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Method for reducing nitrogen oxide emissions and corrosion in a bubbling fluidized bed boiler and a bubbling fluidized bed boiler

机译:减少鼓泡流化床锅炉中氮氧化物排放和腐蚀的方法

摘要

To reduce nitrogen oxide emissions and corrosion in a bubbling fluidized bed boiler that burns biofuel or waste, air is supplied into the boiler furnace (1) in stages so that two sub-stoichiometric combustion zones (I), (II) and a superstoichiometric zone (III) are brought about. The first combustion zone (I) begins from the height level of primary air supply nozzles (3) and it extends above the fluidized bed (2), ending under the height level (hS) of secondary air nozzles (6). The second combustion zone (II) begins from the height level (hS) of the secondary air nozzles (6) and ends under the height level (hT) of tertiary air nozzles (7). The third combustion zone (III) begins from the height level (hT) of the tertiary air nozzles. The length of the first combustion zone (I) is optimized by placing the secondary air nozzles (6) at a height (hS) from the top surface of the fluidized bed (2), which height (hS) is chosen according to a given calculation formula and calculated according to furnace-specific variables, reference values and design point-specific variables. The design point-specific variables are different in a boiler with a high furnace load and in a boiler with a low furnace load.
机译:为了减少燃烧生物燃料或废物的鼓泡流化床锅炉中的氮氧化物排放和腐蚀,将空气分阶段供应到锅炉炉(1)中,以使两个亚化学计量的燃烧区(I),(II)和超化学计量的区(三)带来。第一燃烧区(I)从一次空气喷嘴(3)的高度开始,并在流化床(2)上方延伸,在二次空气喷嘴(6)的高度(hS)以下终止。第二燃烧区(II)从二次空气喷嘴(6)的高度(hS)开始,并在三次空气喷嘴(7)的高度(hT)以下终止。第三燃烧区(III)从第三级空气喷嘴的高度(hT)开始。通过将辅助空气喷嘴(6)放置在距流化床(2)顶表面的高度(hS)处,可以优化第一燃烧区(I)的长度,该高度(hS)是根据给定的计算公式并根据炉子特定变量,参考值和设计点特定变量进行计算。设计点特定变量在高炉负荷的锅炉和低炉负荷的锅炉中是不同的。

著录项

  • 公开/公告号EP2574841A3

    专利类型

  • 公开/公告日2014-02-26

    原文格式PDF

  • 申请/专利权人 FORTUM OYJ;

    申请/专利号EP20120397524

  • 申请日2012-09-26

  • 分类号F23C10;F23G5/30;F27B15;F27B15/02;F27B15/10;

  • 国家 EP

  • 入库时间 2022-08-21 15:48:49

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