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A hybrid microfiltration-granular activated carbon system for water purification and wastewater reclamation/reuse

机译:用于水净化和废水回收/再利用的混合微滤-颗粒活性炭系统

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Microfiltration (MF) does not remove color, natural organic matter (NOM) or synthetic organic chemicals (SOCs). It must be combined with other conventional technologies such as activated carbon adsorption to overcome some of these limitations. The effects of granular activated carbon (GAC) addition on MF performance in terms of quality (dissolved organic carbon) and quantity (permeate flux) were investigated. For a water purification experiment, MF showed preferential rejection of UV_(260)(about 30%) compared to dissolved organic carbon (DOC) (about 10%), indicating that the hydrophobic (aromatic) NOM fraction is more efficiently eliminated. In the hybrid MF membrane system, the removal efficiency of UV_(260)was about 60% compared to 30% by MF alone, and the decreasing rate of membrane permeability was much less than that of a conventional MF membrane process (about 70 days without GAC and 130 days with GAC). This may result from the reduced organic loading to the membrane due to the adsorption of NOM on the GAC. Using MF alone, the average removal efficiency of specific UV absorbance (SUVA, UV_(260)/DOC) was only 20%, but GAC addition increased SUVA removal efficiency up to 50-60%. In conclusion, the addition of GAC resulted in a decrease of hydrophobic NOM and trihalomethane precursors. For the wastewater reclamation/reuse experiment, removal efficiencies of DOC, chemical oxygen demand, total nitrogen, total phosphorus and turbidity were in the range of 42%, 53%, 15%, 13%, and 100% with the MF-GAC hybrid membrane system whereas 25-30%, 20-25%, 5-10%, 5-8% and 100% with the MF membrane alone, respectively. The hybrid process of membrane filtration and GAC was more effective in treatment efficiency than the single process.
机译:微滤(MF)不能去除颜色,天然有机物(NOM)或合成有机化学品(SOCs)。它必须与其他常规技术(例如活性炭吸附)结合使用,以克服其中一些限制。研究了颗粒活性炭(GAC)添加对MF性能的影响(质量(溶解的有机碳)和数量(渗透通量))。对于水净化实验,与溶解的有机碳(DOC)(约10%)相比,MF显示出对UV_(260)(约30%)的优先排斥,表明疏水性(芳族)NOM馏分得到了更有效的消除。在混合MF膜系统中,UV_(260)的去除效率约为60%,而单独使用MF的去除率为30%,并且膜渗透率的降低率远小于传统MF膜工艺的降低率(约70天GAC和GAC需要130天)。这可能是由于NOM在GAC上的吸附导致膜上有机负载减少所致。单独使用MF,特定UV吸收率(SUVA,UV_(260)/ DOC)的平均去除效率仅为20%,但是添加GAC将SUVA去除效率提高至50-60%。总之,添加GAC导致疏水NOM和三卤甲烷前体的减少。对于废水回收/再利用实验,MF-GAC混合动力装置的DOC去除效率,化学需氧量,总氮,总磷和浊度分别为42%,53%,15%,13%和100%膜系统,而单独使用MF膜则分别为25-30%,20-25%,5-10%,5-8%和100%。膜过滤和GAC的混合过程比单一过程更有效。

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