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Wastage rate of water walls in a commercial circulating fluidized bed combustor

机译:商业循环流化床燃烧器中水壁的流失率

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Wastage rate profiles of water walls were determined in a large (200 tonnes steam/h, 4.97 m x 9.90 m x 28.98 rn tall) commercial circulating fluidized bed furnace by measuring tube thickness with an ultrasonic thickness gauge. The wastage rate was most significant in the region just above the refractory lining on all water walls, decreasing with increasing height. Wear in this region was enhanced at the centre of the sidewalls, on some sidewall tubes near the front wall, and on outer areas of the front and rear walls. The wear pattern was complex around the gas exit level. Wastage increased with increasing height on the front wall below the gas exit. Wastage decreased, then increased, with increasing height at the top of the front wall. Above the gas exit level, the wastage on the rear wall was less than on the front wall. Tubes just below the gas exit were subject to appreciable wear on the rear wall. High wastage rates also occurred on some tubes near the centre of the sidewalls at the gas exit level. On all wing walls the wastage rate decreased, then increased, with increasing height. The wastage rate of many tubes below 7 m on all water walls exceeded the maximum acceptable wear rate for steel boiler tubes in a coal-fired utility plant, while for some tubes at the gas exit level on all walls it was close to the maximum acceptable rate.
机译:在大型(200吨蒸汽/h,4.97 m x 9.90 m x 28.98 rn高)商业循环流化床炉中,通过用超声波测厚仪测量管的厚度,确定水壁的流失速率分布。在所有水冷壁上耐火衬层上方的区域,浪费率最高,随高度增加而降低。在该区域的磨损在侧壁的中心,前壁附近的一些侧壁管以及前壁和后壁的外部区域得到了增强。气体出口水平附近的磨损模式很复杂。随着排气口下方前壁高度的增加,损耗增加。随着前壁顶部高度的增加,浪费减少,然后增加。在排气口以上,后壁的浪费少于前壁的浪费。排气口正下方的管子在后壁上受到明显的磨损。在气体出口处靠近侧壁中心的一些管子上也发生了高浪费率。在所有机翼壁上,废料率随高度的增加先降低后增加。在所有水冷壁上,许多低于7 m的管道的浪费率超过了燃煤电厂的钢制锅炉管道的最大可接受磨损率,而对于在所有墙壁上的气体出口处的某些管道,其损耗率接近最大可接受的磨损率。率。

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