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Boreskov Institute of Catalysis of the Siberian Branch of Russian ...

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OP-IV-12The comparative analysis <strong>of</strong> <strong>the</strong> catalystsactivity was carried out with pure perovskites inpowder. All catalysts guarantee much lower T 50values than <strong>the</strong> one related to non catalyticcombustion (816 °C). By inducing a partialsubstitution with 10% <strong>of</strong> Pd at <strong>the</strong> B site animprovement <strong>of</strong> <strong>the</strong> activity was observed for allFig. 1. SEM view <strong>of</strong> LaMn 0.9 Pd 0.1 O 3 obtained catalysts. This should entail a reduction <strong>of</strong> <strong>the</strong>by Solution Combustion Syn<strong>the</strong>sis.overall catalyst costs compared to conventional Pdonlycatalysts currently employed characterized by high Pd loads. More in detail <strong>the</strong> methanehalf conversion temperature (T 50 ) <strong>of</strong> Pd substituted perovskites was lowered <strong>of</strong> about 5, 40and 60 °C for LaCrO 3 (T 50 = 607 °C), LaFeO 3 (T 50 = 535 °C) and LaMnO 3 (T 50 = 485 °C),respectively; <strong>the</strong> best catalyst was found to be LaMn 0.9 Pd 0.1 O 3 (T 50 = 425 °C) and <strong>the</strong>refore itwas selected to be deposited and tested on a cordierite monolith. The catalytic converters(cylindrical cordierite honeycombs by Chauger; cell density: 200 cpsi; length: 25 mm;diameter: 34 mm) were prepared by a preliminary deposition <strong>of</strong> a layer <strong>of</strong> γ-alumina by in situSCS (10 wt% referred to <strong>the</strong> monolith weight) and <strong>the</strong>n 15 wt% (referred to <strong>the</strong> γ-aluminaweight) <strong>of</strong> LaMn 0.9 Pd 0.1 O 3 . The adhesion properties between <strong>the</strong> catalyst and ceramic surfacewas checked by means <strong>of</strong> an ultrasonic bath test: a piece <strong>of</strong> <strong>the</strong> catalytic monolith wasweighted before and after a standard ultrasonic treatment to quantify <strong>the</strong> catalyst loss. Theadhesion between <strong>the</strong> deposited catalyst and <strong>the</strong> channel walls <strong>of</strong> <strong>the</strong> traps was excellent, as<strong>the</strong> loss <strong>of</strong> catalyst by ultrasonic treatment was lower than 1%. Catalytic combustionexperiments were performed in a stainless steel reactor heated in a horizontal split tubefurnace with a heating length <strong>of</strong> 60 cm. The catalyzed monolith was sandwiched between twomullite foams to optimize flow distribution. For <strong>the</strong> temperature control a <strong>the</strong>rmocouple,inserted along one <strong>of</strong> <strong>the</strong> central monolith channel, was used to measure <strong>the</strong> inlet temperature.Lean inlet conditions (0.4% vol.% CH 4 , 10% vol.% O 2 , N 2 balance) were ensured via massflow controllers. The methane conversion <strong>of</strong> <strong>the</strong> LaMn 0.9 Pd 0.1 O 3 cordierite monolith atdifferent GHSVs shows that <strong>the</strong> conversion shifted to lower temperature at lower spacevelocity. The T 50 values are 570 °C, 455 °C and 385 °C at <strong>the</strong> space velocity <strong>of</strong> 80000 h –1 ,40000 h –1 and 10000 h –1 , respectively.References1. Mowery D.L., Graboski M.S., Ohno T.R., McCormick R.L., Appl. Catal. B: Env., 21 (1999) 157.2. Fino D., Russo., Saracco G., Specchia V., Progress in Solid State Chemistry, 35 (2007) 501.163

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