Overall
- Language
- English
- Conflict of Interest
- In relation to this article, we declare that there is no conflict of interest.
- Publication history
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Received September 16, 2024
Accepted March 10, 2025
Available online May 25, 2025
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This is an Open-Access article distributed under the terms of the Creative Commons Attribution Non-Commercial License (http://creativecommons.org/licenses/bync/3.0) which permits
unrestricted non-commercial use, distribution, and reproduction in any medium, provided the original work is properly cited.
Most Cited
Valorization of Corncob as a Sustainable Feedstock for Lactic Acid Production via Improved Biomass-to-Glucose Conversion Based on KOH Pretreatment
https://doi.org/10.1007/s11814-025-00443-y
Abstract
Biorefi ning of food waste has gained increasing attention as a sustainable approach for producing platform chemicals
such as lactic acid. In this study, corncob (CC), a byproduct of corn processing, was utilized as a feedstock for biorefi ning
through biomass hydrolysis and lactic acid fermentation. Due to the low enzymatic digestibility of raw CC caused by its
lignin content, KOH pretreatment was conducted prior to enzymatic hydrolysis to enhance glucose recovery. Among the
tested KOH concentrations (1–5%), 3% KOH pretreatment yielded the highest biomass-to-glucose conversion (25.38%),
with a solid recovery (SR) of 47.60%, glucan content (GC) of 57.23%, and enzymatic digestibility (ED) of 84.70%. These
values represent a signifi cant improvement compared to raw CC (biomass-to-glucose conversion: 7.97%; SR: 100%; GC:
35.22%; ED: 20.57%). Compositional and physicochemical analyses confi rmed that 3% KOH-pretreated CC (3%KpCC) had
a reduced lignin content (11.69%) compared to raw CC (20.48%), along with irregular cracks and crevices that improved
enzymatic digestibility via easier enzyme access. Fermentation of Lacticaseibacillus rhamnosus with the hydrolysate as
an alternative carbon source for 24 h was found to produce about 9.89 g/L lactic acid and 98.9% conversion, similar to the
control medium (about 9.81 g/L production and 98.1% conversion). Overall, the mass balance analysis revealed a 3.2-fold
increase in lactic acid production (251 g/kg biomass) with the 3% KOH pretreatment process compared to the control. This
study demonstrates a signifi cantly improved biorefi nery strategy that eff ectively contributes to both CC waste management
and value-added chemical production.

