A CFD-DEM study of hydrodynamics with heat transfer in a gas-solid fluidized bed reactor for solar thermal applications

被引:55
作者
Bellan, Selvan [1 ,3 ]
Matsubara, Koji [2 ,3 ]
Cho, Hyun Seok [1 ,3 ]
Gokon, Nobuyuki [1 ,3 ]
Kodama, Tatsuya [2 ,3 ]
机构
[1] Niigata Univ, Ctr Transdisciplinary Res, 8050 Ikarashi 2 Nocho, Niigata 9502181, Japan
[2] Niigata Univ, Fac Engn, 8050 Ikarashi 2 Nocho, Niigata 9502181, Japan
[3] Niigata Univ, Pacific Rim Solar Fuels Res Ctr, 8050 Ikarashi 2 Nocho, Niigata 9592181, Japan
关键词
Solar receiver; CFD-DEM modeling; Fluidized bed; Particle-fluid flow; Beam-down solar concentrating system; DOWN REFLECTOR SYSTEM; IMMERSED TUBE; COAL COKES; FLOW; SIMULATION; RECEIVER; MODEL; GASIFICATION; BEHAVIORS; PARTICLES;
D O I
10.1016/j.ijheatmasstransfer.2017.09.015
中图分类号
O414.1 [热力学];
学科分类号
摘要
The particles flow and heat transfer characteristics of a high temperature solar thermochemical fluidized bed reactor have been studied for solar beam-down concentrating systems. A numerical model has been developed by the combined approach of computational fluid dynamics (CFD) and discrete element method (DEM) collisional model since it is an effective approach for studying the gas-solid flow. The discrete ordinate model has been used to solve the radiation heat transfer. An experimental visualization of particles circulation pattern and mixing of two-tower fluidized bed system has been presented. A good agreement has been found between the experimental measurements and numerical predictions. The effect of gas superficial velocity, bed mass and inlet gas temperature on the flow pattern and temperature characteristics of the bed have been investigated. The results showed that the maximum and average temperature of the bed, depends on the top layer position and focal point of the concentrated radiation, decreased when increasing the total mass of the bed. (C) 2017 Elsevier Ltd. All rights reserved.
引用
收藏
页码:377 / 392
页数:16
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