On the extension of Bretherton theory for thin liquid films formed around elongated bubbles

被引:6
作者
Matin, Meisam Habibi [1 ]
Moghaddam, Saeed [1 ]
机构
[1] Univ Florida, Dept Mech & Aerosp Engn, Gainesville, FL 32611 USA
关键词
STEADY PROPAGATION; LONG BUBBLES; FLOW; MOTION; FLUID; PRINCIPLES; DEPOSITION; CAPILLARY; REACTORS;
D O I
10.1063/5.0073966
中图分类号
O3 [力学];
学科分类号
08 ; 0801 ;
摘要
The formation of thin liquid films around an elongated bubble moving in a capillary is pertinent to many applications. However, development of a theoretical model for the film thickness has been a challenge for several decades. The prominent theory characterizing the film thickness was developed by Bretherton. This theory relates the liquid film thickness in axisymmetric capillaries to the flow capillary number (Ca) for values of up to 0.003. Modified forms of the Bretherton theory have been presented for Ca values as high as 2. However, the validity of these models has not been rigorously examined. In addition, the validity of the Bretherton model itself in non-axisymmetric cross section capillaries remains uncharted. The objective of this paper is to determine whether the Bretherton relation can be extended to a broader range of Ca values and non-axisymmetric cross section channels, wherein the film thickness is not uniform along the channel circumference. A series of experiments are conducted on a set of fluids and different channel sizes and cross-sectional geometries to produce a wide range of viscous, surface tension, and inertial forces. The results show that when inertial forces are significant, and modified Bretherton models fail to predict the film thickness at Ca well below 2. The experimental results also show that depending on fluid properties, another key requirement of Bretherton solution of Landau-Levich equation may not be met. In rectangular cross section channels, the difference in surface tension forces along the longer and shorter channel axes, results in great deviation from the existing lubrication-based theories. This deviation greatly expands with the increase in the channel aspect ratio. Published under an exclusive license by AIP Publishing.
引用
收藏
页数:7
相关论文
共 37 条
[1]   Hydrodynamics of gas-liquid Taylor flow in rectangular microchannels [J].
Abadie, Thomas ;
Aubin, Joelle ;
Legendre, Dominique ;
Xuereb, Catherine .
MICROFLUIDICS AND NANOFLUIDICS, 2012, 12 (1-4) :355-369
[2]   Quick deposition of a fluid on the wall of a tube [J].
Aussillous, P ;
Quéré, D .
PHYSICS OF FLUIDS, 2000, 12 (10) :2367-2371
[3]   Effect of surfactant on elongated bubbles in capillary tubes at high Reynolds number [J].
Batchvarov, A. ;
Kahouadji, L. ;
Magnini, M. ;
Constante-Amores, C. R. ;
Shin, S. ;
Chergui, J. ;
Juric, D. ;
Craster, R., V ;
Matar, O. K. .
PHYSICAL REVIEW FLUIDS, 2020, 5 (09)
[4]   Microscale study of mechanisms of heat transfer during flow boiling in a microchannel [J].
Bigham, Sajjad ;
Moghaddam, Saeed .
INTERNATIONAL JOURNAL OF HEAT AND MASS TRANSFER, 2015, 88 :111-121
[5]   Hydraulic fracturing fluid migration in the subsurface: A review and expanded modeling results [J].
Birdsell, Daniel T. ;
Rajaram, Harihar ;
Dempsey, David ;
Viswanathan, Hari S. .
WATER RESOURCES RESEARCH, 2015, 51 (09) :7159-7188
[6]   EFFECT OF SURFACTANTS ON THE MOTION OF DROPS THROUGH CIRCULAR TUBES [J].
BORHAN, A ;
MAO, CF .
PHYSICS OF FLUIDS A-FLUID DYNAMICS, 1992, 4 (12) :2628-2640
[7]   THE MOTION OF LONG BUBBLES IN TUBES [J].
BRETHERTON, FP .
JOURNAL OF FLUID MECHANICS, 1961, 10 (02) :166-188
[8]   Nonlocal Interface Dynamics and Pattern Formation in Gravity-Driven Unsaturated Flow through Porous Media [J].
Cueto-Felgueroso, Luis ;
Juanes, Ruben .
PHYSICAL REVIEW LETTERS, 2008, 101 (24)
[9]   Scaling properties of coating flows in rectangular channels [J].
de Lozar, A. ;
Hazel, A. L. ;
Juel, A. .
PHYSICAL REVIEW LETTERS, 2007, 99 (23)
[10]   The steady propagation of an air finger into a rectangular tube [J].
De Lozar, Alberto ;
Juel, Anne ;
Hazel, Andrew L. .
JOURNAL OF FLUID MECHANICS, 2008, 614 :173-195