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Adsorption of low-concentration H2S on manganese dioxide-loaded activated carbon

机译:低浓度硫化氢在负载二氧化锰的活性炭上的吸附

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Manganese dioxide-loaded activated carbon (AC) absorbents (MnO2/AC) were prepared and characterized by XRD, N-2 adsorption-desorption, BET, and SEM. A mixture of H2S and N-2 was used to evaluate the performance of absorbents in a fixed adsorption bed for H2S removal. Results show that the specific surface area decreased from 580.4 to 390.9 m(2) g(-1) with modification of manganese dioxide and the topography changed significantly. A suitable H2S removal activity was obtained with a manganese dioxide-to-AC ratio of 1: 1, drying temperature of 393 K, and drying time of 24 h. At the adsorption temperature of 313 K and a flow rate of 20 ml min(-1), the H2S breakthrough capacity of 110.7 mg g(-1) was observed. Comparing with the unmodified AC, H2S breakthrough capacity increased by 96.9 mg g(-1). The kinetics of adsorptive removal of H2S over the MnO2/AC adsorbent followed the Bangham model, ln 0.1181/0.1181-q = 3.002t(1.352).
机译:制备了负载二氧化锰的活性炭(AC)吸收剂(MnO2 / AC),并通过XRD,N-2吸附-解吸,BET和SEM对其进行了表征。使用H2S和N-2的混合物评估固定吸附床中用于去除H2S的吸收剂的性能。结果表明,比表面积从580.4减少到390.9 m(2)g(-1),并修饰了二氧化锰,并且形貌发生了显着变化。二氧化锰与AC的比例为1:1,干燥温度为393 K,干燥时间为24 h,获得了合适的H2S去除活性。在313 K的吸附温度和20 ml min(-1)的流速下,观察到H2S穿透能力为110.7 mg g(-1)。与未改性的AC相比,H2S的突破能力增加了96.9 mg g(-1)。 MnO2 / AC吸附剂对H2S的吸附去除动力学遵循Bangham模型,ln 0.1181 / 0.1181-q = 3.002t(1.352)。

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