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循环流化床锅炉二次风射流特性的冷模实验研究 被引量:5

Cold Model Experiments on the Characteristic of Secondary Air Injection in CFB Boiler
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摘要 循环流化床二次风的主要作用是为燃料补充燃烧所需的氧气和加强燃料在炉内的扰动,对锅炉燃烧效率有重要的影响。在一个可视化的循环流化床实验装置上进行了炉内物料浓度、二次风喷口直径和风速对二次风射程与扩散影响的冷模实验。采用向炉内送入高温二次风,然后通过布置在二次风平面的热电偶来测量炉内温度变化的方法,间接反映二次风的射程和扩散情况。结果表明,在固体颗粒浓度一定时,最大射流深度、扩散程度与二次风动量成正比;二次风动量一定时,最大射流深度、扩散程度与固体颗粒浓度成反比。 In circulating fluidized bed (CFB), the main motivation of the secondary air (SA) is providing enough oxygen of combustion and enhancing the disturbance of fuel. SA affects the combustion efficiency of circulating fluidized bed obviously. Cold model experiments on the relationship of particle density, SA injection velocity, diameter of nozzle and characteristic of SA injection studied in a visual cold experimental apparatus. The range and diffusion of SA injection is represented by the temperature change of the thermocouple in CFB boiler. The experimental results show that the max range and diffusion of SA injection is in direct ratio to the momentum of SA injection when particle density remains steady, and in inverse ratio to the particle density when the momentum of SA injection remains steady.
出处 《电站系统工程》 北大核心 2007年第3期11-14,共4页 Power System Engineering
关键词 循环流化床 二次风 颗粒浓度 动量 射程 扩散 CFB secondary air particle density momentum range diffusion
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  • 1吕俊复,金晓钟,杨海瑞,刘青,岳光溪.循环流化床锅炉煤燃烧效率研究(英文)[J].应用基础与工程科学学报,2000,8(1):97-105. 被引量:5
  • 2岑可法,方梦祥,骆仲泱,李绚天,陈飞,王勤辉,陈冠益,倪明江.循环流化床热电气三联产装置研究[J].工程热物理学报,1995,16(4):499-502. 被引量:22
  • 3周一工.国内循环流化床锅炉运行中的问题及原因探讨[J].锅炉技术,1995(1):2-4. 被引量:5
  • 4王勤辉.循环流化床锅炉总体数学模型及性能试验.浙江大学博士论文[M].,1997..
  • 5Johnsson J E. Dam-Johansen Kim. Formation and reduction of NOx in a fluidized bed combustor[A]//Basu P, Large J F(eds). Proceeding of the 3rd international conference on Circulating fluidized Bed Technology[ C]. Oxford,Pergamon Press, 1991 : 1389-1396.
  • 6Zhang W N, Johnsson F, Bo Leekner. Fluid-dynamic boundary layers in CFB boilers[J]. Chem Eng Sci, 1995, 50(2) : 201-210.
  • 7Zhou J, Grace J R, Oin S, et al. Particle velocity profiles in a circulating fluidized bed of square cross-section [ J ].Chem Eng Sci, 1995,50(2) : 237-244.
  • 8Lu Jun fu , Yue Guangxi, Liu Qing, et al. Solid suspension density distribution in the furnace of 75t/h circulating fluidized bed boiler with water-cooled square separator [ A ]//Chen Xuejun, Chen Tingkuan, Chen Zhongqi ( eds ).Prooeeding of 4th international symposium of multiphase flow and heat transfer[ C]. Xi'an, Jiaotong University Press,1999:276-284.
  • 9吕俊复,清华大学学报,1998年,38卷,5期,8页
  • 10李广海,硕士学位论文,1994年

共引文献33

同被引文献47

  • 1侯祥松,杨海瑞,吕俊复,岳光溪.循环流化床中气体扩散规律的研究[J].锅炉技术,2004,35(5):16-20. 被引量:4
  • 2钟文琪,章名耀.喷动流化床射流穿透深度试验研究[J].东南大学学报(自然科学版),2005,35(1):29-34. 被引量:11
  • 3张彦军,李振宇,王凤君,姜义道,于龙.国产首台300 MW循环流化床锅炉设计和运行实践[J].锅炉制造,2006(4):10-13. 被引量:6
  • 4U.S. Clean Coal Technology Demonstration Program. The JEA large-scale CFB combustion demonstration project [R]. Pittsburgh:U.S. Department of Energy and JEA, 2003.
  • 5VENALAINEN I, PSIK R. 460MWe supercritical CFB boiler design for agisza power plant [R]. Barcelona: POWER GEN Europe, 2004.
  • 6ERSOY L E, GOLRIZ M R, KOKSAL M, et al. Circulating fluidized bed hydrodynamics with air staging: an experimental study [J]. Powder Technology, 2004, 145 (1): 25 - 33.
  • 7KIM J H, SHAKOURZADEH K. Analysis and modelling of solid flow in a closed loop circulating fluidized bed with secondary air injection [J]. Powder Technology, 2000, 111(3) : 179 - 185.
  • 8ARASTOOPOUR H. Numerical simulation and experimental analysis of gas/solid flow systems [J]. Powder Technology, 2001, 119(2/3) : 59 - 67.
  • 9FARIBORZ T, NAOKO E, CLAYTON W. Experimental and computational study of gas-solid fluidized bed hydrodynamics [J]. Chemical Engineering Science, 2005, 60(24): 6857-6867.
  • 10CRUZ E, STEWARD F R, PUGSLEY T. New closure models for CFD modeling of high-density circulating fluidized beds [J]. Powder Technology, 2006, 169 (3) : 115 - 122.

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