期刊文献+

直接接触式蒸汽发生器传热性能分析 被引量:3

Analysis of the Heat Transfer Performance of a Direct Contact Type Steam Generator
原文传递
导出
摘要 本文建立了直接接触式蒸汽发生器的数理模型,模拟分析了直接接触式蒸发器的独立变量,如:初始换热温差、工质流率和导热油流率及它们对容积换热系数、总换热体积、工质蒸汽发生量及工质蒸汽出口温度等蒸发器主要换热性能的影响,同时通过试验手段对所建立的数理模型进行了验证,结果表明:蒸汽发生器性能理论曲线与试验值一致性较好,且各独立变量与换热性能间存在复杂的非线性函数关系,为了获得最佳换热性能,有必要对换热系统进行多参数并进行优化。 Established was a mathematical model for direct contact type steam generators,simulated and analyzed was the influence of such independent variables of a direct contact type steam generator as the initial heat exchange temperature difference and the working medium flow rate and heat conduction oil flow rate on the main performance of a steam generator such as its volumetric heat exchange coefficient,total heat exchange volume,working medium steam production capacity and the temperature of the working medium at the outlet and at the same time verified was the mathematical model thus established through employing the test means. It has been found that the values obtained from the theoretical curves of the performance of the steam generator has a relatively good agreement with the test values and a complicated non-linear function relationship does exist between various independent variables and the heat exchange performance. In order to obtain the optimum heat exchange performance,it is necessary to perform a parallel optimization of the heat exchange system.
出处 《热能动力工程》 CAS CSCD 北大核心 2016年第7期15-21,130-131,共7页 Journal of Engineering for Thermal Energy and Power
基金 国家自然科学青年基金资助项目(51406071) 云南农业大学自然科学青年基金资助项目(2015ZR14) 云南省自然科学基金资助项目(2013FB020)
关键词 直接接触式蒸汽发生器 数理模型 容积换热系数 含气率 direct contact type steam generator mathe-matical model volumetric heat exchange coefficient gas content
  • 相关文献

参考文献10

  • 1T. Nomura,M. Tsubota,T. Oya,et al. Heat storage in direct-contact heat exchanger with phase change material [ J ]. Applied Thermal Engineering,2013,50( 1 ) :26 -34.
  • 2P. Zhang,Y. P. Wang,C. L. Guo,et al. Heat transfer in gas-liquid- liquid three-phase direct.-cantact exchanger [ J ]. Chemical Engi- neering Journal,2001,84(3) : 381 -388.
  • 3T. Lemcnand, C. Durandal, D. Della Valle, et al. Turbulent direct- contact heat transfer between two immiscible fluids [ J ]. Interna- tional Journal of Thermal Sciences,2010,49(10) : 1886 -1898.
  • 4Zhang P. , Wang Y. P. , Guo C. L. , et al. Heat transfer in gas-liq- uid-liquid three-phase direct-contact exchanger [ J ]. Chemical En- gineering Journal,84(3) (2001) 381 -388.
  • 5T. Coban, R. Boehm. Performance of a three-phase spray column, direct-contact heat exchanger [ J ]. Transactions of the ASME, 1989,(111) : 165 -172.
  • 6Artur Steiff, Mechael Nitsche, Paul-Michael Weinspach. Heat re- moval by evaporation of volatile component [ J ]. 9th Int. Heat Transfer Conf:Iemsalem Israel. 1990.3:51 -56.
  • 7[美]JosephKestin,主编.地热和地热技术发电指南[M].西藏地热工程处译.水利电力出版社,1988:275-276.
  • 8G. K. Raina, R. K. Wanchoo, P. D. Grover. Direct contact heat transfer with phase change: Motion of evaporating droplets [ J ]. AIChE Journal, 1984,30 (5) : 835 - 837.
  • 9Mark A. Young, Ruben G. Carbonell, David F. OUis. Airliftbiore- actors: Analysis of local two-phase hydrodynamics [ J ]. AIChE Journal,1991,37(3) : 403 -428.
  • 10Pal, S. S. , A. K. Mitra, A. N. Roy. Pressure drop and holdup in vertical two-phase eourrent flow with improved gas-liquid mixing [J]. Ind. Eng. Chem. Process Des. Dev., 1980, 19 (67):112 - 123.

同被引文献17

引证文献3

二级引证文献4

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