插入挡板对流化床反应器中固体颗粒偏析行为的影响:计算研究

IF 2.8 Q2 ENGINEERING, CHEMICAL
Suchart Kreesaeng, B. Chalermsinsuwan, P. Piumsomboon
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引用次数: 0

摘要

在多固体、粒度流化床反应器系统中,通常会出现偏析现象。发生偏析时,小的固体颗粒被夹带到床的顶部,并从反应器中逸出。在燃烧过程中,逸出锅炉的小固体颗粒被燃烧,并在旋风分离器周围受到破坏。本研究采用计算流体动力学方法,使用三种不同大小的固体颗粒研究反应器中的固体颗粒行为。研究了挡板插入、挡板角度、级数及其排列的影响。计算了偏析的百分比,以比较不同反应器系统的行为。与无挡板和有 90 度挡板的情况相比,插入 45 度挡板可减少偏析行为,这归因于固体阻碍和碰撞现象。此外,任何布置的双级挡板都能减少偏析行为。最佳布置是 "高于布置",原因是颗粒在挡板级之间阻碍、旋转和积聚。因此,为了减少偏析行为并加强燃烧化学反应,建议在反应器区域插入挡板。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Effect of Inserting Baffles on the Solid Particle Segregation Behavior in Fluidized Bed Reactor: A Computational Study
In multi-solid, particle-size fluidized bed reactor systems, segregation is commonly observed. When segregation occurred, small solid particles were entrained to the top of the bed and escaped from the reactor. During the combustion process, the small solid particles that escaped from the boiler were burned and subjected to damage around the cyclone separator. This study then employed a computational fluid dynamics approach to investigate solid particle behavior in the reactor using three different sizes of solid particles. The effects of baffle insertion, baffle angle, stage number, and its arrangement were examined. The percentage of segregation was calculated to compare behavior among different reactor systems. The insertion of 45-degree baffles resulted in reduced segregation behavior compared to cases without baffles and with 90-degree baffles, attributed to solid hindering and collision phenomena. Additionally, a double-stage baffle with any arrangement could reduce segregation behavior. The best arrangement was “above-arrangement” due to particles hindering, swirling, and accumulating between the baffle stages. Therefore, to diminish segregation behavior and enhance combustion chemical reactions, the insertion of baffles in the reactor zone is recommended.
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来源期刊
ChemEngineering
ChemEngineering Engineering-Engineering (all)
CiteScore
4.00
自引率
4.00%
发文量
88
审稿时长
11 weeks
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