A Transient Mixed Convection of A Second Grade Viscoelastic

碩士 === 中原大學 === 機械工程研究所 === 84 === A transient mixed convection of a second grade viscoelastic fluid past an inclined backward facing step is studied to reveal combined effects of the Reynolds number, the elastic coefficient and the inclina...

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Bibliographic Details
Main Authors: LIN ,YEN-HON, 林彥宏
Other Authors: HSU,CHENG-HSING
Format: Others
Language:zh-TW
Published: 1996
Online Access:http://ndltd.ncl.edu.tw/handle/12997023586500208678
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Summary:碩士 === 中原大學 === 機械工程研究所 === 84 === A transient mixed convection of a second grade viscoelastic fluid past an inclined backward facing step is studied to reveal combined effects of the Reynolds number, the elastic coefficient and the inclination angle of the channel on the flow and heat transfer. A numerical simulation method is used in the present study. A finite difference method is applied to the stream-vorticity function and energy equations. Related numerical schemes are point and line Gauss-Seidel methods, successive over-relaxation method and alternating-direction method. Results indicate that a primary recirculation zone is formed on the bottom plate, and is located at downstream of the step. Generally speaking, the reattachment length increases with an increase in the inclinati- on angle to a maximum length, and then decreases when the inclination increases further. However, a few cases show a diff- erent trend due to a complicated interaction of forces. The maximum value of the reattachment length is occurred when the inclination angle is 150°or 180°. The reattachment length increases with an increase in Reynolds number and a lowering in elastic coefficient. Under this condiction, the reattachment length is close to or over-shooting the position of local maximum Nux value. In other inclination angle, the position of local maximum Nux value is in the downstream of the reattachment point. With increasing inclination angle, the contact point of isotherm and upper plate moves upward originally, and then it moves downward. The inclination angle is arround 150°when the contact point is close to upstream flow. The moving phenomian is more obvious in the lower elastic coefficient range.