期刊文献+

平行流型列管式固定床反应器的流体力学设计 被引量:1

下载PDF
导出
摘要 提出了平行流列管式固定床反应器管间载热体流动的数学模型。根据此数学模型来设计工业反应器的分布板,在板上合理开设环隙孔或附加开孔,就能实现管间的均匀传热。本文引入的速度均匀率(VUI)可用来定量表示载热体在管间的均匀分配,并给出了设计计算程序。
出处 《化工设计》 CAS 1993年第5期21-26,14,共7页 Chemical Engineering Design
  • 相关文献

同被引文献17

  • 1刘永兵,陈纪忠,阳永荣.固定床反应器中错流流动的数值模拟[J].高校化学工程学报,2006,20(4):527-532. 被引量:4
  • 2CAOXiao-li(曹晓丽).固定床反应器管间流体流动特性的研究[D].上海:华东理工大学,2008.
  • 3Baptista C M S G Cell models of the shell-side flow in multitubular reactors [J]. Ind Eng Chem Res, 1993, 32(6): 1093-1101.
  • 4Stankiewicz A. An advances in modelling and design of multitubular fixed-bed reactors [J]. Chem Eng Teehnol, 1989, 12(1): 113-130, 170-175.
  • 5Stankiewicz A. Dynamic modelling of multitubular catalytic reactors [J]. Chem Eng Technol, 1991, 14(6): 414-420.
  • 6Maciel Filhor. Computer aided design for large scale multitubular reactors [J]. Comput Chem Eng, 1998, 22(supplement 1): 711-714.
  • 7Huadong Li, Volker Kottke. Effect of the leakage on pressure drop and local heat transfer in shell-and-robe heat exchangers for staggered tube arrangement [J]. Int J Heat Mass Transfer, 1998, 41(2): 425-433.
  • 8Huadong Li, Volker Kottke. Analysis of local shellside heat and mass transfer in the shell-and-tube heat exchanger with disc-and-doughnut baffles [J]. International Journal of Heat and Mass Transfer, 1999, 42(18): 3509-3521.
  • 9Davide Del Col, Angelo Muzzolon, Pierangelo Piubello, et al. Measurement and prediction of evaporator shell-side pressure drop [J]. International Journal of Refrigeration, 2005, 28: 320-330.
  • 10Uday C, Kapale, Satish Chand. Modeling for shell-side pressure drop for liquid flow in shell-and-tube heat exchanger [J]. International Journal of Heat and Mass Transfer, 2006, 49(3-4): 601-610.

引证文献1

二级引证文献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