许玉;方贤德;张宏刚;苏向辉;

• 1:南京航空航天大学

摘要(Abstract)：

管内两相流摩擦压力损失计算广泛应用于各种工业领域,一直是热流体科学的重要研究方向。本文对管内两相流摩擦压降计算的研究成果进行了全面总结与归纳,系统综述了分相摩擦倍增因子方法、全相摩擦倍增因子方法以及均相模型方法,并且对各模型进行了评价和分析,可为相关研究提供参考。

关键词(KeyWords)： 两相流;压降;摩擦倍增因子;模型

Abstract:

Keywords:

基金项目(Foundation): 国家自然科学基金资助项目(51176074)

作者(Author): 许玉;方贤德;张宏刚;苏向辉;

Email:

DOI:

参考文献(References)：

• [1]倪晓华,夏清,萧渊.板式换热器的换热与压降计算[J].流体机械,2002,30(3):22-25.
• [2]孔文彬,马小明,江楠.板式换热器板片失效分析[J].压力容器,2011,28(9):42-46.
• [3]高宏宇,钱才富.曲面弓形折流板换热器壳程压力降的数值模拟[J].压力容器,2010,27(2):28-31.
• [4]程聪,张铱鈖.泡沫金属填充板式换热器的传热特性研究[J].压力容器,2012,29(2):13-16.
• [5]刘建,张正国,高学农,等.螺旋折流板与弓型折流板强化管换热器的传热性能对比[J].压力容器,2011,28(3):16-19.
• [6]李卓,俞坚,夏国栋,等.水平矩形小通道内气-液两相流流动特性的研究[J].流体机械,2006,34(8):1-5.
• [7]刘文红,郭烈锦,张西民,等.水平直圆管内油气两相流的压降[J].化工学报,2004,55(6):907-912.
• [8]Lockhart R W,Martinelli R C.Proposed correlation ofdata for isothermal two-phase,two-component flowin pipes[J].Chemical Engineering Progress,1949,45(1):39-48.
• [9]Chisholm D.A theoretical basis for the Lockhart-Mar-tinelli correlation for two-phase flow[J].Internation-al Journal of Heat and Mass Transfer,1967,10(12):1767-1778.
• [10]Friedel L.Improved friction pressure drop correlationfor horizontal and vertical two-phase pipe flow[A].Ispra:ETPFGM,1979:485-492.
• [11]Shannak B A.Frictional pressure drop of gas liquidtwo-phase flow in pipes[J].Nuclear Engineeringand Design,2008,238(12):3277-3284.
• [12]Beattie D R H,Whalley P B.A simple two-phasefrictional pressure drop calculation method[J].Inter-national Journal of Multiphase Flow,1982,8(1):83-87.
• [13]Fang X D,Xu Y,Zhou Z R.New correlations of sin-gle-phase friction factor for turbulent pipe flow andevaluation of existing single-phase friction factorcorrelations[J].Nuclear Engineering and Design,2011,241(3):897-902.
• [14]Nikuradse J.Stroemungsgesetze in rauhen Rohren[Z].Berlin:VDI-Verlag,1933.
• [15]Brkic D.New explicit correlations for turbulent flowfriction factor[J].Nuclear Engineering and Design,2011,241(9):4055-4059.
• [16]Wang C C,Chiang C S,Lu D C.Visual observationof two-phase flow pattern of R-22,R-134a,andR-407C in a 6.5-mm smooth tube[J].Experi-mental Thermal Fluid Science,1997,15(4):395-405.
• [17]Lee J,Mudawar I.Two-phase flow in high-heat-flux micro-channel heat sink for refrigeration coolingapplications:Part I-pressure drop characteristics[J].International Journal of Heat Mass Transfer,2005,48(5):928-940.
• [18]Hwang Y W,Kim M S.The pressure drop in micro-tubes and the correlation development[J].Interna-tional Journal of Heat and Mass Transfer,2006,49(11-12):1804-1812.
• [19]Sun L,Mishima K.Evaluation analysis of predictionmethods for two-phase flow pressure drop in mini-channels[J].International Journal of MultiphaseFlow,2009,35(1):47-54.
• [20]Zhang W,Hibiki T,Mishima K.Correlations of two-phase frictional pressure drop and void fraction inmini-channel[J].International Journal of Heat andMass Transfer,2010,53(1-3):453-465.
• [21]Chisholm D.Pressure gradients due to friction duringthe flow of evaporating two-phase mixtures in smoothtubes and channels[J].International Journal of Heatand Mass Transfer,1973,16(2):347-348.
• [22]Muller-Steinhagen H,Heck K.A simple frictionpressure drop correlation for two-phase flow in pipes[J].Chemical Engineering Progress,1986,20(6):297-308.
• [23]Souza A L,Pimenta M M.Prediction of pressuredrop during horizontal two-phase flow of pure andmixed refrigerants[J].Proceedings of ASME Confer-ence,1995,FED-210:161-171.
• [24]Tran T N,Chyu M C,Wambsganss M W,et al.Two-phase pressure drop of refrigerants during flow boil-ing in small channels:an experimental investigationand correlation development[J].International Jour-nal of Multiphase Flow,2000,26(11):1739-1754.
• [25]Chen I Y,Yang K S,Chang Y J,et al.Two-phasepressure drop of air-water and R-410a in small hori-zontal tubes[J].International Journal of MultiphaseFlow,2001,27(7):1293-1299.
• [26]Cavallini A,Censi G,Del Col D,et al.Condensa-tion of halogenated refrigerants inside smooth tubes[J].HVAC&R Research,2002,8(4):429-451.
• [27]McAdams W H,Wood W K,Bryan R L.Vaporiza-tion inside horizontal tubes-II-Benzene-oil mix-tures[J].Transactions of the ASME,1942,66(8):671-684.
• [28]Cicchitti A,Lombardi C,Silvestri M,et al.Two-phase cooling experiments—pressure drop,heattransfer,and burnout measurements[J].Energia Nu-cleare,1960,7(6):407-425.
• [29]Dukler A E,Wicks W,Cleveland R G.Frictionpressure drop in two-phase flow[J].AIChE Jour-nal,1964,10(1):38-43.
• [30]Ould Didi M B,Kattan N,Thome J R.Prediction oftwo-phase pressure gradients of refrigerants in hori-zontal tubes[J].International Journal of Refrigera-tion,2002,25(7):935-947.
• [31]Dalkilic A S,Agra O,Teke I,et al.Comparison offrictional pressure drop models during annular flowcondensation of R600a in a horizontal tube at lowmass flux and of R134a in a vertical tube at highmass flux[J].International Journal of Heat and MassTransfer,2010,53(9-10):2052-2064.
• [32]Li W,Wu Z.A general correlation for adiabatic two-phase pressure drop in micro/mini-channels[J].International Journal of Heat and Mass Transfer,2010,53(13-14):2732-2739.
• [33]Zhang M,Webb R L.Correlation of two-phase fric-tion for refrigerants in small-diameter tubes[J].Experimental Thermal and Fluid Science,2001,25(3-4):131-139.
• [34]Greco A,Vanoli G P.Evaporation of refrigerants in asmooth horizontal tube:prediction of R22 and R507heat transfer coefficients and pressure drop[J].Ap-plied Thermal Engineering,2004,24(14-15):2189-2206.
• [35]Moreno Quiben J.Experimental and analytical studyof two-phase pressure drops during evaporation inhorizontal tubes[D].Lausanne:Swiss Federal Insti-tute of Technology,2005.
• [36]Park C Y,Hrnjak P S.CO2 and R410A flow boilingheat transfer,pressure drop,and flow pattern at lowtemperatures in a horizontal smooth tube[J].Inter-national Journal of Refrigeration,2007,30(1):166-178.
• [37]Revellin R,Thome J R.Adiabatic two-phase fric-tional pressure drops in microchannels[J].Experi-mental Thermal and Fluid Science,2007,31(7):673-685.
• [38]Da Silva Lima R J,Moreno Quiben J,Kuhn C,etal.Ammonia two-phase flow in a horizontal smoothtube:flow pattern observations,diabatic and adiabat-ic frictional pressure drops and assessment of predic-tion methods[J].International Journal of Heat andMass Transfer,2009,52(9-10):2273-2288.