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高压鼓泡反应器中NOx吸收过程及建模 被引量:1

NOx Absorption Process and Modeling in High Pressure Bubbling Reactor
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摘要 基于鼓泡反应器对NOx吸收中气相NO、NO2和HNO2,液相NOx进行量化,实现NOx质量守恒的测量,误差在±8%以内.建立三区反应模型,以气相出口NO和NO2测量值与模拟值的相对误差为目标函数,获得了最优NO2和NO传质系数、NO氧化动力学常数、液膜体积和表面积等参数.液膜区中HNO3浓度是鼓泡区的193-357倍;NO2和NO吸收分别受气相扩散和液相控制;NO氧化反应受压力影响大,主要是链式反应控制;反应器中液膜产生的本质猜测是气泡夹带的液滴吸附于内表面. Based on the quantification of gas phase NO,NO2,and HNO2,and liquid phase NOx in a bubbling reactor,NOx balance measurement was achieved with a relative error within±8%.A three-region reaction model was set up.The relative errors between the measured and modeled NO and NO2 at the outlet of gas phase were chosen as the objective function to obtain the optimum parameters,including NO2 and NO mass transfer coefficients,NO oxidation rate constant,and volume and surface area of liquid film.The concentration of HNO3 in the liquid film region was 193—357 times of that in the bubbling region.The absorption of NO2 and NO was controlled by gas and liquid diffusion,respectively.NO oxidation reaction was greatly influenced by reactor pressure and controlled dominantly by chain reactions.The formation of liquid film region in the reactor was presumably due to gas bubbling entrainment and attachment onto the inner surface of the reactor.
作者 王文杰 刘敦禹 李伟 李骋 程潜 陈军 金晶 Wang Wenjie;Liu Dunyu;Li Wei;Li Cheng;Cheng Qian;Chen Jun;Jin Jing(Shanghai Xianyuan Environmental Technology Co.,Ltd,Shanghai 200000,China;School of Energy and Power Engineering,University of Shanghai for Science and Technology,Shanghai 200093,China;Shanghai Key Laboratory of Multiphase Flow and Heat Transfer in Power Engineering,Shanghai 200093,China)
出处 《燃烧科学与技术》 EI CAS CSCD 北大核心 2020年第5期482-492,共11页 Journal of Combustion Science and Technology
基金 国家自然科学基金资助项目(51706143) 上海市浦江人才资助项目(16PJ1407900)。
关键词 鼓泡反应器 NO吸收 建模 bubbling reactor NO absorption modeling
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  • 1王曼,李冬,梁瑜海,吴迪.紫外分光光度法测定水中硝酸盐氮的试验研究[J].环境科学与技术,2011,34(S1):231-234. 被引量:20
  • 2张晓燕,李慧敏,李志强.铬酸钡光度法测定硫酸盐的改进研究[J].环境科学与管理,2006,31(4):82-83. 被引量:3
  • 3任晓莉,赵林,杨宝强.NO_x废气吸收的板式塔模型[J].化学工程,2007,35(9):13-16. 被引量:6
  • 4Anam R J, Spilsbury C G. 1992. A study of the extraction of CO2 from the flue gas of a 500MW pulverized coal fired boiler [ J ]. Energy Conversion and Management, 33 ( 5/8 ) : 373-378.
  • 5Fleig D,Normann F,Andersson K,et al. 2009. The fate of sulphur during oxy-fuel combustion of lignite[ J-. Energy Proeedia, 1 ( 1 ) :383-390.
  • 6Croiset E, Thambimuthu K V. 2001. NOx and SO2 emissions from O2/ CO2 recycle coal combustion[J]. Fuel, 80(14) : 2117-2121.
  • 7Andersson K, Johnsson F. 2006. Process evaluation of an 865MW lignite fired O2/CO2 power plant[ J-. Energy Conversion and Management, 47(18) : 3487-3498.
  • 8Robert N. O'Bfien. 1998. Liquid phase conversion of a source of sulfur dioxide to sulfuric acid[ P]. US, 5788949. 1998-8-4.
  • 9阎维平,鲁晓宇,高正阳,等.2010b.在富氧燃烧锅炉烟气CO2捕集中回收SO2与NO的系统[P].中国.201010174003.9.2010-09-22.
  • 10Zhou Y Y, Qian F, Fu Y. 2006. Investigation into interaction between SO2 and NO2 in flue gas[ J]. Environmental Science & Technology, 29(9) :32-40.

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