A detailed numerical study on the interaction between two consecutive Taylor bubbles rising through vertical columns of stagnant Newtonian liquids is reported in this work. The CFD method used is based on the VOF technique implemented in the commercial package ANSYS FLUENT. Simulations were made for a large set of flow conditions, within the laminar regime, covering a range of Morton number of 4.72 x 10(-5)-104 and an interval of Entvos number between 15 and 575. The changes in the shape of the bubbles interface were followed throughout the approach process, and the main hydrodynamic features characterizing the liquid film and the wake region of the trailing bubble were determined as the separation distance became smaller. Numerical data on...
Taylor bubbles are a feature of the slug flow regime in gas–liquid flows in vertical pipes. Their dy...
In this paper an Eulerian/Lagrangian model, describing the hydrodynamics of a gas-liquid bubble colu...
In the computational modeling of two-phase flow, many uncertainties are usually faced in simulations...
A wide-ranging numerical survey of the rising of individual Taylor bubbles through vertical columns ...
A detailed knowledge about multiphase flow systems involving non-Newtonian fluids is of extreme impo...
grantor: University of TorontoThe multi-dimensional liquid velocity field and interfacial ...
Gas-liquid, two-phase flow is encountered in a wide variety of industrial equipment. A few examples ...
The flow in the annular film around individual Taylor bubbles rising trough stagnant and co-current ...
This paper presents a computational fluid dynamics (CFD) of the gas-liquid flow in a bubble column. ...
Numerical simulations of the bubbly flow in two square cross-sectioned bubble columns were conducted...
Numerical simulations and experimental investigations of rising individual Taylor bubble through a v...
An experimental investigation of the flow field around a single Taylor bubble rising in a vertical p...
A computational analysis is carried out to ascertain the effects of steady and pulsatile co-current ...
Thesis: Ph. D., Massachusetts Institute of Technology, Department of Mechanical Engineering, 2016.Ca...
Slug flow is a multiphase flow pattern characterized by the occurrence of long gas bubbles (Taylor b...
Taylor bubbles are a feature of the slug flow regime in gas–liquid flows in vertical pipes. Their dy...
In this paper an Eulerian/Lagrangian model, describing the hydrodynamics of a gas-liquid bubble colu...
In the computational modeling of two-phase flow, many uncertainties are usually faced in simulations...
A wide-ranging numerical survey of the rising of individual Taylor bubbles through vertical columns ...
A detailed knowledge about multiphase flow systems involving non-Newtonian fluids is of extreme impo...
grantor: University of TorontoThe multi-dimensional liquid velocity field and interfacial ...
Gas-liquid, two-phase flow is encountered in a wide variety of industrial equipment. A few examples ...
The flow in the annular film around individual Taylor bubbles rising trough stagnant and co-current ...
This paper presents a computational fluid dynamics (CFD) of the gas-liquid flow in a bubble column. ...
Numerical simulations of the bubbly flow in two square cross-sectioned bubble columns were conducted...
Numerical simulations and experimental investigations of rising individual Taylor bubble through a v...
An experimental investigation of the flow field around a single Taylor bubble rising in a vertical p...
A computational analysis is carried out to ascertain the effects of steady and pulsatile co-current ...
Thesis: Ph. D., Massachusetts Institute of Technology, Department of Mechanical Engineering, 2016.Ca...
Slug flow is a multiphase flow pattern characterized by the occurrence of long gas bubbles (Taylor b...
Taylor bubbles are a feature of the slug flow regime in gas–liquid flows in vertical pipes. Their dy...
In this paper an Eulerian/Lagrangian model, describing the hydrodynamics of a gas-liquid bubble colu...
In the computational modeling of two-phase flow, many uncertainties are usually faced in simulations...