首页> 外文会议>International Conference on Fluidized Bed Combustion; 20050522-25; Toronto(CA) >ON EFFECT OF AIR-SEPARATING GRID ON LOW-GRADE SOLID FUELS COMBUSTION IN A FLUIDIZED BED
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ON EFFECT OF AIR-SEPARATING GRID ON LOW-GRADE SOLID FUELS COMBUSTION IN A FLUIDIZED BED

机译:分离床对流化床低级固体燃料燃烧的影响

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In furnaces and other types of fluidized bed reactors one can easily observe gas bubbles flow and fluid jet preferable rise zones where solid particles in form of fountains are carried away from the layer. Let us call these layers as zones of local flowing. We assume that in these zones of local flowing occurs the removal of unburned fuel particles from fluidized bed. It results in heat leakage up to 20-40% due to mechanical imperfection of fuel combustion in types of vessels with fluidized bed furnaces. We investigated particles with diameter of 2,5 - 3,0 mm motion and local flowing zones formation in a model column of 172 mm in diameter at room temperature. Experimental application of air-separating grid enabled to form at the layer input "flat" and "convex" air velocity line. At the "flat" line the air distributed uniformly on the input section of the device. When the line was "convex" the air velocity at the layer input in the device center was twice higher than at the device periphery. It was found out that at "flat" line when air velocity increases there appeared zones of local flowing in the layer. To eliminate these zones one should increase the height of stationary particles layer. At "convex" line of input air velocity elimination of local flowing zones is possible by stable increase of air velocity or by lowering the height of stationary particles layer. It was concluded that for small fluidized bed fireboxes it is better to apply air-separating grids forming "convex" input air velocity line. The grid under discussion was manufactured to be applied in experimental fluidized bed firebox. There was carried out a detailed study of ordinary anthracite combustion in a firebox. It was established that at "convex" input air velocity line fuel loss due to entrainment amounted 2,0 - 2,5 %. According to experimental results there were designed water boilers with heating efficiency from 300 up to 800 kilowatt. In these water boilers there was applied the grid forming "convex" input air velocity line. During tests there was burned culm (particle size from 0 up to 6 mm, heating efficiency of 20,6 MJ/ kg, output of volatile matter up to 6%, zoning 26,2 - 31,1%). Efficiency factor of these water boilers is 83 - 85% (without entrainment return to the firebox).
机译:在熔炉和其他类型的流化床反应器中,人们可以轻松地观察到气泡的流动和流体喷射的上升区域,在该上升区域中,呈润版液形式的固体颗粒被带离该层。让我们称这些层为局部流动的区域。我们假设在这些局部流动的区域中发生了从流化床中去除未燃烧的燃料颗粒的情况。由于带有流化床炉的容器中燃料燃烧的机械缺陷,它导致高达20-40%的热泄漏。我们在室温下在直径为172 mm的模型柱中研究了直径为2,5-3,0 mm的运动粒子和局部流动区域的形成。空气分离栅的实验应用能够在层输入处形成“平坦”和“凸”空气速度线。在“扁平”线处,空气均匀分布在设备的输入部分。当线是“凸”时,在设备中心的层输入处的空气速度是在设备外围处的空气速度的两倍。发现在“平坦”线处,当空气速度增加时,在层中出现局部流动的区域。为了消除这些区域,应该增加固定颗粒层的高度。在输入空气速度的“凸”线上,可以通过稳定增加空气速度或降低固定颗粒层的高度来消除局部流动区域。结论是,对于小型流化床燃烧室,最好使用形成“凸形”输入空气速度线的空气分隔格栅。所讨论的网格已制造为可用于实验流化床燃烧室。对燃烧室中普通无烟煤燃烧进行了详细研究。已经确定,在“凸”输入空气速度线处,由于夹带引起的燃料损失为2.0-2.5%。根据实验结果,设计了热水锅炉,其加热效率从300千瓦到800千瓦不等。在这些开水器中,使用了形成“凸形”输入空气速度线的网格。在测试过程中,有燃烧的茎秆(颗粒大小从0到6 mm,加热效率为20,6 MJ / kg,挥发物输出高达6%,分区为26,2-31,1%)。这些开水器的效率系数为83-85%(不带夹带返回火箱)。

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