[1] Fried L. Pressure drop and heat transfer for two-phase, two-component flow[C]//Chem Eng Prog Symp Series,1954, 50(9):47-51.
[2] Knott R F, Anderson R N, Acrivos A, et al. An experimental study of heat transfer to nitrogen-oil mixtures[J]. Industrial & Engineering Chemistry, 1959, 51(11):1369-1372.
[3] Sieder E N, Tate G E. Heat transfer and pressure drop of liquids in tubes[J]. Industrial & Engineering Chemistry, 1936, 28(12):1429-1435.
[4] Oliver D R, Wright S J. Pressure drop and heat transfer in gas-liquid slug flow in horizontal tubes[J]. British Chemical Engineering, 1964, 9(9):590-596.
[5] Dorresteijn W R. Experimental study of heat transfer in upward and downward two-phase flow of air and oil through 70 mm tubes[C]//Proc 4th Int Heat Transfer Conf, 1970, 5(5-9):1-10.
[6] Ueda T, Hanaoka M. On upward flow of gas-liquid mixtures in vertical tubes:3rd Report, heat transfer results and analysis[J]. Bulletin of JSME, 1967, 10(42):1008-1015.
[7] Shoham O, Dukler A E, Taitel Y. Heat transfer during intermittent/slug flow in horizontal tubes[J]. Industrial & Engineering Chemistry Fundamentals, 1982, 21(3):312-319.
[8] Hetsroni G, Yi J H, Hu B G, et al. Heat transfer in intermittent air-water flows.Part Ⅱ:Upward inclined tube[J]. International journal of multiphase flow, 1998, 24(2):189-212.
[9] Franca F A, Bannwart A C, Camargo R M T, et al. Mechanistic modeling of the convective heat transfer coefficient in gas-liquid intermittent flows[J]. Heat Transfer Engineering, 2008, 29(12):984-998.
[10] 王鑫, 徐静静, 祁雷, 等. 水平管空气-水段塞流冷却传热研究[J]. 工程热物理学报, 2014, 35(8):1563-1568. |