期刊文献+

R410A-油在7mm C形光管流动沸腾的压降特性

Frictional Pressure Drop Characteristics of R410A-Oil Flow Boiling in 7mm C-Shape Horizontal Smooth Tube
下载PDF
导出
摘要 对R410A-油在7 mm C形水平光管内流动沸腾的压降特性进行了研究,并基于混合物性开发出7 mm C形水平光管内流动沸腾的压降预测关联式.测试段长度2 m,实验工况:质量流率为200,300,400 kg/(m^2·s);蒸发温度5℃;入口干度0.2~0.7;测试段干度变化0.2;润滑油质量分数1%~5%.润滑油的存在引起压降增大,不同干度下,压降都随油浓度的增加而增大,压降最大增加33.5%.基于混合物性开发的关联式预测值与80%以上的实验数据偏差在±15%以内,平均偏差9.13%,最大偏差28.97%. Evaporation pressure drop characteristics of R410A-oil mixture in 7 mm C-shape smooth tube were investigated. The experiment was carried out at evaporation temperature 5 ℃, and inlet quality ranges from 0.2 to 0.7, quality change of test is section 0.2, oil concentration ranges from 1% to 5 %, mass flux range from 200 to 400 kg/(m^2 · s). Oil increases the pressure drop, and the pressure drop becomes much larger with the increase of oil concentration, and the largest increase of pressure drop caused by oil is about 33.5% as compared to that of pure refrigerant. A new pressure drop correlation for R410A-oil mixture in 7 mm C-shape smooth tube is developed based on refrigerant-oil mixture properties. It can agree with 80% experimental data within deviation of ± 15% and the average deviation and maximum deviation are 9.13% and 28.97% respectively.
出处 《上海交通大学学报》 EI CAS CSCD 北大核心 2007年第9期1560-1564,共5页 Journal of Shanghai Jiaotong University
关键词 流动沸腾 摩擦压降 C形光管 制冷剂 润滑油 flow boiling friction pressure drop C-shape tube refrigerant lube oil
  • 相关文献

参考文献15

  • 1Chen I Y,Wang C C,Lin S Y.Measurements and correlations of frictional single-phase and two-phase pressure drops of R410A flow in small U-type return bends[J].International Journal of Heat and Mass Transfer,2004,47:2241-2249.
  • 2Cho K,Tae S J.Evaporation heat transfer for R22 and R407C refrigerant-oil mixture in a microfin tube with a U-bend[J].International Journal of Refrigeration,2000,23:219-231.
  • 3Tichy J A,Duque-Rivera J,Macken N A,et al.Experimental investigation of pressure drop in forced-convection condensation and evaporation of oil-refrigerant Mixtrue[J].ASHRAE Trans,1986,92(2A):461-472.
  • 4Schlager L M,Pate M B.Bergles A E.Heat transfer and pressure drop performance of smooth and internally finned tubes with oil and refrigerant 22 mixtures[J].ASHRAE Trans,1989,95:160-169.
  • 5Schlager L M,Pate M B,Bergles A E.Performance predictions of refrigerant-oil mixtures in smooth tube and internally finned tubes.Part Ⅱ.Design equations[J].ASHRAE Trans,1990,469:170-181.
  • 6Eckels S J,Doerr T M,Pate M B.In-tube heat transfer and pressure drop of R-134a and ester lubricant mixtures in a smooth tube and a micro-fin tube.Part Ⅰ.Evaporation[J].ASHRAE Trans,1994,100(2):265-282.
  • 7Zurcher O,Thome J R,Favrat D.In-tube flow boiling of R-407C,Part Ⅱ.Plain tube results and predictions[J].HVAC & R Research,1997,3(1):54-64.
  • 8Yun R,Heo J H,Kim Y.Evaporative heat transfer and pressure drop of R410A in microchannels[J].International Journal of Refrigeration,2006,29(1):92-100.
  • 9胡海涛,丁国良,汪振策,魏文建,王凯建.R410A-油在Φ7mm水平直光管内流动沸腾阻力特性[J].上海交通大学学报,2007,41(3):370-375. 被引量:9
  • 10魏文建,丁国良,王凯建.A New Experimental Rig of Testing Flow Boiling Heat Transfer of Refrigerantand Lubricant Mixture[J].Journal of Shanghai Jiaotong university(Science),2004,9(4):62-67. 被引量:5

二级参考文献26

  • 1魏文建,丁国良,王凯建.A New Experimental Rig of Testing Flow Boiling Heat Transfer of Refrigerantand Lubricant Mixture[J].Journal of Shanghai Jiaotong university(Science),2004,9(4):62-67. 被引量:5
  • 2Lottin O,Guillemet P,Lebreton J M.Effect of synthetic oil in a compression refrigeration system using R410A.Part Ⅰ.Modelling of the whole system and analysis of its response to an increase in the amount of circulating oil[J].International Journal of Refrigeration,2003,26:772-782.
  • 3Moffat R J.Describing the uncertainties in experimental results[J].Experimental Fluid and Thermal Science,1998,1(1):3-17.
  • 4Lockhart R W,Martinelli R C.Proposed correlation of data for isothermal two-phase two-component flow in pipes[J].Chem Eng Progr,1949,45:39-45.
  • 5Jung D S,Radermacher R.Prediction of pressure drop during horizontal annular flow boiling of pure and mixed refrigerants[J].International Journal of Heat and Mass Transfer,1989,32:2435-2446.
  • 6Chen I Y,Won C L,Wang C C.Influence of oil on R410A two-phase frictional pressure drop in a small U-type wavy tube[J].International Communications in Heat and Mass Transfer,2005,32:797-808.
  • 7Tichy J A,Duque-Rivera J,Macken N A,et al.Experimental investigation of pressure drop in forced-convection condensation and evaporation of oil-refrigerant mixtures[J].ASHRAE Trans,1986,92:461-472.
  • 8Schlager L M,Pate M B,Bergles A E.Heat transfer and pressure drop performance of smooth and internally finned tubes with oil and refrigerant 22 mixtures[J].ASHRAE Trans,1989,95:160-169.
  • 9Eckels S J,Doerr T M,Pate M B.In-tube heat transfer and pressure drop of R-134a and ester lubricant mixtures in a smooth tube and a micro-fin tube.Part Ⅰ.Evaporation[J].ASHRAE Trans,1994,100:265 -282.
  • 10Eckels S J,Doerr T M,Pate M B.Heat transfer coefficients and pressure drops for R-134a and an ester lubricant mixture in a smooth tube and a micro-fin tube[J].ASHRAE Trans,1998,104:366-375.

共引文献11

相关作者

内容加载中请稍等...

相关机构

内容加载中请稍等...

相关主题

内容加载中请稍等...

浏览历史

内容加载中请稍等...
;
使用帮助 返回顶部