期刊文献+

提升管送风特性对充分发展段压降影响的实验及模型研究

Research on Effect of Air Characteristics to Riser of DCFB on Pressure Drop of Fully Developed Zone and Prediction Model
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摘要 双循环流化床提升管床降随着固气质量比的增加而增加。搭建了双循环流化床实验台,系统地分析了提升管送风特性对充分发展段压降的影响规律。结果发现:充分发展段压降随着提升管风速的增加逐渐增大;径向送入二次风产生的压降比风口切向布置时大;风口高度较低时产生的压降较大;随着二次风口数目增加,压降有增加趋势,设置的4种情况下实测压降平均变化率分别为12.28%、2.76%、13.16%和6.96%。建立了提升管充分发展段压降模型,计算发现:实测压降与计算值存在偏差,风口数目影响下二者的偏差较小,平均相对误差仅为3.13%,最大相对误差3.95%,风口高度影响下差距较大,平均相对误差为4.27%,最大相对误差为5.36%。 Pressure drop in a double circulating fluidized bed riser increased with the solid-gas mass ratio.A DCFB cold-state test bench and a pressure drop model were set up.This paper systematically tested the gas-solid flow pressure drop in fully developed zone affected by air characteristics.It shows that the pressure drop increased with the gas velocity of the riser and the same trend was found when the number of tuyeres increased.The drop was greater when the tuyeres were tangential arranged than it was radial arranged.The pressure gradient emerged a bigger drop when the tuyeres were lower from the distribution.The mean change rate was 12.28%,2.76%,13.16% and 6.96%,respectively in the four circumstances that the paper set.It shows that the tested value had a gap with the value calculated by model in fully developed zone,and the gap differ from affected factors.It showed a lower discrepancy affected by numbers of tuyeres,the mean relative error is 3.13% and the maximum relative error is 3.95%.But the mean relative error and the maximum relative error is comparatively larger affected by heights of tuyeres,which are 4.27% and 5.36%,respectively.
出处 《电站系统工程》 北大核心 2011年第5期5-7,共3页 Power System Engineering
基金 国家自然科学基金(50876030) 高校博士点基金(20090036110008)
关键词 提升管 送风特性 充分发展段 压降 模型 riser characteristics of air supply model fully developed zone pressure gradient model
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参考文献9

  • 1Priyanka Kaushal, Tobias Proll, Hermann Hofbauer. Model for biomass char combustion in the riser of a dual fluidized bed gasification unit: Part I-Model development and sensitivity analysis [J]. Fuel Processing Technology, 2008, 89:651"-659.
  • 2王小芳,金保升,钟文琪.高通量循环流化床上升管气固流动特性实验研究[J].中国电机工程学报,2009,29(17):27-31. 被引量:17
  • 3Issangya A S. Flow dynamics in high density circulating fluidized beds [D]. Vancouver: University of British Columbia, 1998.
  • 4Arena U, Cammarota A, Pistone L. High velocity fluidization behavior of solids in a laboratory scale circulation fluidized bed [M]. Toronto: Pergamon Press, 1986. 119- 125.
  • 5Wirth K E, Seiter M, Molerus Q. Concentration and velocities of solids in areas close to the walls in circulating fluidized bed systems [J]. Chemical Engineering and Technology, 1991, 14: 824-828.
  • 6Priyanka Kaushal, Tobias Proll, Hermann Hofbauer. Model development and validation: Co-combustion of residual char, gases and volatile fuels in the fast fluidized combustion chamber of a dual fluidized bed biomass gasifier [J]. Science Direct, 2007, 86: 2687-2695.
  • 7M K Karmakar, A B Datta. Hydrodynamics of a dual fluidized bed gasifier [J]. Advanced Powder Technology, 2010, 2(1): 1 -8.
  • 8Mitali Das, Amrita Bandyopadhyay, B C Meikap, et al. Axial voidage profiles and identification of flow regimes in the riser of a circulating fluidized bed [J]. Chemical Engineering Journal, 2008, 145: 249-258.
  • 9W Yang. A correlation for solid friction factor in vertical pneumatic conveying; lines [J]. AIChEJ, 1978, 24: 548-552.

二级参考文献20

  • 1许明磊,严建华,马增益,王勤,孙巍,岑可法.循环流化床垃圾焚烧炉固体残留物的特性研究[J].中国电机工程学报,2007,27(8):16-21. 被引量:9
  • 2Kim S W, Kirbas G, Bi H, et al. Flow behavior and regime transition in a high-density circulating fluidizedbed riser[l]. Chemical Engineering Science. 2004, 59(18): 3955-3963.
  • 3Contractor R M, Patience G S, Garnett D I. A new process for n-butane oxidation to maleic anhydride using a circulating fluidized- bed Reactor[J]. International Conference on Circulating Fluidized Beds4th, NewYork, America, 1994, 387-391.
  • 4Mei J S, Shadle L J, Yue P, et al. Hydrodynamics of a transport reactor operating in dense suspension upflow conditions for coal combustion applications[C]. The 18th International Conference on Fluidized Bed Combustion, Toronto, Canada, 2005: 423-431.
  • 5Morton F, Pinkston T, Salazar N, et al. Orlando gasification project: Demonstration of a nominal 285 MW coal-based transport gasifier [C]. 23rd Annual International Pittsburgh Coal Conference, Pittsburgh, America, 2006: 10-18.
  • 6Rogers L H, Booras G S, Breault R W. Power systems development facility update on six trig studies[C]. 23rd Annual International Pittsburgh CoalConference, Pittsburgh, America, 2006: 16-26.
  • 7Kim J S, Tachino R, Tsutsumi A. Effects of solids feeder and riser exit configuration on establishing high density circulating fluidized beds [J]. PowderTechnol, 2008, 187(1).. 37-45.
  • 8Du B, Warsitio W, Fan L S. Behavior of the dense-phase transportation regime in a circulating fluidized bed[J]. Ind. Eng. Chem. Res., 2006, 45(10): 741-751.
  • 9Luo Z, Zhao Y, Chen Q, et al. Effect of gas distributor on performance of dense phase high density fluidized bed for separation [J]. Int. J. Miner. Process, 2004, 74 (1-4): 337-341.
  • 10Issangya A S, Bai D, Bi H T, et al. Suspension densities in a high-density circulating fluidized bed riser[J]. Chemical Engineering Science, 1999, 54(22): 5451-5460.

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