2014
DOI: 10.1063/1.4874002
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Combined UHV/high-pressure catalysis setup for depth-resolved near-surface spectroscopic characterization and catalytic testing of model catalysts

Abstract: An ultra-high vacuum (UHV) setup for "real" and "inverse" model catalyst preparation, depth-resolved near-surface spectroscopic characterization and quantification of catalytic activity and selectivity under technologically relevant conditions is described. Due to the allquartz reactor attached directly to the UHV-chamber, transfer of the catalyst for in-situ testing without intermediate contact to the ambient is possible. The design of the UHV-compatible re-circulating batch reactor setup allows the study of … Show more

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Cited by 16 publications
(17 citation statements)
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References 28 publications
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“…Optical and electron micrographs of the catalyst before and after MSR are given in the Supporting Information (Figure S13 and S14). Temperature‐programmed methanol steam reforming experiments were performed by using an UHV‐attached high‐pressure batch reactor with continuous MS detection . The following starting conditions were applied: 12 mbar methanol, 24 mbar water, 8 mbar Ar, and 956 mbar He.…”
Section: Figurementioning
confidence: 99%
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“…Optical and electron micrographs of the catalyst before and after MSR are given in the Supporting Information (Figure S13 and S14). Temperature‐programmed methanol steam reforming experiments were performed by using an UHV‐attached high‐pressure batch reactor with continuous MS detection . The following starting conditions were applied: 12 mbar methanol, 24 mbar water, 8 mbar Ar, and 956 mbar He.…”
Section: Figurementioning
confidence: 99%
“…According to Figure 2, the maximum formation rate of CO 2 increases and the onset temperature for CO 2 formation decreases by running four identical catalytic MSR cycles (Figure 2a nd Figure S1). As shown in Figures 1, 3, and 4, activation is morphologically characterized by oxidative segregation as ac onsequence of decomposition of the intermetallic compound Cu 51 Zr 14 and subsequent( partial)Z rs urface hydroxylation (Zr 3d, BE = 183.1 eV [17] ). Oxidation of the intermetallic compound thus occurs without passivatingt he surfacew ith ZrO 2 .T he direct comparison to the Cu/Zn system,a lready characterized catalytically in the same experimental setup, [8] reveals that activation of the reaction-induced Cu/Zr material leads to a" self-stabiliz-ing" state that is much more stable, and no oxidative/thermal Cu sintering was observed.…”
mentioning
confidence: 99%
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“…For discussion about mass and heat transport limitations, we refer to a thorough discussion of the catalytic setup in Ref. [31].…”
Section: Catalytic Measurementsmentioning
confidence: 99%
“…For the former, sample preparation and characterization was performed in a combined preparation/analysis chamber with attached recirculating batch reaction cell operating at ambient pressures, described in more detail elsewhere (base pressure in the low 10 −9 mbar range) [31]. The sample is heated via e-bombardment, where electrons are ejected from a triple-filament emitter (operated with 30 W heating power) set to −500 V, while the sample is set to +300 V. The electron impact heating power is controlled via the filament emission current.…”
Section: Uhv Setupmentioning
confidence: 99%