Liquid film falling behaviour on horizontal circular cylinder

Han-shik Chung , K. Wusiman , Seong-soo Kim , B. Nasan , H. Afrianto , Hafizur Rehman , Du-youl Choi , Hyo-min Jeong

Journal of Central South University ›› 2012, Vol. 19 ›› Issue (5) : 1353 -1358.

PDF
Journal of Central South University ›› 2012, Vol. 19 ›› Issue (5) : 1353 -1358. DOI: 10.1007/s11771-012-1149-4
Article

Liquid film falling behaviour on horizontal circular cylinder

Author information +
History +
PDF

Abstract

The flow pattern behaviour of falling liquid film over three horizontal cylinders was evaluated. These flows can take three forms: discrete droplets, individual jets, and continuous sheet, and special attention is paid to the effects of the physical properties and geometrical parameters of the first two forms (droplets and jets) because these forms are more important in heat-transfer behaviour and less research has been published for these forms. The flow modes and experimental results were successfully compared with previous experimental literatures, and also the effects of liquid flow rate, tube diameter, and tube spacing on departure site spacing, in both drop and jet modes, were evaluated in the low Galileo number and high viscosity fluid (cooking oil), to help developing criteria for determining falling film modes and their transitions, and to understand the heat transfer characteristics associated with each mode.

Keywords

falling film / flow mode / cylinder

Cite this article

Download citation ▾
Han-shik Chung, K. Wusiman, Seong-soo Kim, B. Nasan, H. Afrianto, Hafizur Rehman, Du-youl Choi, Hyo-min Jeong. Liquid film falling behaviour on horizontal circular cylinder. Journal of Central South University, 2012, 19(5): 1353-1358 DOI:10.1007/s11771-012-1149-4

登录浏览全文

4963

注册一个新账户 忘记密码

References

[1]

MITROVIC J. Influence of tube spacing and flow rate on heat transfer from a horizontal tube to a falling liquid film [C]// Proceedings of the 8th International Heat Transfer Conference. San Francisco, 1986: 1949–1956.

[2]

HuX., JacobiA. M.. The intertube falling film: Part I-Flow characteristics, mode transitions, and hysteresis [J]. Heat Transfer, 1996, 118: 616-625

[3]

HU X, JACOBI A M. Departure-site spacing for liquid droplets and jets falling in thin-film heat exchangers [J]. ACRC CR9, 1997, Urbana, IL61801. 217: 333–3115.

[4]

LienhardJ. H., WongP. T. Y.. The dominant useable wavelength and minimum heat flux during film boiling on a horizontal cylinder [J]. Heat Transfer, 1964, 86: 220-226

[5]

BellmanR., PenningtonR. H.. Effects of surface tension and viscosity on Taylor instability [J]. Appl Math, 1954, 12: 151-162

[6]

YungD., LorentzJ., GanicE. N.. Vapor/liquid interaction and entrainment in falling film evaporators [J]. Heat Transfer, 1980, 102: 20-25

[7]

TaghaviK., DhirV. K.. Taylor instability in boiling, melting and condensation or evaporation [J]. Heat Mass Transfer, 1980, 23: 1433-1445

[8]

AMBRUSTER R, MITROVIC J. Heat transfer in falling film on a horizontal tube [C]// Proceedings of the National Heat Transfer Conference, 1995: 13–21.

[9]

HuX., JacobiA. M.. The intertube falling film: Part 2-Mode effects on sensible heat transfer to a falling liquid film [J]. Heat Transfer, 1996, 118: 626-633

[10]

MohamedA. M. I.. Flow behaviour of liquid falling film on a horizontal rotating tube [J]. Experimental Thermal and Fluid Science, 2007, 31: 325-332

[11]

TANG J, LU Z, B. Yu-Chi. Droplet spacing of falling film flow on horizontal tube bundles [C]// Proceedings of the 18th International Congress of Refrigeration. Montreal, 1991: 474–478.

AI Summary AI Mindmap
PDF

130

Accesses

0

Citation

Detail

Sections
Recommended

AI思维导图

/