［1］ 黄理浩,陶乐仁,郑志皋，等.R410A在管内冷凝换热及压降的实验研究［J］.制冷技术,2011,39(4): 31-34.
HUANG Li-hao, TAO Le-ren, ZHENG Zhi-gao, et al, Experimental study on condensation heat transfer and pressure drop in internally thread enhanced tube with R410A ［J］.Refrigeration Technology, 2011, 39(4): 31-34.
［2］ 张建国,陶乐仁,王伟，等.R22和R410A在水平微肋管内冷凝性能的实验研究［J］.制冷与空调.2010, (2): 10-13.
ZHANG Jianguo, TAO Leren, WANG Wei, et al, Experimental study on condensation heat transfer performance of horizontal microfin tube with R22 and R410A ［J］. Refrigeration & Air Conditioning, 2010, (2): 10-13.
［3］ THOME J R. Engineering Data Book Ⅲ［M］. Lausanne: Wolverine Tube, Inc., 2004: 567-603.
［4］ YANG C Y. A critical review of condensation heat transfer predicting modelseffect of surfacetension force ［J］. Journal of Enhanced Heat Transfer, 1999, 6(2/4): 217-236.
［5］ CAVALLINI A, DEL COL D, DORETTI L, et al, Heat transfer and pressure drop during condensation of refrigerants inside horizontal enhanced tubes ［J］. International Journal of Refrigeration, 2000, 1 (23): 4-25.
［6］ WEBB R L, KIM N H. Principles of Enhanced Heat Transfer ［M］. 2nd ed. New York: Taylor & Francis Group, 2004: 234-243.
［7］ SCHLAGER L M, PATE M B, BERGLES A E. Evaporation and condensation heat transfer and pressure drop in horizontal 12.7mm microfin tubes with refrigerant 22［J］. Journal of Heat Transfer, 1990, 112(4): 1041-1047.
［8］ WU X M, WANG X L, WANG W C. Condensation heat transfer and pressure drop of R22 in 5-mm diameter microfin tubes ［J］. Journal of Enhanced Heat Transfer, 2004,11: 275-282.
［9］ CAVALLINI A, BELLA B, LONGO G A, et al, Experimental heat transfer coefficients during condensation of halogenated refrigerants on enhanced tubes ［J］. Journal of Enhanced Heat Transfer, 1995,(2): 115-125.
［10］ CHOI J Y, KEDZIERSKI M A, DOMANSKI P A, Generalized pressure drop correlation for evaporation and condensation in smooth and microfin tubes ［C］∥Proceedings of IIF-IIR Commission. B1: Paderborn, Germany: B4, 2001: 9-16.
［11］ KEDZIERSKI M A, GONCALVES J M. Horizontal convective condensation of alternative refrigerants within a microfin tube ［J］. Journal of Enhanced Heat Transfer, 1999, 6: 161-178.
［12］ HUANG X C, DING G L, HU H T, et al, Condensation heat transfer characteristics of R410A-oil mixture in 5 mm and 4 mm outside diameter horizontal microfin tubes ［J］. Experimental Thermal and Fluid Science, 2010, 34(7): 845-856.
［13］ DING G L, HU H T, HUANG X C, et al, Experimental investigation and correlation of twophase frictional pressure drop of R410Aoil mixture flow boiling in a 5 mm microfin tube ［J］. International Journal of Refrigeration, 2009, 32(1): 150-161.
［14］ LI W, WU Z. A general criterion for evaporative heat transfer in micro/mini-channels ［J］.International Journal of Heat and Mass Transfer, 2012, 53(9/10): 19671976.
［15］ 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.
［16］ LI W, WU Z. A general correlation for evaporative heat transfer in micro/minichannels ［J］. International Journal of Heat and Mass Transfer, 2010, 53: 1778-1787.
［17］ GNIELINSKI V. New equations for heat and mass transfer in turbulent pipe and channel flow ［J］. International Chemical Engineering, 1976, 16: 359-368.
［18］ PETUKHOV B S. Heat transfer and friction in turbulent pipe flow with variable physical properties ［J］, Advances in Heat Transfer, 1970, 6: 503-564.
［19］ MOFFAT R J. Describing the uncertainties in experimental results ［J］. Experimental Thermal and Fluid Science, 1988, 1(1): 3-17.
［20］ 王旭,吴赞,李冠球,等.不同5 mm内螺纹管的蒸发实验研究及传热和压降关联式的评价［C］∥工程热物理年会. 西安:工程热物理学会. 2011, 745-750.
Wang Xu, WU Zan, LI Guan-qiu, et al. Experimental investigation of condensation in micro-fin tubes of different geometries ［C］∥Annual Conference of Engineering Thermophysics. Xi’an: Chinese Society of Engineering Thermophysics. 2011,745-750.
［21］ RAVIGURURAJAN T S, BERGLES A E. General correlations for pressure drop and heat transfer for single-phase turbulent flow in internally ribbed tubes ［J］. Augmentation of Heat Transfer in Energy Systems, ASME HTD, 1985, 52: 9-20.
［22］ HARAGUCHI H, KOYAMA S, ESAKI J, et al, Condensation heat transfer of refrigerants HCFC134a, HCFC123 and HCFC22 in a horizontal smooth tube and a horizontal micro-fin tube ［C］∥ Proceedings of 30th National Symp.  Yokohama, Japan: \
[s.n.\] 1993, 343-345.
［23］ FRIEDEL L. Improved friction pressure drop correlations for horizontal and vertical twophase pipe flow［C］∥ in: European TwoPhase Flow Group Meeting. Ispra, Italy: \
[s.n.\], 1979, paper E2.
［24］ MULLER-STEINHAGEN H, HECK K. A simple friction pressure drop correlation for two-phase flow pipes ［J］. Chemical Engineering and Processing: Process Intensification, 1986, 20(6): 297-308.
［25］ GRONNERUD R. Investigation of liquid holdup, flow-resistance and heat transfer in circulation type evaporators, part VI: twophase flow resistance in boiling refrigerants ［M］. Bull. de I’ Inst. du Froid, 1979, 255-267.
［26］ BEATTIE D H, WHALLEY P B. Simple two-phase frictional pressure drop calculation method ［J］, International Journal of Multiphase Flow, 1982, (8): 83-87.
［27］ CHURCHILL S W. Friction factor equation spans all fluid flow regimes ［J］. Chemical Engineering, 1977, 84(24): 91-92.
［28］ CAVALLINI A, DEL COL D, DORETTI L, et al. A new computational procedure for heat transfer and pressure drop during refrigerant condensation inside enhanced tubes ［J］. Journal of Enhanced Heat Transfer, 1999, 6(6): 441-456.
［29］ MOSER K, WEBB R L, NA B. A new equivalent Reynolds number model for condensation in smooth tubes［J］. International Journal of Heat Transfer, 1998, 120(2): 410-417.
［30］ SHAH M M. A general correlation for heat transfer during film condensation inside pipes ［J］. International Journal of Heat and Mass Transfer, 1979, 22(4): 547-556.