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35t/h内循环流化床锅炉流动数值模拟 被引量:3

Numerical Simulation of Flow Characteristics in a 35t/h Circulating Fluidized Bed Boiler
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摘要 采用基于颗粒动力学理论的欧拉双流体模型,对35t/h内循环流化床锅炉炉膛的气、固流动特性进行了数值模拟。结果表明:炉膛压差的模拟值与实验值吻合较好,说明欧拉双流体模型能够准确地描述炉膛内气、固流动特性;颗粒体积分数和速度分布特性既揭示了内循环流化床中颗粒的内循环流动机理,又为内循环流化床大型化和流动结构优化提供了参考。 Making use of Euler-Euler model (EEM) which based on granular kinetic theory,the gas-solid flow in a 35t/h oil shale-combustion circulating fluidized bed boiler was simulated to show that the furnace pressure complies well with the experimental data,this indicates that Euler-Euler model can accurately demonstrate the gas-solid' s flow characteristics in the furnace.Both particle volume fraction distribution characteristics and particle velocity distribution characteristics can reveal inner circulation mechanism of the particles in the circulating fluidized bed.This provides a reference for the flow structure optimization of the circulating fluidized bed and its structure upsizing.
出处 《化工机械》 CAS 2014年第5期638-641,共4页 Chemical Engineering & Machinery
基金 国家自然科学基金资助项目(51276034)
关键词 循环流化床锅炉 流动特性 颗粒动力学 欧拉双流体模型 数值模拟 circulating fluidized bed boiler flow characteristics kinetic theory of granular flow Euler-Euler liquid-solid flow model numerical simulation
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参考文献9

  • 1Feng Y Q, Swenser-Smith T, Witt P J, et al. CFD Modeling of Gas-solid Flow in an Internally Circulat- ing Fluidized Bed [ J ]. Powder Technology, 2012, 219:78 -85.
  • 2Lu H L, He Y R,Gidaspow D, et al. Size Segregation of Binary Mixture of Solid in Bubbling Fluidized Beds [J]. Powder Technology, 2003, 134(1/2) :86 -97.
  • 3Zhang N, Lu B N,Wang W,et al. 3D CFD Simulationof Hydrodynamics of a 150 MW0 Circulating Fluidized Bed Boiler[ J]. Chemical Engineering Journal, 2010, 162(2) :821 -828.
  • 4田凤国,章明川,范浩杰,齐永锋,顾明言.内循环流化床颗粒流动特性的数值模拟[J].上海交通大学学报,2007,41(3):347-351. 被引量:4
  • 5王擎,孙佰仲,吕海生,崔玉萍,孙键.循环床炉内气固两相流动特性的数值模拟探讨[J].东北电力学院学报,2004,24(2):1-5. 被引量:1
  • 6Ding J M,Gidaspow D. A Bubbling Fluidization Model using Kinetic Theory of Granular Flow [ J]. AIChE journal, 1990, 36 (4): 523-538.
  • 7Wang Q, Xiao J B, Liu H P. CFD Simulation of Hy- drodynamics on the Dense Zone on a 65t/h Oil Shale- fired High-low Bed CFB Boiler[ J]. Powder Technolo- gy, 2013, 249:339 -352.
  • 8Gidaspow D. Multiphase Flow and Fluidization [ M ]. Salt Lake City : American Academic Press, 1994.
  • 9Eekert E R G, Goldstein R J, Patankar S V, et al. Heat Transfer--A Review of 1980 Literature[J]. In- ternational Journal of Heat and Mass Transfer, 1981, 24(12) : 1863 - 1902.

二级参考文献12

  • 1勾宏图,吴玖桓,张衍国,郭鸿志.垃圾炉内大颗粒运动特性的可视化实验研究[J].锅炉制造,2005(1):8-10. 被引量:3
  • 2Freedman W,Davidson J F.Hold up and liquid circulation in bubble columns[J].Transactions of the Institution of Chemical Engineers,1969,47 (3):251-262.
  • 3Merry J M D,Davidson J F.Gulf stream circulation in shallow fluidized bed[J].Transactions of the Institution of Chemical Engineers,1973,51 (4):361-368.
  • 4Limtrakula S,Chalermwattanataia A,Unggurawiroteb K,et al.Discrete particle simulation of solids motion in a gas-solid Fluidized bed[J].Chemical Engineering Science,2003,58:915-921.
  • 5Smith R,Beardmore K,Gras-Mati A.Molecular dynamics simulation of particle-surface interactions[J].Vacuum,1995,46 (8):1195-1199.
  • 6Cundall P A,Strack O D L.A discrete numerical model for granular assemblies[J].Geotechnique,1979,29:47-65.
  • 7Tsuji Y,Kawaguchi T,Tanaka T.Discrete particle simulation of a fluidized bed[J].Powder Technology,1993,77:79-87.
  • 8Hoomans B P B,Kuipers J A M,Briels W J,et al.Discrete particle simulation of bubble and slug formation in a two-dimensional gas-fluidized bed:A hardsphere approach[J].Chemical Engineering Science,1996,51:99-108.
  • 9Xu B H,Yu A B.Numerical simulation of the gassolid flow in a fluidized bed by combining discrete particle method with computation fluid dynamics[J].Chemical Engineering Science,1997,52:2785-2809.
  • 10Wen C Y,Yu Y H.Mechanics of fluidization[J].Chem Engng Prog Symp Ser,1966,62 (5):100-105.

共引文献3

同被引文献41

  • 1殷庆勇,于海,蔡祥义,郑峰.煤泥、煤矸石混烧循环流化床锅炉的特点分析[J].锅炉技术,2005,36(6):18-20. 被引量:4
  • 2李勇,周力行.k-ε-PDF两相湍流模型和台阶后方气粒两相流动的模拟[J].工程热物理学报,1996,17(2):234-238. 被引量:6
  • 3PatankarSV 张政译.传热与流体流动的数值计算[M].北京:科学出版社,1984.33-44.
  • 4李政,倪维斗,岳光溪,张巍.循环流化床复合压降数学模型[J].动力工程,1997,17(3):13-16. 被引量:17
  • 5Rajan R,Wen C Y. A Comprehensive Model for Fluid- ized Bed Coal Combustion [ J]. A1ChE Journal, 1980, 26 (4) :642 ~ 655.
  • 6Qing W, Hongpeng L, Jingru B, et al. Application of High-Low Bed CFB Combustion Technology to oil Shale Combustion[ J ]. Oil Shale ,2013,30( 2 ) : 147 156.
  • 7Ergun S. Fluid Flow Through Packed Columns [ J ]. Chemical Engineering Progress Symposium Series, 1952,48(2) :89 -94.
  • 8Sivathanu Y R, Faeth G M. Generalized State Rela- tionships for Sealar Properties in Non-Premixed Hy- drocarbon/Air Flames [ J ]. Combustion and Flame, 1990,82(2) :211 -230.
  • 9Gibson M M, Launder B E. Ground Effects on Pres- sure Fluctuations in the Atmospheric Boundary Layer [ J ]. Journal of Fluid Mechanics, 1978,86 ( 3 ) :491 -.511.
  • 10Cbeng P. Two Dimensional Radiating Gas Flow by a Moment Method [ J ]. AtAA Journal, 1964,2 (3) : 1662 - 1664.

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