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Article

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

by
Ryan Oozeerally
1,
Shivendra D. K. Ramkhelawan
1,2,
David L. Burnett
3,
Christiaan H. L. Tempelman
2 and
Volkan Degirmenci
1,*
1
School of Engineering, University of Warwick, Coventry CV4 7AL, UK
2
Department of Chemical Engineering, Rotterdam University of Applied Sciences, Rotterdam Mainport Institute, Rotterdam 3024 EA, The Netherlands
3
School of Metallurgy and Materials, University of Birmingham, Birmingham B15 2TT, UK
*
Author to whom correspondence should be addressed.
Catalysts 2019, 9(10), 812; https://doi.org/10.3390/catal9100812
Submission received: 3 September 2019 / Revised: 17 September 2019 / Accepted: 24 September 2019 / Published: 27 September 2019

Abstract

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 °C. Of these, the hydrothermal synthesis method yields a material with exceptionally high surface area (1967 m2·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 °C in aqueous reaction medium. However, this selectivity dropped dramatically when the reactions were repeated at higher temperatures (~140 °C). Interestingly, greater quantities of mannose were produced at higher temperatures too. The lack of strong Brønsted 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 °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 °C in ~3 h, which implies that the catalyst’s stability was not maintained in the long run.
Keywords: metal organic framework; zeolitic imidazolate framework; HMF; biomass; catalysis; glucose metal organic framework; zeolitic imidazolate framework; HMF; biomass; catalysis; glucose
Graphical Abstract

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MDPI and ACS Style

Oozeerally, R.; Ramkhelawan, S.D.K.; Burnett, D.L.; Tempelman, C.H.L.; Degirmenci, V. ZIF-8 Metal Organic Framework for the Conversion of Glucose to Fructose and 5-Hydroxymethyl Furfural. Catalysts 2019, 9, 812. https://doi.org/10.3390/catal9100812

AMA Style

Oozeerally R, Ramkhelawan SDK, Burnett DL, Tempelman CHL, Degirmenci V. ZIF-8 Metal Organic Framework for the Conversion of Glucose to Fructose and 5-Hydroxymethyl Furfural. Catalysts. 2019; 9(10):812. https://doi.org/10.3390/catal9100812

Chicago/Turabian Style

Oozeerally, Ryan, Shivendra D. K. Ramkhelawan, David L. Burnett, Christiaan H. L. Tempelman, and Volkan Degirmenci. 2019. "ZIF-8 Metal Organic Framework for the Conversion of Glucose to Fructose and 5-Hydroxymethyl Furfural" Catalysts 9, no. 10: 812. https://doi.org/10.3390/catal9100812

APA Style

Oozeerally, R., Ramkhelawan, S. D. K., Burnett, D. L., Tempelman, C. H. L., & Degirmenci, V. (2019). ZIF-8 Metal Organic Framework for the Conversion of Glucose to Fructose and 5-Hydroxymethyl Furfural. Catalysts, 9(10), 812. https://doi.org/10.3390/catal9100812

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