湍动流化床过渡段中颗粒速度分布的光纤测量与模拟Particle Velocity Measurements in Transition Section of Turbulent Fluidized Beds Using Optical Fiber Probe and CFD Simulation
吴诚,高用祥,高希,成有为,王丽军,李希
摘要(Abstract):
流化床中颗粒速度的测量一直是个技术上的难点。今针对光纤测量信号提出一种基于互相关原理的时均速度计算方法。考虑到数据分段计算时其可靠性方面的差异,将互相关系数作为第二权重因子引入时均速度计算公式。利用PV6D光纤探针在200 mm直径流化床中测得的原始信号,对比了三种数据处理方法所得的颗粒时均速度,并分别计算其床层截面颗粒净流率,说明提出的方法可靠性更高。据此测量了流化床过渡段不同高度处颗粒时均速度的径向分布,并采用修正的三段曳力模型来描述具有团聚行为的颗粒曳力,进行计算流体力学模拟。测量与模拟结果均表明,从过渡段到稀相段,床中心区的颗粒速度先降低后升高,其径向分布也从陡峭变平缓,然后再次趋于陡峭。颗粒速度分布的上述规律主要由固含率与气速的径向分布共同作用所致。
关键词(KeyWords): 流化床;颗粒速度;光纤;计算流体力学
基金项目(Foundation): 国家自然科学基金(U1162125);; 中央高校基本科研业务费专项资金(2013QNA4035)
作者(Author): 吴诚,高用祥,高希,成有为,王丽军,李希
参考文献(References):
- [1]Werther J.Measurement techniques in fluidized beds[J].Powder Technol,1999,102(1):15-36.
- [2]Kwauk Moo-son(郭慕孙),LI Hong-zhong(李洪钟).Handbook of fluidization(流态化手册)[M].Beijing(北京):Chemical Industry Press(化学工业出版社),2007.
- [3]JIN Yong(金涌),ZHU Jing-xu(祝京旭),WANG Zhang-wen(汪展文),et al.Fluidization engineering principles(流态化工程原理)[M].Beijing(北京):Tsinghua University Press(清华大学出版社),2001:453-457.
- [4]Saadevandi B A,Turton R.The application of computer-based imaging to the measurements of particle velocity and voidage profiles in a fluidized bed[J].Powder Technol,1998,98(2):183-189.
- [5]WU Cheng(吴诚),GAO Xi(高希),CHENG You-wei(成有为),et al.Calibration and correction of particle velocity signals in optical fiber measurement(光纤法颗粒速度测量信号的标定与校正)[J].Chemical Reaction Engineering and Technology(化学反应工程与工艺),2013,29(2):105-110.
- [6]WU Cheng(吴诚),GAO Xi(高希),LI Xi(李希),et al.Experimental and numerical study of solids concentration distribution in transition section of turbulent fluidized bed(湍动流化床过渡段固含率分布特征的实验及数值模拟)[J].J Chem Ind and Eng(China)(化工学报),2013,64(3):858-866.
- [7]Gao X,Wu C,Cheng Y W,et al.Experimental and numerical investigation of solid behavior in a gas-solid turbulent fluidized bed[J].Powder Technol,2012,228:1-13.
- [8]Gao X,Wang L J,Wu C,et al.Steady-state simulation of core-annulus flow in a circulating fluidized bed(CFB)riser[J].Chem Eng Sci,2012,78:98-110.
- [9]Aguillon J,Shakourzadeh K,Guigon P.A new method for local solid concentration measurement in circulating fluidized bed[J].Powder Technol,1996,86(3):251-255.
- [10]CHENG Chang-jian(程长建),HUANG Jin(黄晋),SONG Wen-li(宋文立),et al.Measurement of particle velocity in CFB by optical cross-correlation method(光信号互相关法测量循环流化床内颗粒速度的应用研究)[J].The Chinese Journal of Process Engineering(过程工程学报),2004,4(z1):626-633.
- [11]Nieuwland J J,Meijer R,Kuipers J A M.Measurements of solids concentration and axial solids velocity in gas-solid two-phase flows[J].Powder Technol,1996,87(2):l27-139.
- [12]E Cheng-lin(鄂承林),LU Chun-xi(卢春喜),GAO Jin-sen(高金森),et al.A new method for the measurement of solids time-averaged velocity in gas-solid two-phase flow(气固两相流中颗粒时均速度的测量新方法)[J].The Chinese Journal of Process Engineering(过程工程学报),2003,3(6):505-511.
- [13]Gidaspow D.Multiphase flow and fluidization:Continuum and kinetic theory descriptions[M].New York:Academic Press,1994:239-294.
- [14]Van der Hoef M A,van Sint Annaland M,Deen N G,et al.Numerical simulation of dense gas-solid fluidized beds:a multiscale modeling strategy[J].Annual Review of Fluid Mechanics,2008,40:40-70.
- [15]Zhang D Z,Vanderheyden W B.The effects of mesoscopic structures on the macroscopic momentum equations for two-phase flows[J].Int J Multiphase Flow,2002,28(5):805-822.
- [16]Mckeen T,Pugsley T.Simulation and experimental validation of a freely bubbling bed of FCC catalyst[J].Powder Technol,2003,129(1):139-152.
- [17]Wen C Y,Yu Y H.Mechanics of fluidization[J].Chem Eng Prog Symp Ser,1966,62(62):100-110.
- [18]Schiller L,Naumann A.A drag coefficient correlation[J].VDI Zeits,1933,77(51):318-320.
- [19]Lu H L,Gidaspow D.Hydrodynamics of binary fluidization in a riser:CFD simulation using two granular temperatures[J].Chem Eng Sci,2003,58(16):3777-3792.
- [20]Johnson P C,Jackson R.Frictional-collisional constitutive relations for granular materials,with application to plane shearing[J].J Fluid Mech,1987,176:67-93.
- [21]Zhu H Y,Zhu J,Li G Z,et al.Detailed measurements of flow structure inside a dense gas-solids fluidized bed[J].Powder Technol,2008,180(3):339-349.
- [22]Zhu J X,Li G Z,Qin S Z.Direct measurements of particle velocities in gas-solids suspension flow using a novel five-fiber optical probe[J].Powder Technol,2001,115:184-192.
- [23]QI Xiao-bo(漆小波),HUANG Wei-xing(黄卫星),ZHU Jing-xu(祝京旭),et al.Radial distribution and axial development of particle velocities in a long CFB riser(循环流化床提升管中颗粒速度的径向分布及其沿轴向的发展)[J].J Chem Eng of Chinese Univ(高校化学工程学报),2002,16(2):168-173.