Effect of Acetic Acid Addition on Decomposition of Xylose in Supercritical Water

被引:9
作者
Chalermsaktrakul, Tanawan [1 ]
Matsumura, Yukihiko [1 ]
机构
[1] Hiroshima Univ, Dept Mech Sci & Engn, 1-4-1 Kagamiyama, Higashihiroshima, Hiroshima 7398527, Japan
关键词
HYDROGEN-PRODUCTION; GASIFICATION; MECHANISM; ISOMERIZATION; DEHYDRATION; FEEDSTOCKS; CELLULOSE; CATALYST; KINETICS; GLUCOSE;
D O I
10.1021/acs.energyfuels.7b02720
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
The supercritical water gasification of xylose, a model substrate for hemicellulose, was carried out at 400 and 450 degrees C and at a constant pressure of 25 MPa in the presence of acetic acid using a continuous flow reactor. More specifically, we aimed to compare the reaction rate constants of xylose decomposition in both the presence and absence of acetic acid. Upon the application of a residence time of 0.5-5 s, a xylose concentration of 1.5 wt %, and an acetic acid concentration of 1.5 wt %, we successfully elucidated the effect of acetic acid on each reaction within the reaction network for the first time. In the presence of acetic acid, the retro-aldol reactions and carbon gasification production (i.e., the radical reactions) were suppressed, while the acetic-acid-catalyzed dehydration of xylulose to furfural (i.e., an ionic reaction) was enhanced by 2 orders of magnitude. As such, reaction control through the addition of chemical species to either stabilize ions or react with radicals appears possible.
引用
收藏
页码:1754 / 1760
页数:7
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