Rate-limiting step analysis of the microbial desulfurization of dibenzothiophene in a model oil system

A mechanistic analysis of the various mass transport and kinetic steps in the microbial desulfurization of dibenzothiophene (DBT) by Rhodococcus erythropolis IGTS8 in a model biphasic (oil–water), small-scale system was performed. The biocatalyst was distributed into three populations, free cells in...

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Main Authors: Abin-Fuentes, Andres, Mohamed, Magdy El-Said, Leung, James, Wang, Daniel I., Prather, Kristala L. Jones
Other Authors: Massachusetts Institute of Technology. Center for Biomedical Innovation
Format: Article
Language:en_US
Published: Wiley Blackwell 2016
Online Access:http://hdl.handle.net/1721.1/101229
https://orcid.org/0000-0002-2046-2726
https://orcid.org/0000-0003-0437-3157
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author Abin-Fuentes, Andres
Mohamed, Magdy El-Said
Leung, James
Wang, Daniel I.
Prather, Kristala L. Jones
author2 Massachusetts Institute of Technology. Center for Biomedical Innovation
author_facet Massachusetts Institute of Technology. Center for Biomedical Innovation
Abin-Fuentes, Andres
Mohamed, Magdy El-Said
Leung, James
Wang, Daniel I.
Prather, Kristala L. Jones
author_sort Abin-Fuentes, Andres
collection MIT
description A mechanistic analysis of the various mass transport and kinetic steps in the microbial desulfurization of dibenzothiophene (DBT) by Rhodococcus erythropolis IGTS8 in a model biphasic (oil–water), small-scale system was performed. The biocatalyst was distributed into three populations, free cells in the aqueous phase, cell aggregates and oil–adhered cells, and the fraction of cells in each population was measured. The power input per volume (P/V) and the impeller tip speed (v[subscript tip]) were identified as key operating parameters in determining whether the system is mass transport controlled or kinetically controlled. Oil–water DBT mass transport was found to not be limiting under the conditions tested. Experimental results at both the 100 mL and 4 L (bioreactor) scales suggest that agitation leading to P/V greater than 10,000 W/ m3 and/or v[subscript tip] greater than 0.67 m/s is sufficient to overcome the major mass transport limitation in the system, which was the diffusion of DBT within the biocatalyst aggregates.
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spelling mit-1721.1/1012292022-09-26T17:28:15Z Rate-limiting step analysis of the microbial desulfurization of dibenzothiophene in a model oil system Abin-Fuentes, Andres Mohamed, Magdy El-Said Leung, James Wang, Daniel I. Prather, Kristala L. Jones Massachusetts Institute of Technology. Center for Biomedical Innovation Massachusetts Institute of Technology. Department of Chemical Engineering Abin-Fuentes, Andres Leung, James Wang, Daniel I. Prather, Kristala L. Jones A mechanistic analysis of the various mass transport and kinetic steps in the microbial desulfurization of dibenzothiophene (DBT) by Rhodococcus erythropolis IGTS8 in a model biphasic (oil–water), small-scale system was performed. The biocatalyst was distributed into three populations, free cells in the aqueous phase, cell aggregates and oil–adhered cells, and the fraction of cells in each population was measured. The power input per volume (P/V) and the impeller tip speed (v[subscript tip]) were identified as key operating parameters in determining whether the system is mass transport controlled or kinetically controlled. Oil–water DBT mass transport was found to not be limiting under the conditions tested. Experimental results at both the 100 mL and 4 L (bioreactor) scales suggest that agitation leading to P/V greater than 10,000 W/ m3 and/or v[subscript tip] greater than 0.67 m/s is sufficient to overcome the major mass transport limitation in the system, which was the diffusion of DBT within the biocatalyst aggregates. National Institutes of Health (U.S.). Biotechnology Training Program (Grant T32GM008334) Saudi Aramco 2016-02-22T15:28:43Z 2016-02-22T15:28:43Z 2013-11 2013-10 Article http://purl.org/eprint/type/JournalArticle 00063592 http://hdl.handle.net/1721.1/101229 Abin-Fuentes, Andres, James C. Leung, Magdy El-Said Mohamed, Daniel I.C. Wang, and Kristala L.J. Prather. “Rate-Limiting Step Analysis of the Microbial Desulfurization of Dibenzothiophene in a Model Oil System.” Biotechnology and Bioengineering 111, no. 5 (November 27, 2013): 876–884. https://orcid.org/0000-0002-2046-2726 https://orcid.org/0000-0003-0437-3157 en_US http://dx.doi.org/10.1002/bit.25148 Biotechnology and Bioengineering Creative Commons Attribution-Noncommercial-Share Alike http://creativecommons.org/licenses/by-nc-sa/4.0/ application/pdf Wiley Blackwell PMC
spellingShingle Abin-Fuentes, Andres
Mohamed, Magdy El-Said
Leung, James
Wang, Daniel I.
Prather, Kristala L. Jones
Rate-limiting step analysis of the microbial desulfurization of dibenzothiophene in a model oil system
title Rate-limiting step analysis of the microbial desulfurization of dibenzothiophene in a model oil system
title_full Rate-limiting step analysis of the microbial desulfurization of dibenzothiophene in a model oil system
title_fullStr Rate-limiting step analysis of the microbial desulfurization of dibenzothiophene in a model oil system
title_full_unstemmed Rate-limiting step analysis of the microbial desulfurization of dibenzothiophene in a model oil system
title_short Rate-limiting step analysis of the microbial desulfurization of dibenzothiophene in a model oil system
title_sort rate limiting step analysis of the microbial desulfurization of dibenzothiophene in a model oil system
url http://hdl.handle.net/1721.1/101229
https://orcid.org/0000-0002-2046-2726
https://orcid.org/0000-0003-0437-3157
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