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A Study on the Effect of Additive Size and Type on Agglomeration and Defluidisation in a Small Fluid Bed Combustor

机译:添加剂尺寸和类型对小型流化床燃烧器结块和脱液影响的研究

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Circulating fluid bed combustors (CFBC) are ideally suited for burning low-rank coals.Particular advantages include their ability to maintain combustion temperatures (800-900°C) below ash fusion point, control of SO_2 emission by using in-bed sorbents, andcontrol of NOx by using lower combustion temperatures and air staging. CFBC’s are,however, not without disadvantages. Depending on the operating conditions and ashproperties, bed agglomeration takes place in the combustor due to the interaction ofmineral matter in coal and bed material (typically silica sand). Potentially this may leadto defluidisation of the bed. In a previous study, it was established that additives such asclay-based minerals could control the agglomeration and defluidisation duringcombustion of a high-sulfur coal.An experimental study was undertaken to assess the effect of size of additive on bedagglomeration and defluidization. Additionally, it was also decided to examine the effectof non-clay based minerals. Two South Australian coals, Lohiel and Bowmans, wereburned in a laboratory scale fluid bed at temperatures of 800 and 850°C with and withoutadditives. Silica sand was used as bed material, and a suite of additives – silica sand oftwo different sizes, calcined alumina, and flyash were used during the tests. Fromphysical observation during the tests, and chemical analysis and electron microscopyafter the tests, it was found that size, rather than type of the additives, is more importantin controlling agglomeration and defluidization. Any additive, which is of fine size, anditself is not a low-melting point compound, can control agglomeration when used as anadditive in a fluid bed combustor. Fine additives provide large surface areas and capturethe fine ash or agglomerate forming constituents, eventually elutriating away from thebed, thereby preventing defluidization. It was also observed that defluidisation is notdependent on the thickness of coating on the bed particles, and sulfate compounds ofsodium and magnesium, and to a lesser extent sodium chloride are responsible foragglomeration and defluidization for the coals tested.
机译:循环流化床燃烧器(CFBC)非常适合燃烧低阶煤。 特殊优势包括其保持燃烧温度的能力(800- 在灰熔点以下900°C),通过使用床内吸附剂控制SO_2的排放以及 通过使用较低的燃烧温度和空气分级来控制NOx。 CFBC是 但是,并非没有缺点。取决于操作条件和灰分 性质,由于燃烧器的相互作用,在燃烧器中发生了床的结块。 煤和床层材料中的矿物质(通常是硅砂)。可能会导致 去除床中的液体。在先前的研究中,已确定添加剂如 粘土基矿物可以控制结块和流化 燃烧高硫煤。 进行了一项实验研究,以评估添加剂尺寸对床的影响 结块和流化。此外,还决定检查效果 非粘土矿物。南澳大利亚的两种煤,Lohiel和Bowmans,分别是 在有和没有温度的情况下,在800和850°C的温度下在实验室规模的流化床中燃烧 添加剂。硅砂被用作床层材料,并添加了一套添加剂–硅砂 在测试过程中使用了两种不同尺寸的煅烧氧化铝和粉煤灰。从 测试过程中的物理观察,化学分析和电子显微镜 在测试之后,发现添加剂的尺寸而不是添加剂的类型更为重要 在控制团聚和流化方面。尺寸合适的任何添加剂,以及 本身不是低熔点化合物,当用作 流化床燃烧室中的添加剂。优良的添加剂可提供较大的表面积并捕获 细粉尘或团聚体形成成分,最终从中洗脱出来 床,从而防止脱液。还观察到去流体不是 取决于床层上的涂层厚度以及硫酸盐化合物 钠和镁,以及少量的氯化钠 所测试的煤的结块和脱液。

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