4.7 Article

Direct solvent-free selective hydrogenation of levulinic acid to valeric acid over multi-metal [NixCoyMnzAlw]-doped mesoporous silica catalysts

Journal

CHEMICAL ENGINEERING JOURNAL
Volume 472, Issue -, Pages -

Publisher

ELSEVIER SCIENCE SA
DOI: 10.1016/j.cej.2023.144591

Keywords

Levulinic acid; Valeric acid; One-pot; Solvent-free; Hydrogenation; Heterogeneous catalyst

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This study developed an efficient direct solvent-free selective hydrogenation reaction of bio-levulinic acid (LA) to valeric acid (VA) using NixCoyMnzAlw-doped mesoporous silica (NMCAS) catalysts. The catalysts exhibited high conversion of LA and high yield of VA, with Mn and Al dopants improving the selectivity towards VA. The research provides an important example of direct solvent-free, selective, and high-yield production of VA over non-noble heterogeneous catalysts.
Valeric acid (VA) and valeric esters (VEs) are among the essential platform chemicals derived from bio-levulinic acid (LA). However, synthesizing VA from LA is still challenging due to solvent consumption, precious metals utilization, and catalyst deactivation. Thus, this study developed an efficient direct solvent-free selective hydrogenation reaction of LA to VA using non-noble metal-based catalysts. NixCoyMnzAlw-doped mesoporous silica (NMCAS) catalysts were synthesized using a facile one-pot procedure, with 100% LA conversion and 96.3% VA yield obtained at 200 degrees C and 3 MPa (H2) over the NMCAS catalyst. Ni-based catalysts provided 100% LA conversion, whereas the Mn-Co-based catalyst exhibited a 79.8% LA conversion. The increase in the selectivity for VA observed with the doping of Mn and Al into the catalysts can be explained by the generation of Bronsted and Lewis acid sites, which facilitated the ring-opening of GVL to form VA. The effects of reaction time, temperature, pressure, and solvent were considered. At elevated temperatures and pressures, the formation of 1,4-PDO, resulting from the C-O bond breakage of O-C-O in the GVL ring-opening and the subsequent dehydrationcyclization to 2-methyltetrahydrofuran (MTHF), including the over-hydrogenation of VA to pentanol, was detected. An increase in the partial pressure of hydrogen enhanced the hydrogenation activity, thus producing 2MTHF and pentanols. The NMCAS catalyst has also been applied with various solvents to study the reaction pathway and produce VEs. This work is the primary example of the direct solvent-free, selective, and high-yield production of VA from LA over non-noble heterogeneous catalysts.

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