西安热工研究院有限公司
纸质出版:2011
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段景卫, 赵志丹, 刘爱军, 等. 某300MW循环流化床锅炉结焦原因分析[J]. 热力发电, 2011,40(1):45-47.
DUAN Jingwei, ZHAO Zhidan, LIU Aijun, et al. CAUSE ANALYSIS OF SLAGGING IN ONE 300 MW CFB BOILER[J]. Thermal power generation, 2011, 40(1): 45-47.
段景卫, 赵志丹, 刘爱军, 等. 某300MW循环流化床锅炉结焦原因分析[J]. 热力发电, 2011,40(1):45-47. DOI:
DUAN Jingwei, ZHAO Zhidan, LIU Aijun, et al. CAUSE ANALYSIS OF SLAGGING IN ONE 300 MW CFB BOILER[J]. Thermal power generation, 2011, 40(1): 45-47. DOI:
对某电厂300 MW循环流化床锅炉结焦原因进行了分析
得出低阻力布风板虽然有良好的布风均匀性
但其正常流化状态抗扰动的能力较弱
在受到扰动时流化态容易恶化
从而形成床料贴壁结焦。同时
锅炉添加床料系统给料点设计不良
导致炉膛内床料粒度不能均匀分布
也是造成流化不良的原因。对此
提出了严格控制起动运行参数
适当增加一次风量
缩短起动时间等措施
在一定程度上可避免结焦。
The causes leading to slagging in 300 MW boiler of one power plant have been analysed
the conclusion obtained is as follows:although the air-distributing plates of low fluid drag have the ability to distribute the air more uniformly
but their disturbance-resistant ability is weaker
in the case of encountering disturbance the normal fluidization regime is easily to deteriorate
thereby
resulting in slagging due to the bed material sticked on the water-cooled wall.At the same time
it has been pointed out that the designed feed points in the bed material adding system of boiler are imperfect
leading to un-uniform distribution of bed material particles in the furnace
being another cause resulting in bad fluidization.For this
some measures have been put forward
i.e.the parameters in start-up and operation have to be strictly controlled
the quantity of primary air has to be suitably increased
thus
can aviod slagging in a certain degree.
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