The patent badge is an abbreviated version of the USPTO patent document. The patent badge does contain a link to the full patent document.

The patent badge is an abbreviated version of the USPTO patent document. The patent badge covers the following: Patent number, Date patent was issued, Date patent was filed, Title of the patent, Applicant, Inventor, Assignee, Attorney firm, Primary examiner, Assistant examiner, CPCs, and Abstract. The patent badge does contain a link to the full patent document (in Adobe Acrobat format, aka pdf). To download or print any patent click here.

Date of Patent:
Jun. 07, 2022

Filed:

Jun. 29, 2017
Applicant:

The University of Western Ontario, London, CA;

Inventors:

Chunbao Xu, London, CA;

Sadra Souzanchi, London, CA;

Tirumala Venkateswara Rao Kasanneni, London, CA;

Zhongshun Yuan, London, CA;

Assignee:
Attorney:
Primary Examiner:
Int. Cl.
CPC ...
C07D 307/50 (2006.01); B01J 8/00 (2006.01); B01J 8/06 (2006.01); B01J 23/20 (2006.01); B01J 27/18 (2006.01); B01J 27/195 (2006.01); B01J 31/10 (2006.01);
U.S. Cl.
CPC ...
C07D 307/50 (2013.01); B01J 8/001 (2013.01); B01J 8/065 (2013.01); B01J 8/067 (2013.01); B01J 23/20 (2013.01); B01J 27/1813 (2013.01); B01J 27/195 (2013.01); B01J 31/10 (2013.01); B01J 2208/00212 (2013.01); B01J 2208/00539 (2013.01); B01J 2231/763 (2013.01); B01J 2531/002 (2013.01);
Abstract

Disclosed is a cost-effective process for catalytic conversion of simple C-based sugars (such as glucose and fructose) and industrial-grade sugar syrups derived from starch (such as different grades of High Fructose Corn Syrup) and cellulosic biomass to 5-HydroxyMethylFurfural (5-HMF) in a continuous-flow tubular reactor in bi-phasic media using inexpensive heterogeneous solid catalysts. Commercial and synthesized heterogeneous solid catalysts were used and their activities in terms of sugar conversion and HMF selectivity and yield were compared. Continuous dehydration of fructose, glucose and industrial-grade sugar syrups derived from corn and wood to HMF was achieved and the stability of selected catalysts and feasibility of catalyst recycling and regeneration were demonstrated. The performance of the catalysts and reactor system were examined under different operating conditions including reaction temperature, feeding flow rate, initial feedstock concentration, catalyst loading, presence of extracting organic solvent and phase transfer catalyst and aqueous to organic phase ratio. At the best operating conditions, HMF yield attained 60%, 45% and 53%, from dehydration of fructose, glucose and HFCS-90, respectively.


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