本實驗主要目的為:改善交錯型鰭管式熱交換器的熱傳性能,利 用修正型的凹窩當作渦流產生器,試圖在適量增加壓降範圍內,增加 熱傳性能,最後會將平板、VG、百葉窗三種鰭片作分析,如下:
(1)在鰭片間距皆為 1.6mm 的情況下,單排管時,VG 型在熱傳 係數大概上升 5~8%,壓降部份大約有 25~30%的上升;百葉窗型雖 然在熱傳係數方面增加較多,有 15~30%的提升量,但也伴隨著 40~50%的壓降增幅。在兩排管時,VG 型提升了 10~15%的熱傳,壓 降也增加約 30~40%;百葉窗型則是有 20~30%的熱傳改善,但壓降 也增加較多,大約增加有 35~50%。在四排管時,不管 VG 還是百葉 窗型,其熱傳與壓降的表現皆與兩排管類似。
(2)在鰭片間距為 2.0mm 時,單排管的 VG 型鰭片,熱傳係數增 加了 8~13%,壓降也同時上升了將近 40%;而至於百葉窗鰭片,在 熱傳係數較平板多出 8~20%,但壓降也多了 35~50%。至於在兩排管 時,VG 型的熱傳係數則是增加約 15%,壓降則是增加 35%左右;百 葉窗型分別增加 17%、40%。四排管時,這兩者的差異性就相當小,
熱傳係數差不多皆增加 17%,壓降約多 38~40%。
(3)鰭片間距由 1.6mm 增至 2.0mm 時,對於百葉窗型鰭片的熱傳 影響甚大,在風速較低的情形下,VG 型鰭片的熱傳效果會較佳。
(4)本實驗使用 VG-1 以及 FG-3 評價方法,結果皆說明:在多數 的情況下,當間距為 1.6mm 時,使用百葉窗型鰭片會是較佳的選擇。
但是,當間距增加,反而會使得 VG 型整體效率提升。
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參考文獻
1. Jacobi A.M.,and Shah R.K.“Heat Transfer Surfaces Enhancement Through the Use of Longitudinal Vortices: A Review of Recent Progress,” Experimental Thermal and Fluid Science, Vol. 11, pp.
295-309, 1995.
2. Fiebig M.”Vortices Generators and Heat Transfer,” Trans. IchemE, Vol.
76,pp. 108-123,1998.
3. 王啟川,”熱交換器設計”,五南圖書出版股份公司,2007 年初版。
4. Edwards F.J., and Alker G.J.R.” The Improvement of Forced Convection Surface Heat Transfer Using Surfaces Protrusions in the Form of (A) cubes and (B) Vortex Generators” , Proc. 5th Int. Heat Transfer Conf., Vol. 2, pp. 244-248 , 1974,.
5. Tiggelbeck S., Mitra N.K., and Fiebig M., ”Comparison of Wing-Type Vortex Generators for Heat Transfer Enhancement in Channel Flows,”
ASME J. of Heat Transfer , Vol. 166 , pp. 880-885 , 1994.
6. Tiggelbeck S., Mitra N.K., and Fiebig M.”Experimental Investigation of Heat Transfer Enhancement and Flow Losses in a channel with Double Rows of Longitudinal Vortex Generators,” Int. J. Heat Mass Transfer, Vol. 36, pp. 2327-2337,1993.
7. Biswas G., Mitra N.K., and Fiebig M.”Heat Transfer Enhancement in Fin-Tube Heat Exchangers by Winglet Type Vortex Generators,” Int. J.
of Heat and Mass Transfer”, Vol. 37, pp. 283-291,1994.
8. Fiebig M., Valencia A., and Mitra N.K. “Wing-Type Vortex Generators for Fin-and-Tube Heat Exchangers,”Experimental Thermal and Fluid Science, Vol. 7, pp. 287-295,1993.
74
9. Fiebig M., Valencia A., and Mitra N.K.,“Heat Transfer Enhancement by Longitudinal Vortices in a Fin-Tube Heat Exchanger Element with Flat Tubes,” ASME J. of Heat Transfer, Vol. 118, pp. 209-211,1996.
10. Fiebig, M., Valencia, A. and Mitra, N.K., “Local Heat Transfer and Flow Losses in Fin-and-Tube Heat Exchangers with Vortex Generators:
A Comparison of Round and Flat Tubes,”Experimental Thermal and Fluid Science,Vol. 8pp.35-45, 1994
11. Chen, Y., Fiebig, M. and Mitra N.K. “Conjugate Heat Transfer of a Finned Tube with a Punched Longitudinal Vortex Generator in Form of a Delta Winglet-Parametric Investigations of the Winglet”, Int. J. of Heat and Mass Transfer, Vol. 41,pp. 3961-3978,1998
12. Chen, Y., Fiebig, M. and Mitra N.K. ”Heat Transfer Enhancement of a Finned Tube with Punched Longitudinal Vortex Generator In-Line ”, Int. J. of Heat and Mass Transfer, Vol. 41,pp. 4151-4166,1998
13. Chen, Y., Fiebig, M. and Mitra N.K. ”Heat Transfer Enhancement of a Finned Tube with Staggered Punched Longitudinal Vortex Generator,”
Int. J. of Heat and Mass Transfer, Vol. 43, pp. 417-435,2000
14. Wang C.C., Lo J., Lin Y.T. and Liu M.S. “Flow Visualization of Wavy-Type Vortex Generator Having Inline Fin-Tube Arrangement,”
Int. J. of Heat and Mass Transfer, Vol. 45,pp. 1933-1944,2001
15. Lin C.N. and Jang J.Y. “Conjugate Heat Transfer and Fluid Flow Analysis in Fin-Tube Heat Exchanger with Wavy-Type Vortex Generators,” J. of Enhanced Heat Transfer, Vol. 9, pp. 123-136, 2002 16. Wu J.M. and Tao W.Q. “Investigation on laminar convection heat
transfer in fin-and-tube heat exchanger in aligned arrangement with longitudinal vortex generator from the viewpoint of field synergy principle,” Applied Thermal Engineering, Vol. 27, pp. 2609-2617,
75
2007.
17. Chu P., He Y.L., Lei Y.G.,Tian L.T., Li R., “Three-dimensional numerical study on fin-and-oval-tube heat exchanger with longitudinal vortex generators,” Applied Thermal Engineering, Vol. 29, pp.
859-876, 2009.
18. Chyu M. K., Yu Y., Ding H., Downs J. P. and Soechting F.
“Concavity Enhanced Heat Transfer in an Internal Cooling Passage
,
” ASME Paper No.97-GT-437, ASME 42nd Int. Gas Turbine and Aero Congress, Orlando, FL. , 1997.19. Moon H. K., Connell T. O’ and Glezer B. “Channel Height Effect on Heat Transfer and Friction in a Dimpled Passage,” ASME Paper No.99-GT-163, ASME Turbo Expo, 1999.
20. Ligrani P. M., Mahmood G. I., Harrison J. L., Clayton C. M., and D. L.
Nelson “Flow Structure and Local Nusselt Number Variations in a Channel with Dimples and Protrusions on opposite Walls,” Int. J. of Heat and Mass Transfer, Vol. 44, pp. 4413-4425, 2001.
21. Hwang S. D., Cho H. H.“Heat Transfer Enhancement of Internal Passage Using Dimple/Protrusion”, HTE-24.
22. Weimershirch H., Martin J. , Clerquin Y., Alexandre P. and Jiraskova S.”Energy Saving in Flight Formation,” Nature, Vol 413, pp.697-698.
23. He J., Liu L., Jacobi A. M.“Air-Side Heat-Transfer Enhancement by a New Winglet-Type Vortex Generator Array in a Plain-Fin Round -Tube Heat Exchanger,” J. of Heat Transfer, Vol. 132, pp. 071801-1~9, 2010.
24. ANSI / AMCA 210-85”Laboratory Method of Testing Fans for Rating,”
American National Standard.
76
25. Schmidt Th.E., Heat transfer calculation for extended surfaces, Refrigerating Engineering ,pp.351-357.
26. Kays W.M. and London A.L. Compact Heat Exchanger. 3rd ed. New York: McGraw-Hill.
27. Webb R.L., Principle of Enhanced Heat Transfer, Chap. 3, John Wiley
& Sons, Inc.,1994.
28. Tafti D. K. and Zhang X. ”Geometry effects on flow transition in multilouvered fins – onset, propagation, and characteristic fre- quencies ,” Int. J. of Heat and Mass Transfer, Vol. 44, pp.
4195-4210,2001.
29. DeJong N. C. and Jacobi A. M.”Localized Folw and Heat Transfer Interactions in Louvered-Fin Arrays,” Int. J. of Heat and Mass Transfer ,Vol. 46,pp. 443-455,2003.