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      Electrocatalytic oxidation of 5-hydroxymethylfurfural to 2,5-furandicarboxylic acid on supported Au and Pd bimetallic nanoparticles

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          Abstract

          Electrocatalytic oxidation of HMF to FDCA was achieved on Pd/C, Au/C and Pd–Au/C catalysts and the synergistic effect of Pd–Au alloying is clearly demonstrated with electrochemical methods.

          Abstract

          This work explores the potential-dependent electrocatalytic oxidation of 5-hydroxymethylfurfural (HMF) in alkaline media over supported Au and Pd nanoparticles and demonstrates the synergistic effects of bimetallic Pd–Au catalysts for the selective formation of 2,5-furandicarboxylic acid (FDCA). Results from electrolysis product analysis at various electrode potentials, along with cyclic voltammetry of HMF and its oxidation intermediates, revealed the unique catalytic properties of Pd and Au for competitive oxidation of alcohol and aldehyde side-groups present in HMF. Aldehyde oxidation was greatly favored over alcohol oxidation on the Au/C catalyst, which was very active for HMF oxidation to 5-hydroxymethyl-2-furancarboxylic acid (HFCA), however high electrode potentials were required for further oxidation of the alcohol group to FDCA. HMF oxidation on Pd/C followed two competitive routes to FDCA and the pathway was dependent on the electrode potential. Oxidation of aldehyde groups occurred much slower on Pd/C than on Au/C at low potentials, but was greatly enhanced at increased potentials or by alloying with Au. It was found that Pd–Au bimetallic catalysts achieved deeply oxidized products (FFCA and FDCA) at lower potentials than monometallic catalysts and the product distribution was dependent on the electrode potential and surface alloy composition. Bimetallic catalysts with 2 : 1 and 1 : 2 Pd–Au molar ratios (Pd 2Au 1/C and Pd 1Au 2/C) exhibited advantages of both single components with facile alcohol and aldehyde group oxidation, resulting in greatly improved HMF conversion rate and selectivity to fully oxidized FDCA.

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          Technology development for the production of biobased products from biorefinery carbohydrates—the US Department of Energy’s “Top 10” revisited

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            Liquid-Phase Catalytic Processing of Biomass-Derived Oxygenated Hydrocarbons to Fuels and Chemicals

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              Phase modifiers promote efficient production of hydroxymethylfurfural from fructose.

              Furan derivatives obtained from renewable biomass resources have the potential to serve as substitutes for the petroleum-based building blocks that are currently used in the production of plastics and fine chemicals. We developed a process for the selective dehydration of fructose to 5-hydroxymethylfurfural (HMF) that operates at high fructose concentrations (10 to 50 weight %), achieves high yields (80% HMF selectivity at 90% fructose conversion), and delivers HMF in a separation-friendly solvent. In a two-phase reactor system, fructose is dehydrated in the aqueous phase with the use of an acid catalyst (hydrochloric acid or an acidic ion-exchange resin) with dimethylsulfoxide and/or poly(1-vinyl-2-pyrrolidinone) added to suppress undesired side reactions. The HMF product is continuously extracted into an organic phase (methylisobutylketone) modified with 2-butanol to enhance partitioning from the reactive aqueous solution.
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                Author and article information

                Journal
                GRCHFJ
                Green Chem.
                Green Chem.
                Royal Society of Chemistry (RSC)
                1463-9262
                1463-9270
                2014
                2014
                : 16
                : 8
                : 3778-3786
                Affiliations
                [1 ]Chemical Engineering Department
                [2 ]Michigan Technological University
                [3 ]Houghton, USA
                [4 ]Materials Science and Technology Division
                [5 ]Oak Ridge National Laboratory
                [6 ]Oak Ridge, USA
                Article
                10.1039/C4GC00401A
                22b691f7-69b2-417a-b058-8d779da904b0
                © 2014
                History

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