2008
DOI: 10.1039/b718286b
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Electrochemical study on the adsorption of carbon oxides and oxidation of their adsorption products on platinum group metals and alloys

Abstract: CO(2) reduction and CO adsorption on noble metals (Pt, Rh, Pd) and their alloys (Pt-Rh, Pd-Pt, Pd-Rh, Pd-Pt-Rh) prepared as thin rough deposits have been studied by chronoamperometry (CA), cyclic voltammetry (CV) and the electrochemical quartz crystal microbalance (EQCM). The influence of alloy surface composition on the values of surface coverage, eps (electron per site) and potential of the oxidation of CO(2) reduction and CO adsorption products is shown. The oxidation of the adsorbate on Pt-Rh alloys procee… Show more

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Cited by 27 publications
(32 citation statements)
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“…The calibration constant determined by Ag and Pd deposition was 1.2 ng Hz À1 , very close to the theoretical value based on Sauerbrey equation [15]. Pd alloys were deposited electrochemically on the Au surfaces according to the procedures described earlier [10,[16][17][18][19][20]. The thickness of the alloy layers was 0.2-0.3 lm.…”
Section: Methodssupporting
confidence: 79%
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“…The calibration constant determined by Ag and Pd deposition was 1.2 ng Hz À1 , very close to the theoretical value based on Sauerbrey equation [15]. Pd alloys were deposited electrochemically on the Au surfaces according to the procedures described earlier [10,[16][17][18][19][20]. The thickness of the alloy layers was 0.2-0.3 lm.…”
Section: Methodssupporting
confidence: 79%
“…Surface compositions were determined from the potential of the peak of surface oxide reduction [1,2,16,[19][20][21][22]. The CV curves are similar to those reported previously in the literature [1,2,[16][17][18][19][20][21][22]. One can distinguish hydrogen adsorption (1) and desorption (1 0 ) signals (the hydrogen region), then a potential range free from Faradaic processes (the double layer region-2), followed by surface oxide generation (3) and oxide reduction (3 0 ) currents (the oxygen region).…”
Section: Methodsmentioning
confidence: 99%
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“…CO and H 2 are main products in this process. Noble metals, such as Pd, platinum (Pt), gold (Au), rhodium (Rh), and their alloys are usually used as the electrodes as well as catalysts, which increase the total cost of the conversion process [24,29]. Transition metals and their complexes, such as [Pd(triphosphine)(PR 3 )](BF 4 ) 2 , aza-macrocyclic complexes of Ni (II), Co (II), and Cu (II), and [Pd(triphosphine)-(CH 3 CN)] 2+ can also be used as the catalysts in this process [23,25,30,31].…”
Section: Catalysts For Co 2 Conversion Into Hydrocarbon Fuelsmentioning
confidence: 99%
“…This phenomenon originated most likely from the CO 2 adsorption on Pt surface accompanied by the generation of some CO at H ads sites (on Pt) according to so called reverse water gas shift reaction. [34][35][36] The appearance of a small anodic peak at about −0.03 V in CO 2 -free electrolyte (solid line in Figure 6a) originated from the analogous (H ads -induced) surface reduction involving bicarbonates or carbonates and leading to traces of CO adsorbates. The second (more positive) small anodic peak appearing at about 0.2 V (Figure 6a, solid line) was attributed to the adsorption of anions (HCO 3 − /CO 3 2− ) and the formation of the surface Pt oxide film.…”
mentioning
confidence: 99%