600MW超临界直流锅炉低氮改造后汽温动态特性试验研究

2号锅炉低氮燃烧器改造后,出现了中高负荷下烟气中CO排放浓度高、低负荷下主蒸汽温度不足以及升降负荷过程中汽温波动幅度大等问题.针对这一系列问题,采取"稳态燃烧调整+动态汽温特性+控制参数修改"的方式进行了试验研究.结果表明:600 MW和450 MW负荷点下,CO排放浓度平均值分别由789 μL/L和170 μL/L降...     

高温烟气伴流的温度和氧浓度对甲烷/氢气扩散火焰的影响(英文)

This paper investigates the effects of coflow O2 level and temperature on diffusion flame of a CH4/H2 jet in hot coflow(JHC) from a burner system similar to that of Dally et al.The coflow O2 mass fraction(y*O2) is varied from 3% to 80% and the temperature(T*cof) from 1200 K to 1700 K.The Eddy Dissipation Concept(EDC) model with detailed reaction mechanisms GRI-Mech 3.0 is used for all simulations.To validate the modeling,several JHC flames are predicted under the experimental conditions of Dally et al.[Proc.Combust.Inst.,29(1),1147-1154(2002)] and the results obtained match well with the measurements.Results demonstrate that,when y*O2 decreased,the diffusion combustion is likely to transform from traditional combustion to MILD(Moderate or Intense Low-oxygen Dilution) combustion mode.When cof T* is higher,the temperature distribution over the whole domain trends to be more uniform.Reducing y*O2 or cof T* leads to less production of intermediate species OH and CO.It is worth noting that if y*O2 is high enough(y*O2>80%),increasing y*O2 does not cause obvious temperature increase.     

再热汽温为623℃的再热器管壁温度优化调整

本文以设计再热蒸汽温度为623℃的1台660 MW机组、1台1 000 MW机组和1台1 000 MW二次再热机组为研究对象,综合分析了造成再热蒸汽温度偏低的原因,并有针对性地进行了优化调整。优化后,再热蒸汽温度均有较大程度的提升,660 MW机组和1 000 MW一次再热机组再热蒸汽温度分别由调整前的609.0℃和599.8℃提高至618.0℃和619.8℃,1 000 MW二次再热机组高/低压高温再热蒸汽温度分别由调整前的603.4℃和601.4℃提高至612.5℃和612.7℃;同时,末级再热器管壁温度高低点的偏差也有所降低。该研究结果可为同类型机组再热器管壁温度的优化调整提供参考。     

同流热气中氧浓度对CH4/H2射流火焰的影响

通过雷诺平均纳维叶斯托克斯方程模型数值模拟研究了同流热气中氧浓度对CH4/H2射流火焰扩散燃烧的影响。研究基于JHC开放火焰实验装置,采用涡耗散概念模型和GRI-3.0详细化学反应机制进行数值模拟,研究同流热气中氧浓度变化的影响。结果显示,随着同流热气中氧浓度的减小,下游温度峰值及中间组分OH的质量分数峰值明显下降,温度分布更均匀。OH质量分数峰值位置比温度峰值位置略微靠外(同流热气侧)。H2CO主要分布在计算域内的低温区,高温时该组分被快速消耗;不同的燃烧模式下H2CO浓度分布差别很大。通过分析发现,要使传统窄小区域的快速燃烧模式过渡到大空间的慢速弥散燃烧,应减小同流热气中氧浓度。     

东方百万机组锅炉管壁温度分布规律研究与应用

为解决东方百万千瓦机组锅炉管壁超温的问题,以东方超超临界百万机组锅炉为研究对象,分别进行了1 000 MW和500 MW负荷的运行试验,研究了管壁温度分布规律及燃烧器拉杆位置和燃尽风配风方式对管壁温度分布的影响特性。结果表明,燃烧器(燃尽风)拉杆采取U型配风方式时,将会导致中间区域受热面管壁温度高,管壁温度呈现出"倒U型"的分布规律;开大中间区域燃烧器(燃尽风)拉杆位置,有助于缓解管壁超温。根据该研究成果,解决了某机组高温再热器管壁超温导致再热蒸汽不足的问题,额定负荷下,再热蒸汽温度由优化前的603.4℃提高至优化后的616.9℃;同时,解决了另一机组低负荷下屏式过热器管壁超温的问题,500 MW负荷、AEF磨煤机组合运行方式下,屏式过热器管壁最高点温度值由616.3℃降低至600.5℃,大大提高了管材的安全裕量。     

Diffusion Flame of a CH4/H2 Jet in a Hot Coflow: Effects of Coflow Oxygen and Temperature

This paper investigates the effects of coflow O₂ level and temperature on diffusion flame of a CH₄/H₂ jet in hot coflow (JHC) from a burner system similar to that of Dally et al. The coflow O₂ mass fraction (y_O2^*) is varied from 3% to 80% and the temperature (T_cof^*) from 1200 K to 1700 K. The Eddy Dissipation Concept (EDC) model with detailed reaction mechanisms GRI-Mech 3.0 is used for all simulations. To validate the modeling, several JHC flames are predicted under the experimental conditions of Dally et al. [Proc. Combust. Inst., 29 (1), 1147-1154 (2002)] and the results obtained match well with the measurements. Results demonstrate that, when y_O2^* decreased, the diffusion combustion is likely to transform from traditional combustion to MILD (Moderate or Intense Low-oxygen Dilution) combustion mode. When T_cof^* is higher, the temperature distribution over the whole domain trends to be more uniform. Reducing y_O2^* or T_cof^* leads to less production of intermediate species OH and CO. It is worth noting that if y_O2^* is high enough (y_O2^*>80%), increasing y_O2^* does not cause obvious temperature increase.