4.7 Article

Modeling Competing Kinetics between Electrochemical Reduction of Furfural on and Side Reactions in Acid

期刊

ENERGY & FUELS
卷 36, 期 18, 页码 11001-11011

出版社

AMER CHEMICAL SOC
DOI: 10.1021/acs.energyfuels.2c01955

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  1. U.S. Department of Energy, Office of Science, Office of Basic Energy Sciences, Catalysis Science program [DE-SC0019134]
  2. U.S. Department of Energy (DOE) [DE-SC0019134] Funding Source: U.S. Department of Energy (DOE)

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This study investigated the electrochemical reactions for the hydrogenation and hydrogenolysis of biomass-derived species over Cu foil catalysts. The results showed that the evaporation of MF and side reactions competed in affecting the product quality balance, with nitrogen sparging promoting MF evaporation and improving the yields of furfuryl alcohol and 2-methylfuran.
The understanding of electrochemical reactions for the hydrogenation and hydrogenolysis (ECH) of biomass derived species is important to design and adapt electrochemical reactors to generate desired chemicals sustainably at high yield. In this work, the ECH of furfural (FF) over Cu foil catalysts to furfuryl alcohol (FA) and 2-methylfuran (MF) was studied in a two-compartment semibatch reactor in acidic electrolytes (0.1 and 0.5 M H2SO4) with nitrogen sparging. We found that FA and MF underwent side reactions that follow first order kinetics with respect to the FA and MF concentrations in 0.1 M H(2)SO(4 )and 0.5 M H2SO4. MF evaporation from the catholyte in the presence of nitrogen sparging followed a first order dependence with the concentration of MF in the catholyte. Our previous work showed the ECH of FF over Cu followed noncompetitive Langmuir-Hinshelwood models. A kinetic model was developed to consider the electrochemical reactions, nonelectrochemical side reactions, and the evaporation of MF to investigate the competition between these three contributions to the mass balances. Insights were provided by using the model to consider two hypothetical cases where 1) evaporation of MF did not occur, and 2) side reactions did not occur, and a third realistic case where evaporation of MF and side reactions occurred. The model showed that without gas sparging promoting MF evaporation, 81.5% of products were undesirable at 98.5% FF conversion in 0.5 M H2SO4, and 30.6% of products were undesirable in 0.1 M H2SO4. N-2 sparging in the catholyte lowered the concentration of MF in the catholyte with a corresponding increase to the concentration in the solvent trap, where side reactions did not occur, allowing for increased MF yields. We showed that despite the faster side reactions to MF in 0.5 M H(2)SO(4 )compared to 0.1 M H2SO4, a higher yield to MF was reached in 0.5 M H(2)SO(4 )than in 0.1 M H(2)SO(4 )due to the beneficial impact of nitrogen sparging and the higher electrochemical production rate of MF.

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