Soledad Torres Calderon, N. B. Pampa-Quispe, Milda A. Cruz Huaranga
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引用次数: 1
摘要
本研究的目的是确定由上流式厌氧污泥毯(UASB)再生污泥获得的活性炭对H2S的吸附效率。H2S吸附系统在秘鲁大学Unión化学实验室进行,固定床塔入水量为4 L·min,吸附剂为36 g(6种不同的活性炭,根据热解温度(PT)和[M] KOH), AC温度为700 oC/1M, AC PT 500 oC/4M, AC PT 500 oC/1M, AC PT 700 oC/4和AC PT 600 oC/2.5 M,最后进行两次重复。采用体积氧化还原法测定其对H2S的吸附。22因子和32因子设计表明,PT对H2S吸附的影响最大,CI分别为99和90%;在PT 700℃和[1M] KOH条件下,活性炭停留20分钟,H2S去除率达到94%。在响应面预测模拟中,温度为635℃,活化剂为[2.6 M] KOH时,H2S去除率约大于96%。因此,污泥用活性炭吸附H2S是一种新的、可行的、可持续的环境替代方法。
Adsorption of hydrogen sulfide by activated carbon produced by regeneration of sludge from upflow anaerobic sludge blanket
The objective of this study was to determine the efficiency of H2S adsorption by activated carbon obtained from the regeneration of sludge from an Upflow Anaerobic Sludge Blanket (UASB). The H2S adsorption system was carried out in the Chemistry laboratory of the Universidad Peruana Unión, the inflow of the fixed bed towers was 4 L·min and 36 g of adsorbent media (6 different Active Carbon (AC), depending on Pyrolization temperatures (PT) and [M] KOH), AC at PT 700 oC/1M, AC PT 500 oC/4M, AC PT 500 oC/1M, AC PT 700 oC/4Mand AC PT 600 oC/2.5 M the last with two repetitions. The adsorption of H2S was determined by the volumetric oxidation-reduction method. The parameter of the greatest influence for the adsorption of H2S was PT at 99 and 90% CI respectively, demonstrated by 22 and 32 factorial designs; satisfactory elimination efficiencies of H2S were obtained and reached 94% during a retention time of 20 minutes of activated carbon at PT 700 oC and [1M] KOH. For the response surface prediction simulation, the optimized parameters for the removal of H2S approximately greater than 96% was at PT of 635 oC and activating agent of [2.6 M] KOH. Therefore, the adsorption of H2S by activated carbons for sludge is a new, viable and sustainable alternative for the environment.