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	       <dc:title>Sulphur poisoning of LaMn{sub 1-x}Mg{sub x}O{sub 3} catalysts for natural gas combustion</dc:title>
	       <dc:creator>Rosso, I; Garrone, E; Geobaldo, F; Onida, B; Saracco, G; Specchia, V [Dipartimento di Scienza dei Materiali e Ingegneria Chimica, Politecnico di Torino, Corso Duca degli Abruzzi, 24-10129 Turin (Italy)]</dc:creator>
	       <dc:subject>03 NATURAL GAS; SULFUR; POISONING; CATALYSTS; NATURAL GAS; COMBUSTION; LANTHANUM COMPOUNDS; MANGANESE OXIDES; MAGNESIUM OXIDES; AGING; METHANE; DEACTIVATION; POLYCYCLIC SULFUR HETEROCYCLES; ODORANTS; SULFUR DIOXIDE; THERMODYNAMIC ACTIVITY; REGENERATION; PEROVSKITES; WATER; AMMONIA; LEACHING; ACTIVATION ENERGY</dc:subject>
	       <dc:subjectRelated></dc:subjectRelated>
	       <dc:description>Ageing treatments were carried out on LaMn{sub 1-x}Mg{sub x}O{sub 3+{delta}} (x=0, 0.2, 0.5) catalysts for methane combustion to throw light on their deactivation mechanism in the presence of tetrahydrothiophene - used in Italy as odorant of natural gas - or directly in the presence of SO{sub 2}. Various characterisation techniques were used in concert: XRD, BET, TEM, SEM-EDS, FTIR, TPD, chemical analysis and atomic absorption. The effects of treatment temperature and exposure on catalytic activity were evaluated: exposure to 200ppmv SO{sub 2} at 800C for 24h causes a rather drastic deactivation of each LaMn{sub 1-x}Mg{sub x}O{sub 3} catalyst. Metal sulphate formation is the major responsible for deactivation. However, the extent of poisoning as well as the catalyst regenerability depends on the catalyst composition. The LaMn{sub 0.5}Mg{sub 0.5}O{sub 3} catalyst can in fact be regenerated completely by water leaching, while LaMn{sub 0.8}Mg{sub 0.2}O{sub 3} and LaMnO{sub 3} perovskites can be regenerated significantly only by leaching with aqueous NH{sub 3} solutions. An explanation of these results, also based on the values of activation energy for each fresh, poisoned and regenerated catalysts, is suggested and a mechanism for catalyst regeneration by water and NH{sub 4}OH solution is proposed.</dc:description>
	       <dcq:publisher></dcq:publisher>
	       <dcq:publisherResearch></dcq:publisherResearch>
	       <dcq:publisherAvailability></dcq:publisherAvailability>
	       <dcq:publisherSponsor></dcq:publisherSponsor>
	       <dcq:publisherCountry>Netherlands</dcq:publisherCountry>
		   <dc:contributingOrganizations></dc:contributingOrganizations>
	       <dc:date>2001-02-26</dc:date>
	       <dc:language>English</dc:language>
	       <dc:type>Journal Article</dc:type>
	       <dcq:typeQualifier></dcq:typeQualifier>
	       <dc:relation>Journal Name: Applied Catalysis. B, Environmental; Journal Volume: 30; Journal Issue: 1-2; Other Information: PBD: 26 Feb 2001</dc:relation>
	       <dc:coverage></dc:coverage>
	       <dc:format>Medium: X; Size: page(s) 61-73</dc:format>
	       <dc:doi>https://doi.org/10.1016/S0926-3373(00)00222-8</dc:doi>
	       <dc:identifier></dc:identifier>
		   <dc:journalName>[]</dc:journalName>
		   <dc:journalIssue>1-2</dc:journalIssue>
		   <dc:journalVolume>30</dc:journalVolume>
	       <dc:identifierReport></dc:identifierReport>
	       <dcq:identifierDOEcontract></dcq:identifierDOEcontract>
	       <dc:identifierOther>Journal ID: ISSN 0926-3373; ACBEE3; TRN: NL01E0690</dc:identifierOther>
	       <dc:source>ECN; EDB-01:033556</dc:source>
	       <dc:rights></dc:rights>
	       <dc:dateEntry>2010-12-30</dc:dateEntry>
	       <dc:dateAdded></dc:dateAdded>
	       <dc:ostiId>20149233</dc:ostiId>
	       <dcq:identifier-purl></dcq:identifier-purl>
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