Microbial cell viability-driven operational strategy for enhanced acetate production in syngas fermentation

Journal Article (2025)
Author(s)

Mungyu Lee (TU Delft - BT/Bioprocess Engineering, Gwangju Institute of Science and Technology)

Ji Yeon Kim (Gwangju Institute of Science and Technology)

Nulee Ji (Gwangju Institute of Science and Technology)

Ludovic Jourdin (TU Delft - BT/Bioprocess Engineering)

A.J.J. Straathof (TU Delft - BT/Bioprocess Engineering)

In Seop Chang (Gwangju Institute of Science and Technology)

Research Group
BT/Bioprocess Engineering
DOI related publication
https://doi.org/10.1016/j.jece.2025.116531
More Info
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Publication Year
2025
Language
English
Research Group
BT/Bioprocess Engineering
Bibliographical Note
Green Open Access added to TU Delft Institutional Repository 'You share, we take care!' - Taverne project https://www.openaccess.nl/en/you-share-we-take-care Otherwise as indicated in the copyright section: the publisher is the copyright holder of this work and the author uses the Dutch legislation to make this work public.@en
Issue number
3
Volume number
13
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Abstract

Syngas fermentation is a promising bioprocessing method that utilises autotrophic organisms to convert C1 gases, such as CO and CO2, into valuable chemicals, offering both environmental and economic benefits. Despite these advantages, the industrial application of gas fermentation remains limited owing to challenges in productivity associated with gas substrates. While previous studies have focused on optimizing reactor design, mass transfer, and growth medium as solutions to these specific challenges, the direct correlation between cell viability and productivity remains unexplored. To address this gap, this study investigates the viability of the acetogenic strain Eubacterium callanderi KIST612 and its impact on acetate production across various operational modes. Unlike conventional single-reactor systems, a dual-reactor strategy was implemented to enhance viable cell retention, leading to improved process efficiency. This approach significantly increased the total carbon conversion rate to 9.30mmolh-1 and the specific productivity of viable cells to 0.13g gcell-1h-1, ultimately achieving the highest acetate titer (34.4gL-1) with >53% cell viability. These findings represent a major advancement over previous studies, demonstrating that maintaining cell viability is critical for optimizing acetate productivity. By integrating viability control into process operations, this study presents a scalable and efficient strategy to enhance gas fermentation performance, improve substrate conversion efficiency, and expand biochemical production potential for industrial applications.

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