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    垃圾焚烧发电联合脱硝过程分析

    Analysis of the combined denitrification process in waste incineration power generation

    • 摘要: 随着国家节能减排的深入推进和环保法规的日益严格,生活垃圾焚烧发电行业烟气排放逐步推行超低排放要求,NOx浓度控制已成为必须解决的问题。为研究垃圾焚烧电厂的烟气脱硝过程,搭建垃圾焚烧发电联合脱硝系统模型,并验证模型的合理性。选取不同含水率垃圾作为燃料,研究氨氮比、过量空气系数对垃圾焚烧炉的燃烧特性、联合脱硝系统的喷氨量、脱硝效率以及氨逃逸的影响。结果表明:在过量空气系数为1.7时, MSW1、MSW2和MSW3燃料工况下的SNCR和SCR最佳氨氮比分别为1.6、1.5、1.2和0.94、0.86和0.78;随着垃圾含水率升高,炉膛烟气水分含量上升、SNCR反应温度下降、SNCR脱硝效率上升,SCR反应温度和脱硝效率下降;随着过量空气系数增大,炉膛温度下降、炉膛上部烟气中的NOx质量浓度降低、SNCR喷氨量减少、SCR反应温度和喷氨量降低。

       

      Abstract: With the deepening of national energy conservation and emission reduction efforts and the increasingly stringent environmental protection regulations, the incineration of household waste for power generation has gradually adopted the ultra-low emission requirements, and NOx concentration control has become a problem that must be addressed. To investigate the flue gas denitrification process in waste incineration power plants, a combined denitrification system model for waste incineration power generation was established and its validity was verified. Different moisture content levels of municipal solid waste (MSW) were selected as fuels to study the effects of ammonia-to-nitrogen ratio and excess air coefficient on the combustion characteristics of the waste incinerator, ammonia injection rate, denitrification efficiency, and ammonia slip in the combined denitrification system. The results show that, when the excess air coefficient is 1.7, the optimal ammonia-to-nitrogen ratios for the SNCR and SCR systems under MSW1, MSW2, and MSW3 fuel conditions are 1.6, 1.5, 1.2 and 0.94, 0.86, 0.78, respectively. As the moisture content of the waste increases, the water content of the flue gas in the furnace increases, the SNCR reaction temperature decreases, and the SNCR denitrification efficiency increases, while the SCR reaction temperature and denitrification efficiency decrease. As the excess air coefficient increases, the furnace temperature decreases, the mass concentration of NOx in the flue gas at the top of the furnace is reduced, the amount of ammonia injected by the SNCR decreases, the reaction temperature and the amount of ammonia injected by the SCR are lowered.

       

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