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Treatment Performance of Photocatalysis/H_2O_2/Metal Membrane Process for Organics Removal

机译:光催化/ H_2O_2 /金属膜工艺去除有机物的处理性能

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The objective of this study is to evaluate the performance of photocatalysis/hydrogen peroxide/metal membrane system. Metal membrane for the separation of TiO_2 particles was used in an experiment and nominal pore size is 0.5 μm. Hydrogen peroxide was tested as oxidants. The removal efficiency of COD_(Ce) and color for initial hydrogen peroxide concentration increases rapidly with an increase in the hydrogen peroxide concentration up to 50 mg/L. The removal efficiency of of COD_(Cr) and color for 50 mg/L of initial hydrogen peroxide concentration was about 95 % and 98 %, respectively. However, the addition of hydrogen peroxide over 50 mg/L inhibits the system efficiency. The addition of hydrogen peroxide in UV/TiO_2 system enhanced removal efficiency of COD_(Cr) and color compared to no addition of hydrogen peroxide. This may be ascribed to capture the electrons ejected from TiO_2 and to produce OH radicals. The application of metal membrane in UV/ TiO_2/H_2O_2 system enhanced removal efficiency of COD_(Cr) and color due to the adsorption of metal membrane surface as well as the production of OH radical. In application of metal membrane with nominal pore size 0.5 μm, TiO_2 particles were effectively separated from the treated water by metal membrane rejection. Photocatalytic metal membrane was much smaller resistance than these of humic acid, TiO_2 and humic acid/ TiO_2 due to humic acid degradation of photocatalytic reaction.
机译:这项研究的目的是评估光催化/过氧化氢/金属膜系统的性能。在实验中使用了用于分离TiO_2颗粒的金属膜,标称孔径为0.5μm。测试过氧化氢作为氧化剂。随着过氧化氢浓度的增加,COD_(Ce)和颜色对初始过氧化氢浓度的去除效率迅速提高,直至50 mg / L。初始过氧化氢浓度为50 mg / L时,COD_(Cr)和色料的去除效率分别约为95%和98%。但是,添加超过50 mg / L的过氧化氢会抑制系统效率。与未添加过氧化氢相比,在UV / TiO_2系统中添加过氧化氢可提高COD_(Cr)和颜色的去除效率。这可能归因于捕获从TiO_2喷射的电子并产生OH自由基。金属膜在UV / TiO_2 / H_2O_2体系中的应用由于金属膜表面的吸附以及OH自由基的产生,提高了COD_(Cr)和颜色的去除效率。在标称孔径为0.5μm的金属膜的应用中,通过金属膜的排斥作用,可以有效地将TiO_2颗粒与处理后的水中分离。由于腐殖酸降解光催化反应,光催化金属膜的电阻比腐殖酸,TiO_2和腐殖酸/ TiO_2的电阻小得多。

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