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1998
DOI: 10.1016/s0013-4686(97)00131-x
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Electrocatalytic hydrogenation of phenol on dispersed Pt: reaction mechanism and support effect

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Cited by 27 publications
(36 citation statements)
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“…In Table 1, entry 13, an increase of the electrochemical efficiency was observed (97%), when MeOH was the co-solvent, and no difference was observed in the presence of tBuOH (Table 1, entry 14), showing that the inert gas effect to expel molecular oxygen is more efficient in water + MeOH solvent, which could be explained by oxygen solubility differences in these two media [39]. Other current density values (109, 262, 350, 405 and 547 mA dm À2 ), different from 175 mA dm À2 (electrode area of 0.1828 dm 2 ), should influence the hydrogenated product yield and these results are given in Table 1, entries 13, [15][16][17][18][19]. ECHs performed at current densities between 109 and 350 mA dm À2 presented electrochemical efficiencies (97-80%) that were in agreement with results described in the literature for nickel-coated electrodes [30].…”
Section: Resultsmentioning
confidence: 93%
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“…In Table 1, entry 13, an increase of the electrochemical efficiency was observed (97%), when MeOH was the co-solvent, and no difference was observed in the presence of tBuOH (Table 1, entry 14), showing that the inert gas effect to expel molecular oxygen is more efficient in water + MeOH solvent, which could be explained by oxygen solubility differences in these two media [39]. Other current density values (109, 262, 350, 405 and 547 mA dm À2 ), different from 175 mA dm À2 (electrode area of 0.1828 dm 2 ), should influence the hydrogenated product yield and these results are given in Table 1, entries 13, [15][16][17][18][19]. ECHs performed at current densities between 109 and 350 mA dm À2 presented electrochemical efficiencies (97-80%) that were in agreement with results described in the literature for nickel-coated electrodes [30].…”
Section: Resultsmentioning
confidence: 93%
“…Cathodes composed of noble metals (Pt, Pd and Rh) [15][16][17][18][19][20] were mostly used in the past. More recently, less expensive materials having larger surface areas have been used such as Raney nickel powder [4][5][6][7]13,22,23], nickel [24][25][26][27] or copper [28][29][30] deposited electrodes and metals dispersed on a polymeric matrix [32,33].…”
Section: Introductionmentioning
confidence: 99%
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“…Amouzegar and coworkers investigated the impact of metal electrochemically active‐surface‐area and electrode material by using Pt/C electrode for phenol ECH. The results showed that the properties of Pt/C such as metal particle size and electrochemical surface area had no influence on the hydrogenation activity . However, the electrode material affected the current efficiency, products distribution and the order of reactants.…”
Section: Liquid‐phase Hydrogenation Of Phenolmentioning
confidence: 98%
“…Several papers have been devoted to the electrocatalytic hydrogenation of phenol (5)(6)(7)(8)(9)(10)(11)(12). It was shown that the addition of six electrons per molecule leads to cyclohexanol via cyclohexanone as intermediate product.…”
Section: Introductionmentioning
confidence: 99%