Add to ORKGAbstract. General closure recommendations for inter-phase interactions were developed using a large number of accurate experimental data sets for dispersed phase holdup profiles in pipeline flows. CFD simulation was used to test a wide range of drag and lift expressions and the most suitable ones were identified. The most suitable dispersion coefficient values in the Viollet and Simonin turbulent dispersion model were also determined. The recommended closure models were found to fairly predict the dispersed phase holdup and its distribution across the pipe diameter and may be used for simulating multi-fluid systems using the Eulerian-Eulerian approach
In this work the concept of multi-scale modeling is demonstrated. The idea of this approach is to us...
In this work the concept of multi-scale modeling is demonstrated. The idea of this approach is to us...
This study describes the development of a two-phase mathematical model for the pre-diction of disper...
Multiphase flow is a common phenomenon in many industrial processes, amongst them the oil and gas in...
In order to qualify CFD codes for accurate numerical predictions of transient evolution of flow regi...
Computational fluid dynamics for multiphase flows is an emerging field. Due to the complexity and di...
The modeling of fluid dynamics through pipelines requires a full understanding of the internal and e...
This paper presents an overview of the physical models for computational fluid dynamic (CFD) predict...
This paper presents a comparison of pressure drop and liquid hold-up as calculated using different m...
Liquid-liquid dispersed flows are commonly encountered in many of the industrial applications such a...
A two-fluid model (Eulerian-Elurian model) is used to simulate dispersed two-phase immiscible liquid...
This paper presents an overview of the physical models for computational fluid dynamic (CFD) predict...
In this work the concept of multi-scale modeling is demonstrated. The idea of this approach is to us...
Computational Fluid Dynamics (CFD) code, FLUENT 6.2 was used to study dispersed flows in horizontal ...
In this work the concept of multi-scale modeling is demonstrated. The idea of this approach is to us...
In this work the concept of multi-scale modeling is demonstrated. The idea of this approach is to us...
In this work the concept of multi-scale modeling is demonstrated. The idea of this approach is to us...
This study describes the development of a two-phase mathematical model for the pre-diction of disper...
Multiphase flow is a common phenomenon in many industrial processes, amongst them the oil and gas in...
In order to qualify CFD codes for accurate numerical predictions of transient evolution of flow regi...
Computational fluid dynamics for multiphase flows is an emerging field. Due to the complexity and di...
The modeling of fluid dynamics through pipelines requires a full understanding of the internal and e...
This paper presents an overview of the physical models for computational fluid dynamic (CFD) predict...
This paper presents a comparison of pressure drop and liquid hold-up as calculated using different m...
Liquid-liquid dispersed flows are commonly encountered in many of the industrial applications such a...
A two-fluid model (Eulerian-Elurian model) is used to simulate dispersed two-phase immiscible liquid...
This paper presents an overview of the physical models for computational fluid dynamic (CFD) predict...
In this work the concept of multi-scale modeling is demonstrated. The idea of this approach is to us...
Computational Fluid Dynamics (CFD) code, FLUENT 6.2 was used to study dispersed flows in horizontal ...
In this work the concept of multi-scale modeling is demonstrated. The idea of this approach is to us...
In this work the concept of multi-scale modeling is demonstrated. The idea of this approach is to us...
In this work the concept of multi-scale modeling is demonstrated. The idea of this approach is to us...
This study describes the development of a two-phase mathematical model for the pre-diction of disper...