Furfural production from xylose using sulfonic ion-exchange resins (Amberlyst) and simultaneous stripping with nitrogen

被引:162
作者
Agirrezabal-Telleria, I. [1 ]
Larreategui, A. [1 ]
Requies, J. [1 ]
Gueemez, M. B. [1 ]
Arias, P. L. [1 ]
机构
[1] Univ Basque Country, Dept Chem & Environm Engn, Sch Engn, Bilbao 48013, Spain
关键词
Furfural; Process optimization; Xylose dehydration; Amberlyst; Stripping; LIQUID-PHASE DEHYDRATION; SOLID ACID CATALYSTS; HIGH-TEMPERATURE; CONVERSION; ZEOLITE; WATER; HYDROLYSIS; KINETICS;
D O I
10.1016/j.biortech.2011.05.015
中图分类号
S2 [农业工程];
学科分类号
0828 ;
摘要
The aim of this work deals with the development of new approaches to the production of furfural from xylose. It combines relatively cheap heterogeneous catalysts (Amberlyst 70) with simultaneous furfural stripping using nitrogen under semi-batch conditions. Nitrogen, compared to steam, does not dilute the vapor phase stream when condensed. This system allowed stripping 65% of the furfural converted from xylose and almost 100% of selectivity in the condensate. Moreover, high initial xylose loadings led to the formation of two water-furfural phases, which could reduce further purification costs. Constant liquid-vapor equilibrium along stripping could be maintained for different xylose loadings. The modeling of the experimental data was carried out in order to obtain a liquid-vapor mass-transfer coefficient. This value could be used for future studies under steady-state continuous conditions in similar reaction-systems. (C) 2011 Elsevier Ltd. All rights reserved.
引用
收藏
页码:7478 / 7485
页数:8
相关论文
共 25 条
[1]   KINETIC-STUDIES OF THE REACTIONS OF KETOSES AND ALDOSES IN WATER AT HIGH-TEMPERATURE .3. MECHANISM OF FORMATION OF 2-FURALDEHYDE FROM D-XYLOSE [J].
ANTAL, MJ ;
LEESOMBOON, T ;
MOK, WS ;
RICHARDS, GN .
CARBOHYDRATE RESEARCH, 1991, 217 :71-85
[2]  
ARNOLD DR, 2003, P S AFR CHEM ENG C S
[3]   Catalytic conversion of sugarcane bagasse, rice husk and corncob in the presence of TiO2, ZrO2 and mixed-oxide TiO2-ZrO2 under hot compressed water (HCW) condition [J].
Chareonlimkun, A. ;
Champreda, V. ;
Shotipruk, A. ;
Laosiripojana, N. .
BIORESOURCE TECHNOLOGY, 2010, 101 (11) :4179-4186
[4]   Liquid-phase catalytic processing of biomass-derived oxygenated hydrocarbons to fuels and chemicals [J].
Chheda, Juben N. ;
Huber, George W. ;
Dumesic, James A. .
ANGEWANDTE CHEMIE-INTERNATIONAL EDITION, 2007, 46 (38) :7164-7183
[5]   Exfoliated titanate, niobate and titanoniobate nanosheets as solid acid catalysts for the liquid-phase dehydration of D-xylose into furfural [J].
Dias, Ana S. ;
Lima, Sergio ;
Carriazo, Daniel ;
Rives, Vicente ;
Pillinger, Martyn ;
Valente, Anabela A. .
JOURNAL OF CATALYSIS, 2006, 244 (02) :230-237
[6]   Liquid-phase dehydration of D-xylose over microporous and mesoporous niobium silicates [J].
Dias, AS ;
Lima, S ;
Brandao, P ;
Pillinger, M ;
Rocha, J ;
Valente, AA .
CATALYSIS LETTERS, 2006, 108 (3-4) :179-186
[7]   Liquid phase dehydration Of D-xylose in the presence of Keggin-type heteropolyacids [J].
Dias, AS ;
Pillinger, M ;
Valente, AA .
APPLIED CATALYSIS A-GENERAL, 2005, 285 (1-2) :126-131
[8]   Dehydration of xylose into furfural over micro-mesoporous sulfonic acid catalysts [J].
Dias, AS ;
Pillinger, M ;
Valente, AA .
JOURNAL OF CATALYSIS, 2005, 229 (02) :414-423
[9]   Kinetics of non-catalyzed decomposition of D-xylose in high temperature liquid water [J].
Jing Qi ;
Lue Xiuyang .
CHINESE JOURNAL OF CHEMICAL ENGINEERING, 2007, 15 (05) :666-669
[10]  
Kim YC, 2001, J IND ENG CHEM, V7, P424