Lagrangian simulation of steady and unsteady laminar mixing by plate impeller in a cylindrical vessel

The steady and unsteady laminar mixing processes agitated by a plate impeller in a cylindrical vessel are computed using a Lagrangian particle method based on the Moving Particle Semi-implicit (MPS) technique. By adopting a novel procedure designed previously to compute the mixing rate in the contex...

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Main Authors: Ng K.C., Ng E.Y.K., Lam W.H.
Other Authors: 55310814500
Format: Article
Published: 2023
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spelling my.uniten.dspace-300252023-12-29T15:44:03Z Lagrangian simulation of steady and unsteady laminar mixing by plate impeller in a cylindrical vessel Ng K.C. Ng E.Y.K. Lam W.H. 55310814500 7201647536 23028104400 Impellers Lagrange multipliers Cylindrical vessels Fluid configuration Initial configuration Lagrangian particle method Lagrangian simulation Mixing performance Moving particle semi-implicit Rotational velocity Mixing The steady and unsteady laminar mixing processes agitated by a plate impeller in a cylindrical vessel are computed using a Lagrangian particle method based on the Moving Particle Semi-implicit (MPS) technique. By adopting a novel procedure designed previously to compute the mixing rate in the context of the Lagrangian particle method, it is observed that the mixing performance is strongly dependent on the initial configuration of the mixing interface dividing the fluids. For equivolume mixing, steady mixing is found to be more prominent in mixing fluids initially located in a separate semicircle compartment (side-by-side fluid configuration), while unsteady mixing is better in mixing fluids that initially resided in a separate annulus (annular fluid configuration). The fluid particles that initially concentrated near the center region experience a more rapid detachment from the impeller's tip (hence rapid mixing) in the steady mixing case due to the consistent centripetal force originated by the steady rotation. Difficulties in radial mixing, particularly for those fluids residing near the vessel wall, however, are observed for the case of steady mixing, and this issue is circumvented by introducing certain unsteadiness on the rotational velocity of the impeller's tip (unsteady mixing), which may serve as an alternative in replacing baffles in promoting radial flows near the vessel. � 2013 American Chemical Society. Final 2023-12-29T07:44:03Z 2023-12-29T07:44:03Z 2013 Article 10.1021/ie400621b 2-s2.0-84880869259 https://www.scopus.com/inward/record.uri?eid=2-s2.0-84880869259&doi=10.1021%2fie400621b&partnerID=40&md5=a11a525dd6b727439445e16f5886c4f8 https://irepository.uniten.edu.my/handle/123456789/30025 52 29 10004 10014 Scopus
institution Universiti Tenaga Nasional
building UNITEN Library
collection Institutional Repository
continent Asia
country Malaysia
content_provider Universiti Tenaga Nasional
content_source UNITEN Institutional Repository
url_provider http://dspace.uniten.edu.my/
topic Impellers
Lagrange multipliers
Cylindrical vessels
Fluid configuration
Initial configuration
Lagrangian particle method
Lagrangian simulation
Mixing performance
Moving particle semi-implicit
Rotational velocity
Mixing
spellingShingle Impellers
Lagrange multipliers
Cylindrical vessels
Fluid configuration
Initial configuration
Lagrangian particle method
Lagrangian simulation
Mixing performance
Moving particle semi-implicit
Rotational velocity
Mixing
Ng K.C.
Ng E.Y.K.
Lam W.H.
Lagrangian simulation of steady and unsteady laminar mixing by plate impeller in a cylindrical vessel
description The steady and unsteady laminar mixing processes agitated by a plate impeller in a cylindrical vessel are computed using a Lagrangian particle method based on the Moving Particle Semi-implicit (MPS) technique. By adopting a novel procedure designed previously to compute the mixing rate in the context of the Lagrangian particle method, it is observed that the mixing performance is strongly dependent on the initial configuration of the mixing interface dividing the fluids. For equivolume mixing, steady mixing is found to be more prominent in mixing fluids initially located in a separate semicircle compartment (side-by-side fluid configuration), while unsteady mixing is better in mixing fluids that initially resided in a separate annulus (annular fluid configuration). The fluid particles that initially concentrated near the center region experience a more rapid detachment from the impeller's tip (hence rapid mixing) in the steady mixing case due to the consistent centripetal force originated by the steady rotation. Difficulties in radial mixing, particularly for those fluids residing near the vessel wall, however, are observed for the case of steady mixing, and this issue is circumvented by introducing certain unsteadiness on the rotational velocity of the impeller's tip (unsteady mixing), which may serve as an alternative in replacing baffles in promoting radial flows near the vessel. � 2013 American Chemical Society.
author2 55310814500
author_facet 55310814500
Ng K.C.
Ng E.Y.K.
Lam W.H.
format Article
author Ng K.C.
Ng E.Y.K.
Lam W.H.
author_sort Ng K.C.
title Lagrangian simulation of steady and unsteady laminar mixing by plate impeller in a cylindrical vessel
title_short Lagrangian simulation of steady and unsteady laminar mixing by plate impeller in a cylindrical vessel
title_full Lagrangian simulation of steady and unsteady laminar mixing by plate impeller in a cylindrical vessel
title_fullStr Lagrangian simulation of steady and unsteady laminar mixing by plate impeller in a cylindrical vessel
title_full_unstemmed Lagrangian simulation of steady and unsteady laminar mixing by plate impeller in a cylindrical vessel
title_sort lagrangian simulation of steady and unsteady laminar mixing by plate impeller in a cylindrical vessel
publishDate 2023
_version_ 1806425943994007552
score 13.214268