dc.contributor.author
Myers, T. G.
dc.date.accessioned
2025-01-07T10:28:04Z
dc.date.available
2025-01-07T10:28:04Z
dc.date.issued
2024-12-01
dc.identifier.uri
http://hdl.handle.net/2072/480002
dc.description.abstract
The Bohart-Adams model provides a standard expression for the breakthrough curve of contaminant at the outlet of a packed column. It is a basic building block for analysis and computations in the field. In this paper we demonstrate that this model can provide highly inaccurate results and that its well-documented success is shown to be a result of using known system parameters as unknown fitting parameters, permitting constant values to vary, permitting unphysical values (such as negative adsorption sites) and an acceptance of poor fits. Using correct system parameters we provide examples where the Bohart-Adams prediction for the breakthrough time is more than double the experimentally observed value. It is shown that the symmetric exponential form is an inevitable consequence of a mathematical model consisting of a balance between advection and a mass sink, where the sink is of the Langmuir form. Finally, we briefly mention a model that fits a wider range of experimental data without resorting to unphysical and inconsistent parameter values.
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dc.description.sponsorship
T. Myers is funded by MCIN/AEI/10.13039/50110 0 011033/and by ERDF A Way of Making Europe, grant number PID2020-115023RB-I00. He acknowledges the CERCA Programme of the Generalitat de Catalunya and the Spanish State Research Agency, through the Severo Ochoa and Maria de Maeztu Program for Centres and Units of Excellence in R & D (CEX2020-001084-M) .
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dc.format.extent
11 p.
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dc.relation.ispartof
International Communications in Heat and Mass Transfer
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dc.rights
Attribution-NonCommercial-NoDerivatives 4.0 International
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dc.rights.uri
http://creativecommons.org/licenses/by-nc-nd/4.0/
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dc.subject.other
Original content
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dc.subject.other
Adsorption column
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dc.subject.other
Toluene-N2 mixture dataset (Reference data)
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dc.subject.other
Cr(III) on zeolite (Reference data)
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dc.subject.other
Contaminant removal
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dc.subject.other
Adsorption
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dc.subject.other
Mathematical model
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dc.subject.other
Bohart-Adams
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dc.title
Is it time to move on from the Bohart-Adams model for column adsorption?
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dc.type
info:eu-repo/semantics/article
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dc.description.version
info:eu-repo/semantics/publishedVersion
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dc.identifier.doi
10.1016/j.icheatmasstransfer.2024.108062
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dc.rights.accessLevel
info:eu-repo/semantics/openAccess