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    燃煤电厂空预器堵塞机制分析及治理措施研究

    Study on the mechanism of air preheater blockage in coal-fired power plants and its control measures

    • 摘要: 在新型电力系统和“新一代煤电升级”背景下,保障深度调峰机组安全运行和提高运行经济性极为重要。为探究空气预热器的积灰、堵塞和腐蚀问题,揭示不同层位沉积物的形成机理,以某 2×660 MW燃煤电厂四分仓回转式空气预热器为研究对象,采用XRD、XRF、SEM-EDS 面扫描和XPS 等手段,对空气预热器中部和底部沉积物的物相组成、微观形貌、元素分布及表面化学状态进行表征分析,并建立传热模型评估其凝结风险。结果表明,中部和底部沉积物中Fe2O3的质量分数分别为51.66%和42.68%,SiO2的质量分数分别为24.00%和29.98%;底部沉积物中SO3含量为9.19%,约为中部沉积物SO3含量(2.35%)的 3.9 倍。中部沉积物主要呈现由飞灰颗粒与铁氧化物共同构成的复合沉积结构,而底部沉积物则形成了由铵盐晶体、腐蚀产物和飞灰颗粒组成的复合污垢层。空气预热器冷端堵塞主要归因于铵盐沉积、飞灰捕集和低温腐蚀的耦合作用。传热模型以100%、75%、50%和40%汽轮机热耗验收工况(THA)作为边界条件进行模拟,结果表明,将一次风流量由基准值的100%降至70%对凝结风险的影响有限;相比之下,当一次风流量维持在基准值的80%时,适度降低二次风流量可显著提高出口烟气温度,并促使凝结区域下移、范围缩小。因此,空气预热器冷端堵塞的防控策略应将温度提升、风量协同调控与吹灰措施纳入周期性运行管理,以降低黏性铵盐持续胶结作用及反复热冲击对换热元件造成的损伤。

       

      Abstract: Against the background of new power systems and next-generation coal-fired power upgrading, ensuring the safe operation and improving the operating economy of deep peak-shaving units are of great importance. To investigate ash deposition, blockage, and corrosion in air preheaters and to reveal the formation mechanisms of deposits at different elevations, a four-sector rotary air preheater in a 2×660 MW coal-fired power plant was selected as the research object. XRD, XRF, SEM-EDS mapping, and XPS were used to characterize the phase composition, micro-morphology, elemental distribution, and surface chemical states of deposits collected from the middle and bottom sections. The heat-transfer model was established to evaluate the condensation risk. The results show that the mass fractions of Fe2O3 in the middle and bottom deposits were 51.66% and 42.68%, while those of SiO2 were 24.00% and 29.98%, respectively. The SO3 content in the bottom deposits was 9.19%, approximately 3.9 times that in the middle deposits (2.35%). The middle deposits mainly exhibited a composite deposition structure composed of fly ash particles and iron oxides, whereas the bottom deposits formed a composite fouling layer consisting of ammonium salt crystals, corrosion products, and fly ash particles. Cold-end blockage of the air preheater was attributed to the coupled effects of ammonium salt deposition, fly ash capture, and low-temperature corrosion. With 100%, 75%, 50%, and 40% turbine heat acceptance (THA) used as boundary conditions, the model showed that reducing the primary air flow rate from 100% to 70% of the baseline value had only a limited effect. In contrast, when the primary air flow rate was maintained at 80% of the baseline value, a moderate reduction in the secondary air flow rate significantly increased the outlet flue gas temperature and shifted the condensation zone downward while narrowing its range. Therefore, mitigation strategies should integrate temperature elevation, coordinated regulation of air flow rates, and soot blowing into periodic operation management, so as to reduce continuous cementation by viscous ammonium salts and damage to heat-transfer elements caused by repeated thermal shock.

       

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