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II International Symposium on Carbon for Catalysis ABSTRACTS

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OP-I-11<br />

DENITROGENATION ACTIVITY OF Cu-Mn CATALYSTS SUPPORTED ON<br />

MINERAL, CARBON AND MINERAL CARBON MATERIALS<br />

Kulazynski M., Walendziewski J., Bratek K.<br />

Faculty of Chemistry, Department of Fuels Chemistry and Technology,<br />

Wroclaw University of Technology, 50-344 Wroclaw, ul. Gdanska 7/9, Poland<br />

e-mail: marek.kulazynski@pwr.wroc.pl<br />

Three groups of catalytic techniques, known as deNO x processes, can be applied <strong>for</strong> the<br />

removal of nitrogen oxides: no-selective reducti<strong>on</strong>, selective catalytic reducti<strong>on</strong> and<br />

decompositi<strong>on</strong>. All of them eliminate nitrogen oxides by c<strong>on</strong>verting them to nitrogen, with<br />

water, carb<strong>on</strong> dioxide and/or oxygen appearing as n<strong>on</strong>toxic byproducts.<br />

Four different supports were used in preparati<strong>on</strong> of DeNOx catalysts: natural<br />

silicaalumina, active coke (grains), mineral carb<strong>on</strong> (m<strong>on</strong>oliths) and cordierite m<strong>on</strong>oliths<br />

coated with active carb<strong>on</strong>. On the base of our earlier studies we have found that the optimal<br />

active phase compositi<strong>on</strong> <strong>for</strong> carb<strong>on</strong> c<strong>on</strong>taining catalysts is 3 wt % Mn and 1.75 wt % Cu.<br />

Catalysts were prepared by dry impregnati<strong>on</strong> metals using salt soluti<strong>on</strong>s of Cu and Mn and<br />

the c<strong>on</strong>centrati<strong>on</strong> of the used salt soluti<strong>on</strong>s allowed obtaining the optimal metals c<strong>on</strong>tent in<br />

the final catalysts. The base physicochemical properties, mechanical strength, porous<br />

structure and specific surface area of the catalysts were determined.<br />

The activity studies were realized in laboratory flow equipment composed of model gas<br />

feeding system and dosage system, reactor and analyzer <strong>for</strong> determining the c<strong>on</strong>tent of nitric<br />

oxide in the gas. The c<strong>on</strong>diti<strong>on</strong>s of the process were: temperature range from 100 o C to<br />

200 o C, <strong>for</strong> carb<strong>on</strong> c<strong>on</strong>taining catalysts and 100-450 o C <strong>for</strong> mineral catalyst, GHSV=5 000 h -1 .<br />

Model gas c<strong>on</strong>tained 6 vol. % O 2 , NO c<strong>on</strong>tent was changed in the range 400- 600 ppm, ratio<br />

NH 3 /NO was equal to 1, and water vapor c<strong>on</strong>tent in the model gas was ~ 1 %. Compositi<strong>on</strong> of<br />

model gas and reacti<strong>on</strong> mixture was analyzed using the MSI 2500 Analyzer.<br />

Active coke, grain <strong>for</strong>m, was from commercial delivery (Hajnówka, Poland), and its<br />

basic properties were as follows, iodine number 200 mg I 2 /g., C/H/N/S compositi<strong>on</strong>:<br />

96/0.9/09/0.5 wt %, respectively. The prepared mineral-carb<strong>on</strong> m<strong>on</strong>oliths c<strong>on</strong>tained 30 wt %<br />

of natural clay (as a binder). They were also characterized by dimensi<strong>on</strong>s, 1000x100x100<br />

mm, wall thickness 2.7 mm and 121 (cells) l<strong>on</strong>gitudal channels (11x11). Pore volume attained<br />

value 0.69 cm 3 /g and specific surface area ca 415 m 2 /g, mainly micropores. Natural clay ,<br />

58

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