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燃煤流化床钙基脱硫剂对NO转变率的影响及机理 被引量:7

Influence and Mechanism of Calcium-based Desulfurizer on NO Conversion in Fluidized Bed of Coal
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摘要 在1 5 0mm× 1 0 0 0mm流化床试验台上 ,温度区间 84 0℃~ 960℃ ,研究了钙基脱硫剂品种、粒径和Ca/S比对NO转变率的影响 .阐述了钙基脱硫剂使NO转变率增加机理 .试验发现 ,同等质量钙基脱硫剂使NO增加的次序为氧化钙、石灰石、方解石 ;Ca/S比越大 ,NO转变率越高 ;粒径为 1~ 2mm时NO转变率最大 ,2~ 3mm时次之 ,0 2~ 1mm时最小 .加入脱硫剂降低了HCl、HF、SO2 的浓度 ,导致O、H、HO2 浓度升高 ,CO的氧化反应加速 ,在床料、燃料灰催化作用下CO与NO的反应减慢 。 On the experimental table of fluidized bed which scale was  150mm×1000mm and temperature interval was from 840℃ to 960℃,the influence of desulfurizer variety,particle size and molar ratios Ca/S on nitrogen conversion to NO were studied.This paper elaborated on the mechanism of calcium-based desulfurizer lead to the increase of NO conversion rate.Experiment presented that given identical quantities,burnt calcium had maximum NO conversion rate,then limestone,calcite last.Nitrogen conversion to NO increased with increasing molar ratios Ca/S.When the particle size was between 1~2mm,the NO conversion rate was the maximum,second was 2~3mm,the last 0.2~1mm.HCl,HF,SO 2 decreased with calcium addition.At the same time H,OH,HO 2 radicals increased.The CO oxidation was favored,the reaction of monoxide and NO catalyzed by char,sand,ash will weaken,therefore NO content will increase.
出处 《环境科学》 EI CAS CSCD 北大核心 2003年第1期143-146,共4页 Environmental Science
基金 国家自然科学基金资助项目 ( 5 983 62 10 ) 浙江省青年科技人才专项资金项目 (RC990 41)
关键词 燃煤流化床 钙基脱硫剂 NO 转变率 转变机理 一氧化氮 废气处理 fluidized bed calcium-based desulfurizer nitrogen conversion to NO mechanism
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  • 1Jensen A, Johnson J E, Dam-Johansen K. Formation of NO and nitrous oxide form homogeneous oxidation of hydrogen cyanide at the fluidized bed combustion conditions. Proc. 12th Int. Conf. on FBC. Rubow L N and commonwealth G. San Diego: ASME Press, 1993,447~454.
  • 2成,曹欣玉,李绚天等.The influence oflimestone addition on NOx emission during sulfur retention in fluidized bed com bustion. In: Ed. Feng J K. Coal combustion. 1988,947~954.
  • 3Amand L E, Andersson S. Emission of Nitrous Oxide from Fluidized Bed Boilers. In:Proc. of 10th Int. Conf. on Fluidized Bed combustion. ASME, 1989,49~55.
  • 4Hayhurst A N, Lawrence A D. The Effect of Solid CaO on the Production of NOx and N2O in Fluidized Bed Combustors: Studies Using Pyridine as a Prototypical Nitrogenous Fuel. Combustion and Flame, 1996,105: 511~527.
  • 5Hiltunen M, Kilpinen P, Hupa M. N2O emission from CFB boilers: Experimental results and chemical interpretation.Proc. 11th Int. conf. on FBC. Ed. Anthony E J. Montreal,Canada: ASME Press, 1991,678~694.
  • 6岑可法等.循环流化床锅炉理论设计与运行.北京:中国电力出版社,1997.398-399.
  • 7刘皓,陆继东,冯波,刘德昌.流化床煤燃烧N_2O,SO_x及NO_x的消减[J].华中理工大学学报,1996,24(11):103-106. 被引量:5
  • 8Liu H, Gibbs B M. The influence of calcined limestone on NOx and N2O emissions from char combustion in fluidized bed combustors. Fuel, 2001,80: 1211~1215.
  • 9Hampart Soumian E,W nimmo. Nitrogen sulfur interaction in coal flame. Fuel,2001,80:887~897.
  • 10Francesco Miccio, Gerhard Loffler. The influence of SO2 level and operating conditions on NOx and N2O emissions during fluidized bed combustions of coal. Fuel, 2001,80:1555~1566.

二级参考文献1

  • 1刘皓,华中理工大学学报,1995年,23卷,5期,110页

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