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循环流化床颗粒团多参数的光散射测量方法 被引量:3

Light scattering measurement method for multi-parameters of particle clusters in circulating fluidized bed
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摘要 针对循环流化床床内颗粒团动态参数和行为特性的测量问题,提出了基于光散射原理的颗粒团运动速度、高度与浓度等多参数同时在线测量方法,利用该方法对二维冷态循环流化床试验台开展颗粒团参数测量,获得了颗粒经测量区造成的光强衰减信号,通过对上下测量单元光强信号进行互相关分析可获得颗粒团运动速度参数;对信号进行低通滤波,根据低频信号极值点时间差及运动速度测量结果,得到颗粒团高度参数;同时根据光强衰减程度计算颗粒团的浓度参数。由此实现了基于光散射原理的循环流化床床内颗粒团运动速度、高度与浓度多参数同时在线测量,测量结果显示,在典型工况下,提升管中心区域颗粒团运动速度较为稳定,平均速度为3.81 m/s,近壁面区域颗粒团运动速度有较大波动且出现负值,平均速度为0.65 m/s;中心区域颗粒浓度较近壁面区域小;中心区域颗粒团高度主要分布在20~40 mm区间,近壁面区域颗粒团高度主要分布在30~60 mm区间。这为循环流化床内颗粒团的形成、结构及其运动研究提供了一种有效的测量手段。 Aiming at the measurement issue of dynamic parameters and behavior characteristics of particle clusters in circulating fluidized bed(CFB),a multi-parameter simultaneous on-line measurement method of velocity,height and concentration of particle clusters based on light scattering principle is proposed.This method is used to measure the parameters of particle clusters in a two-dimensional cold test bench of CFB.The light attenuation signal caused by particle clusters flowing through the measurement zone is obtained.The velocity of particle clusters is obtained from the cross-correlation analysis of the light intensity signals of the upper and lower measurement units.The signal is filtered with low-pass filter,and the height of particle clusters is obtained according to the time difference of the extreme points of the low-frequency signal and the measurement results of motion velocity.At the same time,the concentration is calculated according to the light intensity attenuation.Thus,the multi-parameter on-line measurement of velocity,height and concentration of particle clusters in CFB is realized based on light scattering.The measurement results show that under typical working condition,the velocity of particle clusters in the central zone of riser is quite stable,and the average velocity is 3.81 m/s.The motion velocity of particle clusters in the near wall zone has large fluctuations,even is negative,and the average velocity is 0.65 m/s.The concentration of particle clusters in the central zone is less than that in the near wall zone.The height of particle clusters in the central zone is mainly distributed in the range of 20~40 mm,and the height of particle clusters in the near wall zone is mainly distributed in the range of 30~60 mm.The results provide an effective measurement method for studying the formation,structure and motion of particle clusters in CFB.
作者 杨斌 张驰 平力 殷上轶 姜勇俊 Yang Bin;Zhang Chi;Ping Li;Yin Shangyi;Jiang Yongjun(School of Energy and Power Engineering/Shanghai Key Laboratory of Multiphase Flow and Heat Transfer in Power Engineering,University of Shanghai for Science and Technology,Shanghai 200093,China;School of Energy and Mechanical Engineering,Nanjing Normal University,Nanjing 210042,China)
出处 《仪器仪表学报》 EI CAS CSCD 北大核心 2021年第10期20-26,共7页 Chinese Journal of Scientific Instrument
基金 国家重点研发计划(2016YFB0600601)项目资助。
关键词 多相流测量 循环流化床 颗粒团 光散射 互相关法 multi-phase flow measurement circulating fluidized bed particle cluster light scattering cross-correlation method
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  • 1蒋泰毅,熊友辉.气固两相流速度及质量流量的静电测量法研究[J].华中科技大学学报(自然科学版),2005,33(1):93-95. 被引量:14
  • 2魏飞,罗序昆,金涌,俞芷青,汪展文.运动颗粒团一维连续成像分析系统[J].高校化学工程学报,1994,8(4):360-364. 被引量:3
  • 3阮晓东,刘志皓,瞿建武.粒子图像测速技术在两相流测量中的应用研究[J].浙江大学学报(工学版),2005,39(6):785-788. 被引量:20
  • 4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
  • 5Kim 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.
  • 6Contractor 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.
  • 7Mei 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.
  • 8Morton 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.
  • 9Rogers 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.
  • 10Kim 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.

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