An Experimental Study on Heat/Mass Transfer From a Rectangular Cylinder-Reference-Cited by-同舟云学术

An Experimental Study on Heat/Mass Transfer From a Rectangular Cylinder

Published:2003-11-19 Issue:6 Volume:125 Page:1163-1169
ISSN:0022-1481
Container-title:Journal of Heat Transfer
language:en
Short-container-title:

Author:

Yoo Seong-Yeon¹,Park Jong-Hark¹,Chung Chang-Hwan²,Chung Moon-Ki²

Affiliation:

1. Department of Mechanical Design Engineering, Chungnam National University, Gungdong, Yusungku, Daejeon, 305-764, Korea

2. Korea Atomic Energy Research Institute, Dukjindong, Yusungku, Daejeon, 305-353, Korea

Abstract

Local and average mass transfer rates from a rectangular cylinder having various width to height ratios are measured using naphthalene sublimation technique, and influence of flow characteristics on mass transfer is investigated. The experimental apparatus comprises a wind tunnel, a naphthalene casting facility and a sublimation depth measurement system. Mass transfer data are compared with those of heat transfer which are obtained using thermocouples in the constant heat flux boundary condition, and analogy between heat and mass transfer is examined. The reasons for discrepancy in both transport values are explained in detail.

Publisher

ASME International

Subject

Mechanical Engineering,Mechanics of Materials,Condensed Matter Physics,General Materials Science

Link

http://asmedigitalcollection.asme.org/heattransfer/article-pdf/125/6/1163/5790637/1163_1.pdf

Reference15 articles.

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2. Igarashi, T. , 1985, “Characteristics of the Flow Around Rectangular Cylinders (The Case of the Angle of Attack 0 deg),” Bull. JSME, 28, pp. 1690–1696.

3. Igarashi, T. , 1985, “Heat Transfer from a Square Prism to an Air Stream,” Int. J. Heat Mass Transfer, 28, pp. 175–181.

4. Igarashi, T. , 1986, “Local Heat Transfer from a Square Prism to an Air Stream,” Int. J. Heat Mass Transfer, 29, pp. 774–784.

5. Igarashi, T. , 1987, “Fluid Flow and Heat Transfer Around Rectangular Cylinders (The Case of Width/height Ratio of a Section of 0.33–1.5),” Int. J. Heat Mass Transfer, 30, pp. 893–901.

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