Fast and continuous conversion of xylose to furfural in micropacked bed reactors

被引:21
作者
Lu, Heng-Xing [1 ]
Yang, Wei-Yao [1 ]
Shi, Ying-Xian [1 ]
Wang, Hong -Bin [1 ]
Mao, Heng [1 ]
Sang, Le [1 ]
Zhao, Zhi-Ping [1 ]
机构
[1] Beijing Inst Technol, Sch Chem & Chem Engn, Beijing 102488, Peoples R China
基金
中国国家自然科学基金;
关键词
Xylose dehydration; Micropacked bed reactor; Mixed solid acid; Water; Biomass; CARBON SOLID ACID; DEHYDRATION; CATALYST; BIOMASS; PERFORMANCE; EXTRACTION; PLATFORM; XYLAN; FUEL;
D O I
10.1016/j.ces.2022.118256
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
In this work, the continuous conversion of xylose to furfural in water aqueous based on micropacked bed reactors (lPBRs) with mixed solid acid catalyst of SO24/g-Al2O3 and HND-580 was studied. For liquidsolid process, the best conversion and yield were 96.86% and 44.65% with the reaction time of only 1.6 min at 170 degrees C and 2 MPa, respectively. The reaction rate constant, apparent activation energy, and space-time yield (STY) were 1.37 min(-1), 47.41 kJ.mol(-1), and 5.00 x 10(-3) g.mL(-3).min(-1), respectively. Also, the CO2 can enhance the conversion of xylose to furfural in mPBRs to achieve a high selectively and yield. Compared with the batch operation, the mPBRs can greatly increase the reaction rate and STY of 1-3 order magnitude. Micropacked bed reactor could be an alternative of the batch reactor to achieve a high efficient, green, continuous, and safe dehydration process of biomass. (C) 2022 Elsevier Ltd. All rights reserved.
引用
收藏
页数:11
相关论文
共 54 条
[21]   Site-Dependent Lewis Acidity of γ-Al2O3 and Its Impact on Ethanol Dehydration and Etherification [J].
Jenness, Glen R. ;
Christiansen, Matthew A. ;
Caratzoulas, Stavros ;
Vlachos, Dionisios G. ;
Gorte, Raymond J. .
JOURNAL OF PHYSICAL CHEMISTRY C, 2014, 118 (24) :12899-12907
[22]   Fabrication of sulfonic acid modified mesoporous silica shells and their catalytic performance with dehydration reaction of D-xylose into furfural [J].
Jeong, Gyoung Hwa ;
Kim, Eun Gyu ;
Kim, Saet Byul ;
Park, Eun Duck ;
Kim, Sang Wook .
MICROPOROUS AND MESOPOROUS MATERIALS, 2011, 144 (1-3) :134-139
[23]   Conversion of xylose into furfural in a MOF-based mixed matrix membrane reactor [J].
Jin, Hua ;
Liu, Xinlei ;
Ban, Yujie ;
Peng, Yuan ;
Jiao, Wenmei ;
Wang, Po ;
Guo, Ang ;
Li, Yanshuo ;
Yang, Weishen .
CHEMICAL ENGINEERING JOURNAL, 2016, 305 :12-18
[24]   Kinetic study of the dehydration of D-xylose in high temperature water [J].
Kim, Saet Byul ;
Lee, Mi Ran ;
Park, Eun Duck ;
Lee, Sang Min ;
Lee, HyoKyu ;
Park, Ki Hyun ;
Park, Myung-June .
REACTION KINETICS MECHANISMS AND CATALYSIS, 2011, 103 (02) :267-277
[25]   A modified biphasic system for the dehydration of D-xylose into furfural using SO42-/TiO2-ZrO2/La3+ as a solid catalyst [J].
Li, Huiling ;
Deng, Aojie ;
Ren, Junli ;
Liu, Changyu ;
Wang, Wenju ;
Peng, Feng ;
Sun, Runcang .
CATALYSIS TODAY, 2014, 234 :251-256
[26]   Catalytic dehydration of D-xylose to furfural over a tantalum-based catalyst in batch and continuous process [J].
Li, Xing-Long ;
Pan, Tao ;
Deng, Jin ;
Fu, Yao ;
Xu, Hua-Jian .
RSC ADVANCES, 2015, 5 (86) :70139-70146
[27]   Dehydration of Xylose into Furfural in the Presence of Crystalline Microporous Silicoaluminophosphates [J].
Lima, Sergio ;
Fernandes, Auguste ;
Antunes, Margarida M. ;
Pillinger, Martyn ;
Ribeiro, Filipa ;
Valente, Anabela A. .
CATALYSIS LETTERS, 2010, 135 (1-2) :41-47
[28]   Solvent effect on xylose conversion under catalyst-free conditions: insights from molecular dynamics simulation and experiments [J].
Lin, Qixuan ;
Liao, Shouwei ;
Li, Libo ;
Li, Weiying ;
Yue, Fengxia ;
Peng, Feng ;
Ren, Junli .
GREEN CHEMISTRY, 2020, 22 (02) :532-539
[29]   Furfural production from biomass pretreatment hydrolysate using vapor-releasing reactor system [J].
Liu, Lu ;
Chang, Hou-min ;
Jameel, Hasan ;
Park, Sunkyu .
BIORESOURCE TECHNOLOGY, 2018, 252 :165-171
[30]   Enhancing the conversion of D-xylose into furfural at low temperatures using chloride salts as co-catalysts: Catalytic combination of AlCl3 and formic acid [J].
Lopes, M. ;
Dussan, K. ;
Leahy, J. J. .
CHEMICAL ENGINEERING JOURNAL, 2017, 323 :278-286