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  1. NTU Theses and Dissertations Repository
  2. 工學院
  3. 機械工程學系
Please use this identifier to cite or link to this item: http://tdr.lib.ntu.edu.tw/jspui/handle/123456789/6729
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???org.dspace.app.webui.jsptag.ItemTag.dcfield???ValueLanguage
dc.contributor.advisor陳瑤明
dc.contributor.authorPo-Yen Lien
dc.contributor.author李柏諺zh_TW
dc.date.accessioned2021-05-17T09:17:02Z-
dc.date.available2017-08-01
dc.date.available2021-05-17T09:17:02Z-
dc.date.copyright2012-08-01
dc.date.issued2012
dc.date.submitted2012-07-27
dc.identifier.citation[1] Tuckerman, D.B., and Peace, R. F. W., “High-Performance Heat Sink for VLSI,” IEEE Electron Device Letters, Vol. EDL-2, No.5, pp.126-129, 1981.
[2] Webb, R. L., “Nucleate Boiling on Porous Coated Surfaces,” Heat Transfer Vol. 4, No. 3-4, pp. 71-82, 1983.
[3] Mehendale, S. S., Jacobi, A. M., and Shah, R. K., “Fluid Flow and Heat Transfer at Micro- and Meso-Scales with Applications to Heat Exchanger Design”, Applied Mechanics Review, Vol. 53, pp. 175–193, 2000.
[4] S.G. Kandlikar, W. Grande, “Evolution of microchannel flow passages-thermo hydraulic performance and fabrication technology”, J. Heat Transfer Engineering. Vol. 24, pp. 3–17, 2003.
[5] P. Cheng, H.Y. Wu, F.J. Hong, “Phase-change heat transfer in microsystems,” J. Heat Transfer Vol. 129, pp.101–108, 2007.
[6] Wu H., Wu X., Qu J. and Yu M. “Condensation heat transfer and flow friction in silicon microchannels“ J. of Micromechanics and Microengineering. Vol. 18, 115024 (10pp) 2008.
[7] Wang, H. S., and Rose, J. W., , “A Theory of Film Condensation in Horizontal Noncircular Section Microchannels.” ASME J. Heat Transfer, Vol. 127, pp. 1096–1105, 2005.
[8] Wu, H. Y., and Cheng, P. “Condensation Flow Patterns in Silicon Microchannels,” Int. J. Heat Mass Transfer, Vol. 48, pp. 2186–2197, 2005.
[9] Y. Chen, P. Cheng, Condensation of steam in silicon microchannels, Int. Commun. Heat Mass Transfer Vol. 32, pp. 175–183, 2005.
[10] Wang, H. S., and Rose, J. W. “Film Condensation in Horizontal Micro-channels: Effect of Channel Shape,” Int. J. Therm. Sci., Vol. 45, pp. 1205–1212, 2006.
[11] Hu J. S. and Chao Y. H. “An experimental study of the fluid flow and heat transfer characteristics in micro-condensers with slug-bubbly flow” Int. J. Refrig. Vol. 30, pp.1309–1318, 2007.
[12] H.Y. Wu, M.M. Yu, P. Cheng, X.Y. Wu, Injection flow during steam condensation in silicon microchannels”, J. of Micromechanics and Microengineering. Vol. 17, pp.1618–1627, 2003.
[13] X.J. Quan, P. Cheng, H.Y. Wu, Transition from annular flow to plug/slug flow in condensation of steam in microchannels”, Int. J. Heat Mass Transfer, Vol. 51, pp. 707–716, 2008.
[14] S. M. Kim and I. Mudawar , “Flow condensation in parallel micro-channels – Part 2: Heat transfer results and correlation technique ,” Int. J. of Heat and Mass Transfer , Vol. 55, pp. 984–994, 2012.
[15] H.Y. Wu, P. Cheng, Condensation flow patterns in silicon microchannels, ” Int. J. Heat Mass Transfer Vol. 48, pp. 2186–2197, 2005.
[16] Hwang, Y. W., and Kim, M. S., “The Pressure Drop in Microtubes and the Correlation Development,” Int. J. Heat Mass Transfer, Vol. 49, pp. 1804–1812, 2006.
[17] Quan, X. J., Cheng, P., “An Experimental Investigation on Pressure Drop of Steam Condensing in Silicon Microchannels,” Int. J. Heat Mass Transfer, Vol. 52, pp. 54–58, 2008.
[18] S.M. Kim and I. Mudawar , “Flow condensation in parallel micro-channels – Part 1: Experimental results and assessment of pressure drop correlations ,” Int. J.of Heat and Mass Transfer , Vol. 55, pp.971-983, 2012.
[19] R.L. Webb, “Nucleate boiling on porous coated surfaces, ” J. Heat Transfer Engineering Vol.4, no.3–4, pp.71–82, 1983.
[20] Zhang, L., Wang, E. N., and Koo, J.-M., “Enhanced Nucleate Boiling in Microchannels, ” Proceedings of the 5th IEEE Conference on MEMS, IEEE,Piscataway, NJ, pp. 89–92. 2002
[21] C.N. Ammerman, W.M. You, “Enhancing small-channel convective boiling performance using a microporous surface coating”, J. Heat Transfer Vol. 123, no. 5 pp. 976–983, 2001.
[22] Vikas J. Lakheraa, Akhilesh Gupta, and Ravi Kumar, ’’ Investigation of coated tubes in cross-flow boiling,’’ International Journal of Heat and Mass Transfer Vol. 52, no. 3-4, pp. 908-920, 2009
[23] A. Shekarriz, O. A. Plumb, “Enhancement of film condensation using porous fins”, AIAA J. Thermophys. Heat Transfer, Vol. 3 no.3, pp. 309-314, 1989.
[24] K. J. Renken, D. J. Soltykiewicz and D. Poulikakos, “A study of laminar film condensation on a vertical surface with a porous coating”, Int. Commun. Heat Mass Transfer Vol. 16, pp. 181-192, 1989.
[25] Renken, K. J., Soltykiewicz, O. J. Poulikakos, D., 'A Study in Laminar Film Condensation Within Inclined Thin Porous-Layer Coated Surface,' Int. J. Heat Mass Transfer. Vol. 16, pp. 81-192, 1989.
[26] Renken KJ; Aboye M. “Experiments on film condensation promotion within thin inclined porous coatings”, Int. J. Heat Mass Transfer, Vol. 36, pp. 1347–1355, 1993.
[27] Renken K. J.; Raich M. R. “Forced convection steam condensation experiments within thin porous coatings”, Int. J. Heat Mass Transfer, Vol. 39 no.14 pp.2937–2945, 1996
[28] R. R. Riehl, J. M. Ochterbeck, and P. Seleghim, “Effects of Condensation in Microchannels with a Porous Boundary: Analytical Investigation on Heat Transfer and Meniscus Shape”, J. Brazilian Soc. Mech. Sci., Vol. 24, no. 3, pp. 186–193, 2002.
[29] Butrymowicz D, Marian T, Karwacki J. “Enhancement of condensation heat transfer by means of passive and active condensate drainage techniques” Int. J Therm. Sci. Vol. 26, pp. 473–84,2002.
[30] H. J. Lee and S. Y. Lee , “Pressure Drop Correlations for Two-Phase Flow within Horizontal Rectangular Channels with Small Heights , ” Int. J. of Multiphase Flow , Vol. 27, pp. 783-796, 2000.
[31] Y. Chen et al. , “Numerical simulation for steady annular condensation flow in triangular Microchannels ,” Int. Commun. in Heat and Mass Transfer , Vol. 35 , pp.805–809 , 2008.
[32] Garimella, S., Agarwal, A., and Killion, J. D., “Condensation pressure drop in circular microchannels, ” Heat Trans. Eng., Vol. 26, no.3, pp. 1–8, 2005.
[33] Soliman, H. M., Schuster, J. R., and Berenson, P. J., “A general heat transfer correlation for annular flow condensation, ” J. Heat Trans., Vol. 90, pp. 267–276, 1968.
dc.identifier.urihttp://tdr.lib.ntu.edu.tw/jspui/handle/123456789/6729-
dc.description.abstract微流道兩相蒸發器具有高熱傳係數、高均溫性以及低工質需求等優點,被視為極具潛力的散熱技術。近年來電子元件產品的發熱量日益增高,在有限面積下的傳統單相熱交換器無法有效冷卻時,搭配具有相變化的微流道冷凝器被學者認為是有發展潛力的冷凝元件。
本研究內容旨在燒結樹枝狀銅粉以及添加孔洞成型劑碳酸鈉的方式,以金屬粉末燒結技術製造雙孔徑結構表面微流道,藉由改變多孔隙微流道內大小孔的體積比例增強冷凝熱傳。在冷凝發生時,大孔可提供氣體穿過,而小孔可以吸收工質並且降低液膜厚度,導致液膜熱阻下降,進而提升熱傳效果。
首先建立平整表面微流道測試系統做為比較基礎,測試段是以無氧銅表面製作的30條寬、深各為500μm×155μm流道,以水為工質進行熱性能測試。
  在平整表面微流道的實驗中,熱傳係數以及壓降都有隨著質量通率上升而上升的趨勢。當質量通率增加,流速加快,使得壁面剪應力上升,造成液膜厚度變薄,熱阻減小,熱傳係數因而增加。實驗結果與傳統流道的熱傳經驗公式比較後,發現明顯低估,顯示已不適用於微流道中。與工質不同之微流道經驗式比較後,結果顯示誤差仍太大,目前的微流道熱傳經驗式仍有改進空間。壓降方面比較近年發展的微流道壓降經驗公式,結果相當吻合,顯示具有一定可靠度。
雙孔徑結構表面實驗結果,參數銅粉粒徑為61~70μm,碳酸鈉體積百分比30%與平整表面微流道進行比較,在壓降增加28.6%下,熱傳性能整體平均提升72.9%,此參數之流道吸排水性佳、熱傳面積大、液膜延展性高,是造成熱傳提升的主要原因。
zh_TW
dc.description.abstractThe microchannel evaporator with two phase heat transfer is considered to be one of the most potential cooling techniques because of its high heat flux, good temperature uniformity and the lesser requirement for coolant flow rate.
In recent years, the heat dissipation rate of the high tech products has increased day by day. The traditional single-phase heat exchanger could not efficiently cool down in a limited area, so the microchannel condenser with two phase heat transfer is regarded as a high potential cooling component in the future.
The central purpose of the present research is to enhance the condensation heat transfer by utilizing the two pore size distributions of a biporous surface structure. This surface is sintered from the mixture of dendritic copper powders and the pore former, Na2CO3, which formed the different size pores in the microchannel. By changing the volumetric ratio of pore former, it was able to alter the porosity and the numbers of larger pores, further increasing the heat transfer coefficient. During condensation, vapor could go through the larger pores. The smaller pores could absorb the liquid and help to reduce the liquid film thickness. It decreased the heat resistant and increased the heat transfer coefficient.
First, a plane surface microchannel system was built as a compared base. The test section of the 30 channels where the width and the depth is 500μm and 155μm, respectively. The test section was made by oxygen-free copper. Water steam is using as working fluid.
In the experiment of the plane surface microchannel, the heat transfer coefficient and the pressure drop werw positively related to the increasing mass flux. When increasing the mass flux, the velocity of working fluid becomes faster due to the increasement of wall shear stress. Therefore, it caused the thickness of the liquid film much thinner, decreased the heat resistance and also increased the heat transfer coefficient. Compared with the heat transfer correlation of the conventional channel, the result showed the MAE is quite large. That means there is much room to make progress on the heat transfer correlation of the microchannel. With regard to the pressure drop, comparing with the correlation of microchannel in recent years, it considerably correlated with the results. That shows the result is reliable.
For experiment of the biporous surface microchannel, the parameter with copper powder is 61~70 μm diameter and volumetric ratio of Na2CO3 is 30%. Comparing with the plane surface microchannel, the results showed that the heat transfer coefficient is enhanced to 72.9% on average when increased the pressure drop to 28.6% on average. The main reasons of enhancing the heat transfer are high water absorbing capacity and good ability for reducing liquid thickness.
en
dc.description.provenanceMade available in DSpace on 2021-05-17T09:17:02Z (GMT). No. of bitstreams: 1
ntu-101-R99522118-1.pdf: 3697975 bytes, checksum: 3ca53b788eb5fb1bd69e10e14655b442 (MD5)
Previous issue date: 2012
en
dc.description.tableofcontents目錄
圖目錄 xii
表目錄 xiv
符號表 xvi
第一章 緒論 1
1.1前言 1
1.2文獻回顧 2
1.2.1微流道尺寸界定 2
1.2.2微流道冷凝熱傳研究 4
1.2.3微流道冷凝壓降研究 6
1.2.4多孔隙結構表面流道文獻 7
1.3研究目的 9
第二章 實驗設備與方法 11
2.1測試迴路系統設計 11
2.2平整表面微流道冷凝器 13
2.3雙孔徑結構表面微流道 17
2.3.1實驗材料 17
2.3.2製造設備 17
2.4雙孔徑結構表面微流道製作流程 19
2.5實驗步驟 26
2.5.1實驗預備工作 26
2.5.2測試步驟 27
2.6 實驗數據分析 28
第三章 結果與討論 33
3.1 平整表面微流道冷凝器 33
3.1.2壓降 35
3.1.3與冷凝經驗式比較 36
3.2 具雙孔徑結構表面微流道冷凝器 42
第四章 結論與建議 49
4.1 結論 49
4.1.1平整表面微流道 49
4.1.2雙孔徑結構表面微流道 50
4.2 建議 51
參考文獻 53
附錄 57
dc.language.isozh-TW
dc.subject雙孔徑結構表面zh_TW
dc.subject微流道zh_TW
dc.subject冷凝熱傳增強zh_TW
dc.subjectmicrochannelen
dc.subjectbiporous surfaceen
dc.subjectcondensation heat transfer enhancementen
dc.title多孔性微流道冷凝熱傳增強研究zh_TW
dc.titleCondensation Heat Transfer Enhancement by Porous Microchannelen
dc.typeThesis
dc.date.schoolyear100-2
dc.description.degree碩士
dc.contributor.oralexamcommittee吳聖俊,劉君愷
dc.subject.keyword微流道,冷凝熱傳增強,雙孔徑結構表面,zh_TW
dc.subject.keywordmicrochannel,condensation heat transfer enhancement,biporous surface,en
dc.relation.page63
dc.rights.note同意授權(全球公開)
dc.date.accepted2012-07-27
dc.contributor.author-college工學院zh_TW
dc.contributor.author-dept機械工程學研究所zh_TW
Appears in Collections:機械工程學系

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