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粟刚1 李瑞平2 齐荷梅3

Study on Collaborative Operation Optimization of Limestone-Gypsum Wet Flue Gas Desulfurization and SCR Denitration

  • 摘要: 在燃煤电厂深度减排与灵活调峰背景下,烟气脱硫脱硝系统转向高效低耗的精细化调控。以2×660MW超超临界燃煤机组为对象,围绕石灰石—石膏湿法脱硫与选择性催化还原脱硝工艺,梳理关键参数对系统性能的影响。实践表明,将吸收塔浆液pH值分区控制在5.6-5.8、密度维持在1080-1140kg/m³、液气比动态适配8.5-12.5L/m³,可在保证脱硫效率的同时降低厂用电率;脱硝侧通过优化喷氨,将氨逃逸浓度控制在3μL/L以下,延缓空预器堵塞。研究成果可为同类型机组提供技术参照。

     

    Abstract: Against the background of simultaneous deep emission reduction and flexible peak regulation in coal-fired power plants, the operation of flue gas desulfurization and denitration systems has shifted from simple compliance with environmental standards to refined regulation featuring high efficiency, low consumption and collaboration. Taking a typical 2×660MW ultra-supercritical coal-fired unit as the research object, focusing on the two core processes of limestone-gypsum wet flue gas desulfurization and selective catalytic reduction (SCR) denitration, this paper systematically sorts out the influence rules of key parameters such as absorption tower slurry quality, liquid-gas ratio, oxidation air volume, SCR reactor temperature window and ammonia injection uniformity on system performance. Operation practice shows that controlling the pH value of the absorption tower slurry in the range of 5.6-5.8 by load interval, maintaining the slurry density at 1080-1140kg/m3, and dynamically adjusting the liquid-gas ratio within 8.5-12.5L/m3 can significantly reduce the plant power consumption rate while ensuring desulfurization efficiency. On the denitration side, by optimizing the distribution of ammonia injection grid and ammonia-nitrogen molar ratio, the ammonia slip concentration is controlled below 3μL/L, which effectively delays the blockage of air preheater. The research results can provide technical reference for ultra-low emission and economic operation of similar units.

     

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