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    1000 MW对冲燃烧锅炉侧墙燃烧器浓淡分离主动预防高温腐蚀技术研究

    Research on active prevention of high temperature corrosion by dense-lean separation for burners closest to side walls of an 1000 MW opposed-fired utility boiler

    • 摘要: 对冲燃烧锅炉在低氮燃烧模式下会在燃尽风以下区域形成强还原性气氛,导致侧墙墙水冷壁面临较高的高温腐蚀风险。针对这一问题,贴壁风、燃烧器向中心偏转等方式得到了研究与应用,但针对靠近侧墙燃烧器煤粉浓度对侧墙还原性气氛的影响研究较少。为探究煤粉浓度对对冲燃烧锅炉侧墙水冷壁高温腐蚀速率的影响,运用CFD数值模拟方法对某1000 MW对冲燃烧锅炉靠近侧墙2支燃烧器不同煤粉浓淡比下炉膛燃烧特性、近壁区还原性气氛进行模拟。结果表明:增加侧墙第2支燃烧器与第1支燃烧器浓淡比能够改善主燃区侧墙水冷壁还原性气氛,降低高温腐蚀风险,同时会改变炉膛出口烟气温度分布特征、CO分布特征。近侧墙2支燃烧器浓淡比由1∶1增加至3∶1时,CO体积分数均值由4.08%降低至3.00%,降低幅度26.5%;最大值由8.19%降低至6.45%,降低幅度21.2%。在侧墙燃烧器浓淡比3∶1基础上,将靠近侧墙的第1支燃烧器二次风量增加1/8,侧墙近壁区CO体积分数均值由3.00%降低至1.89%,与基准工况相比降低幅度为53.7%;最大值由6.45%降低至5.34%,与基准工况相比降低幅度为34.8%。浓淡比过高会因粉量分配不均造成炉膛出口CO局部聚集、局部烟气温度升高。应采用3∶1的煤粉浓淡比以平衡主燃区还原性气氛的改善与炉膛出口参数的劣化。同时,需要通过燃烧优化调整避免侧墙第2支燃烧器煤粉浓度升高引起炉膛出口CO体积分数升高。通过调整侧墙燃烧器煤粉浓度及过量空气系数,能够显著改善侧墙水冷壁还原性气氛,可用于对冲燃烧锅炉主燃烧器区侧墙水冷壁高温腐蚀速率优化控制。

       

      Abstract: In the low-NOx combustion mode, the opposed-fired boiler generates a strong reducing atmosphere in the side water-cooled wall, resulting in a high-temperature corrosion trend on the side water-cooled walls in main combustion zone. To address this issue, methods such as closing-to-wall air and inward deflection of burners near the side wall have been studied and applied, but there are few studies on the effect of pulverized coal concentration near the side wall burner on the reducing atmosphere near the side wall. In order to study the effect of pulverized coal concentration on the high-temperature corrosion rate of the side water-cooled wall of an 1000 MW opposed-fired boiler, the CFD numerical method was used to simulate the furnace combustion characteristics and the reducing atmosphere near the side wall under different coal concentration ratios of the two burners closest to the side wall. The results show that with an increase of the concentration ratio of the second burner to the first burner closest to the side wall leads to an decrease in the CO concentration near the side water-cooled wall in the main combustion zone, and reduce the risk of high-temperature corrosion. Meanwhile, it changes the temperature distribution characteristics of the flue gas and the CO distribution characteristics at the furnace outlet. When the ratio of coal concentration between the two burners closest to the side wall increases from 1∶1 to 3∶1, the average CO concentration decreases from 4.08% to 3.00%, and the maximum value decreases from 8.19% to 6.45%. On the basis of the concentration ratio of 3∶1, with an increase by 12.5% of the secondary air of the first burner closest to the side wall, the average CO concentration in the area near the side wall decreases from 3.00% to 1.89%, and the maximum value decreases from 6.45% to 5.34%. Higher concentration ratio will cause local accumulation of CO at the furnace outlet and increase in local flue gas temperature. The pulverized coal concentration ratio of 3∶1 should be used to balance the improvement of the reducing atmosphere in the main combustion zone and the deterioration of the furnace outlet parameters. At the same time, combustion optimization adjustment is required to avoid the risk of increased CO concentration at the furnace outlet caused by increased pulverized coal concentration of the second burner closest to the side wall. By adjusting the pulverized coal concentration and the excess air coefficient of the side wall burner, the reducing atmosphere of the side water-cooled wall can be significantly improved, which can be used to optimize the control of the high-temperature corrosion rate of the side water-cooled wall in the main combustion zone of the opposed-fired boiler.

       

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