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Preparation and performance of activated carbon-supported zinc ferrite absorbent for hot-gas cleaning

机译:活性炭负载锌铁氧体吸收剂的制备及性能进行热气净化

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An efficient absorbent of hydrogen sulfide for hot-gas cleaning was developed. In order to increase the efficiency of the absorbent, activated carbon-supported ferrite was prepared and the absorption behavior of the absorbent was examined using a fixed bed reactor and a thermogravimetric balance. Activated carbon-supported ferrites could be prepared at a much lower calcination temperature (400 °C) than the typical preparation temperature of ca. 1000 °C for a dry process. These ferrites have high surface areas up to 663 m~2/g. Breakthrough behavior was obtained with a fixed-bed flow reactor, with almost complete absorption of hydrogen sulfide from 5000 ppm to nearly zero level being achieved at an absorption temperature of 400 °C. Utilization of Zn and Fe reached nearly 100 %, but ferrite prepared without activated carbon in a similar manner, afforded metal utilization efficiency of about 50 %. The results obtained with a thermogravimetric balance indicated that the initial hydrogen sulfide absorption rate of the activated carbon-supported ferrite was about ten times higher than that of the ferrite prepared by the dry process. Regeneration of activated carbon-supported zinc ferrite can successfully achieve.
机译:开发了一种有效的硫化氢用于热气清洁的吸收剂。为了提高吸收剂的效率,制备活性炭负载的铁素体,使用固定床反应器和热重度平衡检查吸收剂的吸收行为。活化的碳支撑的铁氧体可以在比CA的典型制备温度下更低的煅烧温度(400℃)。干法1000°C。这些铁氧体具有高达663m〜2 / g的高表面积。用固定床流动反应器获得突破性行为,几乎完全吸收5000ppm的硫化氢,在吸收温度为400℃的吸收温度下实现几乎零水平。利用Zn和Fe达到近100%,但铁氧体在没有活性炭的情况下制备类似的方式,得到的金属利用效率约为50%。用热重分析获得的结果表明,活性炭负载的铁氧体的初始硫化氢吸收率约于干法制备的铁素体高约10倍。活性炭支持的锌铁素体的再生成功达到。

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