欢迎登录材料期刊网

材料期刊网

高级检索

在流速0.34 m/s,管外水浴温度60℃和相同管内工质入口温度的条件下,分别在实验室进行了缩放管及其对应光管管内污垢的对比实验.实验的污垢种类是浓度为1000 mg/L的MgO颗粒污垢、硬度800 mg/L的人工硬水作为工质的CaCOa析晶污垢和MgO颗粒与CaCO3析晶混合污垢.结果表明,缩放管具有较好的阻垢性能,但诱导期小于对应光管的诱导期.

参考文献

[1] 杨善让;徐志明;孙灵芳.换热设备的污垢与对策[M].北京:科学出版社,2004
[2] Somerscales E F C;Ponteduro A F;Bergles A E .Particulate Fouling of Heat Transfer Tubes Enhanced on Their Inner Surface, Fouling and Enhancement Interaction[R].ASME HTD-164,1991.
[3] 帅志明;冯海仙;李学泰 .螺旋槽管结垢实验研究[J].中国电机工程学报,1993,14(02):7-12.
[4] Webb R L;Kim N H.Particulate Fouling in Enhanced Tubes[A].New York:ASME,1989:108,315-323.
[5] Li W;Webb R L .Fouling in Enhanced Tubes Using Cooling Tower Water Part Ⅰ: Long-term Fouling Data[J].International Journal of Heat and Mass Transfer,2000,43(19):3567-3578.
[6] Li W;Webb R L .Fouling in Enhanced Tubes Using Cooling Tower Water Part Ⅱ: Combined Particulate and Precipitation Fouling[J].International Journal of Heat and Mass Transfer,2000,43(19):3579-3588.
[7] Dreyster G A;Gorman V l;Aronov I Z .Comparison of Fouling in Tubes with Annular Turbulence Promoters and in Smooth Tubes of Shell-and-Tube Heat Exchangers[J].Heat Transfer-Soviet Research,1983,15:87-93.
[8] Webb R L.Principles of Enhanced Heat Transfer[M].New York: Wiley Interscience,1994
[9] 邓先和,赵晓曦,张亚君.轴流式双壳程缩放管管壳式换热器的工业试验[J].石油炼制与化工,2002(02):11-14.
[10] 张亚君,欧阳荣,邓先和,李志武.强化传热管内的自然对流沸腾换热[J].华南理工大学学报(自然科学版),2004(01):41-43,48.
[11] 付卉,罗小平,邓先和.缩放管传热系数的预测[J].石油化工设备,2004(01):24-26.
[12] 陈颖,邓先和,丁小江,王杨君.场协同理论对充分发展湍流传热性能的数值分析[J].华南理工大学学报(自然科学版),2003(07):42-47,57.
[13] 徐志明,甘云华,张仲彬,杨善让.弧线管传热与污垢性能的实验研究[J].工程热物理学报,2004(03):496-498.
[14] Glen N F;Howarth J H;Jenkins A M.The Estimation of Errors and Uncertainty in the Determination of Fouling Resistances[A].Italy,1997
上一张 下一张
上一张 下一张
计量
  • 下载量()
  • 访问量()
文章评分
  • 您的评分:
  • 1
    0%
  • 2
    0%
  • 3
    0%
  • 4
    0%
  • 5
    0%