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计算流体力学方法模拟规整填料塔内流体流动行为的研究进展 被引量:8

Progress of Simulation of Fluid Flow Behavior in Structured Packed Column by Computational Fluid Dynamics
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摘要 对采用计算流体力学(CFD)方法模拟规整填料塔内流体流动行为的研究进展进行了综述,分别介绍了单相流模型和两相流模型。单相流模型可预测气相或液相在规整填料塔内轴向、径向的扩散行为及气相的压头损失等;两相流模型主要研究规整填料塔内气液相流动行为,利用该模型可计算液体在规整填料表面的流动过程及气液相间的传质行为,其模拟结果比单相流模拟更接近实际。随流体力学学科和计算机技术及现代测量技术的进一步发展,将会促进CFD技术在化工过程中的应用。 Application of computational fluid dynamics (CFD) to simulate fluid flow behavior in structured packed column was reviewed. CFD models include single -phase flow model and two -phase flow model. Using single - phase flow models, axial and radial diffusions of gas - or liquid - phase and formation of dry pressure drop in gas phase can be simulated. The two - phase flow models can be used to describe fluid flow behavior and mass transfer process of gas - liquid two phase flow. The simulation results of the latter are much closer to actual process occurring in structured packed column than those of single -phase flow model. With further developments of fluid dynamics, computer technology and modem measurement techniques, CFD simulation will be more widely used in chemical process.
出处 《石油化工》 EI CAS CSCD 北大核心 2007年第9期961-965,共5页 Petrochemical Technology
基金 天津市自然科学基金项目(023606711)
关键词 计算流体力学 规整填料塔 单相流模型 两相流模型 模拟 computational fluid dynamics structured packed column single -phase flow model two - phase flow model simulation
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参考文献17

  • 1俞晓梅,祝铃钰,姚克俭,朱菊香,胡宇湘.塔板与填料复合技术在吸收稳定塔系中的应用[J].石油化工,2003,32(4):321-324. 被引量:7
  • 2王琨,张鹏,刘春江.计算流体力学在填料塔中的应用[J].天津化工,2004,18(6):5-8. 被引量:4
  • 3Hodson J S, Fletcher J R, Porter K E. Fluid Mechanical Studies of Structured Distillation Packings. In: IChemE Symp Ser Dist & Absp. Vol. 2, No. 142. New York : American Institute of Chemical Engineerings, 1997. 999 - 1 007
  • 4van Gulijk C. Using Computational Fluid Dynamics to Calculate Transversal Dispersion in a Structured Packed Bed. Comput Chem Eng, 1998,22 ( Supplement 1 ) : S767 - S770
  • 5van Baten J M, Ellenberger, Krishna R. Radial and Axial Dispersion of the Liquid Phase Within a KATAPAK -S Structure: Experiments vs. CFD Simulations. Chem Eng Sci, 2001,56(3) : 813 -821
  • 6van Baten J M, Krishna R. Liquid - Phase Mass Transfer Within KATAPAK- S (r) Structures Studied Using Computational Fluid Dynamics Simulations. Catal Today, 2001,69(1 -4) : 371 -377
  • 7van Baten J M, Krishna R. Gas and Liquid Phase Mass Transfer Within KATAPAK- S (r) Structures Studied Using CFD Simulations. Chem Eng Sci, 2002, 57(9) : 1 531 - 1 536
  • 8张鹏,刘春江,袁希钢,余国琮.规整填料塔液相流动的计算流体力学模拟[J].化工学报,2004,55(8):1369-1373. 被引量:11
  • 9张鹏,刘春江,唐忠利,袁希钢,余国琮.规整填料塔内气相流动的计算流体力学模拟[J].天津大学学报(自然科学与工程技术版),2005,38(6):503-507. 被引量:9
  • 10Petre C F, Larachi F, Iliuta I, et al. Pressure Drop Through Structured Packings: Breakdown into the Contributing Mechanisms by CFD Modeling. Chem Eng Sci, 2003,58( 1 ) : 163 - 177

二级参考文献30

  • 1陈大昌,魏建华,刘乃鸿,徐敬先,陆振民.塔填料的工业应用及评价[J].化学工程,1995,23(3):15-23. 被引量:29
  • 2徐崇嗣,姚克俭,计建炳.复合塔及其应用[J].浙江工业大学学报,1995,23(3):207-211. 被引量:3
  • 3Calis H P A, Nijenhuis J, Paikert B C, Dautzenberg M F,van den Bleek C M. CFD modelling and experimental validation of pressure drop and flow profile in a novel structured catalytic reactor packing [J]. Chem Eng Sci,2001,56(4):1713.
  • 4M Tierney, A Nasr, G quarini. The use of proprietary computational fluid dynamics codes for flows in annular packed beds [J]. Separation andpurification technology. 1998,13(2):97.
  • 5Coen van Gulijk. Using computational fluid dynamics to calculate transversal dispersion in a structured packed bed [J]. Computers chemical engineering, 1998,22:s767.
  • 6Higler A P, Krishna R, Ellenberger J, Taylor R. countercurrent operation of a structured catalytically packed-bed reactor: Liquid phase mixing and mass transfer [J]. Chem Eng Sci, 1999,54(21):5145.
  • 7Van Baten J M, Ellenberger J, Krishna R. Radial and axial dispersion of the liquid phase within a KATAPAK-S structure: experiments vs. CFD simulations [J]. Chem Eng Sci, 2001,56(3):813.
  • 8K T Yu,X J Yuan,G Q Dong.Two phase flow and heat transfer[M].ISME,1992,215.
  • 9Spiegel L, Knoche M. Influence of Hydraulic Conditions on Separation Efficiency of Optiflow [J]. Chem Eng Res Des,1999,77(A7):609.
  • 10Edwards D P, Krishnamurthy K R, Potthoff R W. Development of An Improved Method to Quantify Maldistribution and Its Effect on Structured Packing column Performance[J].Chem Eng Res Des, 1999, 77(A7):I 656.

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