One-Pot Synthesisof Valeric Biofuels via Esterification–Hydrogenolysis

The production of valerate esters, a class of transportation biofuels (additives), usually undergoes alternate hydrogenation and acid-catalysis dehydration processes that suffer from inevitable coke deposition and undesirable side reactions. We report a one-pot esterification–hydrogenolysis reaction pathway for valeric biofuels synthesis from biomass-derived 2-furoic acid, which was proceeded over the elaborate CoPt<sub><i>X</i></sub>@Co<sub>3</sub>O<sub>4</sub>-NC (<i>X</i> = 0.01, 0.02, 0.05, and 0.1) catalysts. The catalysts were constructed through a MOF-engaged etching-pyrolysis-replacement strategy to obtain mesoporous pocket cube nanoboxes-in-nanobox morphology and uniform CoPt<sub><i>X</i></sub>@Co<sub>3</sub>O<sub>4</sub> core–shell nanoparticles with Pt moieties in tunable content and size (from single-atom scale to 2.4 nm). The obtained acid-free CoPt<sub><i>X</i></sub>@Co<sub>3</sub>O<sub>4</sub>-NC catalyst achieved an average 92.2% yield of ethyl valerate at a complete conversion of 2-furoic acid, and the reaction ran steadily in a microchannel continuous flow reactor for at least 200 h, which also inhibited the byproduct generation and coke deposition. A mechanistic study suggested that 2-furoic acid was preferably adsorbed on the oxyphilic Co<sub>3</sub>O<sub>4</sub> shell for esterification initially; then the generated esters underwent sequential and exclusive hydrogenolysis steps over the CoPt core to yield valerate esters. The high industrial application prospect of this reaction pathway was additionally highlighted by producing 12 kinds of valeric biofuels from 2-furoic acid and the corresponding C<sub>1</sub> ∼ C<sub>7</sub> primary, secondary, and tertiary alcohols.

Publication Details

Journal
Figshare
Published
2025-02-27
DOI
https://doi.org/10.1021/acscatal.5c00636.s001
Primary Topic
Catalysis for Biomass Conversion
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article
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article

One-Pot Synthesisof Valeric Biofuels via Esterification–Hydrogenolysis

Figshare
Catalysis for Biomass Conversion
article

One-Pot Synthesisof Valeric Biofuels via Esterification–Hydrogenolysis

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Abstract

The production of valerate esters, a class of transportation biofuels (additives), usually undergoes alternate hydrogenation and acid-catalysis dehydration processes that suffer from inevitable coke deposition and undesirable side reactions. We report a one-pot esterification–hydrogenolysis reaction pathway for valeric biofuels synthesis from biomass-derived 2-furoic acid, which was proceeded over the elaborate CoPt<sub><i>X</i></sub>@Co<sub>3</sub>O<sub>4</sub>-NC (<i>X</i> = 0.01, 0.02, 0.05, and 0.1) catalysts. The catalysts were constructed through a MOF-engaged etching-pyrolysis-replacement strategy to obtain mesoporous pocket cube nanoboxes-in-nanobox morphology and uniform CoPt<sub><i>X</i></sub>@Co<sub>3</sub>O<sub>4</sub> core–shell nanoparticles with Pt moieties in tunable content and size (from single-atom scale to 2.4 nm). The obtained acid-free CoPt<sub><i>X</i></sub>@Co<sub>3</sub>O<sub>4</sub>-NC catalyst achieved an average 92.2% yield of ethyl valerate at a complete conversion of 2-furoic acid, and the reaction ran steadily in a microchannel continuous flow reactor for at least 200 h, which also inhibited the byproduct generation and coke deposition. A mechanistic study suggested that 2-furoic acid was preferably adsorbed on the oxyphilic Co<sub>3</sub>O<sub>4</sub> shell for esterification initially; then the generated esters underwent sequential and exclusive hydrogenolysis steps over the CoPt core to yield valerate esters. The high industrial application prospect of this reaction pathway was additionally highlighted by producing 12 kinds of valeric biofuels from 2-furoic acid and the corresponding C<sub>1</sub> ∼ C<sub>7</sub> primary, secondary, and tertiary alcohols.

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Catalysis for Biomass Conversion
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