Regeneration of Pt-Sn/Al(2)O(3)Catalyst for Hydrogen Production through Propane Dehydrogenation Using Hydrochloric Acid
- Authors
- Choi, Yi Sun; Oh, Kyeongseok; Jung, Kwang-Deog; Kim, Won-Il; Koh, Hyoung Lim
- Issue Date
- 2020-08
- Publisher
- MDPI
- Citation
- CATALYSTS, v.10, no.8
- Abstract
- Compared with dehydrogenation in conventional petroleum refinery processes, relatively pure hydrogen can be produced by propane dehydrogenation (PDH) without innate contaminants like sulfur and metals. Among the existing catalysts for PDH, Pt catalysts are popular and are often used in conjunction with Sn as a co-catalyst. Coke formation is a major concern in PDH, where catalyst regeneration is typically achieved by periodic coke burning to achieve sustainable operation. In this study, Pt-Sn/Al(2)O(3)catalysts were regenerated after coke burning in three stages: mixing the catalyst with liquid hydrochloric acid, drying, and calcining under air atmosphere. In this process, the optimum concentration of hydrochloric acid was found to be 35%w/w. HCl treatment was effective for enhancing redispersion of the metal catalysts and aiding the formation of the Pt3Sn alloy, which is considered to be effective for PDH reaction. HCl treatment may provide oxychlorination-like conditions under the calcination atmosphere. The characteristics of the catalysts were examined by X-ray diffraction (XRD), transmission electron microscopy (TEM), temperature-programmed reduction (TPR), X-ray photoelectron spectroscopy (XPS), and CO chemisorption.
- Keywords
- PT-SN CATALYSTS; PT-SN/AL2O3 CATALYSTS; COKE; PERFORMANCE; ALUMINA; SPECTROSCOPY; PT-RE/AL2O3; OXIDATION; PLATINUM; ZIRCONIA; PT-SN CATALYSTS; PT-SN/AL2O3 CATALYSTS; COKE; PERFORMANCE; ALUMINA; SPECTROSCOPY; PT-RE/AL2O3; OXIDATION; PLATINUM; ZIRCONIA; hydrochloric acid treatment; propane dehydrogenation; Pt-Sn; Al2O3; Pt3Sn alloy; regeneration
- ISSN
- 2073-4344
- URI
- https://pubs.kist.re.kr/handle/201004/118325
- DOI
- 10.3390/catal10080898
- Appears in Collections:
- KIST Article > 2020
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