10.07.2015 Views

from first principles PP-I-1

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<strong>PP</strong>-III-70Decomposition and Steam Reforming of Methanolover Pd, Cu - CNT CatalystsMierczynski P. 1 , Vasilev K. 2 , Mierczynska A. 3 , Maniecki T.P. 11 Lodz University of Technology, Institute of General and Ecological Chemistry Zeromskiego116, 90-924 Lodz, Poland2 University of South Australia, Mawson Lakes Adelaide, South Australia SA 5095, Australia3 Ian Wark Research Institute, University of South Australia, Mawson Lakes, SA 5095,Adelaide, Australiamierczyn25@wp.plIntroductionHydrogen and fuel cells are a great opportunity to reduce emissions of toxic compounds suchas nitrogen oxides, carbon oxides, various hydrocarbons, and thus contribute to reducingenvironmental pollution and the possibly tackling global warming [1].Hydrogen is also one of the most important raw materials used for synthesis of chemicalproducts such as ammonia, hydrogen chloride, methanol, synthetic gasoline and it is alsoimportant as a propellant [2, 3]. Today the development of economically viable hydrogengeneration technology that will allow realization of these important future applications is amatter of urgency.ExperimentalThe monometallic palladium and copper catalysts supported on multi-walled carbonnanotubes were prepared by conventional impregnation methods. The multi-walled carbonnanotubes were prepared by CVD method based on catalytic decomposition of 5% ferrocenein toluene at two temperatures 850 and 925°C. The obtained support material wasimpregnated by appropriate aqueous solution of palladium chloride and copper (II) nitrate(V). Then the catalysts were dried and calcined 4h in air at 400°C. The physicochemicalproperties of catalysts were examined by BET, XRD, XPS and TPR methods. Chemisorptionuptakes were measured using ASAP 2020C apparatus <strong>from</strong> Micromeritics (USA). Theactivity tests in methanol steam reforming (SRM) and methanol decomposition were carriedout over palladium and copper catalysts in the temperature range 160 to 320°C in a flowquartz reactor under atmospheric pressure, molar ratio H 2 O/CH 3 OH = 1 and 2.224

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