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TOC removal from Methylene Blue aqueous solutions by adsorption and oxidation in the presence of coal fly ash

机译:在粉煤灰存在下通过吸附和氧化从亚甲基蓝水溶液中去除TOC

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摘要

Total organic carbon (TOC) removal from Methylene Blue aqueous solutions in the presence of coal fly ash was experimented comparing adsorption alone with oxidation potentially catalyzed by ash carried out with oxygen or ozone-enriched oxygen flow. The experiments were performed in continuous stirred tank reactor with fixed amounts of ash and dye solution, while gaseous flow was continuously bubbled in the solution. The results of TOC removal from 20mg/L Methylene Blue aqueous solution showed that in the case of adsorption alone the removal yield rose from 62 to 90% increasing ash dosage from 4.0 to 8.0g/L. However, in oxygen flow only the removal with 4.0g/L increased up to 72% and attained about 80% with ozone-enriched oxygen, yielding the best final values of TOC removed per unit mass of ash of 2.19 and 2.38mg/g, respectively. The kinetic results have been satisfactorily fitted by a pseudo-second-order model yielding a kinetic constant which strongly increased in adsorption alone increasing ash dosage, while a further increase with oxygen was observed only for 4.0g/L of ash. In the treatment with ozone, the removal process was slowed down.
机译:在粉煤灰的存在下,从亚甲基蓝水溶液中去除总有机碳(TOC)进行了实验,比较了单独吸附和可能由氧气或富含臭氧的氧气流进行的灰分催化的氧化。在具有固定量的灰分和染料溶液的连续搅拌釜反应器中进行实验,同时在溶液中连续鼓泡气流。从20mg / L亚甲蓝水溶液中TOC去除的结果表明,在单独吸附的情况下,去除率从62%上升到90%,将灰分剂量从4.0g / L增加到8.0g / L。但是,在氧气流中,只有4.0g / L的去除率增加到72%,而富含臭氧的氧气达到的去除率达到约80%,每单位质量灰分的TOC去除的最佳最终值分别为2.19和2.38mg / g,分别。动力学结果已通过拟二级模型令人满意地拟合,该模型产生的动力学常数在单独吸附增加灰分剂量的情况下会大大增加,而仅对4.0g / L灰分观察到随着氧气的进一步升高。在用臭氧处理中,去除过程减慢了。

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