TY - JOUR
T1 - Production of d-xylonic acid using a non-recombinant Corynebacterium glutamicum strain
AU - Tenhaef, Niklas
AU - Brüsseler, Christian
AU - Radek, Andreas
AU - Hilmes, René
AU - Unrean, Pornkamol
AU - Marienhagen, Jan
AU - Noack, Stephan
N1 - Copyright © 2018 Elsevier Ltd. All rights reserved.
PY - 2018/11
Y1 - 2018/11
N2 - It was found that Corynebacterium glutamicum ΔiolR devoid of the transcriptional regulator IolR accumulates high amounts of d-xylonate when cultivated in the presence of d-xylose. Detailed analyses of constructed deletion mutants revealed that the putative myo-inositol 2-dehydrogenase IolG also acts as d-xylose dehydrogenase and is mainly responsible for d-xylonate oxidation in this organism. Process development for d-xylonate production was initiated by cultivating C. glutamicum ΔiolR on defined d-xylose/d-glucose mixtures under batch and fed-batch conditions. The resulting yield matched the theoretical maximum of 1 mol mol-1 and high volumetric productivities of up to 4 g L-1 h-1 could be achieved. Subsequently, a novel one-pot sequential hydrolysis and fermentation process based on optimized medium containing hydrolyzed sugarcane bagasse was developed. Cost-efficiency and abundance of second-generation substrates, good performance indicators, and enhanced market access using a non-recombinant strain open the perspective for a commercially viable bioprocess for d-xylonate production in the near future.
AB - It was found that Corynebacterium glutamicum ΔiolR devoid of the transcriptional regulator IolR accumulates high amounts of d-xylonate when cultivated in the presence of d-xylose. Detailed analyses of constructed deletion mutants revealed that the putative myo-inositol 2-dehydrogenase IolG also acts as d-xylose dehydrogenase and is mainly responsible for d-xylonate oxidation in this organism. Process development for d-xylonate production was initiated by cultivating C. glutamicum ΔiolR on defined d-xylose/d-glucose mixtures under batch and fed-batch conditions. The resulting yield matched the theoretical maximum of 1 mol mol-1 and high volumetric productivities of up to 4 g L-1 h-1 could be achieved. Subsequently, a novel one-pot sequential hydrolysis and fermentation process based on optimized medium containing hydrolyzed sugarcane bagasse was developed. Cost-efficiency and abundance of second-generation substrates, good performance indicators, and enhanced market access using a non-recombinant strain open the perspective for a commercially viable bioprocess for d-xylonate production in the near future.
U2 - 10.1016/j.biortech.2018.07.127
DO - 10.1016/j.biortech.2018.07.127
M3 - Journal articles
C2 - 30092487
SN - 0960-8524
VL - 268
SP - 332
EP - 339
JO - Bioresource technology
JF - Bioresource technology
ER -