Abstract:In aqueous phase, the rates of hydrogenation of aromatic substrates such as phenol on Pt/C and Rh/C are influenced by varying activity of hydronium ions. Decreasing the pH from 8 to 1 increases the rate of hydrogenation of phenol on Pt at 20 bar H 2 and 80 °C by 15-fold. This increase is attributed to weakening of the hydrogen binding energy (HBE) on the metal surface with decreasing pH. A weaker HBE at lower pH is also predicted by ab initio molecular dynamics simulations, providing atomistic insight into the… Show more
“…Two catalysts, Pd/HNO 3 CF‐12h and Pd/HNO 3 CF‐6h, were investigated at pH 2.5, 5.2, and 10.5 (Figure S17). The ECH rates increased with decreasing pH, paralleling a recent study . Importantly, the differences between both catalysts become more pronounced as the pH increases.…”
Acid functionalization of acarbon support allows to enhance the electrocatalytic activity of Pd to hydrogenate benzaldehyde to benzyl alcohol proportional to the concentration of Brønsted-acid sites.I nc ontrast, the hydrogenation rate is not affected when H 2 is used as ar eduction equivalent. The different responses to the catalyst properties are shown to be caused by differences in the hydrogenation mechanism between the electrochemical and the H 2 -induced hydrogenation pathways.T he enhancement of electrocatalytic reduction is realized by the participation of support-generated hydronium ions in the proximity of the metal particles.
“…Two catalysts, Pd/HNO 3 CF‐12h and Pd/HNO 3 CF‐6h, were investigated at pH 2.5, 5.2, and 10.5 (Figure S17). The ECH rates increased with decreasing pH, paralleling a recent study . Importantly, the differences between both catalysts become more pronounced as the pH increases.…”
Acid functionalization of acarbon support allows to enhance the electrocatalytic activity of Pd to hydrogenate benzaldehyde to benzyl alcohol proportional to the concentration of Brønsted-acid sites.I nc ontrast, the hydrogenation rate is not affected when H 2 is used as ar eduction equivalent. The different responses to the catalyst properties are shown to be caused by differences in the hydrogenation mechanism between the electrochemical and the H 2 -induced hydrogenation pathways.T he enhancement of electrocatalytic reduction is realized by the participation of support-generated hydronium ions in the proximity of the metal particles.
“…They found that the higher reaction rate is attributed to weakening of the hydrogen binding energy on the metal surface with decreasing pH. [34] Comparing the catalytic results with the ones reported in literature (Table 1), commercial Pd/AC 5 % in our operating conditions shows good catalytic performance during both Na-Muc and t,t-MA hydrogenation. Low pressure and temperature allowed to reach full conversion and high AdA yield avoiding the use of pressurized hydrogen, which is a matter of concern for industrial safety reasons.…”
Section: Hydrogenation Of Transtrans Muconic Acidsupporting
confidence: 73%
“…reported the same catalytic behavior during phenol hydrogenation. They found that the higher reaction rate is attributed to weakening of the hydrogen binding energy on the metal surface with decreasing pH …”
sodium muconate and trans,trans‐muconic acid were heterogeneously hydrogenated to adipic acid, a strategic intermediate for the industry of polyamides and high performance polymers. Hydrogen pressure, metal to substrate ratio, substrate concentration and reaction temperature were varied to study the effect of these parameters on the reaction products. Commercial Pd/AC 5 % was used as catalyst and characterized by TEM, BET and XPS analyses. The results revealed that temperature is the parameter which mainly affect the reaction. Moreover, hydrogenation of trans,trans‐muconic acid is faster than sodium muconate reduction. Full conversion and full yield toward adipic acid was obtained using trans,trans‐muconic acid as substrate after 60 min at the following operating conditions: temperature=70 °C, metal/substrate=1/200 (molPd/molsub), trans,trans‐muconic acid concentration=1.42E‐02M and hydrogen pressure=1 bar. In all reactions (2E)hexenedioic acid was detected as main intermediate.
“…For example, during the hydrogenation of maleic acid at a wired Pt–water interface, changes in rate with H 2 pressure were attributed to spontaneous electrical polarization, without accounting for changes in chemical driving force (i.e., the H 2 reaction order). 46 Likewise, pH-dependent CO oxidation 47 , 48 and phenol hydrogenation 49 rates were indirectly attributed to spontaneous polarization on the basis of shifts in the CO infrared spectrum and molecular dynamics simulations, respectively, but could not rule out contributions from chemical pH effects. Thus, it remains unclear whether spontaneous electrical polarization indeed plays a role in liquid-phase thermochemical heterogeneous catalysis.…”
Large oriented electric
fields spontaneously arise at all solid–liquid
interfaces via the exchange of ions and/or electrons with the solution.
Although intrinsic electric fields are known to play an important
role in molecular and biological catalysis, the role of spontaneous
polarization in heterogeneous thermocatalysis remains unclear because
the catalysts employed are typically disconnected from an external
circuit, which makes it difficult to monitor or control the degree
of electrical polarization of the surface. Here, we address this knowledge
gap by developing general methods for wirelessly monitoring and controlling
spontaneous electrical polarization at conductive catalysts dispersed
in liquid media. By combining electrochemical and spectroscopic measurements,
we demonstrate that proton and electron transfer from solution controllably,
spontaneously, and wirelessly polarize Pt surfaces during thermochemical
catalysis. We employ liquid-phase ethylene hydrogenation on a Pt/C
catalyst as a thermochemical probe reaction and observe that the rate
of this nonpolar hydrogenation reaction is significantly influenced
by spontaneous electric fields generated by both interfacial proton
transfer in water and interfacial electron transfer from organometallic
redox buffers in a polar aprotic
ortho
-difluorobenzene
solvent. Across these vastly disparate reaction media, we observe
quantitatively similar scaling of ethylene hydrogenation rates with
the Pt open-circuit electrochemical potential (
E
OCP
). These results isolate the role of interfacial electrostatic
effects from medium-specific chemical interactions and establish that
spontaneous interfacial electric fields play a critical role in liquid-phase
heterogeneous catalysis. Consequently,
E
OCP
—a generally overlooked parameter in heterogeneous catalysis—warrants
consideration in mechanistic studies of thermochemical reactions at
solid–liquid interfaces, alongside chemical factors such as
temperature, reactant activities, and catalyst structure. Indeed,
this work establishes the experimental and conceptual foundation for
harnessing electric fields to both elucidate surface chemistry and
manipulate preparative thermochemical catalysis.
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