
pmid: 24664518
AbstractThis study demonstrates that an electrochemical dehydrogenation process can be used to oxidize glycerol to glyceraldehyde and glyceric acid even without using stoichiometric chemical oxidants. A glyceric acid selectivity of 87.0 % at 91.8 % glycerol conversion was obtained in an electrocatalytic batch reactor. A continuous‐flow electrocatalytic reactor had over an 80 % high glyceric acid selectivity at 10 % glycerol conversion, as well as greater reaction rates than either an electrocatalytic or a conventional catalytic batch reactor.
Glycerol, energy conversion, MEMBRANE REACTOR, FUEL-CELLS, Catalysis, BIOMASS, Electrochemistry, PLATINUM-BISMUTH CATALYST, ALDEHYDES, Temperature, METAL-CATALYSTS, ALCOHOLS, Hydrogen-Ion Concentration, biofuels, PRODUCTS, CONVERSION, BIMETALLIC CATALYSTS, heterogeneous catalysis, electrochemistry, oxidation reaction, Hydrogenation, Oxidation-Reduction
Glycerol, energy conversion, MEMBRANE REACTOR, FUEL-CELLS, Catalysis, BIOMASS, Electrochemistry, PLATINUM-BISMUTH CATALYST, ALDEHYDES, Temperature, METAL-CATALYSTS, ALCOHOLS, Hydrogen-Ion Concentration, biofuels, PRODUCTS, CONVERSION, BIMETALLIC CATALYSTS, heterogeneous catalysis, electrochemistry, oxidation reaction, Hydrogenation, Oxidation-Reduction
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