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330MW前墙燃烧煤粉锅炉炉内温度场的数值模拟及优化 被引量:15
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作者 王政允 孙保民 +3 位作者 郭永红 肖海平 刘欣 白涛 《中国电机工程学报》 EI CSCD 北大核心 2009年第20期18-24,共7页
某电厂330MW机组锅炉采用双调风旋流燃烧器,前墙布置。该厂实际运行中一次风速与设计值相比相差较大,较大的一次风速造成了燃烧器一次风管磨损严重,同时后墙水冷壁高温腐蚀的可能性增大。该文提出保持原燃烧器一次风管尺寸不变,减小中... 某电厂330MW机组锅炉采用双调风旋流燃烧器,前墙布置。该厂实际运行中一次风速与设计值相比相差较大,较大的一次风速造成了燃烧器一次风管磨损严重,同时后墙水冷壁高温腐蚀的可能性增大。该文提出保持原燃烧器一次风管尺寸不变,减小中心风管直径、增大一次风流通面积以减小一次风速的改造方案。为研究改变中心风管直径后的4层燃烧器对炉膛燃烧的影响,采用数值模拟的方法对该型锅炉炉内的温度场进行数值计算,得到5种不同方案下该型锅炉炉内的温度场分布,并分析了中心风管直径的改变对炉内温度场的影响规律,即后墙近壁区温度随着中心风管直径的减小呈现先降低后升高的趋势。通过对5种方案数值模拟结果的比较分析,得到了对炉膛后墙安全性影响最小的方案,为电厂的实际改造提供参考。 展开更多
关键词 前墙燃烧 电站锅炉 旋流燃烧 温度场 数值模拟 中心风管
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利港电厂2×350MW机组锅炉低氮燃烧改造及其对锅炉运行的影响 被引量:10
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作者 王东平 贾宏禄 刘小平 《热力发电》 CAS 北大核心 2008年第12期38-44,共7页
利港电厂对两台FW公司设计的前墙燃烧锅炉进行了以降低氮氧化物排放为目标的改造。通过更换新型低氮燃烧器和增加燃尽风(OFA)喷口,使氮氧化物排放降低了60%,但锅炉飞灰含碳量有所增加。鉴于此,对改造后的燃烧系统进行了调整优化,最终达... 利港电厂对两台FW公司设计的前墙燃烧锅炉进行了以降低氮氧化物排放为目标的改造。通过更换新型低氮燃烧器和增加燃尽风(OFA)喷口,使氮氧化物排放降低了60%,但锅炉飞灰含碳量有所增加。鉴于此,对改造后的燃烧系统进行了调整优化,最终达到了在不同氧量、不同磨煤机组合和不同燃用煤种下,降低氮氧化物排放浓度,减少再热器管排温度偏差,遏制飞灰含碳量增加和防止出现堆渣的效果。 展开更多
关键词 锅炉 前墙燃烧 燃烧 燃尽风 氧量 NOx 排放 飞灰含碳量
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Numerical analysis of reasons for the CO distribution in an opposite-wall-firing furnace
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作者 Xiao-qiang XIE Jian-guo YANG +3 位作者 Chao-yang ZHU Chuan-huai LIU Hong ZHAO Zhi-hua WANG 《Journal of Zhejiang University-Science A(Applied Physics & Engineering)》 SCIE EI CAS CSCD 2020年第3期193-208,共16页
In practical operations,the carbon monoxide(CO)distribution in an opposite-wall-firing furnace(OWFF)is characterized by a high concentration near the side walls and a low concentration in the center,accompanied by a s... In practical operations,the carbon monoxide(CO)distribution in an opposite-wall-firing furnace(OWFF)is characterized by a high concentration near the side walls and a low concentration in the center,accompanied by a series of combustionrelated issues.To find the reasons for the CO distribution,a numerical study was conducted on a 660 MWe OWFF.The CO concentration profiles,distribution coefficients of coal and air,mixing coefficients,and the aerodynamic characteristics were extracted for analysis.The CO distribution within the furnace greatly depends on the mixing of coal and air.A mismatch between the aerodynamic behaviors of coal and air causes the non-uniform distribution of CO.Taking into consideration that distinctive flow patterns exist within the different regions,the formation mechanisms of the CO distribution can be divided into two components:(1)In the burner region,the collision of opposite flows leads to the migration of gas and particles toward the side wall which,together with the vortexes formed at furnace corners,is responsible for unburned particles concentrated and oxygenized from the furnace center to the side wall.Thus,high CO concentrations appear in these areas.(2)As the over-fire air(OFA)jet is injected into the furnace,it occupies the central region of furnace and pushes the gas from the burner region outward to the side wall,which is disadvantageous for the mixing effect in the side wall region.As a consequence,a U-shaped distribution of CO concentration is formed.Our results contribute to a theoretical basis for facilitating the control of variation in CO concentration within the furnace. 展开更多
关键词 Opposite-wall-firing furnace(OWFF) Carbon monoxide(CO)distribution Distributions of coal and air Gas/particle flow Corner vortex Over-fire air(OFA)
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