Development of a model to determine mass transfer coefficient and oxygen solubility in bioreactors

The objective of this paper is to present an experimentally validated mechanistic model to predict the oxygen transfer rate coefficient (Kla) in aeration tanks for different water temperatures. Using experimental data created by Hunter and Vogelaar, the formula precisely reproduces experimental resu...

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Main Author: Johnny Lee
Format: Article
Language:English
Published: Elsevier 2017-02-01
Series:Heliyon
Subjects:
Online Access:http://www.sciencedirect.com/science/article/pii/S2405844016307848
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spelling doaj-074f8e4aafce43feba7fbee3fd09db3c2020-11-25T03:34:17ZengElsevierHeliyon2405-84402017-02-0132e00248Development of a model to determine mass transfer coefficient and oxygen solubility in bioreactorsJohnny Lee0Corresponding author at: 317 Pine Valley Drive, Kitchener, Ontario, N2P 2V5, Canada.; Kitchener, Waterloo, Ontario, CanadaThe objective of this paper is to present an experimentally validated mechanistic model to predict the oxygen transfer rate coefficient (Kla) in aeration tanks for different water temperatures. Using experimental data created by Hunter and Vogelaar, the formula precisely reproduces experimental results for the standardized Kla at 20 °C, comparatively better than the current model used by ASCE 2–06 based on the equation Kla20 = Kla. (θ)(20−T) where T is in °C. Currently, reported values for θ range from 1.008 to 1.047. Because it is a geometric function, large error can result if an incorrect value of θ is used. Establishment of such value for an aeration system can only be made by means of series of full scale testing over a range of temperatures required. The new model predicts oxygen transfer coefficients to within 1% error compared to observed measurements. This is a breakthrough since the correct prediction of the volumetric mass transfer coefficient (Kla) is a crucial step in the design, operation and scale up of bioreactors including wastewater treatment plant aeration tanks, and the equation developed allows doing so without resorting to multiple full scale testing for each individual tank under the same testing condition for different temperatures. The effect of temperature on the transfer rate coefficient Kla is explored in this paper, and it is recommended to replace the current model by this new model given by:Kla20=Kla(Eρσ)20(Eρσ)T(T20T)5where T is in degree Kelvin, and the subscripts refer to degree Celsius; E, ρ, σ are properties of water. Furthermore, using data from published data on oxygen solubility in water, it was found that solubility bears a linear and inverse relationship with the mass transfer coefficient.http://www.sciencedirect.com/science/article/pii/S2405844016307848Physics methodsPhysical chemistryEnergyChemical engineeringCivil engineering
collection DOAJ
language English
format Article
sources DOAJ
author Johnny Lee
spellingShingle Johnny Lee
Development of a model to determine mass transfer coefficient and oxygen solubility in bioreactors
Heliyon
Physics methods
Physical chemistry
Energy
Chemical engineering
Civil engineering
author_facet Johnny Lee
author_sort Johnny Lee
title Development of a model to determine mass transfer coefficient and oxygen solubility in bioreactors
title_short Development of a model to determine mass transfer coefficient and oxygen solubility in bioreactors
title_full Development of a model to determine mass transfer coefficient and oxygen solubility in bioreactors
title_fullStr Development of a model to determine mass transfer coefficient and oxygen solubility in bioreactors
title_full_unstemmed Development of a model to determine mass transfer coefficient and oxygen solubility in bioreactors
title_sort development of a model to determine mass transfer coefficient and oxygen solubility in bioreactors
publisher Elsevier
series Heliyon
issn 2405-8440
publishDate 2017-02-01
description The objective of this paper is to present an experimentally validated mechanistic model to predict the oxygen transfer rate coefficient (Kla) in aeration tanks for different water temperatures. Using experimental data created by Hunter and Vogelaar, the formula precisely reproduces experimental results for the standardized Kla at 20 °C, comparatively better than the current model used by ASCE 2–06 based on the equation Kla20 = Kla. (θ)(20−T) where T is in °C. Currently, reported values for θ range from 1.008 to 1.047. Because it is a geometric function, large error can result if an incorrect value of θ is used. Establishment of such value for an aeration system can only be made by means of series of full scale testing over a range of temperatures required. The new model predicts oxygen transfer coefficients to within 1% error compared to observed measurements. This is a breakthrough since the correct prediction of the volumetric mass transfer coefficient (Kla) is a crucial step in the design, operation and scale up of bioreactors including wastewater treatment plant aeration tanks, and the equation developed allows doing so without resorting to multiple full scale testing for each individual tank under the same testing condition for different temperatures. The effect of temperature on the transfer rate coefficient Kla is explored in this paper, and it is recommended to replace the current model by this new model given by:Kla20=Kla(Eρσ)20(Eρσ)T(T20T)5where T is in degree Kelvin, and the subscripts refer to degree Celsius; E, ρ, σ are properties of water. Furthermore, using data from published data on oxygen solubility in water, it was found that solubility bears a linear and inverse relationship with the mass transfer coefficient.
topic Physics methods
Physical chemistry
Energy
Chemical engineering
Civil engineering
url http://www.sciencedirect.com/science/article/pii/S2405844016307848
work_keys_str_mv AT johnnylee developmentofamodeltodeterminemasstransfercoefficientandoxygensolubilityinbioreactors
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