期刊文献+

缠绕管中结晶结垢的模拟研究

Simulation of Crystal Scaling in Helical Tube
下载PDF
导出
摘要 利用CFD模拟探究了缠绕管结构参数与操作参数对管内结垢的影响。结果表明,在相同的传热面积下,缠绕直径越小,传热效率越高,管内流体温度更高,管内更容易形成污垢。管径越小,管壁温度越容易传递到管内流体,管内更容易形成污垢。而缠绕角度则不会影响管内的结垢规律。与直管相比,当换热面积相同且恒定壁温或恒定热流时,缠绕管内流体温度较高,结垢率更大。当换热面积和换热量相同时,缠绕管内结垢率更小。 This work used CFD simulation to investigate the influence of helical pipe structure parameters and operating parameters on the fouling in the tube.Results showed that with the same heat exchange area, the smaller the helical tube diameter, the higher the heat transfer efficiency, and the higher the temperature of the fluid in the tube, which made it easier to form fouling in the tube. The smaller the pipe diameter, the easier it was for the pipe wall temperature to be transferred to the fluid in the pipe, leading to easier fouling in the pipe. The helical angle would not affect the fouling law in the tube. Compared with straight pipes, when the heat exchange area was the same with the constant wall temperature or the heat flow was constant, the fluid temperature in the helical pipe was higher, and the fouling rate was greater. When the heat exchange area and heat exchange amount were the same, the fouling rate in the helical pipe was smaller.
作者 钟维民 郭燕妮 Zhong Weimin;Guo Yanni(China Petroleum&Chemical Corporation,Beijing 100728;Zhejiang University,Hangzhou 310027,China)
出处 《广东化工》 CAS 2021年第9期42-46,共5页 Guangdong Chemical Industry
关键词 缠绕管 CFD模拟 结垢 结构参数 操作参数 helical tube CFD simulation crystal fouling structure parameters operating parameters
  • 相关文献

参考文献6

二级参考文献48

  • 1汪家铭.低温甲醇洗净化工艺技术进展及应用概况[J].江苏化工,2007,26(4):13-17. 被引量:12
  • 2赵国华,姜峰,李修伦.超声波技术在制盐工业中的应用前景[J].海湖盐与化工,2004,33(5):34-36. 被引量:8
  • 3鲍智江,李建隆,王伟文.硫酸钙在调和液中的溶解度[J].化学工程,1995,23(5):21-25. 被引量:33
  • 4Garrett-Price B A. Fouling of Heat Exchangers Characterristics Costs Preventoin Contral and Removal Noyes Publications[J]. Park Ridge N. J, 1985.
  • 5Suitor J W, Marner W J, Ritter R B. The History and Status of Research in Fouling of Heat Exchanger in Cooling Water Service [J]. The Canadian Journal ofChemicalEngineering, 1977, (55): 374-380.
  • 6Epstein N. Fouling in Heat Exchangers[C]. In Proceedings of the Sixth International Heat Transfer Conference. Toronto, Canada, August, Vol. 4, Hemisphere, Washington, D. C. , 1978: 279-284.
  • 7刘中良,1996年
  • 8STEINHAGEN R,STEINHAGEN H M,MAANI K.Problems and costs due to heat exchanger fouling in New Zealand industries[J].Heat Transfer Engineering,1993,14(1):19-30.
  • 9LEE S H.A study of physical water treatment technology to mitigate the mineral fouling in heat exchanger[D].Michigan:Drexel University,2002.
  • 10RITTER R B.Crystalline fouling studies[J].Trans ASME,1983,105:374-378.

共引文献104

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