1977
DOI: 10.1002/zaac.19774350136
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The role of Cr2O3 in Catalyst for Water‐Gas Shift Reaction

Abstract: The influence of Cr2O3 presence in the iron‐chromium catalysts for high‐temperature water‐gas shift reaction was studied. The surface stabilizing effect of Cr2O3 addition to Fe2O3, formed from iso‐ortho‐Fe(OH)3, was found. The two‐stage stabilizing effect was proved.

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Cited by 13 publications
(3 citation statements)
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“…Although Cr is generally thought of as a structural stabilizer that retards sintering of iron oxide, , the ability of Cr to shuttle between Cr 6+ and Cr 3+ valence states was considered as proof that Cr can facilitate the HT-WGS redox cycle . The present in situ XANES redox study demonstrates that the initial Cr 6+ is indeed reduced to Cr 3+ during WGS/RWGS reaction conditions, but neither CO 2 or H 2 O possesses enough oxidizing potential to oxidize Cr 3+ back to Cr 6+ .…”
Section: Discussionmentioning
confidence: 76%
“…Although Cr is generally thought of as a structural stabilizer that retards sintering of iron oxide, , the ability of Cr to shuttle between Cr 6+ and Cr 3+ valence states was considered as proof that Cr can facilitate the HT-WGS redox cycle . The present in situ XANES redox study demonstrates that the initial Cr 6+ is indeed reduced to Cr 3+ during WGS/RWGS reaction conditions, but neither CO 2 or H 2 O possesses enough oxidizing potential to oxidize Cr 3+ back to Cr 6+ .…”
Section: Discussionmentioning
confidence: 76%
“…The chromium oxide is mainly added to suppress particle growth during the calcination treatment. 163,164 For similar reasons, sometimes silica is added. 165 Two mechanisms have been proposed in the literature.…”
Section: Active Phasesmentioning
confidence: 99%
“…An unsupported iron–chromium oxide catalyst was used to remove CO from the H 2 stream for the Haber–Bosch ammonia synthesis process because CO is a poison for the ammonia synthesis Fe-based catalyst . The iron–chromium oxide WGS catalyst technology was subsequently applied to control the H 2 /CO ratio of syngas for production of hydrogen from methane steam reforming, methanol synthesis, and Fischer–Tropsch synthesis of hydrocarbons. ,, Until the 1980s, the patent and scientific literature focused on improving the synthesis of the existing iron–chromium oxide catalyst. Research in the 1980s began to explore, by trial-and-error, the effect of a wide range of promoters to try to stabilize surface area, increase activity, and enhance thermal stability of catalysts under the WGS reaction conditions. The additives can be broadly divided into two categories: chemical promoters (Cu, Rh) and textural promoters (Cr, Al, Th, Zr, Zn, Mg). …”
Section: Introductionmentioning
confidence: 99%