活性炭-陶瓷球作为钌催化剂的载体:表征及树脂出水湿式催化氧化(CWAO

Wei-min Liu, YiQiang Hu, S. Tu
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引用次数: 0

摘要

通过在填料床反应器中对树脂出水进行湿式氧化,评价了活性炭-陶瓷球作为钌催化剂载体的性能。采用氮气吸附、CO化学吸附和扫描电镜对活性炭-陶瓷球和钌催化剂进行了表征。活性炭-陶瓷球的比表面积和总孔体积随着koh - carbon比的增大而增大,其中样品KC-120的比表面积和总孔体积分别高达1100 m2g-1和0.69 cm3 -1(碳含量为4.73 wt. %)。将RuCl3溶液浸渍在KC-120上,制备了活性炭陶瓷球负载钌催化剂,载体中钌的负载固定在1-5 wt. %的AC。作为最佳催化剂,3wt . % Ru/KC-120催化剂在树脂出水的CWAO中表现出较高的稳定性。在反应温度200℃、氧压1.5 MPa、水流速0.75 L h-1、氧流速13.5 L h-1条件下,化学需氧量(COD)和苯酚去除率分别为92%和96%。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Active Carbon-ceramic Sphere as Support of Ruthenium Catalysts: Characterization and Catalytic Wet Air Oxidation (CWAO) of Resin Effluent
Active carbon-ceramic sphere as support of ruthenium catalysts were evaluated through the catalytic wet air oxidation (CWAO) of resin effluent in a packed-bed reactor. Active carbon-ceramic sphere and ruthenium catalysts were characterized by N2 adsorption, CO chemisorption and SEM measurements. BET surface area and total pore volume of active carbon(AC) in active carbon-ceramic sphere increase with increasing KOH-to-Carbon ratio, AC in the sample KC-120 possesses values as high as 1100 m2g-1 and 0.69 cm3g -1(carbon percentage: 4.73 wt. %), especially. Active carbon-ceramic sphere supported ruthenium catalysts were prepared using the RuCl3 solution impregnation onto KC-120, the ruthenium loading was fixed at 1-5 wt. % of AC in the support. As optimum catalyst, the 3 wt. % Ru/KC-120 catalyst displays the higher stability in the CWAO of resin effluent during 30 days. Chemical oxygen demand (COD) and phenol removal were about 92% and 96% at the reaction temperature of 200 oC, oxygen pressure of 1.5 MPa, the water flow rate of 0.75 L h-1 and the oxygen flow rate of 13.5 L h-1.
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