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内旋/直流复合流化下循环流化床的脱硫 被引量:6

Desulphurization in Circulating Fluidized Beds Under Composite Internally Swirling and Straight Flowing Conditions
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摘要 提出了内旋/直流复合流化方式的循环流化床脱硫方法,并用热线风速仪测量了直管段内的冷态气相流场。试验表明,内旋/直流流化是非均匀布风的流化方式;2股气流的混合在距直管段入口2倍直径前基本结束,切向速度在直管段下游近壁处仍较大。复合流化的轴向紊流度接近壁面处最强,而切向紊流度在半径中心有最大值。叶片装在喉部的综合效果好于装在渐扩段,内旋/直流流化的效果好于直流流化。 A composite internally swirling-straight flow proposed. The cold state flow field in the straight pipe desulphurization method for circulating fluidized beds is being section was measured with a hot wire anemometer. Test results indicated that composite internally swirling-straight flow fluidization is a fluidizing method with non-uniform flow distribution; mixing of the two currents basically terminate within a distance, twice the diameter away from the straight pipe's entrance, but tangential velocity near the wall, down stream the straight pipe section, remains still quite high. Axial turbulence intensity of composite fluidization is highest near the pipe wall, but the tangential turbulence intensity is highest midway the radius. Blade effects are more pronounce, if installed in the throat, rather than in the diffuser section. Composite internally swirling-straight flow fluidization is more effective than pure straight flow.
出处 《动力工程》 EI CSCD 北大核心 2007年第4期596-600,共5页 Power Engineering
关键词 环境工程学 烟气脱硫 循环流化床 复合流化 切向速度 紊流度 environmental engineering flue gas desulfurization CFB composite fluidization tangent velocity turbulence intensity
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  • 1周涌,由长福,祁海鹰,徐旭常.锅炉结渣过程数值模拟研究进展[J].燃烧科学与技术,2004,10(4):375-382. 被引量:13
  • 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徐跃年.飞灰循环流化床燃烧脱硫试验研究[J].煤气与热力,1995,15(5):29-31. 被引量:4
  • 4赵旭东,王怀彬,于军.新型低阻高效旋风除尘器性能的模化实验研究[J].污染防治技术,1996,9(3):134-137. 被引量:3
  • 5Wang H, Harb J N. Modeling of ash deposition in large-scale combustion facilities burning pulverized coal [J]. Progress in Energy and Combustion Science, 1997, 23(3): 267-282.
  • 6Richards G H, Slater P N, Harb J N. Simulation of ash deposit growth in a pulverized coal-fired pilot scale reactor [J]. Energy & Fuels, 1993, 7(6): 774-781.
  • 7Fan J R, Zha X D, Sun P, et al. Simulation of ash deposit in a pulverized coal-fired boiler [J]. Fuel, 2001, 80(5): 645-654.
  • 8Shih T H, Liou W W, Shabbir A, et al. A new κ-ε eddy viscosity model for high Reynolds number turbulent flows [J]. Computers Fluids, 1995, 24(3): 227-238.
  • 9Wang H. Modeling of Ash Formation and Deposition in PC Fired Utility Boilers [D]. Provo, USA: Brigham Young University, 1998.
  • 10MOORTEL VAN DEN T,AZARIO E,SANTINI R,et al.Experimental analysis of the gas-particle flow in a circulating fluidized bed using a phase doppler particle analyzer[J].Chemical Engineering Science,1998,53(10):1883-1899.

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