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

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PP-III-40ratio, an increase in <strong>the</strong> propane conversion and almost no change in <strong>the</strong> selectivity towardsbutene are observed. In addition, a slightly decrease in <strong>the</strong> selectivity towards propene withincrease <strong>of</strong> Si/Al ratio is observed (not shown here).These are likely to be related to <strong>the</strong>change <strong>of</strong> zeolites acidity with varying Si/Al and <strong>the</strong>refore <strong>the</strong> number <strong>of</strong> iron cationsintroduced into zeolites. In <strong>the</strong> low Si/Al ratios (Si/Al < 40), <strong>the</strong> percent <strong>of</strong> products such asCH 4 , C 2 H 2 , C 2 H 4 , C 2 H 6 , C 3 H 6 formed via <strong>the</strong> hydrocraking <strong>of</strong> butane are enhanced. But, <strong>the</strong>higher Si/Al ratios lead to an increase in oxidative dehydrogenation <strong>of</strong> butane to butene andbutadiene.X C4H10,%7060504030201000 100 200 300 400Time,minSM27Fe1.0Z23Fe1.0Z30Fe1.0Z50Fe1.0Z80Fe1.0Z280Fe1.0SC4H8,%70605040302010SM27Fe1.0Z30Fe1.0Z50Fe1.0Z80Fe1.0Z280Fe1.000 100 200 300 400Time, minFig.1. Butane conversion and butane selectivity as a function <strong>of</strong> time in <strong>the</strong> presence <strong>of</strong> N 2 O in <strong>the</strong> feed(W cat = 0.5 g, T= 723 K, C 4 H 10 :N 2 O=1:1, F total =200ml/min). ZxFey: x= SiO 2 /Al 2 O 3 and y= wt. % Fe.The presence <strong>of</strong> O 2 as well as N 2 O in <strong>the</strong> feed over Z280Fe1.0 not only prevents <strong>the</strong>formation <strong>of</strong> butane and butadiene, but also leads to a significantly decrease in <strong>the</strong> conversion<strong>of</strong> butane, from 50 % to 3.0 %. The butane mainly converts to CO x via total oxidationThe nature <strong>of</strong> <strong>the</strong> iron species responsible for <strong>the</strong> N 2 O decomposition (not shown here)and dehydrogenation <strong>of</strong> butane appears clearly different as could be observed with <strong>of</strong> H 2 -TPR, UV/vis, XPS, DRIFT, and NH 3 -TPD. It can be concluded that although N 2 Odecomposition and <strong>the</strong> total oxidation <strong>of</strong> butane are favoured over isolated iron-oxo/hydroxocationsformed over Fe-ZSM-5 with low Si/Al, <strong>the</strong> uncharged nonosized multinuclear ironoxoclusters formed in 80 and 140 <strong>of</strong> Si/Al can mostly catalyze <strong>the</strong> dehydrogenation <strong>of</strong> butane.Additionally, in this work <strong>the</strong> kinetics <strong>of</strong> global and elementary steps for oxidativedehydrogenation <strong>of</strong> butane can be obtained under <strong>the</strong> unsteady-state and steady-stateexperiments.References:1. A. Ates and A. Reitzmann, J. Catal., 2005, 235, 164-174.2. E. Ananieva and A. Reitzmann, Chem. Eng. Sci., 2004, 59, 5509-5517.381

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