Hostname: page-component-848d4c4894-mwx4w Total loading time: 0 Render date: 2024-06-24T06:27:36.754Z Has data issue: false hasContentIssue false

A Study of Duct Flow Passing in a Horizontal Channel with a Cylinder Source Adjacent to Planar Boundary

Published online by Cambridge University Press:  05 May 2011

L. W. Wang*
Affiliation:
Department of Mechanical Engineering, Yuan Ze University, Taoyuan, Taiwan 32003, R. O. C.
Y. C. Kung*
Affiliation:
Department of Mechanical Engineering, Yuan Ze University, Taoyuan, Taiwan 32003, R. O. C.
K. H. Lin*
Affiliation:
Department of Mechanical Engineering, Yuan Ze University, Taoyuan, Taiwan 32003, R. O. C.
S. H. Sung*
Affiliation:
Department of Mechanical Engineering, Yuan Ze University, Taoyuan, Taiwan 32003, R. O. C.
C. Y. Wu*
Affiliation:
Department of Mechanical Engineering, Yuan Ze University, Taoyuan, Taiwan 32003, R. O. C.
*
*Professor
*Research Assistant
*Research Assistant
*Research Assistant
*Research Assistant
Get access

Abstract

The purpose of the present study is to investigate laminar fully developed flow in a horizontal rectangular channel with a cylinder solutal source adjacent to planar boundary. The boundaries in this experiment include four cases:

(A) Cylinder is cathode and top plate is anode;

(B) Cylinder is anode and top plate is cathode;

(C) Cylinder is cathode and bottom plate is anode;

(D) Cylinder is anode and bottom plate is cathode.

The influences of the mass transfer rate and the boundary types between the sources have also been investigated. An experimental investigation of mixed convection mass transfer between a cylinder and a plate mass source with an electrochemical system is carried in a horizontal rectangular channel. The working fluid here is CuSO4 + H2SO4 + H2O. The shadowgraph technique is used to visualize the flow and to determine the nature and effect of solutal driven secondary flows in a horizontal channel. The ranges of the parameters in the work are Pr = 7, Ar = 1, Sc = 1700 ∼ 2400, Re = 50 ∼ 200 (Red= 12.5 ∼50), Grm = 9.45 × 105, d/H = 0.25, h/d=0, 3.

Type
Articles
Copyright
Copyright © The Society of Theoretical and Applied Mechanics, R.O.C. 2006

Access options

Get access to the full version of this content by using one of the access options below. (Log in options will check for institutional or personal access. Content may require purchase if you do not have access.)

References

1Ostrach, S., “Fluid Mechanics in Crystal Growth – The 1982 Freeman Scholar Lecture,” ASME Journal of Fluids Engineering, 105, pp. 520 (1982).CrossRefGoogle Scholar
2Kamotani, Y., Wang, L. W., Ostrach, S. and Jiang, H. D., “Experimental Study of Natural Convection in Shallow Enclosures with Horizontal Temperature and Concentration Gradients,” Int. J. Heat Mass Transfer, 28(1), pp. 165173 (1985).Google Scholar
3.Wang, L. W., Kung, Y. C. and Lai, S. D., “Heat and Mass Transfer in an Inclined Semi-Annular Enclosure,” Journal of Mechanics, 20, pp. 2732 (2004).CrossRefGoogle Scholar
4.Wang, L. W., Kung, Y. C., Wu, C. Y., Kang, M. F. and Wang, S. L., “Thermosolutal Convection in an Inclined Rectangular Enclosure with a Partition,” Journal of Mechanics, 20, pp. 233239 (2004).CrossRefGoogle Scholar
5.Cheng, K. C. and Hwang, G. J., “Numerical Solution for Combined Free and Forced Laminar Convection in Horizontal Rectangular Channels,” Journal of Heat Transfer, 91, pp. 5966 (1969).CrossRefGoogle Scholar
6.Chou, F. C. and Hwang, G. J., “Combined Free and Forced Laminar Convection in Horizontal Rectangular Channels for High ReRa,” Can. J. Chem. Eng., 62, pp. 830836(1984).Google Scholar
7.Achenbach, E., “Distribution of Local Pressure and Skin Friction Around a Circular Cylinder in Cross-Flow up to Re = 5 × 106,” Journal of Fluid Mechanics, 34, pp.625639(1968).Google Scholar
8.Bearman, P. W. and Zdravkovich, M. M., “Flow Around a Circular Cylinder Near a Plane Boundary,” Journal of Fluid Mechanics, 189(1), pp. 3348 (1978).Google Scholar
9.Angrilli, F. S., “Bergamaschi and V.Cossalter, Investigation of Wall Induced Modifications to Vortex Shedding from a Circular Cylinder,” ASME Journal of Fluids Engineering, 104, pp. 518522 (1982).CrossRefGoogle Scholar
10.Grass, A. J., Raven, P. W. J., Stuart, R. J. and Bray, J. A., “The Influence of Boundary Layer Velocity Gradients and Bed Proximity on Vortex Shedding from Free- Spanning Pipelines,” J. Energy Resources Technol., 106, pp. 7078(1984).CrossRefGoogle Scholar
11.Hsiao, F. B., Hsu, I. C. and Hsu, C. C., “Instability Modal Behavior of the Acoustically Excited Impinging Plane Jet with a Small Cylinder,” Journal of Mechanics, 20(2), pp. 145157(2004).CrossRefGoogle Scholar
12.Mao, Y., “Seabed Scour under Pipelines,” Proceedings of the Seventh International Conference on Offshore Mechanics and Arctic Engineering, Houston, TX, pp. 33–38 (1988).Google Scholar
13.Jensen, B. L., “Large Scale Vortices in the Wake of a Cylinder Placed Near a Wall,” Second International Conference on Laser Anemometry, University of Strathclyde, Glasgow, UK, pp. 111 (1987).Google Scholar
14.Zdravkovich, M., “Review of Interference-Induced Oscillations in Flow Past Two Parallel Circular Cylinders in Various Arrangements,” J. Wind Eng. Ind. Aerodyn., 28, pp. 183200 (1988).Google Scholar
15.Taneda, S., “Experimental Investigation of Vortex Streets,” Journal of the Physical Society of Japan, 20, pp. 17141721 (1965).CrossRefGoogle Scholar
16.Abou-Ellail, M. and Morcos, S. M., “Buoyancy Effects in the Entrance Region of Horizontal Rectangular Channels,” Journal of Heat Transfer, 105, pp. 924928(1983).Google Scholar
17.Incropera, F. P. and Schutt, J. A., “Numerical Simulation of Laminar Mixed Convection in the Entrance Region of Horizontal Rectangular Ducts,” Numerical Heat Transfer, 8, pp. 707729(1985).Google Scholar
18.Incropera, F. P., Knox, A. L. and Maughan, J. R., “Mixed Convection Flow and Heat Transfer in the Entrance Region of a Horizontal Rectangular Duct,” Journal of Heat Transfer, 109, pp. 434439 (1987).CrossRefGoogle Scholar
19.Mahaney, H. V., Incropera, F. P. and Ramadhyani, S., “Development of Laminar Mixed Convection Flow in a Horizontal Rectangular Duct with Uniform Bottom Heating,” Numerical Heat Transfer, 12, pp. 137155 (1987).CrossRefGoogle Scholar
20.Chou, F. C. and Hwang, G. J., “Vorticity-Velocity Method for Graetz Problem with the Effect of Natural Convection in a Horizontal Rectangular Channel with Uniform Wall Heat Flux,” Journal of Heat Transfer, 109, pp. 704710 (1987).CrossRefGoogle Scholar
21.Chou, F. C. and Hwang, G. J., “Numerical Analysis of the Graetz Problem with Natural Convection in an Uniformly Heated Horizontal Tube,” Int. J. Heat Mass Transfer, 31, pp. 12991308(1988).CrossRefGoogle Scholar
22.Schlichting, H., Boundary Layer Theory, 7th Ed., McGraw-Hill, New York (1979).Google Scholar
23.White, F. M., Viscous Fluid Flow, 2nd Ed., McGraw-Hill, New York (1991).Google Scholar
24.Wilke, C. R., “Eisenberg, M., and Tobias, C. W., “Correlation of Limiting Current under Free Convection Conditions,” J. Electrochem. Soc., 100, pp. 513523 (1953).CrossRefGoogle Scholar
25.Newman, J., Electrochemical Systems, 2nd Ed., Prentice- Hall, Englewood Cliffs, New Jersey (1991).Google Scholar
26.Kline, S. J. and McClintock, F. A., “Describing Uncertainty in Single-Sample Experiments,” Mechanical Engineering, 75, pp. 38 (1953).Google Scholar
27.Wang, L. W., Kung, Y. C., Jou, H. H. and Su, G. T., “Duct Flow Passing through a Horizontal Channel with Tandem Cylinder Sources,” Experimental Heat Transfer, 18(2), pp. 95108 (2005).CrossRefGoogle Scholar