward ;
Mignard, Dimitri ;
Ding, Yulong ;
Li, Yongliang .
APPLIED ENERGY, 2015, 155 :804-815
[5]   INFLUENCE OF BED SIZE ON FLOW CHARACTERISTICS AND POROSITY OF RANDOMLY PACKED-BEDS OF SPHERES [J].
BEAVERS, GS ;
SPARROW, EM ;
RODENZ, DE .
JOURNAL OF APPLIED MECHANICS-TRANSACTIONS OF THE ASME, 1973, 40 (03) :655-660
[6]   Thermal analysis and exergy evaluation of packed bed thermal storage systems [J].
Bindra, Hitesh ;
Bueno, Pablo ;
Morris, Jeffrey F. ;
Shinnar, Reuel .
APPLIED THERMAL ENGINEERING, 2013, 52 (02) :255-263
[7]   Fluid flow through granular beds [J].
Carman, PC .
CHEMICAL ENGINEERING RESEARCH & DESIGN, 1997, 75 :S32-S48
[8]   Analysis of heat and mass transfer enhancement in porous material subjected to electric fields (effects of particle sizes and layered arrangement) [J].
Chaktranond, Chainarong ;
Rattanadecho, Phadungsak .
EXPERIMENTAL THERMAL AND FLUID SCIENCE, 2010, 34 (08) :1049-1056
[9]   Heat transfer and pressure drop in empty, baffled, and packed tubes I - Heat transfer in packed Tubes [J].
Colburn, AP .
INDUSTRIAL AND ENGINEERING CHEMISTRY, 1931, 23 :910-913
[10]   Enhancement of convection heat-transfer in a rectangular duct [J].
Demirel, Y ;
Al-Ali, HH ;
Abu-Al-Saud, BA .
APPLIED ENERGY, 1999, 64 (1-4) :441-451