Integrated supercritical carbon dioxide extraction for efficient furfural production from xylose using formic acid as a catalyst

被引:1
|
作者
Namhaed, Kritsana [1 ,2 ,3 ]
Peres, Yolande [1 ]
Kiatkittipong, Worapon [2 ]
Triquet, Thibaut [1 ]
Cognet, Patrick [1 ]
机构
[1] Univ Toulouse, Lab Genie Chim, CNRS, INPT,UPS, F-31062 Toulouse 09, France
[2] Silpakorn Univ, Fac Engn & Ind Technol, Dept Chem Engn, Nakhon Pathom 73000, Thailand
[3] Univ Toulouse, Lab Genie Chim, Toulouse, France
来源
关键词
Xylose; Formic acid; Furfural; Supercritical CO 2; Semi -batch process; DEHYDRATION; CONVERSION; KINETICS; OPTIMIZATION; HYDROLYSIS; SYSTEM;
D O I
10.1016/j.supflu.2024.106274
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
This study investigates the production of furfural via formic acid-catalyzed dehydration of xylose and the effect of simultaneous extraction of furfural using supercritical carbon dioxide (Sc-CO2). The addition of Sc-CO2 results in a secondary reaction pathway comprised of two steps: CO2-catalyzed isomerization of xylose into the reactive intermediate xylulose, followed by furfural production from xylulose, catalyzed by formic acid. Xylose dehydration with CO2 in both batch and semi-batch systems yielded a higher furfural yield and selectivity compared with systems without CO2. The Sc-CO2 extraction in a semi-batch system prevents furfural degradation by maintaining high productivity, even with increased initial xylose concentration. A maximum furfural yield of 68.5% (71.4% selectivity and 99% separation efficiency) was achieved after 5 h at 140 degrees C and 20 MPa with a constant flow rate of 5 g/min of CO2 and initial concentrations of 10 g/L of xylose and 10 wt% of formic acid.
引用
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页数:10
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