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Andrew Cowell

Bio: Andrew Cowell is an academic researcher from Glasgow Caledonian University. The author has contributed to research in topics: Slug flow & Reliability (statistics). The author has an hindex of 7, co-authored 21 publications receiving 200 citations.

Papers
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Journal ArticleDOI
TL;DR: In this article, the authors developed a model of a section of pneumatic conveying line, a horizontal or vertical 90° bend, in the commercial CFD software package FLUENT and described the multiphase flow behavior by the mixture or Eulerian method.
Abstract: Pneumatic conveying of powdered and granular materials is a very common transport technology across a broad range of industries, for example, chemicals, cosmetics, pharmaceuticals, and power generation. As the demands of these industries for greater efficiency increases and to comply with environmental regulations there is a need for a more fundamental understanding of the behavior of materials in pneumatic conveying systems. The approach presented in this article is to develop a model of a section of pneumatic conveying line, a horizontal or vertical 90° bend, in the commercial CFD software package FLUENT and to describe the multiphase flow behavior by the mixture or Eulerian method. Models of this type have been used in the past to show qualitative and quantitative agreement between model and experiment. The model results presented were compared with experimental data gathered from an industrial-scale pneumatic conveying test system. Broad qualitative agreement in trends and flow patterns were found. Qu...

38 citations

Journal ArticleDOI
TL;DR: In this paper, the amount of particle deposition in the horizontal pipeline after a conveying was calculated by controlling the solids feeding rate using a rotary valve and by monitoring the solid flow out of the system using dynamic load cells.
Abstract: Solids deposition in the horizontal pipeline of a pneumatic conveying system was studied both mathematically and experimentally. Mathematically modelled results using the coupled discrete element method (DEM) and computational fluid dynamics (CFD) approach have demonstrated an intensive exchange of particles between the stationary layer (deposited particles) and the moving slug and a variation of solids concentration and pressure and velocity distributions across the slug. Slug flows were also visualised experimentally through a glass section and analysed by a high-speed video camera. The amount of particle deposition in the pipeline after a conveying was calculated by controlling the solids feeding rate using a rotary valve and by monitoring the solids flow out of the system using dynamic load cells. Experimentally generated data have quantitatively shown a tendency of more solids deposition with lower gas mass flow rate in slug flows except that, below a certain amount of solids mass flow rate, the deposition becomes independent of gas flow rate.

34 citations

01 May 2003
TL;DR: In this paper, the amount of particle deposition in the horizontal pipeline after a conveying was calculated by controlling the solids feeding rate using a rotary valve and by monitoring the solid flow out of the system using dynamic load cells.
Abstract: Solids deposition in the horizontal pipeline of a pneumatic conveying system was studied both mathematically and experimentally. Mathematically modelled results using the coupled discrete element method (DEM) and computational fluid dynamics (CFD) approach have demonstrated an intensive exchange of particles between the stationary layer (deposited particles) and the moving slug and a variation of solids concentration and pressure and velocity distributions across the slug. Slug flows were also visualised experimentally through a glass section and analysed by a high-speed video camera. The amount of particle deposition in the pipeline after a conveying was calculated by controlling the solids feeding rate using a rotary valve and by monitoring the solids flow out of the system using dynamic load cells. Experimentally generated data have quantitatively shown a tendency of more solids deposition with lower gas mass flow rate in slug flows except that, below a certain amount of solids mass flow rate, the deposition becomes independent of gas flow rate.

33 citations

Journal ArticleDOI
TL;DR: In this paper, three step geometries were modelled: an abrupt step, a gradual step and a step-up step from a pipe bore of 75-100mm.

28 citations

Journal ArticleDOI
01 Dec 2005-Fuel
TL;DR: In this article, the results of a project to determine the suitability of Chinese coals for dry feed to the entrained flow gasifier that forms part of the above cycle are presented.

17 citations


Cited by
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Journal ArticleDOI
TL;DR: Zhu et al. as discussed by the authors provided a summary of the studies based on discrete particle simulation in the past two decades or so, with emphasis on the microdynamics including packing/flow structure and particle-particle, particle-fluid and particle wall interaction forces.

1,253 citations

Journal ArticleDOI
TL;DR: In this paper, the authors discuss the fundamentals involved in developing a CFD solution and provide a state-of-the-art review on various CFD applications in the food industry such as ventilation, drying, sterilisation, refrigeration, cold display and storage, and mixing.
Abstract: Computational fluid dynamics (CFD) is a powerful numerical tool that is becoming widely used to simulate many processes in the food industry. Recent progression in computing efficacy coupled with reduced costs of CFD software packages has advanced CFD as a viable technique to provide effective and efficient design solutions. This paper discusses the fundamentals involved in developing a CFD solution. It also provides a state-of-the-art review on various CFD applications in the food industry such as ventilation, drying, sterilisation, refrigeration, cold display and storage, and mixing and elucidates the physical models most commonly used in these applications. The challenges faced by modellers using CFD in the food industry are also discussed.

392 citations

Journal ArticleDOI
TL;DR: In this paper, a coarse grain model for large-scale DEM simulations is proposed, where a modeled particle whose size is larger than the original particle is used instead of a crowd of original particles.

245 citations

Journal ArticleDOI
TL;DR: Current DEM models for several common pharmaceutical processes including material transport and storage, blending, granulation, milling, compression, and film coating are reviewed.

211 citations

Journal ArticleDOI
TL;DR: The emphasis is given to the modelling of key phenomena such as flow regimes and transition, pipe wear, particle attrition, and electrostatics in the gas-solid flow characteristics and process performance over a broad range of conditions.

144 citations