期刊文献+

新型湿法除尘除有害气体斜板塔的流场分析 被引量:3

Analysis of flowfield in new types of towers with sloping plates for wet dedusting and hazardous gas removal
下载PDF
导出
摘要 研究对象为2种新型湿法除尘除有害气体的斜板塔:矩形斜板塔和伞罩形斜板塔。为了观察塔内流场分布规律,运用CFD(计算流体力学)软件,气相采用标准κ-ε湍流模型描述,液相采用颗粒轨道模型描述,对2种新型塔内气液两相流动进行了数值模拟。预测了无喷淋和有喷淋两种情况下的气相湍流流场,不同空塔气速不同液气比的塔内压力损失。结果表明:采用中心出口的圆柱型塔可以有效地避免气体“死区”的产生;新型斜板塔能有效地增大气液接触面积,延长气体的塔内停留时间;加入喷淋液体以后,气相流场明显均匀化。该模拟也为塔体的进一步优化设计提供了依据。 The tower with rectangle sloping plates and the tower with umbrella sloping plates as two new types of towers for wet dedusting and hazardous gas removal were studied. In order to observe the distribution laws of the towers' flowfield, the gas-liquid two-phase flow in the two new types of towers was numerically simulated by using computational fluid dynamics (CFD) software, in which the gas flow and the motion of liquid droplets were respectively described with standard κ-ε turbulence model and particle trajectory method. It was predicted that the gas turbulence flowfield with/without spray, and the pressure loss of towers for two-phase flow. Simulation results showed that the dead areas could be effectively avoided in the cylinder towers with the central outlet, gas-liquid contact areas were effectively increased and the gas residence time was delayed,and the uniformity of gas flowfield was improved greatly when spray was introduced also. The study could provide foundation for optimizing the towers' design.
出处 《环境工程学报》 CAS CSCD 北大核心 2007年第6期77-82,共6页 Chinese Journal of Environmental Engineering
基金 新世纪优秀人才支持计划项目(NCET-04-0769) 教育部科学技术研究重点项目(105126) 湖南省自然科学基金重点项目(03JJY2002)
关键词 斜板塔 数值模拟 气液两相流 标准κ-ε湍流模型 颗粒轨道模型 the towers with sloping plates numerical simulation gas-liquid two-phase flow standard κ-ε turbulence model particle trajectory model
  • 相关文献

参考文献10

  • 1裴清清,张旭东,魏先勋.三种型式的湿式除尘器性能对比试验[J].环境科学学报,1997,17(1):106-109. 被引量:3
  • 2[4]Ranade V.V.An efficient computational model for simulating flow in stirred vessels:A case of Rushton turbine.Chemical Engineering Science,1997,52(24):4473~4484
  • 3[5]Cockx A.,Line A.,Roustan M.,et al.Numerical simulation and physical modeling of the hydrodyna-mics in an air-lift internal loop reactor.Chemical Engineering Seience,1997,52(21):3787~3793
  • 4[6]Dudek S.A.,Rogers J.A.,Gohara W.F.Computational fluid dynamics(CFD)model for predicting two-phase flow in a flue-gas-desulfurization wet scrubber.In:Proceedings of EPRI-DOE-EPA Combined Utility Air Pollutant Control Symposium.Georgia:Atlanta,1999.16~20
  • 5[9]Griffiths W.D.,Boysan F.Computational fluid dynamics (CFD)and empirical modeling of the performance of a number of cyclone samplers.Journal of Aerosol Science,1996,27(2):281~304
  • 6[11]Fluent Inc.Fluent 6.2 User's guide.Lebanon:Fluent Inc.,2005.74~78
  • 7王晓瑾,彭炯,陈晋南,薄以匀,齐金彦,庄德安.除尘脱硫装置气液两相流场的数值模拟[J].北京理工大学学报,2006,26(4):356-360. 被引量:6
  • 8周山明,金保升,仲兆平,孙克勤.大型烟气脱硫塔的流体动力学模拟及优化设计[J].东南大学学报(自然科学版),2005,35(1):105-110. 被引量:40
  • 9[14]王福军编.计算流体动力学分析-CFD软件原理与应用.北京:清华大学出版社,2005.216~223
  • 10罗运柏,胡宗定.烟气脱硫三相流化床反应器的数学模拟与预测放大[J].化工学报,2002,53(2):122-127. 被引量:9

二级参考文献26

  • 1陆慧林,刘文铁,别如山,何玉荣,孙永立,李炳熙.增湿活化反应器内气—液滴—固三相流场的数值模拟[J].工程热物理学报,2001,22(S1):197-200. 被引量:10
  • 2周山明,金保升,仲兆平,孙克勤.大型烟气脱硫塔的流体动力学模拟及优化设计[J].东南大学学报(自然科学版),2005,35(1):105-110. 被引量:40
  • 3王祖武,李绍箕,胡将军,尹兆森,王聪玲.1万m^3/h三相流化床烟气脱硫中间试验初步研究[J].环境工程,1994,12(6):20-24. 被引量:10
  • 4张俊丰,童志权.喷流塔脱硫除尘技术研究[J].环境污染治理技术与设备,2005,6(2):84-87. 被引量:6
  • 5Meikap B C, Kundu G, Biswas M N. Modeling of anovel multistage bubble column scrubber for flue gas desulfurization [J]. Chem Eng Journal, 2002, 86(3) :331 - 342.
  • 6Kill S, Michelsen M L, Johnson K D. Experimental investigation and modeling of wet flue gas desulfurization pilot plant [J]. Ind Eng Chem Res, 1998,37(7) : 2792- 2806.
  • 7Orme M. Experiments on droplet collisions, bounce ,coalescence and disruption [ J ]. Prog Energy Combust Sci, 1997, 23(1) : 65 -79.
  • 8Lain S, Aliod R. Study on the eulerian dispersed phase equations in non-uniform turbulent two-phase flows:discussion and comparison with experiments [ J ]. International Journal of Heat and Fluid Flow, 2000,21 (3) :374 - 380.
  • 9Michalski J A. The influence of aerodynamic characteristics on mass exchange efficiency in FGD scrubbers[J]. Chem Eng Technol, 1999, 22(4) : 343 -351.
  • 10陈静滨,新订公害防止的技术与法规.大气篇(译),1988年

共引文献52

同被引文献29

引证文献3

二级引证文献5

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