Euler–Lagrange Modeling of Bubbles Formation in Supersaturated Water

Phase transition, and more specifically bubble formation, plays an important role in many industrial applications, where bubbles are formed as a consequence of reaction such as in electrolytic processes or fermentation. Predictive tools, such as numerical models, are thus required to study, design o...

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Main Authors: Alessandro Battistella, Sander S. C. Aelen, Ivo Roghair, Martin van Sint Annaland
Format: Article
Language:English
Published: MDPI AG 2018-08-01
Series:ChemEngineering
Subjects:
CFD
Online Access:http://www.mdpi.com/2305-7084/2/3/39
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spelling doaj-d20e8b649fd241f2ab05083fec0fd2832020-11-24T21:32:39ZengMDPI AGChemEngineering2305-70842018-08-01233910.3390/chemengineering2030039chemengineering2030039Euler–Lagrange Modeling of Bubbles Formation in Supersaturated WaterAlessandro Battistella0Sander S. C. Aelen1Ivo Roghair2Martin van Sint Annaland3Chemical Process Intensification, Department of Chemical Engineering and Chemistry, Eindhoven University of Technology, 5612AE Eindhoven, The NetherlandsChemical Process Intensification, Department of Chemical Engineering and Chemistry, Eindhoven University of Technology, 5612AE Eindhoven, The NetherlandsChemical Process Intensification, Department of Chemical Engineering and Chemistry, Eindhoven University of Technology, 5612AE Eindhoven, The NetherlandsChemical Process Intensification, Department of Chemical Engineering and Chemistry, Eindhoven University of Technology, 5612AE Eindhoven, The NetherlandsPhase transition, and more specifically bubble formation, plays an important role in many industrial applications, where bubbles are formed as a consequence of reaction such as in electrolytic processes or fermentation. Predictive tools, such as numerical models, are thus required to study, design or optimize these processes. This paper aims at providing a meso-scale modelling description of gas–liquid bubbly flows including heterogeneous bubble nucleation using a Discrete Bubble Model (DBM), which tracks each bubble individually and which has been extended to include phase transition. The model is able to initialize gas pockets (as spherical bubbles) representing randomly generated conical nucleation sites, which can host, grow and detach a bubble. To demonstrate its capabilities, the model was used to study the formation of bubbles on a surface as a result of supersaturation. A higher supersaturation results in a faster rate of nucleation, which means more bubbles in the column. A clear depletion effect could be observed during the initial growth of the bubbles, due to insufficient mixing.http://www.mdpi.com/2305-7084/2/3/39CFDEuler–Lagrangebubble columnphase transitionsupersaturation
collection DOAJ
language English
format Article
sources DOAJ
author Alessandro Battistella
Sander S. C. Aelen
Ivo Roghair
Martin van Sint Annaland
spellingShingle Alessandro Battistella
Sander S. C. Aelen
Ivo Roghair
Martin van Sint Annaland
Euler–Lagrange Modeling of Bubbles Formation in Supersaturated Water
ChemEngineering
CFD
Euler–Lagrange
bubble column
phase transition
supersaturation
author_facet Alessandro Battistella
Sander S. C. Aelen
Ivo Roghair
Martin van Sint Annaland
author_sort Alessandro Battistella
title Euler–Lagrange Modeling of Bubbles Formation in Supersaturated Water
title_short Euler–Lagrange Modeling of Bubbles Formation in Supersaturated Water
title_full Euler–Lagrange Modeling of Bubbles Formation in Supersaturated Water
title_fullStr Euler–Lagrange Modeling of Bubbles Formation in Supersaturated Water
title_full_unstemmed Euler–Lagrange Modeling of Bubbles Formation in Supersaturated Water
title_sort euler–lagrange modeling of bubbles formation in supersaturated water
publisher MDPI AG
series ChemEngineering
issn 2305-7084
publishDate 2018-08-01
description Phase transition, and more specifically bubble formation, plays an important role in many industrial applications, where bubbles are formed as a consequence of reaction such as in electrolytic processes or fermentation. Predictive tools, such as numerical models, are thus required to study, design or optimize these processes. This paper aims at providing a meso-scale modelling description of gas–liquid bubbly flows including heterogeneous bubble nucleation using a Discrete Bubble Model (DBM), which tracks each bubble individually and which has been extended to include phase transition. The model is able to initialize gas pockets (as spherical bubbles) representing randomly generated conical nucleation sites, which can host, grow and detach a bubble. To demonstrate its capabilities, the model was used to study the formation of bubbles on a surface as a result of supersaturation. A higher supersaturation results in a faster rate of nucleation, which means more bubbles in the column. A clear depletion effect could be observed during the initial growth of the bubbles, due to insufficient mixing.
topic CFD
Euler–Lagrange
bubble column
phase transition
supersaturation
url http://www.mdpi.com/2305-7084/2/3/39
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