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Removal of selected hazardous organic compounds by electro-Fenton oxidation process.

机译:通过电子芬顿氧化工艺去除选定的有害有机化合物。

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摘要

Electro-Fenton oxidation process is used to remove selected hazardous organic compounds from aqueous solutions. Hydrogen peroxide (H2O 2) is electro-generated by the reduction of dissolved oxygen in acidic solutions.{09}The optimal conditions are cathodic potential of −0.5V vs. saturated calomel electrode (SCE), oxygen mass flow rate of 8.2 × 10 −2 mol/min, and pH 2. The average current density and current efficiency are 6.4 A/m2 and 81%, respectively. Fe2+ is electro-regenerated from ferric salt or Fenton's iron sludge. The optimal cathodic potential is −0.1 V vs. SCE. At this potential, the average current density is in linear proportion to [Fe3+] 0, showing a slope of 8.48 × 10−3 (A/m 2)(mg/L)−1. The average current efficiency varies with [Fe3+]0, i.e., 75% at [Fe3+] 0 = 100 mg/L and 96∼98% at [Fe3+]0 ≥ 500 mg/L. Fe2+ can also be effectively regenerated from Fenton's iron sludge. The Fenton oxidation process can effectively degrade all selected polycyclic aromatic hydrocarbons (PAHs), namely, naphthalene, fluorene, phenanthrene, fluoranthene, pyrene, and anthracene. A “time-squared” kinetic model, C = C0 exp(− kobst2), is developed to describe the reaction kinetics in the continuous dosing mode. Methanol and ethanol inhibit the PAHs degradation by competing for hydroxyl radicals. The Fenton oxidation process is also used to degrade selected chlorinated aliphatic hydrocarbons (CAHs), namely, tetrachloroethylene (PCE), trichloroethylene (TCE), 1,1-dichloroethylene (DCE), and chloroform. PCE, TCE and DCE can be effectively degraded, while chloroform is difficult to degrade due to their structure difference. The dosing mode of H2O2 and Fe2+ significantly affects the reaction efficiency. Trichloroacetic and dichloroacetic acids are the major byproducts in the oxidation of PCE and TCE, respectively. Based on the byproducts identified, possible reaction pathways are established and kinetically modeled. Electro-Fenton oxidation process is more efficient than conventional Fenton oxidation process due to the continuous regeneration of Fe2+ at the cathode. This demonstrates that the electro-Fenton oxidation process is an effective technology for the removal of hazardous organic contaminants from aqueous solutions.
机译:电子芬顿氧化工艺用于从水溶液中去除选定的有害有机化合物。过氧化氢(H 2 O 2 )是通过还原酸性溶液中的溶解氧而产生的。{09}最佳条件是阴极电位为-0.5V vs饱和甘汞电极(SCE),氧气质量流量为8.2×10 -2 mol / min和pH为2。平均电流密度和电流效率为6.4 A / m 2 < / super>和81%。 Fe 2+ 是从铁盐或芬顿氏铁污泥中电再生的。最佳阴极电位为-0.1 V vs. SCE。在此电位下,平均电流密度与[Fe 3 + ] 0 成线性比例,斜率为8.48×10 -3 (A / m 2 )(mg / L) -1 。平均电流效率随[Fe 3 + ] 0 的变化而变化,即[Fe 3 + ] 0时为75%。 sub> = 100 mg / L,[Fe 3 + ] 0 ≥500 mg / L时为96〜98%。 Fe 2 + 也可以从芬顿的铁污泥中有效地再生。 Fenton氧化过程可以有效降解所有选定的多环芳烃(PAH),即萘,芴,菲,荧蒽,pyr和蒽。一个“时间平方”动力学模型, C = C 0 exp(- k obs t 2 )用于描述连续加料模式下的反应动力学。甲醇和乙醇通过竞争羟基自由基来抑制PAHs降解。 Fenton氧化过程还用于降解选定的氯化脂肪族烃(CAH),即四氯乙烯(PCE),三氯乙烯(TCE),1,1-二氯乙烯(DCE)和氯仿。 PCE,TCE和DCE可以有效降解,而氯仿由于结构差异而难以降解。 H 2 O 2 和Fe 2 + 的加料方式显着影响反应效率。三氯乙酸和二氯乙酸分别是PCE和TCE氧化的主要副产物。基于所鉴定的副产物,建立可能的反应途径并进行动力学建模。由于在阴极处不断地再生Fe 2 + ,因此电芬顿氧化工艺比常规芬顿氧化工艺更有效。这证明了电芬顿氧化工艺是从水溶液中去除有害有机污染物的有效技术。

著录项

  • 作者

    Qiang, Zhimin.;

  • 作者单位

    University of Delaware.;

  • 授予单位 University of Delaware.;
  • 学科 Engineering Environmental.; Environmental Sciences.
  • 学位 Ph.D.
  • 年度 2002
  • 页码 239 p.
  • 总页数 239
  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类 环境污染及其防治;环境科学基础理论;
  • 关键词

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