Increase in stability of BaCo/CeO2 catalyst by optimizing the loading amount of Ba promoter for high-temperature water-gas shift reaction using waste-derived synthesis gas
Yeol-Lim Lee,
Kyoung-Jin Kim,
Won-Jun Jang,
Jae-Oh Shim,
Kyung-Won Jeon,
Hyun-Suk Na,
Hak-Min Kim,
Jong Wook Bae,
Sung Chan Nam,
Byong-Hun Jeon and
Hyun-Seog Roh
Renewable Energy, 2020, vol. 145, issue C, 2715-2722
Abstract:
The loading amount of Ba promoter in the 15 wt% Co/CeO2 catalyst system was varied from 0 wt% to 3 wt%, and the resulting catalysts were used for the high-temperature water-gas shift (HTS) reaction. The catalysts were prepared by the incipient wetness co-impregnation method and studied through various characterization techniques such as X-ray diffraction, Brunauer–Emmet–Teller measurements, CO–chemisorption, H2–temperature programmed reduction, X-ray photoelectron spectroscopy, and transmission electron microscopy. The doping of Ba as a promoter in the optimal amount (1–2 wt%) improves the reducibility of the catalyst and enhances its sintering resistance. However, the doping of an excessive amount (≥3 wt%) of the promoter lowers the reducibility of the catalyst, resulting in the instability of the active phase (Co0). Overall, the 1% BaCo/CeO2 catalyst exhibited the best performance even at a severe reaction condition (CO conc. = 38%, GHSV = 143,000 h−1) owing to the strong resistance to the sintering and high stability of the active phase.
Keywords: Waste-derived synthesis gas; High-temperature water-gas shift; Ba promoter; Co/CeO2 catalyst; Stability (search for similar items in EconPapers)
Date: 2020
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Persistent link: https://EconPapers.repec.org/RePEc:eee:renene:v:145:y:2020:i:c:p:2715-2722
DOI: 10.1016/j.renene.2019.08.050
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