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In relation to this article, we declare that there is no conflict of interest.
Publication history
Received November 16, 2025
Revised November 16, 2025
Accepted January 22, 2026
Available online May 25, 2026
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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Hydrothermal Pretreatment and Liquefaction Co-Production of Xylooligosaccharides and Bio-Based Polyols from Wheat Straw

College of Chemical Engineering, Shenyang University of Chemical Technology 1Guangzhou Institute of Energy Conversion, Chinese Academy of Sciences 23 R&D Center of Xuyi Attapulgite Energy and Environmental Materials
zhanghr@ms.giec.ac.cn, cxd_cxd@hotmail.com
Korean Journal of Chemical Engineering, May 2026, 43(6), 1535-1542(8)
https://doi.org/10.1007/s11814-026-00656-9

Abstract

In this study, wheat straw (WS) was pretreated using hydrothermal technology to the co-produce xylo-oligosaccharides (XOS) and bio-based polyols, thereby enabling the efficient utilization of all components of WS. The results showed that hydrothermal pretreatment significantly reduced the hemicellulose content in WS (from 21.18% to 11.93%), with an XOS yield of 44.9%, and simultaneously increased the relative contents of cellulose and lignin in hydrothermally pretreated wheat straw (HWS). Subsequently, the liquefaction behavior of HWS was investigated using glycerol as the main liquefaction solvent and sulfuric acid as the catalyst. Hydrothermal pretreatment could disrupt the dense structure of WS, increase the exposed surface area of cellulose, and significantly enhance porosity, thereby improving liquefaction efficiency. The liquefaction effect was optimal. The liquefied residue rate (LR) of HWS was 8.17% under the optimal conditions (PEG-400 to glycerol ratio of 4:6, a reaction time of 120 min, a temperature of 170℃, a catalyst dosage of 3%, and a liquid-to-solid ratio of 5:1), and the hydroxyl value was 496 mg KOH/g, which was lower than that of WS. In addition, hydrothermal pretreatment could significantly increase glycerol concentration in the liquefaction solvent, thereby reducing liquefaction costs.

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