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Continuous succinic acid fermentation using immobilised Actinobacillus succinogenes

Dissertation (MEng)--University of Pretoria, 2013.

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Other Authors: Nicol, Willie
Format: Thesis
Language:English
Published: University of Pretoria 2014
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access_status_str Open Access
author2 Nicol, Willie
author_browse Nicol, Willie
author_facet Nicol, Willie
collection Thesis
dc_rights_str_mv © 2013 University of Pretoria. All rights reserved. The copyright in this work vests in the University of Pretoria. No part of this work may be reproduced or transmitted in any form or by any means, without the prior written permission of the University of Pretoria.
description Dissertation (MEng)--University of Pretoria, 2013.
format Thesis
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institution University of Pretoria (South Africa)
language English
last_indexed 2026-06-10T12:38:19.381Z
license_str Other — see source repository
provenance_str_mv Harvested via OAI-PMH from UPSpace — University of Pretoria Institutional Repository
publishDate 2014
publishDateRange 2014
publishDateSort 2014
publisher University of Pretoria
publisherStr University of Pretoria
record_format dspace
source_str UPSpace — University of Pretoria Institutional Repository
spelling oai:repository.up.ac.za:2263/40818 Continuous succinic acid fermentation using immobilised Actinobacillus succinogenes Nicol, Willie karishma.maharaj@gmail.com Maharaj, Karishma Succinic acid Actinobacillus succinogenes Continuous fermentation Biofilm Pyruvate formate lyase Pyruvate dehydrogenase UCTD Dissertation (MEng)--University of Pretoria, 2013. Actinobacillus succinogenes cells were grown on Poraver® support particles in a packed-bed reactor. Dilution rates (D) of 0.054–0.72 h-1 were investigated. Glucose was used as substrate. CO2 (g) was bubbled into a complex medium to satisfy the fixation requirements and maintain anaerobic conditions. At D ≥ 0.31 h-1, an initial glucose concentration of 35 g.L-1 was used; at lower dilution rates, this was increased to 60 g.L-1 in order to avoid substrate limitations. By-product formation included acetic and formic acids. A maximum productivity of 10.7 g.L-1 was obtained at D = 0.7 h-1. It was found that the system provided repeatable results at a given D. The longest steady state period was maintained for about 97 h at D = 0.31 h-1. Steady state stability was maintained for > 72 h at D < 0.31 h-1. For periods longer than 75 h, however, inhibitory acid titres resulted in a gradual decline in productivity. At higher dilution rates, long-term stability could not be maintained. The low acid titres produced significant biofilm sloughing following aggressive biofilm growth, resulting in oscillatory system behaviour. For fermentation times < 115 h, the dilution rate was secondary to the attachment area in determining the total biomass at steady state. Total biomass values were then used to determine specific rates. A clear trend was observed, with the specific glucose consumption rate, and specific acid production rates, increasing with increasing D. This was explained by assuming a maintenance-driven system at all Ds studied. A product analysis indicated that at ΔS < 15 g.L-1, pyruvate formate lyase was the preferred oxidative route. A shift to the pyruvate dehydrogenase pathway occurred at higher ΔS values, so that the highest YSS values obtained exceeded 0.85 g.g-1. A decrease in C3 by-product formation resulted in high YSS values being maintained, indicating an additional, unknown source of nicotinamide adenine dinucleotide (NADH). It is recommended that any process utilising immobilised A. succinogenes cells should operate at an intermediate D, in order to maintain long-term reactor stability, high productivities and good yields. gm2014 Chemical Engineering unrestricted 2014-07-17T12:08:28Z 2014-07-17T12:08:28Z 2014-04-08 2013 Dissertation Maharaj, K 2013, Continuous succinic acid fermentation using immobilised Actinobacillus succinogenes, MEng dissertation, University of Pretoria, Pretoria, viewed yymmdd <http://hdl.handle.net/2263/40818> E14/4/287/gm http://hdl.handle.net/2263/40818 en © 2013 University of Pretoria. All rights reserved. The copyright in this work vests in the University of Pretoria. No part of this work may be reproduced or transmitted in any form or by any means, without the prior written permission of the University of Pretoria. application/pdf University of Pretoria
spellingShingle Succinic acid
Actinobacillus succinogenes
Continuous fermentation
Biofilm
Pyruvate formate lyase
Pyruvate dehydrogenase
UCTD
Continuous succinic acid fermentation using immobilised Actinobacillus succinogenes
title Continuous succinic acid fermentation using immobilised Actinobacillus succinogenes
title_full Continuous succinic acid fermentation using immobilised Actinobacillus succinogenes
title_fullStr Continuous succinic acid fermentation using immobilised Actinobacillus succinogenes
title_full_unstemmed Continuous succinic acid fermentation using immobilised Actinobacillus succinogenes
title_short Continuous succinic acid fermentation using immobilised Actinobacillus succinogenes
title_sort continuous succinic acid fermentation using immobilised actinobacillus succinogenes
topic Succinic acid
Actinobacillus succinogenes
Continuous fermentation
Biofilm
Pyruvate formate lyase
Pyruvate dehydrogenase
UCTD
url http://hdl.handle.net/2263/40818