期刊文献+

大型波纹规整填料塔二维返混特性实验测量与模拟 被引量:2

Experimental Measurement and Simulation of Two Dimensional Dispersion in Commercial Scale Column Containing Corrugated Structure Packing
下载PDF
导出
摘要 以热水为示踪剂,对填充有塑料制250Y板波纹规整填料的直径1m的填料塔进行了二维返混特性研究.实验填料塔装填高度2,000mm,装填10层填料,每层200mm,层与层之间交错90°摆放.实验中示踪剂为连续注入,采用铂电阻温度探头分别测量了填料塔距塔顶400mm和1000mm 2个平面的无因次温度分布.应用柱坐标二维返混模型得到了轴向和径向返混系数Dz和Dr,结果发现因为规整填料的各向异性,由模型计算得到的温度场在距离塔顶较远的1000mm平面与实验符合较好,而在较近的400mm平面与实验相差较大.在此基础上提出了基于直角坐标系的各向异性返混模型,每层填料逐层计算,层之间按实际情况旋转90°,结果表明使用相同的Dz和Dr为参数,得到的温度场在400mm平面和1000mm平面均与实验符合良好. The two-dimensional dispersion in a commercial scale column containing plastic 250Y Mellapak corrugated structure packing was studied by using hot water as tracer.The experimental column was 1000mm in diameter with a 2000mm height of packing.The packed bed consisted of 10 structured packing layers(packages),each 200mm in thickness,which were placed alternatively with 90°rotation.The water temperatures were measured by a number of platinum resistance thermometers installed in two cross sections of the column,apart from the top inlet by 400,and 1000mm respectively.By applying the axial symmetrical dispersion model in cylindrical coordinate,the axial and radial dispersion coefficients Dz and Dr were obtained.It was found that the simulated temperature field agreed well with the experimental data in the 1000mm section,but not in the 400mm section.This is due to the fact that the flow in Mellapak packing is anisotropic,and displays isotropic character only after several alternatively installed layers of structured packing.In order to overcome such difficulty,an integrated layers model was established in Cartesian coordinate,by which the calculation was performed layer by layer with 90°rotation to account for the anisotropic effect.The simulated temperature field by such integrated layers model with Dz and Dras known parameters agrees satisfactorily with the experimental data in both 400mm and 1000mm sections.
出处 《天津大学学报》 EI CAS CSCD 北大核心 2012年第9期775-778,共4页 Journal of Tianjin University(Science and Technology)
基金 天津市自然科学基金资助项目(10JCYBJC06200)
关键词 返混 规整填料 无因次温度 返混系数 dispersion structure packing dimensionless temperature dispersion coefficient
  • 相关文献

参考文献9

  • 1Ahn,BJ,Zoulalian,A,Smith,JM.Axial dispersion in packed beds with large wall effect. American Institute of Chemical Engineers Journal . 1986
  • 2Vortmeyer D,Winter R P.Impact of porosity and veloc-ity distribution on the theoretical prediction of fixed bedchemical reactor performance. Chem Reac Eng . 1982
  • 3Andrzej K,Mieczys aw J,Hartmut S,et al.Dynamictracer study of column packings for catalytic distilla-tion. Chemical Engineering . 2005
  • 4Delmas H,Froment G F.A simulation model accountingfor structural radial non-uniformities in fixed bed reac-tors. Chemical Engineering Science . 1988
  • 5Winterberg M,Tsotsas E,Krischke A,et al.A simpleand coherent set of coefficients for modelling of heat andmass transport with and without chemical reaction intubes filled with spheres. Chemical Engineering Science . 2000
  • 6Carberry J J,Bretton R H.Axial dispersion of mass in flow through fixed beds. American Institute of Chemical Engineers Journal . 1958
  • 7Leitao A,Carlos P,Santos S,et al.Tracer experi-ments in fixed beds:Effect of flow maldistribution onthe estimation of transport kinetic parameters. ChemEng J . 1994
  • 8Selvaraju N,Pushpavanam S.Adsorption characteristics on sand and brick beds. Chemical Engineering . 2009
  • 9VortmeyerD,,SchusterJ.Evaluation of steady flow profiles in rectangular and circular packed beds by a variational method. ChemEngngSci . 1983

同被引文献31

引证文献2

二级引证文献3

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