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Lee, Kang Soo
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dc.citation.endPage 11 -
dc.citation.startPage 1 -
dc.citation.title FUEL -
dc.citation.volume 161 -
dc.contributor.author Jeong, Seongha -
dc.contributor.author Lee, Kang Soo -
dc.contributor.author Keel, Sang In -
dc.contributor.author Yun, Jin Han -
dc.contributor.author Kim, Yong Jin -
dc.contributor.author Kim, Sang Soo -
dc.date.accessioned 2024-07-22T17:35:14Z -
dc.date.available 2024-07-22T17:35:14Z -
dc.date.created 2024-07-22 -
dc.date.issued 2015-12 -
dc.description.abstract The general desulfurization process referred to as "indirect sulfation" takes place via a two-step process. Calcination makes limestone decompose to calcium oxide (CaO), and then SO2 molecules are adsorbed onto the calcined limestone. However, if the CO2 partial pressure in the system is higher than the equilibrium CO2 pressure over the limestone, an adsorption reaction between limestone and SO2 molecules can take place directly in the uncalcined state. This one-step process, called "direct sulfation," can apply to desulfurization in pressurized fluid-bed combustion (PFBC) or an oxy fuel combustion system capturing CO2. Limestone samples were reacted in a TGA apparatus, and the degrees of sulfation were measured under 100% air conditions for indirect sulfation and 80% CO2/20% O-2 conditions for direct sulfation to compare the mechanisms and kinetics of the two sulfation processes. SEM images of sulfated particles and EDS analyses showed that the gas diffusion of indirect sulfation takes place readily through macro-pores between the grains at a low conversion rate, and SO2 adsorption occurs over the interior of the limestone particles, whereas SO2 adsorption in direct sulfation takes place at the reaction interface, and the product (CaSO4) layer permeates into the interior from the surface of the limestone particles as direct sulfation proceeds. Thus, the grain model and the shrinking unreacted core model are applicable to describing the kinetics of indirect and direct sulfation, respectively. These model predictions agreed with experimental data, and the kinetic parameters obtained from experiments are consistent with the mechanisms. Furthermore, the high activation energy of the diffusion of direct sulfation and indirect sulfation with high conversion indicate that the diffusion mechanisms in the particles in direct sulfation and indirect sulfation at high conversion are both gas diffusion in pores and solid-state diffusion. These results may contribute to understanding why the characteristics of direct sulfation differ from those of indirect sulfation under certain conditions. (C) 2015 Elsevier Ltd. All rights reserved. -
dc.identifier.bibliographicCitation FUEL, v.161, pp.1 - 11 -
dc.identifier.doi 10.1016/j.fuel.2015.08.034 -
dc.identifier.issn 0016-2361 -
dc.identifier.scopusid 2-s2.0-84939811072 -
dc.identifier.uri https://scholarworks.unist.ac.kr/handle/201301/83260 -
dc.identifier.wosid 000362304600001 -
dc.language 영어 -
dc.publisher ELSEVIER SCI LTD -
dc.title Mechanisms of direct and in-direct sulfation of limestone -
dc.type Article -
dc.description.isOpenAccess FALSE -
dc.relation.journalWebOfScienceCategory Energy & Fuels; Engineering, Chemical -
dc.relation.journalResearchArea Energy & Fuels; Engineering -
dc.type.docType Article -
dc.description.journalRegisteredClass scie -
dc.description.journalRegisteredClass scopus -
dc.subject.keywordAuthor Direct sulfation -
dc.subject.keywordAuthor Indirect sulfation -
dc.subject.keywordAuthor Limestone -
dc.subject.keywordAuthor Calcium carbonate -
dc.subject.keywordAuthor Mechanism -
dc.subject.keywordAuthor Diffusion -
dc.subject.keywordPlus CALCIUM-BASED SORBENTS -
dc.subject.keywordPlus PRESSURE -
dc.subject.keywordPlus CALCINATION -
dc.subject.keywordPlus KINETICS -
dc.subject.keywordPlus RANGE -

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