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Pore structure analysis of an SCR catalyst using a new method for interpreting nitrogen sorption hysteresis

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dc.contributor.author Salmas, CE en
dc.contributor.author Androutsopoulos, GP en
dc.date.accessioned 2014-03-01T01:16:57Z
dc.date.available 2014-03-01T01:16:57Z
dc.date.issued 2001 en
dc.identifier.issn 0926-860X en
dc.identifier.uri https://dspace.lib.ntua.gr/xmlui/handle/123456789/14287
dc.subject pore structure en
dc.subject nitrogen sorption en
dc.subject SCR catalyst en
dc.subject CPSM model en
dc.subject tortuosity en
dc.subject.classification Chemistry, Physical en
dc.subject.classification Environmental Sciences en
dc.subject.other Catalysis en
dc.subject.other Hysteresis en
dc.subject.other Mathematical models en
dc.subject.other Nitrogen en
dc.subject.other Pore size en
dc.subject.other Porosimeters en
dc.subject.other Porous materials en
dc.subject.other Reduction en
dc.subject.other Sorption en
dc.subject.other Corrugated pore structure model (CPSM) en
dc.subject.other Pore volume distribution en
dc.subject.other Selective catalytic reduction (SCR) en
dc.subject.other Surface area distribution en
dc.subject.other Tortuosity en
dc.subject.other Catalysts en
dc.title Pore structure analysis of an SCR catalyst using a new method for interpreting nitrogen sorption hysteresis en
heal.type journalArticle en
heal.identifier.primary 10.1016/S0926-860X(00)00814-0 en
heal.identifier.secondary http://dx.doi.org/10.1016/S0926-860X(00)00814-0 en
heal.language English en
heal.publicationDate 2001 en
heal.abstract Nitrogen sorption hysteresis of a selective catalytic reduction (SCR) catalyst in its "fresh" and "used" form. [Catal. Today 56 (2000) 335] was analysed by employing the Corrugated Pore Structure Model (CPSM-nitrogen) reported elsewhere [Ind. Eng, Chem. Res. 39 (2000) 3747 and Ind. Eng. Chem. Res., 39 (2000) 3764]. The BET surface area and intrinsic pore volume, and surface area distributions were deduced via the CPSM fitting over the relevant hysteresis loop and compared to those obtained by applying various conventional methods. CPSM predictions of the total specific pore surface area, are in perfect agreement with BET estimates, while those calculated by the Roberts method, irrespective of the hysteresis loop branch chosen, deviate substantially. CPSM prediction of tortuosity factors (CPSM-tortuosity [Ind. Eng. Chem. Res., in press]) for the catalysts under consideration were found to be: tau (CpSM,fresh) = 4.6 and 4.5. These values are typical of porous catalysts and approach those determined experimentally (i.e, tau = 5-6 [Appl. Catal. 10 (1996) 2991). The pore volume distribution of the latter catalyst obtained from mercury porosimetry measurements approaches that deduced by the CPSM method. (C) 2001 Elsevier Science B,V. All rights reserved. en
heal.publisher ELSEVIER SCIENCE BV en
heal.journalName Applied Catalysis A: General en
dc.identifier.doi 10.1016/S0926-860X(00)00814-0 en
dc.identifier.isi ISI:000167525900032 en
dc.identifier.volume 210 en
dc.identifier.issue 1-2 en
dc.identifier.spage 329 en
dc.identifier.epage 338 en


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