It appears you don't have support to open PDFs in this web browser. To view this file, Open with your PDF reader
Abstract
In aqueous mediums, the chemical environment for catalytic reactions is not only comprised of water molecules but also of corresponding ionized species, i.e., hydronium ions, which can impact the mechanism and kinetics of a reaction. Here we show that in aqueous-phase hydrogenation of furfural on Pd/C, increasing the hydronium ion activities by five orders of magnitude (from pH 7 to pH 1.6) leads to an increase of less than one order of magnitude in the reaction rate. Instead of a proton-coupled electron transfer pathway, our results show that a Langmuir-Hinshelwood mechanism describes the rate-limiting hydrogen addition step, where hydrogen atom adsorbed on Pd is transferred to the carbonyl C atom of the reactant. As such, the strength of hydrogen binding on Pd, which decreases with increasing hydronium ion concentration (i.e., 2 kJ molH2−1 per unit pH), is a decisive factor in hydrogenation kinetics (rate constant +270%). In comparison, furfural adsorption on Pd is pH-independent, maintaining a tilted geometry that favors hydrogen attack at the carbonyl group over the furan ring.
Hydrogen binding and furfural adsorption are critical steps in Pd-catalyzed furfural hydrogenation reactions in aqueous phases. Here, the authors explore how hydronium ion at different pH values modifies the rate constant for this reaction.
You have requested "on-the-fly" machine translation of selected content from our databases. This functionality is provided solely for your convenience and is in no way intended to replace human translation. Show full disclaimer
Neither ProQuest nor its licensors make any representations or warranties with respect to the translations. The translations are automatically generated "AS IS" and "AS AVAILABLE" and are not retained in our systems. PROQUEST AND ITS LICENSORS SPECIFICALLY DISCLAIM ANY AND ALL EXPRESS OR IMPLIED WARRANTIES, INCLUDING WITHOUT LIMITATION, ANY WARRANTIES FOR AVAILABILITY, ACCURACY, TIMELINESS, COMPLETENESS, NON-INFRINGMENT, MERCHANTABILITY OR FITNESS FOR A PARTICULAR PURPOSE. Your use of the translations is subject to all use restrictions contained in your Electronic Products License Agreement and by using the translation functionality you agree to forgo any and all claims against ProQuest or its licensors for your use of the translation functionality and any output derived there from. Hide full disclaimer
Details



1 Technische Universität München, Department of Chemistry and Catalysis Research Center, Garching, Germany (GRID:grid.6936.a) (ISNI:0000000123222966); The Hong Kong Polytechnic University, Hung Hom, Kowloon, Research Institute for Future Food and Department of Applied Biology and Chemical Technology, Hong Kong, China (GRID:grid.16890.36) (ISNI:0000 0004 1764 6123)
2 Technische Universität München, Department of Chemistry and Catalysis Research Center, Garching, Germany (GRID:grid.6936.a) (ISNI:0000000123222966)
3 Technische Universität München, Department of Chemistry and Catalysis Research Center, Garching, Germany (GRID:grid.6936.a) (ISNI:0000000123222966); Shandong University, Key Laboratory for Liquid–Solid Structural Evolution and Processing of Materials (Ministry of Education), School of Materials Science and Engineering, Jinan, China (GRID:grid.27255.37) (ISNI:0000 0004 1761 1174)
4 Technische Universität München, Department of Chemistry and Catalysis Research Center, Garching, Germany (GRID:grid.6936.a) (ISNI:0000000123222966); East China Normal University, Shanghai Key Laboratory of Green Chemistry and Chemical Processes, School of Chemistry and Molecular Engineering, Shanghai, China (GRID:grid.22069.3f) (ISNI:0000 0004 0369 6365)
5 Technische Universität München, Department of Chemistry and Catalysis Research Center, Garching, Germany (GRID:grid.6936.a) (ISNI:0000000123222966); Pacific Northwest National Laboratory, Institute for Integrated Catalysis, Richland, USA (GRID:grid.451303.0) (ISNI:0000 0001 2218 3491)