Bubbles morphology, frequency and rising velocity in yield stress fluid under downward gas injection

Mixing in a reactor can be achieved mechanically or by the injection of a gas. This can be done by injecting a gas towards the bottom of the tank. The induced flow recirculation and then the stirring quality depends on the bubbles morphology, rising velocity and frequency detachment. This study focu...

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Main Authors: Laurent Jossic, Philippe Séchet, Albert Magnin, Ali Hojeij, Stéphane Hattou
Format: Article
Language:English
Published: Elsevier 2023-11-01
Series:Chemical Engineering Journal Advances
Subjects:
Online Access:http://www.sciencedirect.com/science/article/pii/S2666821123000844
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author Laurent Jossic
Philippe Séchet
Albert Magnin
Ali Hojeij
Stéphane Hattou
author_facet Laurent Jossic
Philippe Séchet
Albert Magnin
Ali Hojeij
Stéphane Hattou
author_sort Laurent Jossic
collection DOAJ
description Mixing in a reactor can be achieved mechanically or by the injection of a gas. This can be done by injecting a gas towards the bottom of the tank. The induced flow recirculation and then the stirring quality depends on the bubbles morphology, rising velocity and frequency detachment. This study focus on the case where the stirred fluid exhibits a yield stress. It is in line with previous studies on the gas cavity at the injection point [1], the induced flow recirculation [2] and the numerical simulation [3]. Here we quantified the bubbles diameters, aspect ratios and velocities as a function of the air flow rate, rheological parameters and tank size. Scaling laws and correlations based on the characteristic dimensionless numbers governing the flow have been proposed and validated experimentally. It was found that bubble frequencies and consequently bubble volumes and velocities are mainly governed by the balance between inertial and buoyancy forces. However, viscous and yield stress effects play an important role along buoyancy and inertial in defining the bubble aspect ratios. Weakly inertial flows are characterized by elongated bubbles while high inertial flows produce almost spherical bubbles. These experimental results are of practical interest for the design of reactor or digester where yield stress fluids have to be stirred.
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spelling doaj.art-04b70ae45c5346619858f78b272420102023-12-17T06:42:09ZengElsevierChemical Engineering Journal Advances2666-82112023-11-0116100527Bubbles morphology, frequency and rising velocity in yield stress fluid under downward gas injectionLaurent Jossic0Philippe Séchet1Albert Magnin2Ali Hojeij3Stéphane Hattou4Corresponding author.; Laboratoire Rhéologie et Procédés, Université Grenoble Alpes, Grenoble INP, CNRS (UMR 5520), BP 53 Domaine Universitaire, Grenoble Cedex 9 38041, FranceLEGI, Université Grenoble Alpes, Grenoble INP, CNRS (UMR 5519), BP 53 Domaine Universitaire, Grenoble Cedex 9 38041, FranceLaboratoire Rhéologie et Procédés, Université Grenoble Alpes, Grenoble INP, CNRS (UMR 5520), BP 53 Domaine Universitaire, Grenoble Cedex 9 38041, FranceLaboratoire Rhéologie et Procédés, Université Grenoble Alpes, Grenoble INP, CNRS (UMR 5520), BP 53 Domaine Universitaire, Grenoble Cedex 9 38041, FranceArkolia Energies, Mudaison 34130, FranceMixing in a reactor can be achieved mechanically or by the injection of a gas. This can be done by injecting a gas towards the bottom of the tank. The induced flow recirculation and then the stirring quality depends on the bubbles morphology, rising velocity and frequency detachment. This study focus on the case where the stirred fluid exhibits a yield stress. It is in line with previous studies on the gas cavity at the injection point [1], the induced flow recirculation [2] and the numerical simulation [3]. Here we quantified the bubbles diameters, aspect ratios and velocities as a function of the air flow rate, rheological parameters and tank size. Scaling laws and correlations based on the characteristic dimensionless numbers governing the flow have been proposed and validated experimentally. It was found that bubble frequencies and consequently bubble volumes and velocities are mainly governed by the balance between inertial and buoyancy forces. However, viscous and yield stress effects play an important role along buoyancy and inertial in defining the bubble aspect ratios. Weakly inertial flows are characterized by elongated bubbles while high inertial flows produce almost spherical bubbles. These experimental results are of practical interest for the design of reactor or digester where yield stress fluids have to be stirred.http://www.sciencedirect.com/science/article/pii/S2666821123000844Yield stress fluidBubblesGas injectionStirring
spellingShingle Laurent Jossic
Philippe Séchet
Albert Magnin
Ali Hojeij
Stéphane Hattou
Bubbles morphology, frequency and rising velocity in yield stress fluid under downward gas injection
Chemical Engineering Journal Advances
Yield stress fluid
Bubbles
Gas injection
Stirring
title Bubbles morphology, frequency and rising velocity in yield stress fluid under downward gas injection
title_full Bubbles morphology, frequency and rising velocity in yield stress fluid under downward gas injection
title_fullStr Bubbles morphology, frequency and rising velocity in yield stress fluid under downward gas injection
title_full_unstemmed Bubbles morphology, frequency and rising velocity in yield stress fluid under downward gas injection
title_short Bubbles morphology, frequency and rising velocity in yield stress fluid under downward gas injection
title_sort bubbles morphology frequency and rising velocity in yield stress fluid under downward gas injection
topic Yield stress fluid
Bubbles
Gas injection
Stirring
url http://www.sciencedirect.com/science/article/pii/S2666821123000844
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AT alihojeij bubblesmorphologyfrequencyandrisingvelocityinyieldstressfluidunderdownwardgasinjection
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