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用直接数值模拟方法对流化床内颗粒运动区域的研究 被引量:3

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摘要 本文采用直数值模拟技术,对不同直径和密度的颗粒在流化床内的流化运动区域进行了探讨研究,得到了与之相关的结论。
作者 袁竹林
出处 《洁净煤燃烧与发电技术》 2000年第1期18-23,共6页
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同被引文献11

  • 1Hoomans B P B,Kuipers J A M,Briels,et al.Discrete particle simulation of bubble and slug formation in a two-dimensiontal gas-fluidized bed:A hard-sphere approach[J].Chem.Engng.Sci.1996(51) :99-108. 被引量:1
  • 2Tsuji Y,Kawaguchi T,Tanaka T.Discrete particle simulationof two dimensional fluidized bed [J].Powder Technol.1993(77) :79-87. 被引量:1
  • 3Xu B H Y A B.Numerical simulation of the gas-solid in a fluidized bed by combining discrete particle method with computation fluid dynamics[J].Chem.Engng.Sci,1997 (52):2785 -2809. 被引量:1
  • 4Sunun Limtrakula, Ativuth Chalermwattanataia, Kosol Unggurawiroteb, et al. Discrete particle simulation of solids motion in a gas-solid fluidized bed [ J ]. Chemical Engineering Science, 2003,58 (6) : 915-921. 被引量:1
  • 5Tsuji Y, Kawaguchi T, Tanaka T. Discrete particle simulation of a fluidized bed[ J]. Powder Technology, 1993,77 ( 1 ) :79-87. 被引量:1
  • 6Hoomans 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 hard-sphere approach[J]. Chemical Engineering Science, 1996, 51( 1 ) :99-108. 被引量:1
  • 7Wen C Y, Yu Y H. Mechanics of fluidization[ J]. Chem Engng Prog Symp Ser, 1966,62(5) ,100-105. 被引量:1
  • 8Nagato S, Kamisada M, Kosugi S. Characteristics of the internally circulating fluidized bed boiler[A]. Proceeding of Fourth China-Japan Fluidization Science and Technology Symposium[ C ]. Beijing:Science Press, 1991.56-65. 被引量:1
  • 9Ohshita T, Higo T, Kosugi S. Formation of internally circulating flow and control of overall heat transfer coefficient in a fluidized-bed boiler [ J ]. Heat-Transfer Japanese Research, 1994,23(4) :349-363. 被引量:1
  • 10欧阳洁,李静海.模拟气固两相流动非均匀结构的颗粒运动分解轨道模型[J].中国科学(B辑),1999,29(1):29-38. 被引量:22

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