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The utilization of Ca-rich and Ca-Si-rich fly ashes in zeolites production

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dc.contributor.author Moutsatsou, A en
dc.contributor.author Stamatakis, E en
dc.contributor.author Hatzitzotzia, K en
dc.contributor.author Protonotarios, V en
dc.date.accessioned 2014-03-01T01:25:17Z
dc.date.available 2014-03-01T01:25:17Z
dc.date.issued 2006 en
dc.identifier.issn 0016-2361 en
dc.identifier.uri https://dspace.lib.ntua.gr/xmlui/handle/123456789/17634
dc.subject Alkaline activation en
dc.subject Lignite fly ash en
dc.subject NaP en
dc.subject NaP1 en
dc.subject Synthesized zeolites en
dc.subject.classification Energy & Fuels en
dc.subject.classification Engineering, Chemical en
dc.subject.other Alkaline earth metals en
dc.subject.other Calcium en
dc.subject.other Chemistry en
dc.subject.other Coal combustion en
dc.subject.other Density (specific gravity) en
dc.subject.other Heavy metals en
dc.subject.other Lignite en
dc.subject.other Mineralogy en
dc.subject.other pH en
dc.subject.other Scanning electron microscopy en
dc.subject.other Silicate minerals en
dc.subject.other Silicon en
dc.subject.other Sodium compounds en
dc.subject.other X ray diffraction analysis en
dc.subject.other Zeolites en
dc.subject.other Alkaline activation en
dc.subject.other Lignite fly ash en
dc.subject.other NaP en
dc.subject.other NaP1 en
dc.subject.other Synthesized zeolites en
dc.subject.other Fly ash en
dc.title The utilization of Ca-rich and Ca-Si-rich fly ashes in zeolites production en
heal.type journalArticle en
heal.identifier.primary 10.1016/j.fuel.2005.09.008 en
heal.identifier.secondary http://dx.doi.org/10.1016/j.fuel.2005.09.008 en
heal.language English en
heal.publicationDate 2006 en
heal.abstract Two Greek lignite fly ashes (FAs), with relatively different mineralogy and chemistry, were examined for their ability of giving rise to zeolitic material under alkaline activation. The two FAs were collected from Ptolemais (PFA) and Megalopolis (MFA) Lignite Power Plants and underwent a hydrothermal treatment utilizing sodium hydroxide solution 1 M, at a temperature of 90 degrees C for 24 h. Four different FA/NaOH ratios (25, 50, 100 and 150 g L-1) were examined for each of the FAs. Experimental products were characterized by means of X-ray diffraction analysis and scanning electron microscopy and also evaluated in terms of their cation exchange capacity (CEC), specific surface area (SSA), specific gravity (SG) and pH. Results showed relatively similar behavior for the two FAs and a significant mono-mineral zeolite formation for FA/NaOH = 50 a L-1. For the particular ratio, NaP1 (Gobbinsite, GIS-type), and NaP zeolites were formed from aluminosilicate glass digestion. For lower FA/NaOH ratios, the excess of NaOH seems to be prohibitive for zeolite growth, while for the highest solid/liquid ratios, the NaOH quantity seems to be insufficient for the effective activation of the FAs. The values of CEC and SSA were also higher for FA/NaOH = 50 g L-1, with the MFA presenting the best results. The authors' current work focuses on testing the products of the aforementioned zeolitization process for their potential of retaining heavy metals from a contaminated soil. (C) 2005 Published by Elsevier Ltd. en
heal.publisher ELSEVIER SCI LTD en
heal.journalName Fuel en
dc.identifier.doi 10.1016/j.fuel.2005.09.008 en
dc.identifier.isi ISI:000234764900009 en
dc.identifier.volume 85 en
dc.identifier.issue 5-6 en
dc.identifier.spage 657 en
dc.identifier.epage 663 en


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