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双锥导流式进气分布器内流场的数值模拟 被引量:5

Numerical Simulation of the Flow Field in Double Cone-Diversion Gas Distributor
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摘要 双锥导流式进气分布器是针对大型反应器开发的进气均布装置,今利用FLUENT软件采用κ-ε湍流模型,对其在不同结构参数下的流场分布进行了数值模拟。考察了分布器外锥对分布器性能的影响,通过改变外锥上导流槽的尺寸和方位,得出了在既定的床径下达到沿分布器内锥外表面压力均布要求时的外锥最优尺寸。通过模拟分布器内锥在不同的开孔率及四个不同锥角时床内的流场分布,考察了气体分布随内锥开孔率及锥角的变化趋势,分析得出使分布器压降低,流场分布最优时的内锥开孔率及锥角分别为0.89%、60°。并与实验测试结果进行了比较,模拟结果与实验结果基本吻合。 Double cone intake distributor, a new type of symmetric intake device, was designed and developed for large-scale reactor. In order to evaluate the proposed device, FLUENT software was used to simulate the flow fields of the new type distributor with different structural parameters. In this work, the κ-ε turbulent model was adopted to investigate the effect of the size and location of the drained cells on the outside cone. Then, for a given bed dimension, the optimal drained cell size and location on the outside cone were obtained, using them the demand of forming a well pressure distribution along the outside surface of the inside cone of the distributor can be matched. Additionally, the effects of the aperture ratio on the inside cone and the change of the cone angle on the flow distribution were also studied via simulating the flow field distributions of the fluidized bed using various distributors with inside cones having different aperture ratios and cone angles. The results show that the proposed new type device has better flow distribution and lower pressure drop when the aperture ratio of the inside cone is 0.89% and the cone angle is 60°. The measuring results of the experiments agree well with those obtained by simulation, and it indicates that the numerical simulation can forecast the flow field well.
出处 《高校化学工程学报》 EI CAS CSCD 北大核心 2009年第6期945-950,共6页 Journal of Chemical Engineering of Chinese Universities
关键词 双锥 气体分布器 开孔率 锥角 double cone gas distributor ratios of aperture cone angle
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  • 1刘德新,李鑫钢,徐世民.CFD优化双切向环流式气体分布器设计[J].化工进展,2007,26(z1):127-130. 被引量:3
  • 2崔守业,许友好,程从礼,龚剑洪.MIP技术的工业应用及其新发展[J].石油学报(石油加工),2010,26(S1):23-28. 被引量:14
  • 3董谊仁.填料塔进气结构及其设计[J].化工设计,1993,3(3):1-8. 被引量:7
  • 4山红红,李春义,钮根林,杨朝合,张建芳.流化催化裂化技术研究进展[J].石油大学学报(自然科学版),2005,29(6):135-150. 被引量:31
  • 5Xu Youhao. Advance in China fluid catalytic cracking (FCC) process [J]. Scientia Sinica Chimica, 2014, 44(1): 13-24.
  • 6Jin Yong(金涌), Yu Zhiqing(俞芷青), Sun Zhufan(孙竹范), Peng Bingpu(彭秉璞). Investigationon branched pipe distributors for fluidized beds (Ⅱ): Deternination of desigh parameters for branched pipe distributors [J]. 化工学报, 1984, (3): 203-213.
  • 7Wang Zhangmao(王樟茂), Zhang Nianying(张年英), Lü Dewei(吕德伟), Chen Gantang(陈甘棠), Liu Qing(刘青), Jiang Yinrui(江银瑞), Lai Chenlie(赖成烈). Study on characteristics of perforated gas-sidtributors in a commercial fluidized bed [J]. 石油化工, 1986, 7: 399-405.
  • 8Li Guang, Yang Xiaogang, Dai Gance. CFD simulation of effects of the configuration of gas distributors on gas-liquid flow and mixing in a bubble column [J]. Chemical Engineering Science, 2009, 64: 5104-5116.
  • 9Akbari V, Borhani T N G, Godini H R, Hamid M K A. Model-based analysis of the impact of the distributor on the hydrodynamic performance of industrial polydisperse gas phase fluidized bed polymerization reactors [J]. Powder Technology, 2014, 267: 398-411.
  • 10Bahadori F, Rahimi R. Simulations of gas distributors in the design of shallow bubble column reactors [J]. Chem. Eng. Tech., 2007, 30: 443-447.

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