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Direct electrochemical extraction increases microbial succinic acid production from spent sulphite liquor

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    • 바이오플라스틱
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      1. 용매
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      1. 계면활성제⁄증점제
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      2. 식품첨가제
논문

Direct electrochemical extraction increases microbial succinic acid production from spent sulphite liquor

학술지

Green chemistry : an international journal and green chemistry resource : GC

저자명

Pateraki, Chrysanthi; Andersen, Stephen J.; Ladakis, Dimitrios; Koutinas, Apostolis; Rabaey, Korneel

초록

<P>The fermentative production of succinic acid leads to increasing toxicity over time, and requires base addition to counteract acidification. Here we integrated a fed-batch <I>Basfia succiniciproducens</I> succinic acid fermentation with membrane electrolysis. This approach brings the broth in direct contact with an OH<SUP>&#x2212;</SUP> and H<SUB>2</SUB> producing cathode, and enables <I>in situ</I> extraction of succinate towards the low volume H<SUP>+</SUP> and O<SUB>2</SUB> producing anode compartment. In the latter, the succinate is acidified to succinic acid and precipitated. The key advantage of the cathodic process is the production of base maintaining fermentation pH with limited external base addition. The bacterial cells are recycled through the cathode compartment of the electrochemical cell, and exposed to H<SUB>2</SUB>, creating biological reducing power. Fermentations were executed with glucose, xylose and ultrafiltered spent sulphite liquor (SSL), the side stream generated <I>via</I> acidic sulphite pulping of <I>Eucalyptus globulus</I> wood. The membrane was not permeable to cells, color and solids, which resulted in combined succinate extraction, clarification, acidification and concentration in a single unit operation. The succinic acid to by-product ratio increased, favoring the production of succinic acid over lactic, formic and acetic acids, with up to 15% higher total sugars to succinic acid conversion yield. The OH<SUP>&#x2212;</SUP> production due to water reduction resulted in lower NaOH usage (up to 33% less) for maintaining the pH during fermentation. The maximum productivity also increased by 30% to a rate of 0.41 g L<SUP>&#x2212;1</SUP> h<SUP>&#x2212;1</SUP> with the electrochemical system, with 1.65 kW h per kg succinic acid extracted in the case of SSL and 2.4 and 1.9 kW h per kg succinic acid extracted in the case of glucose and xylose, respectively. Considering the aforementioned advantages, this integrated system could evolve into a breakthrough technology in sustainable industrial succinic acid production from crude industrial side streams.</P><P>Graphic Abstract</P><P>The fermentative production of succinic acid leads to increasing toxicity over time, and requires continuous succinic acid removal from the broth to improve fermentation efficiency.<BR/><IMG SRC='http://pubs.rsc.org/services/images/RSCpubs.ePlatform.Service.FreeContent.ImageService.svc/ImageService/image/GA?id=c9gc00361d'/><BR/></P>

발행연도

2019

발행기관

The Royal Society of Chemistry

ISSN

1463-9262

ISSN

1463-9270

21

9

페이지

pp.2401-2411

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논문; 2019-01-01

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