期刊文献+

蓄热式催化蒸汽重整氢气发生器中蓄热体数值分析 被引量:4

Numerical Analysis for a Regenerative and Generative Hydrogen Unit
下载PDF
导出
摘要 利用数值计算对蓄热体的换热进行分析,给出影响蓄热体换热的因素,进行优化设计,得到了更合理的结果.根据优化设计,提出了重整器运行的建议参数,包括换向时间、比表面积、陶瓷载体导热系数和陶瓷密度及其比热.计算表明,增加比表面积,可以提高蓄热体的蓄热能力并提高余热回收率.同时,计算表明,对于蓄热式催化重整器而言,燃料与水蒸汽的流动方向应采用与热烟气相同的流动方向. It is a new type of hydrogen generator that is regenerative and can produce hydrogen by catalytic steam reforming.The generator is a key part of the device. According to the numerical simulation, we analyzed the heat transfer in the regenerator, gave the factors of heat transfer in the generator, and conducted the optimum design. The generator can be designed more reasonably and more effectively. According to optimum design, the operating parameters for reforming device including the time of changing direction, specific surface area, conductivity, density and specific heat of ceramic carrier were suggested. The computations show that with the increase of specific surface area, the regenerative energy by regenerator increases, so does recover rate of heat amount. The computations also show that for a regenerativereforming device, the flow direction of fuel and steam is the same as that of flue gas.
出处 《燃烧科学与技术》 EI CAS CSCD 2003年第3期261-266,共6页 Journal of Combustion Science and Technology
关键词 蓄热体 催化蒸汽重整反应 氢发生器 换热因素 regenerator catalytic steam reforming reaction hydrogen generator heat transfer factors
  • 相关文献

参考文献3

  • 1蒋绍坚,曹小玲,汪洋洋,熊家政,李勇,鲁志昂.蜂窝陶瓷蓄热体传热数学模型及传热系数求解[J].工业炉,2001,23(3):50-53. 被引量:16
  • 2Fu Weibiao, Qin Chuan, Li Changle. Experimental study on ignition of premixed gases with steam under catalytic reforming reaction[ J ].Fuel Processing Technology,2001,72 : 131-143.
  • 3Fu Weibiao, Hou Lingyun, Zhong Beijing et al. An analysis of the ignition of premixed gases by a hot spherical surface with catalytic reforming reaction [ J ]. Fuel,2002,82 : 539-544.

二级参考文献3

共引文献15

同被引文献22

  • 1李茂德,程惠尔.高温空气燃烧系统中陶瓷蓄热体传热特性分析研究[J].热科学与技术,2004,3(3):255-260. 被引量:24
  • 2陈红,何祖威.一维流体相变过程的统一分布参数模型及数值仿真方法[J].系统仿真学报,2005,17(3):571-573. 被引量:4
  • 3HIROSHI T,GUPTA A,JASEGAEA T,et al.High temperature air combustion from energy conservation to pollution reduction[M].Sweden:The CRC Press,2003.
  • 4須滕淳,多田健.ハニカム型リジェネ燃焼シヌテムの開發と應用事例[J].工業加熱,1998,35(3):26-35.
  • 5SHAH R K.A correlation for longitudinal heat conduction effects periodic flow heat exchanger[J].ASME J Eng Power,1995,97:453-454.
  • 6SHEN C M,WOREK W M.The effect of wall conduction on the performance of regenerative heat exchanger[J].Energy,1992,17:1199-1213.
  • 7HILL A,WILLMOTT A J.Accurate and rapid thermal regenerator calculations[J].Int J Heat Mass Transfer,1989,32:465-476.
  • 8DRAGUTINOVIC G D,BACLIC B S.Operation of counter-flow regenerators (international series on developments in heat transfer V4)[M].Boston:Computational Mechanics Publications,1998.
  • 9ZHENG C H,CLEMEMNTS B.The thermal performance characteristics of regenerators in HiTACG furnaces[A].Gaswarme-Institute E V Essen 6th International Symposium on High Temperature Air Combustion and Gasification[C].Ruhrgebiet:Gaswarme-Institut International,2005.1-12.
  • 10KLEIN H,EIGENBERGER G.Approximate solutions for metallic regenerative heat exchangers[J].Int J Heat and Mass Transfer,2001,44:3553-3563.

引证文献4

二级引证文献2

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