Kreutzer M T, Kapteijn F, Moulijn J A, et al. Inertial and interfacial effects on pressure drop of Taylor flow in capillaries [J]. AIChE Journal, 2005, 51 (9): 2428-2440
[2]
Liu H, Vandu C O, Krishna R. Hydrodynamics of Taylor flow in vertical capillaries: flow regimes, bubble rise velocity, liquid slug length, and pressure drop [J]. Industrial & Engineering Chemistry Research, 2005, 44 (14): 4884-4897
[3]
Han Y, Shikazono N. Measurement of liquid film thickness in micro square channel [J]. International Journal of Multiphase Flow, 2009, 35 (10): 896-903
[4]
Dang Minhui (党敏辉), Ren Mingyue (任明月), Chen Guangwen (陈光文). Effect of microchannel inlet configuration on Taylor bubble formation in microreactors [J]. CIESC Journal (化工学报), 2014, 65 (3): 805-812
[5]
Qian D, Lawal A. Numerical study on gas and liquid slugs for Taylor flow in a T-junction microchannel [J]. Chemical Engineering Science, 2006, 61 (23): 7609-7625
[6]
Shao N, Salman W, Gavriilidis A, et al. CFD simulations of the effect of inlet conditions on Taylor flow formation [J]. International Journal of Heat and Fluid Flow, 2008, 29 (6): 1603-1611
[7]
He Xiao (贺潇), Che Defu (车得福). CFD simulation of wall shear stress in vertical and inclined upward slug gas-liquid flow [J]. Journal of Chemical Industry and Engineering (China) (化工学报), 2008, 59 (6): 1390-1395
[8]
Taha T, Cui Z. Hydrodynamics of slug flow inside capillaries [J]. Chemical Engineering Science, 2004, 59 (6): 1181-1190
[9]
Zheng D, He X, Che D. CFD simulations of hydrodynamic characteristics in a gas-liquid vertical upward slug flow [J]. International Journal of Heat and Mass Transfer, 2007, 50 (21): 4151-4165
[10]
Araújo J D P, Miranda J M, Campos J B L M. Flow of two consecutive Taylor bubbles through a vertical column of stagnant liquid—a CFD study about the influence of the leading bubble on the hydrodynamics of the trailing one [J]. Chemical Engineering Science, 2013, 97: 16-33
[11]
Asadolahi A N, Gupta R, Fletcher D F, et al. CFD approaches for the simulation of hydrodynamics and heat transfer in Taylor flow [J]. Chemical Engineering Science, 2011, 66 (22): 5575-5584
[12]
Irandoust S, Andersson B. Liquid-film in taylor flow through a capillary [J]. Industrial & Engineering Chemistry Research, 1989, 28 (11): 1684-1688
[13]
Aussillous P, Quéré D. Quick deposition of a fluid on the wall of a tube [J]. Physics of Fluids (1994-present), 2000, 12 (10): 2367-2371
[14]
Leung S S, Gupta R, Fletcher D F, et al. Effect of flow characteristics on Taylor flow heat transfer [J]. Industrial & Engineering Chemistry Research, 2011, 51 (4): 2010-2020
[15]
Taylor G I. Deposition of a viscous fluid on the wall of a tube [J]. Journal of Fluid Mechanics, 1961, 10 (2): 161-165
[16]
Warnier M J F, de Croon M, Rebrov E V, et al. Pressure drop of gas-liquid Taylor flow in round micro-capillaries for low to intermediate Reynolds numbers [J]. Microfluidics and Nanofluidics, 2010, 8 (1): 33-45
[17]
Walsh E, Muzychka Y, Walsh P, et al. Pressure drop in two phase slug/bubble flows in mini scale capillaries [J]. International Journal of Multiphase Flow, 2009, 35 (10): 879-884
[18]
Lockhart R, Martinelli R. Proposed correlation of data for isothermal two-phase, two-component flow in pipes [J]. Chem. Eng. Prog., 1949, 45 (1): 39-48
