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

Authors :
Pateraki, Chrysanthi
Andersen, Stephen J.
Ladakis, Dimitrios
Koutinas, Apostolis
Rabaey, Korneel
Source :
Green Chemistry; 5/7/2019, Vol. 21 Issue 9, p2401-2411, 11p
Publication Year :
2019

Abstract

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 Basfia succiniciproducens succinic acid fermentation with membrane electrolysis. This approach brings the broth in direct contact with an OH<superscript>−</superscript> and H<subscript>2</subscript> producing cathode, and enables in situ extraction of succinate towards the low volume H<superscript>+</superscript> and O<subscript>2</subscript> 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<subscript>2</subscript>, creating biological reducing power. Fermentations were executed with glucose, xylose and ultrafiltered spent sulphite liquor (SSL), the side stream generated via acidic sulphite pulping of Eucalyptus globulus 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<superscript>−</superscript> 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<superscript>−1</superscript> h<superscript>−1</superscript> 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. [ABSTRACT FROM AUTHOR]

Details

Language :
English
ISSN :
14639262
Volume :
21
Issue :
9
Database :
Complementary Index
Journal :
Green Chemistry
Publication Type :
Academic Journal
Accession number :
136282399
Full Text :
https://doi.org/10.1039/c9gc00361d