期刊文献+

变压吸附两相流FLUENT模型的建立 被引量:2

Establishment of two phase coupling pressure swing adsorption model in FLUENT
下载PDF
导出
摘要 利用FLUENT中气-固多孔介质模型可模拟多孔介质内气体的流动规律。针对FLUENT自带的单相多孔介质模型不能表现变压吸附气体与固体吸附颗粒之间的传质、传热问题,采用FLUENT用户自定义函数编程,反映吸附分离传质、传热和动量传递,将多孔介质单相模型耦合为更准确的气固两相流模型,并加以验证。结果表明,出口氧气平均摩尔浓度误差在2%左右,模拟与实验结果吻合较好。 Gas-solid porous media model based on the FLUENT can simulate the law of gas flow in porous media.The program of FLUENT built for single-phase porous media model can not express the mass transfer,heat transfer problems existed between gas and solid particles on PSA adsorption.The functional programs of user definition in FLUENT are set up and validated to reflect the adsorption separation and mass transfer,heat and momentum transfer FLUENT for single-phase porous media model,in which the porous medium as a single-phase model coupling phase flow model shows good accuracy.The results show that the error of the average export oxygen molar concentration is about 2% error,and the simulation and experimental results agree well.
出处 《现代化工》 CAS CSCD 北大核心 2013年第9期130-135,共6页 Modern Chemical Industry
关键词 变压吸附 FLUENT 多孔介质 气-固两相流模型 pressure swing adsorption FLUENT porous media gas-solid two phase coupling model
  • 相关文献

参考文献21

  • 1曾嵘,关建郁.Progress in Pressure Swing Adsorption Models During the Recent 30 Years[J].Chinese Journal of Chemical Engineering,2002,10(2):228-235. 被引量:4
  • 2卜令兵,郜豫川,张剑锋,杨云,李小荣.变压吸附数值模拟的研究[J].煤化工,2009,37(4):30-32. 被引量:5
  • 3Farooq S,Ruthven D M,Boniface H A.Numerical simulation of a pressure swing adsorption oxygen unit[J].Chemical Engineering Science,1989,44 (12):2809-2816.
  • 4Teague K G,Edgar T F.Predictive Dynamic Model of a Small Pressure Swing Adsorption Air Separation Unit[J].Industrial & Engineering Chemistry Research,1999,38 (10):3761-3775.
  • 5戴先知,刘应书.变压吸附过程数学模型及其应用[J].低温与特气,2006,24(1):36-42. 被引量:6
  • 6Sadeghzadeh Ahari J,Pakseresht S,Mahdyarfar M,et al.Predictive Dynamic Model of Air Separation by Pressure Swing Adsorption[J].Chemical Engineering & Technology,2006,29(1):50-58.
  • 7Huang W C,Chou C T.Comparison of radial-and axial-flow rapid pressure swing adsorption processes[J].Industrial & Engineering Chemistry Research,2003,42(9):1998-2006.
  • 8Nouh S A,Lau K K,Shanff A M.Modeling and simulation of fixed bed adsorption column using integrated CFD approach[J].Journal of Applied Sciences,2010,10 (24):3229-3235.
  • 9Zheng X,Liu Y,Liu W.Two-Dimensional Modeling of the Transport Phenomena in the Adsorber During Pressure Swing Adsorption Process[J].Industrial & Engineering Chemistry Research,2010,49(22):11814-11824.
  • 10Glueckauf E,Coates J I.241.Theory of chromatography.Part Ⅳ.The influence of incomplete equilibrium on the front boundary of chromatograms and on the effectiveness of separation[J].Journal of the Chemical Society,1947,(Resumed):1315-1321.

二级参考文献57

  • 1朱大方.氨厂弛放气提氢吸附过程的平衡模型[J].天然气化工—C1化学与化工,1994,19(3):21-27. 被引量:2
  • 2魏丽婷,赖喜德,杨炯波,杨炯良.PSA制氢工艺管网中均压过程的仿真[J].西华大学学报(自然科学版),2006,25(4):52-54. 被引量:4
  • 3MAHLE J J,FRIDAY D K,LEVAN M D.Pressure Swing Adsorption for Air Purification.1.Temperature Cycling and Role of Weakly Adsorbed Carrier Gas[J].Ind Eng Chem Res,1996,35:2342-2354.
  • 4Lu Z P,LOUREIRO J M,LEVAN M D,RODRIGUES A E.Dynamics of Pressurization and Blowdown of an Adiabafie Bed:Ⅲ[J].Gas Separation & Purification,1992,6:15-23.
  • 5RUTHVEN D M,FAROOQ S,KNAEBEL K S.PressureSwing Adsorption[M].New York:VCH Publishers,1994.
  • 6GLUECKAUF E.Theory of Chromatography.Part 10.Formulate for Diffusion into Spheres and Their Applicationto Chromatography[J].Trans Faraday Soc,1955,51:1540-1551.
  • 7JEE J G,LEE J S,LEE C H.Air Separation by a SmallScall Two-Bed Medical O2 Pressure Swing Adsorption[J].Ind Eng Chem Res,2001,40:3647-3658.
  • 8SERBEZOV A,SOTIRCHOS S V.Mathematical Modeling of the Adsorptive Separation of Multicomponent Gaseous Mixtures[J].Chem Eng Sei,1997,52:79-91.
  • 9TODD R S,WEBLEY P A.Maeropore Diffusion DustyGas Coefficient for Pclletised Zeolites from Breakthrough Experiments in the O2/N2 System[J].Ind Eng Chem Res,2005,60:4593-4608.
  • 10CRUZ P,MAGALHAES F D,MENDES A.Generalized Linear Driving Force Approximation for Adsorption of Multlcomponent Mixtures[J].Chem Eng Sci,2006,61:3519-3531.

共引文献12

同被引文献13

引证文献2

二级引证文献1

相关作者

内容加载中请稍等...

相关机构

内容加载中请稍等...

相关主题

内容加载中请稍等...

浏览历史

内容加载中请稍等...
;
使用帮助 返回顶部