Construction of Ni−Re Supported on Hydrotalcite‐Derived MgAl Catalysts for Promoting the Ring Hydrogenation of Furfural into Tetrahydrofurfuryl Alcohol in Water

Author:

Kittisabhorn Aurucha1,Ahmed Imtiaz1,Ratchahat Sakhon1,Chaiwat Weerawut1,Koo‐amornpattana Wanida1,Klysubun Wantana2,Poo‐arporn Yingyot2,Limphirat Wanwisa2,Khemthong Pongtanawat3,Assabumrungrat Suttichai45,Srifa Atthapon1ORCID

Affiliation:

1. Department of Chemical Engineering Faculty of Engineering Mahidol University Nakhon Pathom 73170 Thailand

2. Synchrotron Light Research Institute Nakhon Ratchasima 30000 Thailand

3. National Nanotechnology Center (NANOTEC) National Science and Technology Development Agency (NSTDA) Pathum Thani 12120 Thailand

4. Center of Excellence in Catalysis and Catalytic Reaction Engineering Department of Chemical Engineering, Faculty of Engineering Chulalongkorn University Bangkok 10330 Thailand

5. Bio-Circular-Green-economy Technology & Engineering Center (BCGeTEC) Department of Chemical Engineering Faculty of Engineering Chulalongkorn University Bangkok 10330 Thailand

Abstract

AbstractBiomass‐derived feedstocks play a vital role in sustainable economies for renewable energy, waste management, energy security, and commercial prospects. This study focused on promoting the ring hydrogenation of furfural (FAL) into tetrahydrofurfuryl alcohol (THFA) in an aqueous solution using a potential Ni−Re‐supported hydrotalcite‐derived MgAl catalyst at different Ni : Re molar ratios. Structural analyses, such as an in situ time‐resolved X‐ray absorption near edge structure, under H2 reduction elucidated the simultaneous transformation of Re6+ and Re7+ to Re0 with the remaining highly stable Ni2+. The construction of Ni−Re on hydrotalcite‐derived MgAl catalyst resulted in the alleviated H2 reduction behavior, facilitated H2 adsorption and desorption processes, and suitable catalyst acidity detected by H2 temperature‐programmed reduction, and H2 and NH3 temperature‐programmed desorption experiments, respectively. Under optimized conditions, a maximum THFA yield of 78 % with a complete FAL conversion was attained using Ni1Re0.16/MgO−Al2O3 catalyst at a reaction temperature of 140 °C, H2 pressure of 20 bar, catalyst loading of 20 %, and reaction time of 2 h in a H2O system. Isotopic deuterium (D2O) labeling revealed that D substitution was notably pronounced through isotopic exchange between the D atom from D2O and H atom in FAL during its hydrogenation to THFA.

Funder

Mahidol University

Publisher

Wiley

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