首页> 外文期刊>Applied Catalysis, B. Environmental: An International Journal Devoted to Catalytic Science and Its Applications >Catalytic wet air oxidation of phenol with modified activated carbons and Fe/activated carbon catalysts
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Catalytic wet air oxidation of phenol with modified activated carbons and Fe/activated carbon catalysts

机译:改性活性炭和铁/活性炭催化剂对苯酚的湿式催化氧化

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A commercial activated carbon was modified by different oxidative treatments to introduce different oxygen surface groups.A gentle oxidation in gas phase with a poor oxygen stream and a more severe oxidation in liquid phase with a HNO3 solution were used.The resulting activated carbons and the corresponding Fe-impregnated(2.5% Fe)ones were tested for the wet air oxidation of phenol.A trickle-bed reactor at 400 K and 8 atm of total pressure in a wide range of space time(20-320 g_(CAT)h/g_(Phenol))was used.The performance of the carbon supports and Fe catalysts was assessed by following phenol and TOC conversions,as well as the toxicity of the effluents.The fresh and used catalysts were characterized by nitrogen adsorption,TPD analyses and pH_(slurry).Gas-phase oxidation increased mainly the carbonyl/quinone groups and also carboxylic anhydride groups,whereas HNO3 oxidation significantly increased all the oxygen surface groups,but more significantly phenol,carbonyl/quinone and lactone groups.Regarding the preparation of the catalysts,Fe itself plays a promoting role in the formation or destruction of oxygen surface groups during calcinations,the latter being only observed when the activated carbon was oxidized with HNO3.Phenol and TOC conversions increased with the initial acidity of the catalyst.The introduction of Fe enhanced the activity and toxicity abatement at high enough space times,compared to an activated carbon with the same amounts of oxygen surface groups.This can be attributed to the increase in the acidity that the Fe itself provokes and the promoter role of Fe in the oxidation reaction of phenol.After the catalytic wet air oxidation process,surface area and micropore volume decreased whereas the amount of oxygen surface groups increased,as well as the total acidity,except for the activated carbon treated with HNO3.Also Fe dispersion significantly diminishes.However,the final surface distribution did not affect the catalyst activity.The presence of Fe reduced the detrimental effect of wet oxidation on the porous structure of the activated carbons.
机译:商用活性炭通过不同的氧化处理进行了改性,引入了不同的氧表面基团,使用了较弱的氧气在气相中进行了温和的氧化,并使用了HNO3的溶液对液相进行了更严格的氧化,从而得到了活性炭和相应的测试了浸有Fe的(2.5%Fe)酮对苯酚的湿空气氧化作用。滴滤床反应器在400 K和8 atm大气压下的宽时空范围内(20-320 g_(CAT)h /使用g_(Phenol))。通过以下苯酚和TOC转化率评估碳载体和Fe催化剂的性能以及废水的毒性。通过氮气吸附,TPD分析和pH_气相氧化主要增加羰基/醌基以及羧酸酐基团,而HNO3氧化显着增加所有氧表面基团,但酚,羰基/醌和内酯关于催化剂的制备,Fe本身在煅烧过程中对氧表面基团的形成或破坏起促进作用,后者仅在活性炭被HNO3氧化时才能观察到。苯酚和TOC的转化率随初始酸度增加而增加。与具有相同数量氧表面基团的活性炭相比,引入铁可以在足够高的空间时间下提高活性和减少毒性,这可以归因于铁本身引起的酸性增加和Fe在苯酚的氧化反应中起促进剂的作用。在催化湿式空气氧化过程之后,表面积和微孔体积减小,而氧表面基团的数量增加,总酸度增加,用HNO3处理的活性炭除外铁的分散也明显减少。但是,最终的表面分布并没有影响催化剂的活性。引起湿式氧化对活性炭多孔结构的不利影响。

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