Numerical investigation of particle wear and breakage effects on heat transfer mechanisms and conversion efficiency in energy storage fluidized beds

被引:0
作者
Li, Xiang [1 ]
Jiang, Hongchuan [1 ]
Su, Zhaoxing [1 ]
Liang, Cai [1 ]
Liu, Daoyin [1 ]
Duan, Lunbo [1 ]
Chen, Huichao [1 ]
Chen, Xiaoping [1 ]
机构
[1] Southeast Univ, Sch Energy & Environm, Key Lab Energy Thermal Convers & Control, Minist Educ, Nanjing 210096, Peoples R China
关键词
Wear and breakage; CFD-DEM simulation; Thermochemical energy storage; Heat transfer mechanisms; Fluidization; Attrition-enhanced reactivity; CAO-BASED PELLETS; CO2; CAPTURE; ATTRITION; MODEL; FRAGMENTATION; GASIFICATION; SIMULATION; SORBENTS; SOLIDS;
D O I
10.1016/j.est.2025.117208
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
Fluidized bed reactors are renowned for their excellent mixing and rapid heat transfer capabilities, making them widely used in thermochemical energy storage (TCES) systems. However, particle attrition can significantly affect heat transfer dynamics and system stability, especially under high-temperature reactive conditions. In this study, the spatiotemporal evolution of wear and breakage in a CaCO3/CaO-based energy storage bed is simulated under a CFD-DEM framework, and their quantitative impacts on heat transfer and energy performance are analyzed. Results indicate that attrition are mainly concentrated in the middle and upper regions of the bed, with breakage primarily occurring in the core region-46.67 % of the total breakage occurs within the first 5 s. In contrast, wear mainly develops near the wall region, peaking at 28.68 % during the 15-20 s interval. Attrition increases radiative heat transfer by 10 % and nearly doubles conductive heat transfer, while also introducing a bimodal distribution in heating rate due to particle size variation. Although the average conversion rate and heat release efficiency are significantly enhanced, the reduction in bed porosity and particle kinetic energy negatively impacts bed fluidity and stability. This work provides new insights into the coupling between particle attrition and thermal behavior in reactive fluidized beds, offering guidance for optimizing particle design and reactor operation in TCES applications.
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页数:22
相关论文
共 36 条
[1]   CONTACT AND RUBBING OF FLAT SURFACES [J].
ARCHARD, JF .
JOURNAL OF APPLIED PHYSICS, 1953, 24 (08) :981-988
[2]   Fragmentation of grains in a two-dimensional packing [J].
Astrom, JA ;
Herrmann, HJ .
EUROPEAN PHYSICAL JOURNAL B, 1998, 5 (03) :551-554
[3]   Thermochemical heat storage performance and structural stability of SiO2-coated CaO particles under fluidization in CaO/Ca(OH)2 cycles [J].
Bian, Zhiguo ;
Li, Yingjie ;
Fang, Yi ;
Ren, Yu ;
Zhao, Jianli .
JOURNAL OF ENERGY STORAGE, 2024, 85
[4]   CO2 capture and attrition performance of CaO pellets with aluminate cement under pressurized carbonation [J].
Chen, Huichao ;
Zhao, Changsui ;
Yang, Yanmei ;
Zhang, Pingping .
APPLIED ENERGY, 2012, 91 (01) :334-340
[5]   DISCRETE NUMERICAL-MODEL FOR GRANULAR ASSEMBLIES [J].
CUNDALL, PA ;
STRACK, ODL .
GEOTECHNIQUE, 1979, 29 (01) :47-65
[6]   A BUBBLING FLUIDIZATION MODEL USING KINETIC-THEORY OF GRANULAR FLOW [J].
DING, J ;
GIDASPOW, D .
AICHE JOURNAL, 1990, 36 (04) :523-538
[7]   Calcination of calcium-based sorbents at pressure in a broad range of CO2 concentrations [J].
García-Labiano, F ;
Abad, A ;
de Diego, LF ;
Gayán, P ;
Adánez, J .
CHEMICAL ENGINEERING SCIENCE, 2002, 57 (13) :2381-2393
[8]   Impact attrition of particulate solids. Part 1: A theoretical model of chipping [J].
Ghadiri, M ;
Zhang, Z .
CHEMICAL ENGINEERING SCIENCE, 2002, 57 (17) :3659-3669
[9]   COMBUSTION AND GASIFICATION OF COALS IN FIXED-BEDS [J].
HOBBS, ML ;
RADULOVIC, PT ;
SMOOT, LD .
PROGRESS IN ENERGY AND COMBUSTION SCIENCE, 1993, 19 (06) :505-586
[10]   MASS-TRANSFER TO LARGE PARTICLES IN FLUIDIZED-BEDS OF SMALLER PARTICLES [J].
LANAUZE, RD ;
JUNG, K ;
KASTL, J .
CHEMICAL ENGINEERING SCIENCE, 1984, 39 (11) :1623-1633