Three-fluid model along with two-group average bubble number density equations have been applied for the classification of bubbles in vertical gas-liquid flow. The current study focused on (i) consideration of three-fluid model transport equations governing the conservation of mass and momentum, (ii) formulation of two-group averaged bubble number density equations, (iii) classification of bubble interaction between spherical bubbles (Group-1) and cap bubbles (Group-2), (iv) consideration of source and sink terms via the proposal of Hibiki and Ishii (Nuclear Engineering and Design 202, 39-76) in the averaged bubble number density equations and (v) assessment by means of the experimental data sets at the bubbly-to-cap flow transition. Reason...
To provide a closure relation for interfacial area concentration in the two-fluid model, two-group i...
Many flow regimes in Nuclear Reactor Safety Research are characterized by multiphase flows, with one...
Numerical simulations of the gas-liquid bubbly flow in a bubble column were conducted with the comme...
The basic concept of two-group average bubble number density equations along with three-fluid model ...
In consideration of the practical importance regarding the application of gas-liquid flow in a verti...
In this paper, modelling gas-liquid bubbly flows is achieved by the introduction of a population bal...
Gas-liquid bubbly flows with wide range of bubble sizes are commonly encountered in many industrial ...
Gas-liquid bubbly flows with wide range of bubble sizes are commonly encountered in many industrial ...
In this paper, modelling gas-liquid bubbly flows is achieved by the introduction of a population bal...
Two-fluid modeling approach is considered as one of the most practical and accurate macroscopic form...
To model the spatial evolution of the geometrical structure of the gas bubbles in isothermal vertica...
In the two-fluid model for two-phase flows, interfacial area concentration is one of the most import...
In this study, the internal phase distributions of gas-liquid bubbly flow in a horizontal pipe have ...
The evolution of bubble size distribution is an important consideration in vertical gas-liquid flow,...
The one-dimensional two-fluid model approach has been traditionally used in thermal-hydraulics codes...
To provide a closure relation for interfacial area concentration in the two-fluid model, two-group i...
Many flow regimes in Nuclear Reactor Safety Research are characterized by multiphase flows, with one...
Numerical simulations of the gas-liquid bubbly flow in a bubble column were conducted with the comme...
The basic concept of two-group average bubble number density equations along with three-fluid model ...
In consideration of the practical importance regarding the application of gas-liquid flow in a verti...
In this paper, modelling gas-liquid bubbly flows is achieved by the introduction of a population bal...
Gas-liquid bubbly flows with wide range of bubble sizes are commonly encountered in many industrial ...
Gas-liquid bubbly flows with wide range of bubble sizes are commonly encountered in many industrial ...
In this paper, modelling gas-liquid bubbly flows is achieved by the introduction of a population bal...
Two-fluid modeling approach is considered as one of the most practical and accurate macroscopic form...
To model the spatial evolution of the geometrical structure of the gas bubbles in isothermal vertica...
In the two-fluid model for two-phase flows, interfacial area concentration is one of the most import...
In this study, the internal phase distributions of gas-liquid bubbly flow in a horizontal pipe have ...
The evolution of bubble size distribution is an important consideration in vertical gas-liquid flow,...
The one-dimensional two-fluid model approach has been traditionally used in thermal-hydraulics codes...
To provide a closure relation for interfacial area concentration in the two-fluid model, two-group i...
Many flow regimes in Nuclear Reactor Safety Research are characterized by multiphase flows, with one...
Numerical simulations of the gas-liquid bubbly flow in a bubble column were conducted with the comme...