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Mercury oxidation catalyzed by carbonaceous surfaces: Impact of surface area and water vapor

机译:碳质表面催化的汞氧化:表面积和水蒸气的影响

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This study evaluated the oxidation of mercury under simulated coal-fired power plant flue gas conditions. The effect of surface area and H2O on mercury oxidation catalyzed by the surface of activated carbon as well as on the performance of activated carbon for mercury uptake is evaluated under different experimental conditions. Approximately 17-20 μg/m~3 of elemental mercury in a simulated flue gas was fed at a flow rate of 1 L/min to a 20 cm long and 22 mm inner diameter quartz tube used as a fixed-bed reactor. The reactor was kept in a 50 cm long tube furnace, which was used to maintain the temperature of the fixed bed at 140 °C. In every experimental run, 40 mg of activated carbon was charged into the quartz tube along with 4 gm of glass beads, which were used to provide support for the sorbent. Prior to use, glass beads were washed with distilled water and heated to 500 °C for 4 hours.
机译:该研究评估了模拟燃煤发电厂烟气条件下汞的氧化。在不同的实验条件下评价表面积和H2O对由活性炭表面催化的汞氧化对汞摄取的性能的影响,并在不同的实验条件下评价。在模拟烟道气中大约17-20μg/ m〜3的元素汞以1升/分钟的流速进给至20厘米长,22mm内径石英管用作固定床反应器。将反应器保持在50cm长管炉中,用于将固定床的温度保持在140℃。在每个实验过程中,将40mg活性炭加入石英管中,与4克的玻璃珠一起加入石英管中,用于为吸附剂提供载体。在使用之前,用蒸馏水洗涤玻璃珠,并加热至500℃持续4小时。

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