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Operating regimes in circulating fluidized bed combustors: fast fluidization or bubbling-entrained bed?

机译:在循环流化床燃烧器中的经营制度:快速流化或鼓泡夹带床?

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摘要

Circulating fluidized bed combustors (or boilers) are one of the most widely used gas-solid convertors around the globe. As it plays an essential role in boiler design, different researchers have suggested different operating regimes for CFB combustors, based on their findings from experiments or practical experiences. Although there seems to be some consensus, a clear expression or conclusion that would be widely accepted in both the industry and academic community has yet to come. By analyzing and comparing reported data, in particular the particle size distributions (PSD) of different bed materials, from a variety of literature, it is reasoned that in commercial boilers the bottom part of the circulating fluidized bed combustor is operated in the bubbling regime even though under high gas velocities, and the upper part of the furnace can be viewed as an entrained bed. Such statement is well supported by analyzing hydrodynamic behaviors including solids volume fraction, solids velocity distribution and so forth, of real industrial boilers or pilot CFB combustor units.
机译:循环流化床燃烧器(或锅炉)是全球最广泛使用的气固转换器之一。由于它在锅炉设计中发挥着重要作用,基于实验或实践经验的发现,不同的研究人员提出了CFB燃烧器的不同操作制度。虽然似乎有一些共识,但在行业和学术界尚未到来的明确表达或结论。通过分析和比较报告的数据,特别是不同床材料的粒度分布(PSD),从各种文献中,在商业锅炉中,循环流化床燃烧器的底部在鼓泡状态下运行虽然在高气体速度下,但炉子的上部可以被视为夹带床。通过分析包括固体体积分数,固体速度分布等的流体动力学行为,实际工业锅炉或飞行员CFB燃烧装置,得到了这种陈述。

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