• 论文
主办单位:煤炭科学研究总院有限公司、中国煤炭学会学术期刊工作委员会
300 MW亚临界循环流化床机组NOx排放建模
  • Title

    NOx emission model of 300 MW subcritical circulating fluidized bed unit

  • 作者

    刘春高明明张洪福张国华岳光溪

  • Author

    LIU Chun;GAO Mingming;ZHANG Hongfu;ZHANG Guohua;YUE Guangxi

  • 单位

    新能源电力系统国家重点实验室(华北电力大学)清华大学 能源与动力工程系

  • Organization
    State Key Labof Alternate Electric PowerSystem with Renewable Energy Sources ( North China Electric Power University )
    Departmentof Energy and Power Engineering , Tsinghua University
  • 摘要

    随着污染物排放标准日益严格,SNCR已成为一种广泛应用于循环流化床(CFB)机组降低NOx排放的新技术,然而循环流化床机组变负荷时NOx排放浓度波动较大,加大SNCR控制难度。由于变负荷NOx动态排放模型研究较少,为实现变负荷过程循环流化床机组NOx的动态预测,对炉内NOx生成机理与SNCR反应机理进行分析,以给煤量、风量、喷氨量、床温等参数作为输入,结合数学建模方法,建立NOx动态排放模型。结合某300MW亚临界循环流化床机组实际运行数据进行不同负荷动态仿真,结果表明,该模型在动态过程中能较好拟合NOx排放趋势,300MW与150MW典型负荷工况及变负荷工况下模型计算值与真实值平均绝对误差分别为3.5、1.2、5.7mg/m3,精度较高,可实现CFB机组NOx排放实时预测,预测时间为4~5min。开展了不同工况给煤量、送风量、尿素流量及多变量的开环阶跃试验,结果表明,模型能较好反映NOx排放过程的动态特性。研究结果可为CFB机组超低排放控制优化提供参考。

  • Abstract

    With the increasingly strict pollutant emission standards, SNCR has become a new technology widely used in circulating fluid⁃ized bed (CFB) units to reduce NOx emissions. However, the difficulty of SNCR control will be increased due to the fluctuation of NOxemission concentration during variable load operation of circulating fluidized bed units. Due to the variable load dynamic NOx emis⁃sion model study is less, and in order to the realization of the dynamic prediction of NOx load change process of circulating fluidized bedunit, the article mechanism of NOx formation and SNCR reaction mechanism inside the furnace was analyzed, with coal and air volume,injection amount of ammonia, as input parameters, such as bed temperature, and mathematical modeling methods were used to establish aNOx dynamic emission model. Combined with the actual operation data of a 300 MW subcritical CFB unit, the dynamic simulation of dif⁃ferent loads was carried out. The results show that the model can better fit the NOx emission trend in the dynamic process. The average ab⁃solute errors between the calculated values of the model and the real values under 300 MW and 150 MW typical load conditions and varia⁃ble load conditions are 3.5, 1.2 and 5.7 mg/ m3, respectively, with high accuracy, which can realize the real-time prediction of NOxemission of CFB unit, with the predicted time of 4-5 min. Then, the open-loop step experiments of coal supply, air supply, urea flowand multi-variable under different working conditions were carried out. The experimental results show that the model can better reflect thedynamic characteristics of NOx emission process. The results can provide reference for the optimization of ultra-low emission control ofCFB units.

  • 关键词

    循环流化床变负荷NOx排放SNCR预测模型

  • KeyWords

    circulating fluidized bed;load change;NOx emission;SNCR;prediction model

  • 基金项目(Foundation)
    国家重点研发计划资助项目(2022YFB4100304)
  • 文章目录

    0 引言

    1 NOx浓度排放模型

       1.2 燃烧模型

       1.3 NOx原始排放模型

       1.4 SNCR反应模型

    2 模型仿真验证

       2.1 稳态验证

       2.2 动态验证

       2.3 开环阶跃试验

    3 结论

  • DOI
  • 引用格式
    刘春,高明明,张洪福,等.300 MW 亚临界循环流化床机组 NOx排放建模[J].洁净煤技术,2023,29(8):109-115.
  • Citation
    LIU Chun,GAO Mingming,ZHANG Hongfu,et al.NOx emission model of 300 MW subcritical circulating fluidized bed unit[J].Clean Coal Technology,2023,29(8):109-115.
  • 相关文章
  • 图表
    SNCR反应器模型示意
    SNCR反应器模型示意
    300 MW工况模型计算值与真实值对比
    300 MW工况模型计算值与真实值对比
    150 MW工况模型计算值与真实值对比
    150 MW工况模型计算值与真实值对比
    变负荷过程中机组实际运行数据
    变负荷过程中机组实际运行数据
    变负荷过程NOx模型计算值与机组实际值对比结果
    变负荷过程NOx模型计算值与机组实际值对比结果
    300 MW和200 MW给煤量阶跃时NOx质量浓度
    300 MW和200 MW给煤量阶跃时NOx质量浓度
    300 MW和200 MW送风量阶跃时NOx质量浓度
    300 MW和200 MW送风量阶跃时NOx质量浓度
    300 MW和200 MW尿素流量阶跃时NOx质量浓度
    300 MW和200 MW尿素流量阶跃时NOx质量浓度
    200 MW给煤量与送风量同时阶跃时NOx质量浓度
    200 MW给煤量与送风量同时阶跃时NOx质量浓度
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