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Steam Reforming of Glycerol for Hydrogen Production over Ni Catalysts Supported by CeO_2-Al_2O_3 Xerogel

机译:CEO_2-AL_2O_3 Xerogel支持的Ni催化剂氧化甘油的蒸汽重整

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The Ni catalysts supported by CeO_2-Al_2O_3 xerogel were prepared by sol-gel method. The effect of hydrolysis ratio (R at 16.5 and 165) on CeO_2-Al_2O_3 textural properties and phase formation were investigated. The results revealed that the porous texture and the Ni crystalline phase can be controlled by adjusting the hydrolysis ratio. A high surface area and small Ni crystallite size were obtained by using the hydrolysis ratio of 16.5. For hydrogen production via glycerol steam reforming, the Ni catalyst supported on CeO_2-Al_2O_3 xerogel showed a better catalytic performance than that supported on commercial alumina. The promoted Ni catalyst supported on commercial alumina suddenly deactivated after first 12 h, whereas that on Al_2O_3 xerogel performed the catalytic stability more than 20 h. This demonstrated that the catalyst prepared by sol-gel method is an interesting catalyst for using in the glycerol steam reforming because of the catalytic stability enhancement.
机译:通过溶胶 - 凝胶法制备CeO_2-Al_2O_3 Xerogel支持的Ni催化剂。研究了水解比(16.5和165时)对CeO_2-Al_2O_3纹理性质和相形成的影响。结果表明,可以通过调节水解比来控制多孔纹理和Ni结晶相。通过使用16.5的水解率获得高表面积和小的Ni微晶尺寸。对于通过甘油蒸汽重整的氢气产生,CeO_2-Al_2O_3 Xerogel上负载的Ni催化剂显示出比商业氧化铝支持的更好的催化性能。在前12小时后,在商业氧化铝上突然停用的促进的Ni催化剂,而在Al_2O_3 Xerogel上,催化稳定性大于20小时。这证明了通过溶胶 - 凝胶法制备的催化剂是由于催化稳定性增强而在甘油蒸汽重整中使用的有趣催化剂。

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