期刊文献+

竖直和水平圆管换热器在内热源液池内的两相换热特性

Two Phase Heat Transfer Characteristics of Horizontal and Vertical Tube Heat Exchangers in Pool with Internal Heat Source
下载PDF
导出
摘要 针对溶液堆整体模拟试验模型的结构尺寸和运行工况,建立了内热源液池内自然对流和鼓泡驱动同时作用下竖直和水平圆管换热器的两相流动和换热模型,进行了相应的数值模拟计算。数值计算得到不同加热强度和鼓泡流量下的对流换热性能,与相应试验结果进行了比较分析。利用相似理论和量纲分析,推导了内热源液池内两相流动换热的无因次准则关系式,根据数值计算结果总结出换热Nu数的经验关系式。最后,分析比较了竖直和水平圆管换热器的两相对流换热特性,为溶液堆内换热器设计和布置提供理论参考。 Based on the geometrical structure and operation condition of test prototype of medical isotope reactor, the three-dimensional physical and mathematical models on the natural convection and bubbly driven two-phase convective heat transfer in the pool with internal heat source and with horizontal and vertical tube heat exchanger immerged were proposed, and the corresponding numerical simulation was performed. The computed heart transfer coefficients for different internal heat source and bubble flow rate were gained and compared with the detected ones by employing the analogy theory and dimension analysis, the empirical criteria correlations of Nusselt number of two phase heat transfer for the horizontal and vertical heat transfer exchanger was derived and compared with each other, which was provided with theoretical reference for the selection of the heat exchanger tube layout.
出处 《核动力工程》 EI CAS CSCD 北大核心 2009年第4期41-46,共6页 Nuclear Power Engineering
基金 中国核动力研究设计院空泡物理和自然循环重点实验室2005年基金5148209105JW2001资助
关键词 自然对流 鼓泡驱动流 耦合传热 数值模拟 Natural convection, Bubbly driven flow, Conjugated heat transfer, Numerical simulation
  • 相关文献

参考文献9

  • 1Delnoij E, Lammers F A, Kuipers J A M, et al. Dynamic Simulation of Dispersed Gas-Liquid Two-Phase Model[J]. Chemical Engineering Science, 1997, 52:1429 - 1458.
  • 2Majumdar D M, Farouk B, Shah Y T. Hydrodynamic Mod- eling of Three-Phase Flows Through a Vertical Column[J]. Chemical Engineering Science, 1997, 52:4485 - 4497.
  • 3Sokolinch A, Eigenberger G, Applicability of the Standard K-ε Turbulence Model to the Dynamic Simulation of Bubble Columns: Part I .Detailed Numerical Simulations[J].Chemical Engineering Science, 1999,54, 2273 - 2284.
  • 4欧阳洁,李静海.鼓泡流化床中动态行为的离散模拟[J].自然科学进展(国家重点实验室通讯),2000,10(2):154-160. 被引量:3
  • 5尾花英朗,徐中权.热交换器设计手册[M].北京:石油工业出版社,1982.
  • 6Qinghua Chen, Amano R S, Zhou, Linli, et al. Evaporative Heat Transfer Experiment of Air-Water Bubbly Flow[C]. Proceedings of the 2003 AS/VIE Design Engineering Technical Conferences and Computers and Information in Engineering Conference, 2003, 1:712 - 721.
  • 7崔文智,陈清华,李隆键,周琳莉.空气-水鼓泡流动的阻力与蒸发传热特性[J].重庆大学学报(自然科学版),2004,27(11):88-91. 被引量:1
  • 8郭锦烈.两相与多相流体力学[M].西安:西安交通大学出版社.2002.
  • 9刘叶,卢冬华,陈军等.均匀内热源池式空间盘管换热器传热特性研究[R].空泡物理和自然循环实验室年报,2006,233-236.

二级参考文献8

  • 1曹玉春,李晓东,严建华,池涌,岑可法.管式布风流化床密相区气固流动特性数值模拟[J].浙江大学学报(工学版),2005,39(6):795-800. 被引量:5
  • 2[1]ESMAEELI A, TRYGGVASON G. Direct numerical simulations of bubbly flows. Part I. Low Reynolds number arrays[J]. J Fluid Mech, 1998, 377:313-345.
  • 3[2]DUDUKOVIC M P, DEVANATHAN N. Bubble column reactors: some recent developments in chemical reactor technology for environmentally safe reactors[J]. NATO ASI Series E Appl Sci, 1993, 225:379-408.
  • 4[3]KUMAR S B, DEVANATHAN N, MOSLEMIAN D, et al. Effect of scale on liquid recirculation in bubble columns[J]. Chem Eng Sci, 1994, 49(24B):5 637-5 652.
  • 5[4]ADKINS D R, SHOLLENBERGER K A I, O'HERN T J, et al. Pressure effects on bubble column flow characteristics[A]. ANS Proceedings of the National Heat Transfer Conference[C]. American Nuclear Society, Lagrange Park, IL., 1996:318-325.
  • 6[6]MIZUSHINA,MIYASHITA. A new design of gas-liquid contacting heat exchanger[J]. Journal of Chemical Engineering Japan, 1968, 32(10): 987-992.
  • 7尾花英朗.热交换器设计手册[M].北京:石油工业出版社,1981..
  • 8欧阳洁,李静海.模拟气固两相流动非均匀结构的颗粒运动分解轨道模型[J].中国科学(B辑),1999,29(1):29-38. 被引量:22

共引文献12

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