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

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OP-I-8KINETICS OF CARBON MONOXIDE OXIDATION OVER CuO/CeO 2CATALYSTSJ.L. Ayastuy, A. Gurbani, M.P. González-Marcos, M.A. Gutiérrez-OrtizDept. <strong>of</strong> Chemical Engineering, Faculty <strong>of</strong> Science and Technology, University <strong>of</strong> <strong>the</strong> BasqueCountry. P.O.Box 644, 48940-E, Bilbao, SpainFax: 0034-946013500, e-mail: joseluis.ayastuy@ehu.esIntroductionCeria supported CuO catalyst have been reported as very active in low temperature COoxidation catalyst [1,2] due to its high capacity to storage and supply oxygen [3] <strong>the</strong> COoxidation is believed to follow Mars-Van Krevelen (MVK) mechanism, but also Langmuir-Hinshelwood (LH) mechanism is reported in literature [4]. In this work <strong>the</strong> kinetics <strong>of</strong> pureCO oxidation over CuO/ceria catalysts has been investigated and <strong>the</strong> experimental data werefit with several mechanistic models.ExperimentalCuO/CeO 2 catalyst was prepared by wet impregnation with CuO loading <strong>of</strong> 7% in weight(being real value 6.9), dried and calcined in air at 400°C for 5 h. Previous to kineticexperiments, catalyst was reduced in hydrogen stream at 300°C for 1 h. The catalyst wascharacterized by BET, XRD, H 2 -TPR, CO-TPD, O 2 -TPD and oxidation-reduction cycles.Kinetic experiments were carried out in differential regime, with gas total flow rate <strong>of</strong>200 cm 3 /min and for several feed stream composition, being <strong>the</strong> catalyst particles size <strong>of</strong> 0.16-0.25 mm. The experiments were carried out at four temperatures (in <strong>the</strong> range 300 to 353 K)and <strong>the</strong> obtained 61 experimental data were fit to power law rate and several mechanistic rateequations (LH and MVK).Genetic algorithm (GA) was used to optimization <strong>of</strong> rate equations parameters, byminimizing <strong>the</strong> objective functionN∑ ( rexp− rcalc)i = 1. The initial population <strong>of</strong> 100 individuals,mutation fraction <strong>of</strong> 0.1 and 200 generations were found as optimal values for running <strong>the</strong> GA.ResultsThe OSC capacity <strong>of</strong> <strong>the</strong> catalyst measured at 120°Cby CO-He-O 2 steps (Figure 1) reveals that after oxygenstep followed by helium step, CO 2 is produced afterswitching to CO, being supplied <strong>the</strong> necessary oxygenby ceria lattice (calculated to be 0.18 mmol O 2 /g). Thisagrees with CO-TPD (not shown), in which <strong>the</strong>preadsorbed CO is removed in form <strong>of</strong> CO 2 , with Figu re 1. CO, CO 2 and O 2 evolution during5%O 2 →He→5%CO steps at 120ºC.240

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