dc.contributor.author |
Prithiraj, Alicia
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|
dc.contributor.author |
Tichapondwa, Shepherd Masimba
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|
dc.contributor.author |
Chirwa, Evans M.N.
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|
dc.date.accessioned |
2024-09-12T07:50:30Z |
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dc.date.available |
2024-09-12T07:50:30Z |
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dc.date.issued |
2024-05 |
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dc.description |
DATA AVAILABILITY STATEMENT :
The data that support the findings of this study are available on request from the corresponding author. The data are not publicly available due to privacy or ethical restrictions. |
en_US |
dc.description.abstract |
This study focused on presenting the newly developed growth model for bacterial species present in a petrochemical processing plant in South Africa. The findings of the study serve as a theoretical basis for future experiments aimed at understanding the formation of bacterial metabolites as the bacteria develops. An unstructured kinetic model using AQUASIM 2.3, together with experimental spectrophotometric results, were used to evaluate the growth of Gram-negative bacteria in a batch reactor system. Spectrophotometer results showed the absence of a stationary phase. The exponential bacterial growth phase supported the total organic carbon (TOC) results, showing that bacterial growth occurred on days 6 and 13; this is rarely reported in literature, as the growth in this system was much slower than the growth of single-strain studies. The TOC concentration values indicated that carbon sources did not deplete in the death phase, suggesting the presence of a long-term stationary phase and the production of acetate. The presence of Pseudomonas sp. and sulphate-reducing bacteria (SRB) are commonly reported in industrial systems as they play a role in equipment failure in industry. However, in this multispecies study, methods using third generation sequencing together with high-performance liquid chromatography (HPLC) have shown that the selective attachment and production of acetate by abundant Clostridium sp. has ascertained their role in equipment failures in the petrochemical environment. |
en_US |
dc.description.department |
Chemical Engineering |
en_US |
dc.description.librarian |
hj2024 |
en_US |
dc.description.sdg |
SDG-09: Industry, innovation and infrastructure |
en_US |
dc.description.sponsorship |
National Research Foundation and Rand Water Chair in Water Utilization. |
en_US |
dc.description.uri |
http://wileyonlinelibrary.com/journal/cjce |
en_US |
dc.identifier.citation |
Prithiraj A., Tichapondwa S., Chirwa E.M.N. 2024, 'Kinetic growth model and metabolic effect of a bacterial consortia from a petrochemical processing plant', Canadian Journal of Chemical Engineering, vol. 102, no. 5, pp. 1814-1824, doi : 10.1002/cjce.25154. |
en_US |
dc.identifier.issn |
0008-4034 (print) |
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dc.identifier.issn |
1939-019X (online) |
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dc.identifier.other |
10.1002/cjce.25154 |
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dc.identifier.uri |
http://hdl.handle.net/2263/98145 |
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dc.language.iso |
en |
en_US |
dc.publisher |
Wiley |
en_US |
dc.rights |
© 2023 The Authors. The Canadian Journal of Chemical Engineering published by Wiley Periodicals LLC on behalf of Canadian Society for Chemical Engineering.
This is an open access article under the terms of the Creative Commons Attribution-NonCommercial-NoDerivs License. |
en_US |
dc.subject |
Petrochemical processing plant |
en_US |
dc.subject |
South Africa (SA) |
en_US |
dc.subject |
Total organic carbon (TOC) |
en_US |
dc.subject |
Pseudomonas sp. |
en_US |
dc.subject |
Sulphate-reducing bacteria (SRB) |
en_US |
dc.subject |
High-performance liquid chromatography (HPLC) |
en_US |
dc.subject |
Kinetic model |
en_US |
dc.subject |
Petrochemical industry |
en_US |
dc.subject |
Mixed bacterial culture |
en_US |
dc.subject |
Metabolites |
en_US |
dc.subject |
SDG-09: Industry, innovation and infrastructure |
en_US |
dc.title |
Kinetic growth model and metabolic effect of a bacterial consortia from a petrochemical processing plant |
en_US |
dc.type |
Article |
en_US |