首页> 美国卫生研究院文献>Frontiers in Chemistry >Advanced oxidation of the commercial nonionic surfactant octylphenol polyethoxylate Triton™ X-45 by the persulfate/UV-C process: effect of operating parameters and kinetic evaluation
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Advanced oxidation of the commercial nonionic surfactant octylphenol polyethoxylate Triton™ X-45 by the persulfate/UV-C process: effect of operating parameters and kinetic evaluation

机译:过硫酸盐/ UV-C工艺可对商用非离子表面活性剂辛基酚聚乙氧基化物Triton™X-45进行高级氧化:操作参数和动力学评估的影响

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摘要

This study explored the potential use of a sulfate radical (SO·−4)-based photochemical oxidation process to treat the commercial nonionic surfactant octylphenol polyethoxylate (OPPE) Triton™ X-45. For this purpose, the effect of initial S2O2−8 (0–5.0 mM) and OPPE (10–100 mg/L) concentrations on OPPE and its organic carbon content (TOC) removal were investigated at an initial reaction pH of 6.5. Results indicated that very fast OPPE degradation (100%) accompanied with high TOC abatement rates (90%) could be achieved for 10 and 20 mg/L aqueous OPPE at elevated S2O2−8 concentrations (≥2.5 mM). S2O2−8/UV-C treatment was still capable of complete OPPE removal up to an initial concentration of 40 mg/L in the presence of 2.5 mM S2O2−8. On the other hand, TOC removal efficiencies dropped down to only 40% under the same reaction conditions. S2O2−8/UV-C oxidation of OPPE was also compared with the relatively well-known and established H2O2/UV-C oxidation process. Treatment results showed that the performance of S2O2−8/UV-C was comparable to that of H2O2/UV-C oxidation for the degradation and mineralization of OPPE. In order to elucidate the relative reactivity and selectivity of SO·−4 and HO·, bimolecular reaction rate coefficients of OPPE with SO·−4 and HO· were determined by employing competition kinetics with aqueous phenol (47 μM) selected as the reference compound. The pseudo-first-order abatement rate coefficient obtained for OPPE during S2O2−8/UV-C oxidation (0.044 min−1) was found to be significantly lower than that calculated for phenol (0.397 min−1). In the case of H2O2/UV-C oxidation however, similar pseudo-first-order abatement rate coefficients were obtained for both OPPE (0.087 min−1) and phenol (0.140 min−1). From the kinetic study, second-order reaction rate coefficients for OPPE with SO·−4 and HO· were determined as 9.8 × 108 M−1 s−1 and 4.1 × 109 M−1 s−1, respectively. The kinetic study also revealed that the selectivity of SO·−4 was found to be significantly higher than that of HO·.
机译:这项研究探索了使用基于硫酸根(SO --- 4)的光化学氧化工艺来处理商用非离子表面活性剂辛基酚聚乙氧基化物(OPPE)Triton™X-45的潜在用途。为此,研究了初始S2O 2- 8(0–5.0 mM)和OPPE(10–100 mg / L)浓度对OPPE及其有机碳含量(TOC)去除的影响。初始反应pH为6.5。结果表明,当S2O 2 8浓度升高(≥2.5)时,10和20 mg / L水性OPPE可以实现非常快速的OPPE降解(100%)和较高的TOC减少率(90%)。毫米)。在存在2.5 mM S2O 2- 8的情况下,S2O 2- 8 / UV-C处理仍能够完全去除OPPE,直至初始浓度为40 mg / L 。另一方面,在相同反应条件下,TOC去除效率仅下降至40%。还比较了OPPE的S2O 2- 8 / UV-C氧化与相对著名的H2O2 / UV-C氧化工艺。处理结果表明,S2O 2- 8 / UV-C的氧化性能与H2O 2 / UV-C的氧化性能相当,可降解OPPE。为了阐明SO ·- 4 和HO ·的相对反应性和选择性,OPPE与SO 的双分子反应速率系数通过采用竞争动力学与选择为参考化合物的苯酚水溶液(47μM)来确定·− 4 和HO ·。在S 2 O 2 − 8 / UV-C氧化过程中(0.044 min -1 )明显低于苯酚计算值(0.397 min -1 )。但是,在H 2 O 2 / UV-C氧化的情况下,两种OPPE均获得相似的伪一级去除率系数(0.087 min - 1 )和苯酚(0.140 min -1 )。从动力学研究中,确定SO ·- 4 和HO ·的OPPE的二阶反应速率系数为9.8×10 8 M −1 s -1 和4.1×10 9 M -1 s < sup> -1 。动力学研究还表明,SO ·- 4 的选择性显着高于HO ·

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