Intensifying Cyclopentanone Synthesis from Furfural Using Supported Copper Catalysts

This work addresses catalytic strategies to intensify the synthesis of cyclopentanone, a bio-based platform chemical and a potential SAF precursor, via Cu-catalyzed furfural hydrogenation in aqueous media. When performed in a single step, using either uniform or staged catalytic bed configuration, high temperature and hydrogen pressures (180 °C and 38 bar) are necessary for maximum CPO yields (37 and 49 %, respectively). Parallel furanic ring hydrogenation of furfural and polymerisation of intermediates, namely furfuryl alcohol (FFA), limit CPO yields. Employing a two step configuration with optimal catalyst bed can curb this limitation. First, the furanic ring hydrogenation can be suppressed by using milder conditions (i. e., 150 °C and 7 bar, and 14 seconds of residence time). Second, FFA hydrogenation using tandem catalysis, i. e., a mix of β-zeolite and Cu/ZrO<sub>2</sub>, at 180 °C, 38 bar and 0.6, allows sufficient time for CPO formation and minimises polymerisation of FFA, thereby resulting in 60 % CPO yield. Therefore, this work recommends a split strategy to produce CPO from furfural. Such modularity may aid in addressing flexible market needs.

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Publication Details

Journal
ChemSusChem
Published
2024-09-28
DOI
https://doi.org/10.1002/cssc.202401484
Citations
10
Primary Topic
Catalysis for Biomass Conversion
Type
article
Field-Weighted Citation Impact
1.84

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article

Intensifying Cyclopentanone Synthesis from Furfural Using Supported Copper Catalysts

Adarsh Patil, Maurik J.S. Engelbert van Bevervoorde, Fernanda Neira D’Angelo
10 citations
ChemSusChem
Catalysis for Biomass Conversion
1.84
article

Intensifying Cyclopentanone Synthesis from Furfural Using Supported Copper Catalysts

Adarsh Patil, Maurik J.S. Engelbert van Bevervoorde, Fernanda Neira D’Angelo
article en
10 citations

Abstract

This work addresses catalytic strategies to intensify the synthesis of cyclopentanone, a bio-based platform chemical and a potential SAF precursor, via Cu-catalyzed furfural hydrogenation in aqueous media. When performed in a single step, using either uniform or staged catalytic bed configuration, high temperature and hydrogen pressures (180 °C and 38 bar) are necessary for maximum CPO yields (37 and 49 %, respectively). Parallel furanic ring hydrogenation of furfural and polymerisation of intermediates, namely furfuryl alcohol (FFA), limit CPO yields. Employing a two step configuration with optimal catalyst bed can curb this limitation. First, the furanic ring hydrogenation can be suppressed by using milder conditions (i. e., 150 °C and 7 bar, and 14 seconds of residence time). Second, FFA hydrogenation using tandem catalysis, i. e., a mix of β-zeolite and Cu/ZrO<sub>2</sub>, at 180 °C, 38 bar and 0.6, allows sufficient time for CPO formation and minimises polymerisation of FFA, thereby resulting in 60 % CPO yield. Therefore, this work recommends a split strategy to produce CPO from furfural. Such modularity may aid in addressing flexible market needs.

ChemSusChemVol. 18(4)
Eindhoven University of Technology (NL)
European Commission
Openalex Percentile: Top 15%
Catalysis for Biomass Conversion
1.84
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