ZIF-8 Metal Organic Framework for the Conversion of Glucose to Fructose and 5-Hydroxymethyl Furfural

被引:39
|
作者
Oozeerally, Ryan [1 ]
Ramkhelawan, Shivendra D. K. [1 ,2 ]
Burnett, David L. [3 ]
Tempelman, Christiaan H. L. [2 ]
Degirmenci, Volkan [1 ]
机构
[1] Univ Warwick, Sch Engn, Coventry CV4 7AL, W Midlands, England
[2] Rotterdam Univ Appl Sci, Rotterdam Mainport Inst, Dept Chem Engn, NL-3024 EA Rotterdam, Netherlands
[3] Univ Birmingham, Sch Met & Mat, Birmingham B15 2TT, W Midlands, England
基金
英国工程与自然科学研究理事会;
关键词
metal organic framework; zeolitic imidazolate framework; HMF; biomass; catalysis; glucose; ZEOLITIC IMIDAZOLATE FRAMEWORK-8; CARBON-DIOXIDE CAPTURE; LIGNOCELLULOSIC BIOMASS; HETEROGENEOUS CATALYST; HIGH-PRESSURE; SN-BETA; ACID; ISOMERIZATION; DEHYDRATION; ACTIVATION;
D O I
10.3390/catal9100812
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
Herein, Zeolitic imidazolate framework-8 (ZIF-8) is considered as an easy and cheap to prepare alternative catalyst for the isomerization of glucose and production of 5-hydroxymethyl furfural (HMF). For the synthesis of the ZIF-8 catalysts two preparation methods were evaluated, being room temperature and hydrothermal synthesis at 140 degrees C. Of these, the hydrothermal synthesis method yields a material with exceptionally high surface area (1967 m(2).g(-1)). As a catalyst, the ZIF-8 materials generated excellent fructose yields. Specifically, ZIF-8 prepared by hydrothermal synthesis yielded a fructose selectivity of 65% with a glucose conversion of 24% at 100 degrees C in aqueous reaction medium. However, this selectivity dropped dramatically when the reactions were repeated at higher temperatures (similar to 140 degrees C). Interestingly, greater quantities of mannose were produced at higher temperatures too. The lack of strong BrOnsted acidity in both ZIF-8 materials resulted in poor HMF yields. In order to improve HMF yields, reactions were performed at a lower pH of 1.0. At 140 degrees C the lower pH was found to drive the reaction towards HMF and double its yield. Despite the excellent performance of ZIF-8 catalysts in batch reactions, their activity did not translate well to the flow reactor over a continuous run of 8 h, which was operating with a residence time of 6 min. The activity of ZIF-8 halved in the flow reactor at 100 degrees C in similar to 3 h, which implies that the catalyst's stability was not maintained in the long run.
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页数:14
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