首页> 外文期刊>Journal of Environmental Management >Degradation and mineralization of Bisphenol A (BPA) in aqueous solution using advanced oxidation processes: UV/H_2O_2 and UV/S_2O_8~(2-) oxidation systems
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Degradation and mineralization of Bisphenol A (BPA) in aqueous solution using advanced oxidation processes: UV/H_2O_2 and UV/S_2O_8~(2-) oxidation systems

机译:UV / H_2O_2和UV / S_2O_8〜(2-)氧化系统对双酚A(BPA)在水溶液中的降解和矿化

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摘要

This work reports on the removal and mineralization of an endocrine disrupting chemical, Bisphenol A (BPA) at a concentration of 0.22 mM in aqueous solution using inorganic oxidants (hydrogen peroxide, H_2O_2 and sodium persulfate, Na_2S_2O_8; S_2O_8~(2-)) under UV irradiation at a wavelength of 254 nm and 40 W power (I_0 = 1.26 × 10~(-6) E s~(-1)) at its natural pH and a temperature of 29 ± 3 ℃. With an optimum persulfate concentration of 1.26 mM, the UV/S_2O_8~(2-) process resulted in -95% BPA removal after 240 min of irradiation. The optimum BPA removal was found to be -85% with a H_2O_2 concentration of 11.76 mM. At higher concentrations, either of the oxidants showed an adverse effect because of the quenching of the hydroxyl or sulfate radicals in the BPA solution. The sulfate-based oxidation process could be used over a wider initial pH range of 3-12, but the hydroxyl radical-based oxidation of BPA should be carried out in the acidic pH range only. The water matrix components (bicarbonate, chloride and humic acid) showed higher scavenging effect in hydroxyl radical-based oxidation than that in the sulfate radical-based oxidation of BPA. UV/S_2O_8~(2-) oxidation system utilized less energy (307 kWh/m~3) EE/O in comparison to UV/H_2O_2 system (509 kWh/m~3) under optimum operating conditions. The cost of UV irradiation far outweighed the cost of the oxidants in the process. However, the total cost of treatment of persulfate-based system was much lower than that of H_2O_2-based oxidation system.
机译:这项工作报告了使用无机氧化剂(过氧化氢,H_2O_2和过硫酸钠,Na_2S_2O_8,S_2O_8〜(2-))在水溶液中以0.22 mM的浓度清除和矿化内分泌干扰物双酚A(BPA)。在其自然pH和29±3℃的温度下,以254 nm波长和40 W功率(I_0 = 1.26×10〜(-6)E s〜(-1))进行紫外线照射。在最佳过硫酸盐浓度为1.26 mM的情况下,UV / S_2O_8〜(2-)过程在照射240分钟后可去除-95%的BPA。发现最佳的BPA去除为-85%,H_2O_2浓度为11.76 mM。在较高浓度下,由于BPA溶液中的羟基或硫酸根基团被淬灭,氧化剂中的任何一种均显示出不利的影响。基于硫酸盐的氧化过程可以在3-12的较宽初始pH范围内使用,但是BPA的基于羟基自由基的氧化应仅在酸性pH范围内进行。水基成分(碳酸氢盐,氯化物和腐殖酸)在双酚A的羟基自由基氧化中表现出更高的清除效果。在最佳运行条件下,与UV / H_2O_2系统(509 kWh / m〜3)相比,UV / S_2O_8〜(2-)氧化系统使用的能量更少(307 kWh / m〜3)EE / O。在此过程中,紫外线照射的成本远远超过氧化剂的成本。但是,过硫酸盐基系统的总处理成本远低于H_2O_2基氧化系统。

著录项

  • 来源
    《Journal of Environmental Management》 |2015年第1期|266-275|共10页
  • 作者单位

    Department of Chemical Engineering, Indian Institute of Technology, Roorkee, Roorkee 247667, Uttarakhand, India;

    Department of Chemical Engineering, Indian Institute of Technology, Roorkee, Roorkee 247667, Uttarakhand, India;

    Department of Chemical Engineering, Indian Institute of Technology, Roorkee, Roorkee 247667, Uttarakhand, India;

  • 收录信息 美国《科学引文索引》(SCI);美国《化学文摘》(CA);
  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类
  • 关键词

    Persulfate; Peroxide; Humic acid; Electrical energy per order; Cost analysis;

    机译:过硫酸盐;过氧化物;腐植酸;每个订单的电能;成本分析;

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