Abstract:Toluene (TL)/methylcyclohexane
(MCH) is an attractive organic hydride couple for secure storage and
transportation of large amounts of hydrogen. Electrochemical hydrogenation
of TL to MCH can achieve energy savings compared with hydrogenation
using molecular hydrogen generated separately, and catalyst development
to improve the kinetics of electrochemical TL hydrogenation is imperative.
Here, we found that using rhodium to modify Pt nanoparticles (NPs)
supported on carbon black (Pt/C) significantly improved th… Show more
“…To check whether Cu adatoms are completely exchanged with Rh atoms in the present galvanic replacement conditions, the amount of Rh substituted for Cu adatoms deposited at an E upd of 0.35 V was quantified by atomic absorption spectroscopy according to the previous Rh quantification method . Consequently, it was determined as 1.8 nmol cm –2 .…”
Section: Resultsmentioning
confidence: 99%
“…62,63 To check whether Cu adatoms are completely exchanged with Rh atoms in the present galvanic replacement conditions, the amount of Rh substituted for Cu adatoms deposited at an E upd of 0.35 V was quantified by atomic absorption spectroscopy according to the previous Rh quantification method. 54 Consequently, it was determined as 1.8 nmol cm −2 . Since the amount of Cu adatoms evaluated from the charge for Cu-upd was 2.7 nmol cm −2 , the mole ratio of the replaced Rh to Cu adatoms is 2/3, indicating that the Cu adatoms on the Pt electrode were quantitatively replaced with rhodium.…”
Section: Evaluation Of Ecsa For Polycrystalline Pt and Rhmentioning
confidence: 99%
“…Bimetallic Pt–Rh catalysts have also been used to catalyze the oxidation of CO, ,− formic acid, ,, and methanol − and to catalyze hydrogenation. − Their catalytic activities were often evaluated on the basis of mass activity, defined as the current per total mass of Pt and Rh, because it was difficult to evaluate the ECSAs of Rh and Pt individually using hydrogen adsorption/desorption peaks. We recently found that the catalytic activity of carbon-black-supported Pt nanoparticles toward the electrochemical hydrogenation of toluene was significantly enhanced by Rh modification . Moreover, we succeeded in determining the ECSA and coverage of Rh on Pt nanoparticles using the CO-stripping technique, which gave a more quantitative understanding of the synergistic effect of using Rh together with Pt.…”
Section: Introductionmentioning
confidence: 99%
“…We recently found that the catalytic activity of carbon-black-supported Pt nanoparticles toward the electrochemical hydrogenation of toluene was significantly enhanced by Rh modification. 54 Moreover, we succeeded in determining the ECSA and coverage of Rh on Pt nanoparticles using the CO-stripping technique, which gave a more quantitative understanding of the synergistic effect of using Rh together with Pt. Consequently, it was found that an increase in the Rh coverage resulting from an extension of the Rh surface in two dimensions contributed to an increased rate of electrochemical toluene hydrogenation, which was attributed to an increase in the rate of addition of H ads generated on Rh to toluene adsorbed on Pt at the extended interface between Rh and Pt, but the growth of Rh deposits in three dimensions did not contribute to an increased rate of electrochemical toluene hydrogenation, which has not yet been explained.…”
Pt/Rh bimetal catalysts are often used in various reactions such as alcohol oxidation and hydrogenation. For comparison, their catalytic activity is often standardized by the real surface area or electrochemical surface area. However, the conventional method of using the electric charge for hydrogen desorption is difficult to apply to Pt/Rh bimetal catalysts because the potential regions of hydrogen desorption for Pt and Rh overlap. In this study, Rh-adlayer-modified Pt (Rh x /Pt) electrodes with different Rh coverages were prepared by underpotential depositions of Cu adatoms at different potentials followed by galvanic replacement of Cu with rhodium, and CO stripping was applied to determine the Rh coverages of these electrodes. No CO that had been adsorbed on a Pt electrode was removed by potentiostatic CO oxidation at 0.75 V vs reversible hydrogen electrode for 15 s in an Ar-saturated 0.5 M sulfuric acid solution at 5 °C, but 85% of CO on an Rh electrode was removed. The Rh coverages for the Rh x / Pt electrodes corrected on the basis of this result were in good agreement with the corresponding Rh coverages estimated from the electric charge for the stripping of the Cu adlayer. Moreover, the Rh x /Pt electrodes exhibited noteworthy CO-stripping and COadsorption behaviors. A single CO-stripping cyclic voltammetry peak was observed regardless of Rh coverage, and shifted toward lower potential as the Rh coverage was increased. This result resembled the trend of initiation potentials of chemisorbed oxygen formation, suggesting a bifunctional mechanism. In infrared reflectance−absorption spectra of the CO-adsorbed Rh x /Pt electrodes, a single asymmetric band assigned to "atop" CO was observed irrespective of the Rh coverage, and shifted to lower wavenumbers as the Rh coverage was increased. The d-band center estimated from the valence level spectra of the Rh x /Pt electrodes, which reflected the Pt 5d electronic structure, shifted downward as the Rh coverage was increased.
“…To check whether Cu adatoms are completely exchanged with Rh atoms in the present galvanic replacement conditions, the amount of Rh substituted for Cu adatoms deposited at an E upd of 0.35 V was quantified by atomic absorption spectroscopy according to the previous Rh quantification method . Consequently, it was determined as 1.8 nmol cm –2 .…”
Section: Resultsmentioning
confidence: 99%
“…62,63 To check whether Cu adatoms are completely exchanged with Rh atoms in the present galvanic replacement conditions, the amount of Rh substituted for Cu adatoms deposited at an E upd of 0.35 V was quantified by atomic absorption spectroscopy according to the previous Rh quantification method. 54 Consequently, it was determined as 1.8 nmol cm −2 . Since the amount of Cu adatoms evaluated from the charge for Cu-upd was 2.7 nmol cm −2 , the mole ratio of the replaced Rh to Cu adatoms is 2/3, indicating that the Cu adatoms on the Pt electrode were quantitatively replaced with rhodium.…”
Section: Evaluation Of Ecsa For Polycrystalline Pt and Rhmentioning
confidence: 99%
“…Bimetallic Pt–Rh catalysts have also been used to catalyze the oxidation of CO, ,− formic acid, ,, and methanol − and to catalyze hydrogenation. − Their catalytic activities were often evaluated on the basis of mass activity, defined as the current per total mass of Pt and Rh, because it was difficult to evaluate the ECSAs of Rh and Pt individually using hydrogen adsorption/desorption peaks. We recently found that the catalytic activity of carbon-black-supported Pt nanoparticles toward the electrochemical hydrogenation of toluene was significantly enhanced by Rh modification . Moreover, we succeeded in determining the ECSA and coverage of Rh on Pt nanoparticles using the CO-stripping technique, which gave a more quantitative understanding of the synergistic effect of using Rh together with Pt.…”
Section: Introductionmentioning
confidence: 99%
“…We recently found that the catalytic activity of carbon-black-supported Pt nanoparticles toward the electrochemical hydrogenation of toluene was significantly enhanced by Rh modification. 54 Moreover, we succeeded in determining the ECSA and coverage of Rh on Pt nanoparticles using the CO-stripping technique, which gave a more quantitative understanding of the synergistic effect of using Rh together with Pt. Consequently, it was found that an increase in the Rh coverage resulting from an extension of the Rh surface in two dimensions contributed to an increased rate of electrochemical toluene hydrogenation, which was attributed to an increase in the rate of addition of H ads generated on Rh to toluene adsorbed on Pt at the extended interface between Rh and Pt, but the growth of Rh deposits in three dimensions did not contribute to an increased rate of electrochemical toluene hydrogenation, which has not yet been explained.…”
Pt/Rh bimetal catalysts are often used in various reactions such as alcohol oxidation and hydrogenation. For comparison, their catalytic activity is often standardized by the real surface area or electrochemical surface area. However, the conventional method of using the electric charge for hydrogen desorption is difficult to apply to Pt/Rh bimetal catalysts because the potential regions of hydrogen desorption for Pt and Rh overlap. In this study, Rh-adlayer-modified Pt (Rh x /Pt) electrodes with different Rh coverages were prepared by underpotential depositions of Cu adatoms at different potentials followed by galvanic replacement of Cu with rhodium, and CO stripping was applied to determine the Rh coverages of these electrodes. No CO that had been adsorbed on a Pt electrode was removed by potentiostatic CO oxidation at 0.75 V vs reversible hydrogen electrode for 15 s in an Ar-saturated 0.5 M sulfuric acid solution at 5 °C, but 85% of CO on an Rh electrode was removed. The Rh coverages for the Rh x / Pt electrodes corrected on the basis of this result were in good agreement with the corresponding Rh coverages estimated from the electric charge for the stripping of the Cu adlayer. Moreover, the Rh x /Pt electrodes exhibited noteworthy CO-stripping and COadsorption behaviors. A single CO-stripping cyclic voltammetry peak was observed regardless of Rh coverage, and shifted toward lower potential as the Rh coverage was increased. This result resembled the trend of initiation potentials of chemisorbed oxygen formation, suggesting a bifunctional mechanism. In infrared reflectance−absorption spectra of the CO-adsorbed Rh x /Pt electrodes, a single asymmetric band assigned to "atop" CO was observed irrespective of the Rh coverage, and shifted to lower wavenumbers as the Rh coverage was increased. The d-band center estimated from the valence level spectra of the Rh x /Pt electrodes, which reflected the Pt 5d electronic structure, shifted downward as the Rh coverage was increased.
“…[8] Subsequently, H ads are added to unsaturated bonds (e. g., C=C) or consumed through hydrogen evolution reaction (HER) path. [9][10][11] The key to improve ECH performance is to intensify the adsorption of unsaturated chemical bonds on catalyst surface as well as weaken the PdÀ H binding to facilitate H ads transfer and addition to substrate. Previous studies have indicated that tensile strain could upshift the d-band center to intensify the species adsorption (e. g., C=C) to speed up ECH.…”
Electrochemical hydrogenation (ECH) uses electricity to drive proton (H + ) reduction for hydrogenation, which can greatly reduce energy supply and environmental pollution, representing an ideal alternative to traditional thermal hydrogenation. In this work, we put forward tensile-strained PdRuCu alloy to promote ECH. Tensile strain promotes the adsorption of C=C by changing the d-band center. Meanwhile, alloying Ru and Cu into Pd lattice facilitates hydrogenation by weakening PdÀ H bonding. Therefore, PdRuCu icosahedra display excellent ECH performance of 2-methyl-3-buten-2-ol (MBE) with specific activity of 227.4 μmol MBE nm À 2 min À 1 at À 0.3 V versus reversible hydrogen electrode (RHE), about 16.1 and 10.5 times higher than that of commercial Pd/C and Ru/C, respectively. In addition, PdRuCu icosahedra was excellent in the scaling up of substrate concentration combined with anisyl alcohol oxidation to produce high-value added anisaldehyde at anode. This work provides a guideline for the rational design of highly active and durable metallic catalyst in ECH.[a] K.
Electrochemical hydrogenations (EChH) constitute a sustainable alternative to conventional thermocatalytic hydrogenation. Here, we explored the EChH of the vitamin E and A synthon 2‐methyl‐3‐butyn‐2‐ol in a scalable zero‐gap electrolyzer and revealed crucial effects of electrolyte composition and convection parameters to consider for optimization. We show that high Faraday efficiencies can be achieved with low to moderate concentrations of neutral or alkaline electrolytes. While the flow rate has a strong impact on performance, electrode compression and cell orientation can be used for fine tuning. We achieved a Faraday efficiency of up to 69 % for the targeted semi‐hydrogenated product at current densities of 80 mA cm−2 at 2.2 V cell voltage and a concentration of 1 M 2‐methyl‐3‐butyn‐2‐ol.
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