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不同进口形式方形分离器的试验研究 被引量:3

Experimental Study of a Square-shaped Separator with Different Inlet Forms
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摘要 通过改变分离器进气形式,对方形分离器的性能进行了试验研究。结果表明:各分离器的切割粒径,随进口风速的增大而减小(见图5),随进口颗粒浓度的增大先减小后增大(见图7、图9);各分离器的阻力,随进口风速的增大而增大(见图6),随进口颗粒浓度的增大而减小(见图8、图10)。在分离特性方面,正切向单进口形式优于正切向双进口,在斜切向双进口形式优于斜切向单进口,正切向进气形式优于斜切向进气。在阻力方面,正切向双进口形式优于正切向单进口,斜切向单进口形式优于斜切向双进口,斜切向进气形式优于正切向进气。研究结果为方形分离器结构的优化设计提供了依据。 By changing the steam inlet forms of a separator,an experimental study has been conducted of the performance of a square-shaped separator.The results of the study indicate that the cut particle diameter of various separators decreases with an increase of inlet air speed (see Fig.5) and with an increase of the particle concentration at the inlet,the particle diameter first decreases and then increases (see Fig.7 and 9).The drag forces of various separators increase with an increase of the inlet air speed (see Fig.6) and decrease with an increase of the inlet particle concentration (see Fig.8 and 10).With respect to separation characteristics,the single inlet form of tangential direction is better than the double inlet form of the said direction; the double inlet form of oblique tangential direction is superior to the single inlet form of the said direction.The inlet form of the tangential direction is better than the inlet of the oblique tangential direction.As for the drag forces,the double inlet form of the tangential direction is better than the single inlet form of the aforementioned direction; the single inlet form of the oblique tangential direction is superior to the double inlet form of the said direction and the gas inlet form of the oblique tangential direction is better than that of the tangential direction.The research results can provide an underlying basis for the structural optimization design of square-shaped separators.
出处 《热能动力工程》 EI CAS CSCD 北大核心 2008年第3期293-297,共5页 Journal of Engineering for Thermal Energy and Power
关键词 循环流化床 分离器 方形旋风分离器 分离机理 分离效率 circulating fluidized bed,separator,square-shaped cyclone separator,separation mechanism,separation efficiency
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参考文献10

  • 1岑可法,倪明江,骆仲泱,等.循环流化床锅炉里路设计与运行[M].北京:中国电力出版社,1998.
  • 2FENG JUNKAI, YUE GUANGXI. New achievements of development of CFBC boilersin china//Proceedings of the intemational conference on energy and environment[ C ]. Shanghai, 1998 : 505 - 510.
  • 3GAMLE R, HYPPANEN T, KAURANEN T. Pyroflow, compact a second generation CFB boiler by ahlstrom pyrop - ower//Proeeeding of the 12^th International Conference on Fluidized Bed Combustion[C] .USA: San Diego California, 1993:751 -760.
  • 4王东,程乐鸣,周强,骆仲泱.卧式热交换式方形分离器分离性能的试验研究[J].热能动力工程,2003,18(3):229-233. 被引量:3
  • 5岑可法 倪明江 骆仲泱 等 中国专利.方形下排气热交换分离器[P].94235842.X.1996—02—07.
  • 6岳光溪,张绪炜,李岩登.带加速段的水冷方形旋风分离器[P].ZL专利号93235842.X,清华大学,1995.
  • 7吕俊复,张守玉,刘青,张建胜,杨海瑞,岳光溪,沈解忠,于龙.循环流化床锅炉的飞灰含碳量问题[J].动力工程,2004,24(2):170-174. 被引量:57
  • 8王玉召,吕俊复,张建胜,刘青,岳光溪,沈解忠,苏小平.220t/h水冷方形分离器循环流化床锅炉的性能[J].动力工程,2005,25(3):343-347. 被引量:7
  • 9余战英,魏铜生,陈晓宇,谭厚章,惠世恩,徐通模.不同结构因素下方形旋风分离器分离性能的实验研究[J].动力工程,2004,24(1):147-151. 被引量:4
  • 10YAXIN SU, YURU MAO. Experimental study on the gas - solid suspension flow in a square cyclone separator [ J ]. Chemical Engineering Journal ,2006, 121:551 - 58.

二级参考文献29

  • 1郑洽余,刘信刚,金燕.循环流化床锅炉燃烧室内焦炭粒子燃烧特性的研究[J].工程热物理学报,1995,16(1):106-110. 被引量:16
  • 2由长福 岳光溪 等.方形分离器三维流场的测定及数值模拟[J].动力工程,1995,15(5):1-6.
  • 3程乐鸣 骆仲泱 方梦祥 等.卧式热交换式方形分离器[P].中国专利:ZL 00201914.0..
  • 4CHENG LEMING, ZHOU QIANG, LUO ZHONGYANG, et al. Development of a horizontal heat-exchanger square cyclone[ A]. CLrculating Huidtzed Bed Technology Ⅶ, Proc ot the 7th Inter Conf on Circulating Ruidlzed Beds [ C ]. Canada: Niagara Falls, Ontario,2002.551 - 558.
  • 5SAHA S K, BASU P, DYITA A. Performance of a novel horizontal gas-solid separator in a circulating fluidized bed riser[ A ]. Circulating Fluidized Bed Technology Ⅶ, Proc of the 7th Inter Conf on Circulating Fluidized Beds[ C] . Canada: Niagara Falls, Ontario, 2002.567 - 574.
  • 6陈江波 曹柏林.方形下排气分离器的流场与分离机理[C]..中国工程热物理学会燃烧学术会议论文[C].,1995..
  • 7姚建奎.新型旋风分离器的研究[C]..中国工程热物理学会多相流热物理学术会议论文[C].,1991..
  • 8Li Yong,Yue Guangxi,Lu Junfu,et al.An investigation of carbon loss of boilers burning hard coals[C].In:Donald W Geiling,Donald L Bonk eds.Proceeding of 16th International Conference on Fluidized Bed Combustion,ASME,2001,Nevada[CD].
  • 9Li Y,Zhang J,Liu Q,et al.A study of the reactivity and formation of the unburnt carbon in CFB fly ashes[J].Developments in Chemical Engineering and Mineral Processing,2001(9):3-4.
  • 10李玮琪 吕俊复 凌晓聪.循环流化床中飞灰碳形成的模型研究[C]..中国电机工程学会第四届青年学术会议论文集[C].,2002-10..

共引文献64

同被引文献38

  • 1王玉召,吕俊复,张建胜,刘青,岳光溪,沈解忠,苏小平.220t/h水冷方形分离器循环流化床锅炉的性能[J].动力工程,2005,25(3):343-347. 被引量:7
  • 2王玉召,王启民,吕俊复,岳光溪.带入口加速段的方形分离器内气固两相流动数值模拟[J].中国电机工程学报,2007,27(11):45-49. 被引量:9
  • 3SHIBAGAKI G, AKIO N. Foster wheeler Circulating Fluidized Bed (CFB) boilers in pulp & paper industries and the recent technology development[ J ]. Japanese Journal of Paper Technology, 1999, 42(5), 59 - 64.
  • 4MAKKONEN P, FOSTER W. CFB with the new superheater[J]. VGB Power Tech, 2000, 80(2), 30-34.
  • 5DE S, NAG P K. Pressure drop and collection efficiency of cyclone and impact separators in a CFB[J]. Int J Energy Research, 1999, 23(1) : 51 -60.
  • 6SHIN M S, KIM H S, JANG D S, et al. Numerical and experimental study on a high efficiency cyclone dust separator for high temperature and pressurized environments [ J ]. Applied Thermal Engineering, 2005, 25(11/12) : 1821 - 1835.
  • 7HU L Y, ZHOU 1, X, ZHANG J, et al, Studies on strongly swirling flows in the full space of a volute cyclone separator [ J ]. AIChE Journal, 2005, 51(3): 740- 749.
  • 8ZHANG R, BASU P. Simple model for prediction of solid collection efficiency of a gas-solid separator [ J ]. Powder Technology, 2004, 147(1/2/3) : 86 - 93.
  • 9ZHAO B T. A theoretical approach to pressure drop across cyclone separators [ J ]. Chemical Engineering and Technology, 2004, 27(10) : 1105- 1108.
  • 10SU Y X, M Y R. Experimental study on the gas-solid suspension flow in a square cyclone separator [ J ]. Chemical Engineering Journal, 2006, 121(1): 51-58.

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