Hyeong Gyun Ahn
Current Organizations / Institutes
The organizations/institutes from the scholar's latest article
Research Subjects
Research Interests
Hyeong Gyun Ahn has a total of 9 co-authors. Here are the top co-authors by number of shared publications:
- Jun Seok Kim
Department of Chemical Engineering, Kyonggi University, Suwon 16227, Korea
2 shared publications - Hyun Jin Jung
Department of Chemical Engineering, Dankook University, Yongin 16890, Gyeonggi, Korea
1 shared publication - Hyunjoon Kim
Kyonggi University
1 shared publication - Hyunjoon Kim1 shared publication
- Ja Eun Lee
Department of Chemical Engineering, Kyonggi University, 154-42, Gwanggyosan-ro, Suwon 16227, Gyeonggi, Republic of Korea
1 shared publication - Kyeong Keun Oh
R&D Center, SugarEn Co., Ltd., Yongin 16890, Gyeonggi-do, Korea
1 shared publication
Latest Publications
- Open Access
- 2 October 2024
- Published by MDPI AG in Polysaccharides
- Vol. 5 (4) , 552-566
Optimized Furfural Production Using the Acid Catalytic Conversion of Xylan Liquor from Organosolv-Fractionated Rice Husk
This study determined the optimal production of furfural (FuR) from liquid hydrolysate xylan liquor obtained through a two-stage pretreatment process using NaOH for de-ashing and EtOH for the delignification of raw rice husk (RH). The de-ashing pretreatment was conducted at 150 °C, with 6.0% (w/v) NaOH and a reaction time of 40 min. The optimal conditions for delignification pretreatment, performed using an organosolv fractionation method with EtOH, were a reaction temperature of 150 °C, 60% (v/v) EtOH, 0.25% (w/v) H2SO4, and a reaction time of 90 min. Through a two-stage pretreatment process, a liquid hydrolysate in the form of xylan liquor was obtained, which was subjected to an acid catalytic conversion process to produce FuR. The process conditions were varied, with reaction temperatures of 130–170 °C, H2SO4 catalyst concentrations of 1.0–3.0 wt.%, and reaction times of 0–90 min. The Response Surface Methodology tool was used to identify the optimal FuR yield from xylan liquor. Ultimately, the optimal process conditions for the acid catalytic conversion were found to be a substrate-to-catalyst ratio of 2:8, a reaction temperature of 168.9 °C, a catalyst concentration of 1.9 wt.%, and a reaction time of 41.24 min, achieving an FuR yield of 67.31%.
- 2 October 2024
- Published by MDPI AG in Polysaccharides
- Vol. 5 (4) , 552-566
Open AccessOptimized Furfural Production Using the Acid Catalytic Conversion of Xylan Liquor from Organosolv-Fractionated Rice Husk
This study determined the optimal production of furfural (FuR) from liquid hydrolysate xylan liquor obtained through a two-stage pretreatment process using NaOH for de-ashing and EtOH for the delignification of raw rice husk (RH). The de-ashing pretreatment was conducted at 150 °C, with 6.0% (w/v) NaOH and a reaction time of 40 min. The optimal conditions for delignification pretreatment, performed using an organosolv fractionation method with EtOH, were a reaction temperature of 150 °C, 60% (v/v) EtOH, 0.25% (w/v) H2SO4, and a reaction time of 90 min. Through a two-stage pretreatment process, a liquid hydrolysate in the form of xylan liquor was obtained, which was subjected to an acid catalytic conversion process to produce FuR. The process conditions were varied, with reaction temperatures of 130–170 °C, H2SO4 catalyst concentrations of 1.0–3.0 wt.%, and reaction times of 0–90 min. The Response Surface Methodology tool was used to identify the optimal FuR yield from xylan liquor. Ultimately, the optimal process conditions for the acid catalytic conversion were found to be a substrate-to-catalyst ratio of 2:8, a reaction temperature of 168.9 °C, a catalyst concentration of 1.9 wt.%, and a reaction time of 41.24 min, achieving an FuR yield of 67.31%.
- Open Access
- 25 December 2023
- Published by The Korean Society for New and Renewable Energy in New & Renewable Energy
- Vol. 19 (4) , 11-19
Sulfuric Acid Catalytic Conversion to Levulinic Acid from Cellulosic Biomass
- 25 December 2023
- Published by The Korean Society for New and Renewable Energy in New & Renewable Energy
- Vol. 19 (4) , 11-19
Open AccessSulfuric Acid Catalytic Conversion to Levulinic Acid from Cellulosic Biomass