ISSN: 0256-1115 (print version) ISSN: 1975-7220 (electronic version)
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Conflict of Interest
In relation to this article, we declare that there is no conflict of interest.
Publication history
Received March 18, 2025
Revised May 24, 2025
Accepted May 29, 2025
Available online October 25, 2025
Acknowledgements
Lignin · Alkaline thermal treatment · Hydrogen production · Carbon neutral · Renewable resource
articles 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.
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High-Yield Hydrogen Production from Lignin via Optimized Alkaline Thermal Treatment with CO

Department of Chemical Engineering and Materials Science , Graduate Program in System Health Science and Engineering, Ewha Womans University 1Ewha-Syensqo R&I Center 2Syensqo-Site d’Aubervilliers
wjkim1974@ewha.ac.kr
Korean Journal of Chemical Engineering, October 2025, 42(12), 2987-2995(9)
https://doi.org/10.1007/s11814-025-00504-2

Abstract

Current thermochemical methods for hydrogen (H 2 ) production, such as coal gasifi cation and steam reforming, inevitably

produce anthropogenic CO 2 . In contrast, biomass-derived H 2 off ers a carbon–neutral pathway. Despite its high energy density,

lignin—accounting for ~ 30% of lignocellulosic biomass—has been underutilized. This study presents an alkaline thermal

treatment (ATT) process that effi ciently converts lignin into high-purity H 2 while minimizing CO 2 emissions by sequestering

carbon as solid carbonate, potentially rendering the process carbon negative. Compared to conventional gasifi cation, the ATT

process operates at 170–450 °C lower temperature. Under optimized conditions, lignin-ATT produced 116.02 mmol H 2 /g

lignin (2.6 L H 2 /g lignin), the highest H 2 yield reported for lignocellulosic biomass, far exceeding cellulose-ATT (39.07 mmol

H 2 /g cellulose), with a maximum H 2 purity of 94.75%. Importantly, this study confi rms that stoichiometric NaOH addition

enables H 2 production reaching nearly 97% of the theoretical maximum yield at signifi cantly lower temperatures than steam

gasifi cation. The reactivity of diff erent alkaline hydroxides is also compared. This study also demonstrates a sustainable

approach using black liquor, real waste lignin, and a NaOH recycling system. This strategy reduces the production costs and

generates CaCO₃ as a valuable by-product.

Keywords

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