Continuous catalytic upgrading of fast pyrolysis oil using iron oxides in red mud

被引:23
|
作者
Kastner, James R. [1 ]
Hilten, Roger [1 ]
Weber, Justin [1 ]
McFarlane, Andrew R. [2 ]
Hargreaves, Justin S. J. [2 ]
Batra, Vidya S. [3 ]
机构
[1] Univ Georgia, Coll Engn, Biochem Engn, Athens, GA 30602 USA
[2] Univ Glasgow, Sch Chem, WestCHEM, Glasgow G12 8QQ, Lanark, Scotland
[3] TERI Univ, Ctr Energy & Environm, New Delhi 110003, India
来源
RSC ADVANCES | 2015年 / 5卷 / 37期
关键词
BAUXITE MINING WASTE; BIO-OIL; BIOMASS PYROLYSIS; ACID; REDUCTION; TRANSFORMATION; KETONIZATION; LEVOGLUCOSAN; HYDROCARBONS; EXTRACTION;
D O I
10.1039/c5ra01548k
中图分类号
O6 [化学];
学科分类号
0703 ;
摘要
A catalyst composed primarily of magnetite was prepared from red mud, via H-2 reduction at 300 degrees C, which significantly increased the surface area. Ammonia and CO2 temperature programmed desorption indicated both acid and base active sites. Continuous reaction studies conducted with individual compounds, mixtures of model compounds, and water extracted fast pyrolysis oil indicated that acetone was the primary product from acetic acid, and acetone and 2-butanone from acetol. Levoglucosan went down the same pathway, since it formed acetic acid, formic acid, and acetol. Total conversion and yields approached 100% and 22 mol% ketones at 400 degrees C and a W/F of 6 h for a model mixture and 15-20 mol% ketones at W/F 1.4-4 h and 400-425 degrees C using water extracted oil. Space time yields approached 60 g ketones per L-cat per h for the model mixture and 120 g per L-cat per h for a commercial oil. The catalyst simultaneously reduced acidity, allowed recovery of carbon, and generated upgradable intermediates from the aqueous fraction of fast pyrolysis oil in a "continuous" process.
引用
收藏
页码:29375 / 29385
页数:11
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