Experimental and numerical 3D study of a Taylor drop rising in a stagnant heavier liquid

被引:9
作者
Direito, F. J. N. [1 ]
Morgado, A. O. [1 ]
Rocha, L. A. M. [1 ]
Miranda, J. M. [1 ]
Campos, J. B. L. M. [1 ]
机构
[1] Univ Porto, Fac Engn, Dept Engn Quim, Ctr Estudos Fenomenos Transporte, Rua Dr Roberto Frias, P-4200465 Oporto, Portugal
关键词
SLUG FLOW; SURFACE-TENSION; RISE VELOCITY; BUBBLES; PATTERNS; SYSTEMS; MOTION; PIPES; TUBES;
D O I
10.1063/1.4979262
中图分类号
O3 [力学];
学科分类号
08 ; 0801 ;
摘要
The present work concerns 3D numerical simulations and experiments on the rise of individual liquid Taylor drops through vertical columns of stagnant heavier liquids. Asymmetric effects are assessed for different conditions, following the observations in a previous work. Furthermore, the disturbances in the continuous phase due to the Taylor drop are studied. Experiments were performed with pairs of liquids in ranges not studied in the literature. Simulations targeted a broad range of dimensionless numbers and were done in a commercial code, using its implementation of the volume of fluid method in a three-dimensional domain. Results were processed according to relevant dimensionless numbers. Different behaviors are found concerning the existence or not of flow and drop shape asymmetries. Depending on the viscosity ratio, three ranges with different characteristics were identified. Relevant results are also reported concerning drop velocity when compared to the literature two-dimensional model. Drop influence in the surrounding continuous phase is also reported. Published by AIP Publishing.
引用
收藏
页数:13
相关论文
共 35 条
[1]  
[Anonymous], 1979, Nature
[2]  
[Anonymous], 1980, Numerical heat transfer and fluid flow
[3]   Simulation of slug flow systems under laminar regime: Hydrodynamics with individual and a pair of consecutive Taylor bubbles [J].
Araujo, J. D. P. ;
Miranda, J. M. ;
Campos, J. B. L. M. .
JOURNAL OF PETROLEUM SCIENCE AND ENGINEERING, 2013, 111 :1-14
[4]   Wide-ranging survey on the laminar flow of individual Taylor bubbles rising through stagnant Newtonian liquids [J].
Araujo, J. D. P. ;
Miranda, J. M. ;
Pinto, A. M. F. R. ;
Campos, J. B. L. M. .
INTERNATIONAL JOURNAL OF MULTIPHASE FLOW, 2012, 43 :131-148
[5]   Experimental investigation on liquid-liquid-gas flow: Flow patterns and pressure-gradient [J].
Bannwart, A. C. ;
Rodriguez, O. M. H. ;
Trevisan, F. E. ;
Vieira, F. F. ;
de Carvalho, C. H. M. .
JOURNAL OF PETROLEUM SCIENCE AND ENGINEERING, 2009, 65 (1-2) :1-13
[6]   Flow patterns in heavy crude oil-water flow [J].
Bannwart, AC ;
Rodriguez, OMH ;
de Carvalho, CHM ;
Wang, IS ;
Vara, RMO .
JOURNAL OF ENERGY RESOURCES TECHNOLOGY-TRANSACTIONS OF THE ASME, 2004, 126 (03) :184-189
[7]   A CONTINUUM METHOD FOR MODELING SURFACE-TENSION [J].
BRACKBILL, JU ;
KOTHE, DB ;
ZEMACH, C .
JOURNAL OF COMPUTATIONAL PHYSICS, 1992, 100 (02) :335-354
[8]  
Brown R.A. S., 1961, The Canadian J. of Chemical Eng, V39, P159
[9]  
Campos J.M., 2013, Notas para o Estudo da Mecanica dos Fluidos, V1
[10]  
Clark N.J., 1969, Elements of Petroleum Reservoirs