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研究生:陳俊宇
研究生(外文):Jun-yu Chen
論文名稱:R-290/R-600a冷媒-潤滑油混合物在蛇狀細管排內之凝結熱傳與壓降特性之研究
論文名稱(外文):Condensation heat transfer and pressure drop characteristics of R-290/ R-600a refrigerant-lubricant mixtures in the serpentine small-tube bank
指導教授:溫茂育溫茂育引用關係
學位類別:碩士
校院名稱:正修科技大學
系所名稱:機電工程研究所
學門:工程學門
學類:機械工程學類
論文種類:學術論文
論文出版年:2006
畢業學年度:94
語文別:中文
論文頁數:87
中文關鍵詞:R-290R-600a冷媒-潤滑油混合物凝結熱傳蛇狀細彎管
外文關鍵詞:condensation heat transferpressure dropserpentine small-tube bandsR-290/R-600arefrigerant-oil mixtures
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本研究主旨在探討碳氫化合物冷媒R-290(丙烷)與R-600a(異丁烷)-潤滑油混合物流經不同彎道數(U-bend)之蛇狀細管( )之冷凝熱傳與兩相壓降特性之實驗研究。實驗量測含油濃度為0~5%、質量速度為 、飽和溫度為40°C、熱通量為 。
實驗結果顯示,冷凝熱傳係數隨著質量速度、蛇狀細管之彎道數目增加而增加。隨著添加潤滑油濃度增加而減少。管內兩相壓降隨著質量速度、蛇狀細管之彎道數目增加與潤滑油含量增加而增加。
This study presents an experimental investigation of the characteristics of condensation heat transfer and pressure drop for hydrocarbon refrigerant of R-290 (propane) and R-600a (isobutane)-oil mixtures flowing in the different numbers of serpentine small-tube bands having an inside diameter of 2.54 mm. These measurements were performed for refrigerant-lubricant mixtures ranging from 0 to 5% lubricant concentrations, the mass flow flux for refrigerant-oil mixtures ranges from 300 to 600 , the saturation temperature was 40°C and the heat flux was 40 .
The experimental results show that the condensation heat transfer coefficient were increased in the mass flow rate and the numbers of bends tube, but it decreased in the lubricant concentrations. In addition, the two–phase pressure drops were increased in the mass flow rate、the numbers of bends tube and the lubricant concentrations.
目錄iii
表目錄v
圖目錄vi
符號說明ix
第一章 緒論1
1-1前言1
1-2文獻回顧4
1-2.1冷凝熱傳4
1-2.2管內壓降6
1-3研究目的10
第二章 實驗方法14
2-1 實驗系統14
2-1.1 測試段14
2-1.2 冷媒循環系統15
2-1.3 水循環系統16
2-2 實驗量測設備16
2-2.1 溫度量測17
2-2.2 壓力量測17
2-2.3 流量量測17
2-2.4 資料收集系統17
2-3 實驗過程18
2-3.1 系統測漏18
2-3.2 系統冷媒填充18
2-4 實驗步驟19
2-5 資料換算19
2-5.1 熱傳資料換算20
2-5.2 兩相壓降資料換算23
2-5.3 油集中度35
第三章 結果與討論37
3-1 冷凝熱傳37
3-2 兩相壓降特性43
第四章 結論與建議59
參考文獻62
附錄A 誤差分析65
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7.Yan, Y.-Y., and Lin, T.-F., 1998, “Evaporation Heat Transfer and Pressure Drop of Refrigerant R-134a in a Small Pipe,” Int. J. Heat Mass Transfer, Vol. 41, pp. 4183-4194.
8.Tichy, J.A., Macken, N.A., Duval, W.M.B., 1985, “An Experimental Investigation of Heat Transfer in Forced Convection Condensation of Oil-Refrigerant Mixtures,” ASHRAE Trans., Vol. 91(1A), pp. 297-309.
9.Shao, D.W., Granryd, E., 1995, “Heat Transfer and Pressure Drop of HFC134a-Oil Mixtures in a Horizontal Condensing Tube,” Int. J. of Refrigeration, Vol. 18, pp. 524-533.
10.Schlager, L.M., Pate, M.B., Bergles, A.E., 1988a, “Evaporation and Condensation of Refrigerant-Oil Mixtures In a Smooth Tube and a Micro-Fin Tube,” ASHRAE Trans, Vol. 94, Part 1, pp. 149-166.
11.Schlager, L.M., Pate, M.B., Bergles, A.E., 1988b, “Evaporation and condensation of Refrigerant-Oil Mixtures In a Low-Fin Tube,” ASHRAE Trans, Vol. 94, Part 2, pp. 1176-1194.
12.Eckels, S.J., Pate, M.B., 1991, “In-Tube Evaporation and Condensaton of Refrigerant-Lubricant Mixtures of HFC-134a and CFC-12,” ASHRAE Trans, Vol. 97, Part 2, pp. 62-71.
13.Eckels, S.J., Doerr, T.M., and Pate, M.B., 1994b, “In Tube Heat Transfer and Pressure Drop of R-134a and Ester Lubricant Mixtures in a Smooth Tube and a Micro-Fin Tube: Part II-Condensation,” ASHRAE Trans, Vol. 100, Part 2, pp. 283-294.
14.Eckels, S.J., Doerr, T.M., Pate, M.B., 1998a, “Heat Transfer Coefficients and Pressure Drops for R-134a and an Ester Lubricant Mixtures in a Smooth Tube and a Micro-Fin Tube,” ASHRAE Trans, Vol. 104, pp. 366-375.
15.Eckels, S.J., Doerr, T.M., and Pate, M.B., 1998b, “A Comparison of Heat Transfer and Pressure Drop Performance of R-134a-Lubricant Mixture In Different Diameter Smooth Tubes and Micro-Fin Tubes,” ASHRAE Trans, Vol. 104, pp. 376-386.
16.林建順, 2001, “純冷媒R134a及冷媒與潤滑油混合流體於小管內之性能比較,” 中央大學機械工程研究所碩士論文.
17.Eric, N., Thome, J.R., Favrat, D., 1997, “Flow Boiling and Pressure Drop Measurements for R-134a/Oil Mixtures Part 1:Evaporation in a Microfin Tube,“ HVAC&R Research, Vol. 3, pp. 38-53.
18.Collier, J.G., 1982, Convective Boiling and Condensation, 2nd ed., McGraw-Hill International Book Company, pp. 32, pp. 90-93, pp. 341.
19.Zivi, S.M., 1964, “Estimation of Steady State Steam Void-Fraction by Means of Principle of Minimum Entropy Production,” Int. J. Heat Transfer, Vol. 86, pp. 237-252.
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