شماره ركورد كنفرانس :
4689
عنوان مقاله :
Effect of Ce addition on catalytic performance of Ni/MCM-41 for hydrogen production via ethanol steam reforming
پديدآورندگان :
Rahmanzadeh Lida Babol Noshirvani University of Technology, P.O. , Taghizadeh Mazandarani Majid taghizadeh@nit.ac.ir Babol Noshirvani University of Technology, P.O.
كليدواژه :
Ethanol steam reforming , Ni , MCM , 41 , hydrogen , Fixed bed reactor.
عنوان كنفرانس :
اولين كنفرانس ملي كاتاليست ايران
چكيده فارسي :
Among different metals that used for ethanol steam reforming, Ni based catalysts has been commonly used since it is highly active and its cost is relatively low [1]. Product distribution and catalyst stability during steam reforming reaction are controlled by the type of utilized support. MCM-41 mesoporous molecular sieves have attracted much interest due to their noticeable surface areas and highly ordered pore structures [2]. In the present study, MCM-41 mesoporous material and highly active and quite stable Ni/MCM-41 catalyst were synthesized through direct hydrothermal and wet impregnation procedure, respectively. The effect of Ce impregnation into Ni/MCM-41 catalyst was evaluated in steam reforming of ethanol. Physical properties of obtained samples characterized by X-ray diffraction (XRD), Fourier transform infrared spectroscopy (FT-IR), Scanning electron microscopy (SEM) and H2 temperature program reduction (H2-TPR). The best catalytic results over ethanol steam reforming reaction, were obtained with Ce-Ni/MCM-41 catalyst, i.e. 94% ethanol conversion and 76.5% hydrogen selectivity. These results remained constant about 90 h time on stream and ethanol conversion decreased to 78% after 120 h.