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Adsorption removal of refractory organic matter in bio-treated municipal solid waste landfill leachate by anion exchange resins

机译:阴离子交换树脂吸附去除生物处理过的城市生活垃圾填埋场渗滤液中的难降解有机物

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Refractory organic matters (ROM) are the dominant organic matters in the membrane bioreactor -treated MSW landfill leachate, which are usually resistant to microbial degradation. Advanced membrane systems, which are expensive and generally for drinking water treatment, have to be used to make the final effluent meet discharge requirements. Anion exchange approach might be another option to remove ROM from leachate. In this study, the adsorption isotherms and kinetics were performed to illustrate the adsorption mechanism of anion exchange resins, 717 and D301R-Cl, for removing ROM from leachate. The results demonstrated that the adsorption isotherms for both resins were best represented by Langmuir model. The measured adsorption capacities of the 717 and D301-Cl resins were 39.84 and 35.84 mg COD g−1dry resin, respectively. The adsorption kinetics of ROM onto both resins followed a pseudo-second-order model and the measured rate constants were 0.00278 and 0.00236 g mg−1 min−1for the 717 and D301R-Cl resins, respectively. Additionally, intra-particle diffusion analysis indicated that the adsorption of ROM was controlled by both film and intra-particle diffusions. Based on the UV/Vis spectra and fluorescence EEM analysis, the UV humic-like substances were preferentially adsorbed on both resins, although more on D301R-Cl resin than 717 resin. Furthermore, column studies showed that the adsorption of ROM on both 717 and D301R-Cl resins can be divided into two phases: monolayer adsorption and multilayer adsorption, while the desorption demonstrated similar pattern but different efficiency due to the unique property of resin. The results suggested that the resins could remove ROM from leachate efficiently, while the practical progress needs to be further optimized.
机译:难降解有机物(ROM)是膜生物反应器处理的MSW垃圾填埋场渗滤液中的主要有机物,通常能抵抗微生物降解。必须使用昂贵且通常用于饮用水处理的先进膜系统,以使最终废水满足排放要求。阴离子交换方法可能是从渗滤液中去除ROM的另一种选择。在这项研究中,进行了吸附等温线和动力学,以说明阴离子交换树脂717和D301R-Cl从渗滤液中去除ROM的吸附机理。结果表明,两种树脂的吸附等温线最好用Langmuir模型表示。 717和D301-Cl树脂的吸附容量分别为39.84和35.84 mg COD g-1干树脂。 ROM在两种树脂上的吸附动力学遵循伪二级模型,对于717和D301R-Cl树脂,测得的速率常数分别为0.00278和0.00236 g mg-1 min-1。此外,颗粒内扩散分析表明,ROM的吸附受薄膜和颗粒内扩散的控制。根据UV / Vis光谱和荧光EEM分析,尽管两种D301R-Cl树脂比717树脂吸收更多的UV腐殖质样物质,但它们还是优先吸附在这两种树脂上。此外,柱研究表明,ROM在717和D301R-Cl树脂上的吸附可分为两个阶段:单层吸附和多层吸附,而解吸则表现出相似的模式,但由于树脂的独特性能,其效率不同。结果表明,该树脂可以有效地去除渗滤液中的ROM,但实际应用尚需进一步优化。

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