2017
DOI: 10.1021/acscatal.7b01822
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Spinel-Structured ZnCr2O4 with Excess Zn Is the Active ZnO/Cr2O3 Catalyst for High-Temperature Methanol Synthesis

Abstract: A series of ZnO/Cr 2 O 3 catalysts with different Zn:Cr ratios was prepared by coprecipitation at a constant pH of 7 and applied in methanol synthesis at 260−300 °C and 60 bar. The X-ray diffraction (XRD) results showed that the calcined catalysts with ratios from 65:35 to 55:45 consist of ZnCr 2 O 4 spinel with a low degree of crystallinity. For catalysts with Zn:Cr ratios smaller than 1, the formation of chromates was observed in agreement with temperature-programmed reduction results. Raman and XRD results … Show more

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Cited by 118 publications
(93 citation statements)
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“…In general, the Cu:Zn ratio as well as the synthesis route is chosen in such a way that an intimate contact between Cu and ZnO is achieved to maximize the number of Cu-Zn interface sites. A significant influence of pure ZnO sites under the conditions of the low-temperature methanol synthesis can be neglected 31 , and the absence of acidic OH groups on the structural promoter Al 2 O 3 is also excluded due to the absence of acid-catalysed products such as dimethyl ether (Supplementary Note 3) 4 . For Al 2 O 3 , it is generally accepted that it acts as physical spacer to enhance the lifetime as well as the surface area of the Cu/ZnO catalyst maintaining economical methanol production rates over several years 4 .…”
Section: Resultsmentioning
confidence: 99%
“…In general, the Cu:Zn ratio as well as the synthesis route is chosen in such a way that an intimate contact between Cu and ZnO is achieved to maximize the number of Cu-Zn interface sites. A significant influence of pure ZnO sites under the conditions of the low-temperature methanol synthesis can be neglected 31 , and the absence of acidic OH groups on the structural promoter Al 2 O 3 is also excluded due to the absence of acid-catalysed products such as dimethyl ether (Supplementary Note 3) 4 . For Al 2 O 3 , it is generally accepted that it acts as physical spacer to enhance the lifetime as well as the surface area of the Cu/ZnO catalyst maintaining economical methanol production rates over several years 4 .…”
Section: Resultsmentioning
confidence: 99%
“…S1. † [44][45][46][47][48] In the reaction, the selectivity of methanol is as high as 92.58% at 300 C under 2.0 MPa (Table S2 †). In detail, CO is absorbed at the oxygen vacancies then dissociated and hydrogenated by H 2 gradually to CH 3 O, followed by further hydrogenation to methanol.…”
Section: Design Of Active Physical Mixture Catalysts In Sto Reactionmentioning
confidence: 99%
“…Simultaneously, the ratio of O defect /O lattice was obviously enhanced from 0.79 to 12.09, which indicates that the sites supplied by oxygen vacancies favour CO adsorption and continuous activation. [44][45][46][47][48] OH increased in the H 2 -activated Zn-Cr catalyst, which resulted in the adsorption of formed H 2 O on the catalyst surface from the process of Cr 3+ reduction. In general, with increasing syngas (CO/H 2 ) pressure and reaction temperature in the STO reaction, the oxygen vacancies concentration also increased, which was conducive for the release of surface oxygen on the Zn-Cr catalyst in an anaerobic environment.…”
mentioning
confidence: 99%
“…Zn−Cr mixed oxides has been applied in methanol synthesis from syngas, and the oxygen vacancies can be formed on surface of Zn−Cr spinel . Besides, the nonstoichiometric ZnCr 2 O 4 spinel with excess Zn has an improved activity toward C−O bond activation . But tuning the oxygen vacancy of Zn−Cr spinel is rarely reported.…”
Section: Figurementioning
confidence: 99%