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.

Sulphur poisoning of LaMn1-xMgxO3 catalysts for natural gas combustion / Rosso, I.; Garrone, Edoardo; Geobaldo, Francesco; Onida, Barbara; Saracco, Guido; Specchia, Vito. - In: APPLIED CATALYSIS. B, ENVIRONMENTAL. - ISSN 0926-3373. - 30:1-2(2001), pp. 61-73. [10.1016/S0926-3373(00)00222-8]

Sulphur poisoning of LaMn1-xMgxO3 catalysts for natural gas combustion

GARRONE, EDOARDO;GEOBALDO, FRANCESCO;ONIDA, BARBARA;SARACCO, GUIDO;SPECCHIA, Vito
2001

Abstract

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.
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Utilizza questo identificativo per citare o creare un link a questo documento: https://hdl.handle.net/11583/1405905
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