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Hydrodechlorination of 2,3,5-Trichlorophenol in Methanol/Water on Carbon Supported Pd-Rh Catalysts

机译:碳载Pd-Rh催化剂上甲醇/水中2,3,5-三氯苯酚的加氢脱氯

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Catalytic hydrodechlorination of 2,3,5-trichlorophenol was studied over 0.97%Pd/C, 0.98%Rh/C, and 0.8%Pd/0.19%Rh/C catalysts in various methanol/water mixtures. The catalysts were prepared by incipient-wetness impregnation of carbon support and characterized by Brunauer-Emmet-Teller (BET) surface area, temperature-programmed reduction (TPR), and X-ray diffraction (XRD) methods. Increasing calcination temperature caused an increase in crystallite size, whereas the initial hydrodechlorination reaction rate was decreased. The catalyst calcined at the calcination temperature (400°C) exhibited the highest catalytic performance; 0.97%Pd/C catalyst, which had the highest crystallite size, was found to be the most active and selective toward the formation of 2,3-dichlorophenol among other catalysts. The hydrodechlorination of 2,3,5-trichlorophenol was accelerated by increasing the percentage of methanol in water/methanol mixtures up to 50% (v/v), and beyond, where the reaction rate was slowed down. Hydrodechlorination activity of carbon-supported catalysts were in the order of Pd/C > Pd/Rh/C > Rh/C.
机译:在各种甲醇/水混合物中,分别在0.97%Pd / C,0.98%Rh / C和0.8%Pd / 0.19%Rh / C催化剂上研究了2,3,5-三氯苯酚的催化加氢脱氯。通过碳载体的初期湿润浸渍制备催化剂,并通过Brunauer-Emmet-Teller(BET)表面积,程序升温还原(TPR)和X射线衍射(XRD)方法进行表征。煅烧温度升高导致晶粒尺寸增加,而初始加氢脱氯反应速率降低。在煅烧温度(400℃)下煅烧的催化剂表现出最高的催化性能。发现具有最大微晶尺寸的0.97%Pd / C催化剂在其他催化剂中对形成2,3-二氯苯酚最具活性和选择性。通过将甲醇在水/甲醇混合物中的百分比提高到50%(v / v),甚至超过反应速度减慢的速度,可以加速2,3,5-三氯苯酚的加氢脱氯。碳载催化剂的加氢脱氯活性为Pd / C> Pd / Rh / C> Rh / C。

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