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  7. Volume 31
  8. Issue 04
Please use this identifier to cite or link to this item: http://localhost:80/xmlui/handle/123456789/19646
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dc.contributor.authorHUI WANG-
dc.contributor.authorLIU, GUO JIE-
dc.contributor.authorYAO WANG-
dc.contributor.authorWEI QING Ll-
dc.contributor.authorLl ZHOU-
dc.contributor.authorSEN SHI-
dc.contributor.authorJIAN SUN-
dc.date.accessioned2023-09-19T04:20:42Z-
dc.date.available2023-09-19T04:20:42Z-
dc.date.issued2009-08-20-
dc.identifier.citationMathieu, Y., Tzanis, L., Soulard, M., Patarin, J., Vierling, M., & Molière, M. (2013). Adsorption of SOx by oxide materials: A review. Fuel processing technology, 114, 81-100.en_US
dc.identifier.issn0253-5106-
dc.identifier.urihttp://142.54.178.187:9060/xmlui/handle/123456789/19646-
dc.description.abstractKinetics of So2 removal using a copper-based sorbent CuO/γ-Al2O3 and a cerium modified copper sorbent CuO-CeO2/γ-Al2O3 were measured on a TGA and their kinetics behaviors were simulated with a proposed empirical rate model (ERM). The purpose of cerium addition to the copper sorbent was to study the difference of sorbent's kinetics. The cerium modified copper sorbent showed a higher reaction rate on initial sulfation than the regular copper sorbent. Both sorbents however had similar calculated activation energy. The proposed ERM model appeared to describe the SO2 removal kinetics well in the temperature range 250-400 ºC.en_US
dc.description.sponsorshipThe chemical society of Pakistan is an approved society from the PSF.en_US
dc.language.isoenen_US
dc.publisherHEJ Research Institute of Chemistry, University of Karachi, Karachi.en_US
dc.titleKinetics of DeSOx Reaction on Copper and Cerium-based Sorbent-Catalystsen_US
dc.typeArticleen_US
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