催化氧化法在钻井废水处理中的应用

在油气田深井钻探过程中产生的钻井液,经固-液分离处理后产生的废水具有化学需氧量高、色度高、矿化度高、含油量高等特点,须进一步进行处理。采用Fenton试剂对钻井废水进行了催化氧化处理实验。结果表明,处理后, 废水中化学需氧量(COD)去除率可达82%,色度去除率为98.5%。H2O2/Fe2+投量摩尔比、H2O2/初始COD摩尔比、pH值和反应时间对废水COD、色度的去除率均有较大影响。用Fenton试剂催化氧化工艺处理聚磺体系钻井废水还具有处理效率高、操作简便、适用范围广等优点。     

UV/Fenton法处理高浓度香料废水的试验研究

研究了UV/Fenton法处理高浓度废水的新技术以及有关影响因素。试验:pH在2－4，COD／H2O2＝1：1.5,Fe^2 浓度为1.7g／L的条件下，反应时间90min，COD去除率可达99.6%。     

染料废水物理化学处理技术的现状与进展

本文按吸附、膜滤、混凝、氧化刑、离子交换、Fenton试剂、光催化氧化、湿式氧化、电化学等方法分别论述了染料废水物理化学处理技术的现状和发展趋势。     

光助氧化技术在水处理中应用

对UV／H2O2技术、UV／O3技术、UV／O3／H2O2技术、photo—Fenton技术以及UV／TiO2技术进行了总结,对不同技术的原理、研究进展及应用进行了评述,并对今后光助氧化技术的研究方向提出了一些建议。     

Fenton及电-Fenton处理难降解有机废水技术

Fenton法与电-Fenton法属于高级氧化技术(Advanced Oxidation Technologjes,AOTs),是由H2O2与催化剂Fe2 所构成的氧化体系.在Fenton体系中,H2O2在Fe2 的催化剂作用下,能产生两种活泼的氢氧自由基(HO2·和·OH),从而引发和传播自由基链反应,加快有机物和还原性物质的氧化.本文简要介绍了Fenton法与电-Fenton反应的机理和应用在催化氧化难降解废水领域中的处理技术及研究进展.     

氧化法处理水中酚的研究方法综述

目前氧化法处理含酚废水的方法有化学氧化法即臭氧氧化法、Fenton试剂氧化法等，酶催化氧化法以及光化学氧化法即光敏化氧化、光催化氧化法等；分析了它们的优势及存在的问题；并提出了今后的研究方向，即臭氧-生物活性炭、臭氧辐射、臭氧-H2O2技术，水溶性酶制剂连接到固体载体上制成固化酶，H2O2－BAC、O3－H2O2－BAC联用技术等。     

O2-Fenton试剂处理对氨基苯磺酸废水的探讨

利用由O2和Fenton试剂组成的类Fenton系统处理对氨基苯磺酸废水,取得了很好的降解效果.当FeSO4(10g/L)投加量为1.2mL、H2O2(3%)投加量为3mL时,COD去除率可达到70%.     

高级氧化技术处理难降解有机废水

介绍了高级氧化技术处理难降解有机废水的原理及应用情况,如湿式氧化法、Fenton法、光化学法、电化学法、臭氧氧化法等;并分别指出各高级氧化技术在处理难降解有机废水过程中存在的问题和发展趋势。     

改进的Fenton法处理难降解有机废水应用进展

系统分析了各种改进的Fenton氧化技术对有机物的降解机理,概述了近年来改进的Fenton法在处理难降解的有机废水中的应用进展,并展望了改进Fenton氧化技术未来的发展趋势和研究重点,以期为Fenton氧化技术在处理难降解有机废水中的研究和应用提供参考。     

Fenton试剂与改性凹凸棒石联合处理微污染水中苯酚的实验研究

研究了Fenton试剂联合聚二甲基二烯丙基氯化铵（PDMDAAC）改性凹凸棒石对模拟微污染水中苯酚的去除效果。考察了pH值、反应时间、投加量、温度等因素对苯酚去除效果的影响。结果表明：先采用Fenton试剂氧化再用改性凹凸棒石吸附对微污染水中苯酚具有较好的去除效果，在pH=9、温度为25℃、改性凹凸棒石投加量为5g／L、吸附时间20min的条件下，苯酚去除率达98．2％。     

Fenton氧化法在废水处理中的应用

Fenton氧化技术在水处理中的运用正得到越来越多的关注，本文总结了Fenton氧化技术的发展和研究现状，包括Fenton试剂反应机理，影响因素（pH,[Fe^2 ]/[H2O2],反应温度，投加方式，化学絮凝），反应动力学，改良形式等，并认为Fenton氧化技术是一种很有应用前景的废水处理技术。     

高浓度油田压裂废水降低CODCr的预处理方法

针对高浓度油田压裂废水黏度高、浊度大、含油量高等特点,强化预处理工艺,降低CODCr值。文章通过实验证明了强氧化剂(Fenton试剂)与混凝剂PAC+PAM相结合的工艺可有效降低高浓度含油废水CODCr值,进而通过Fenton试剂与混凝剂的投药量、pH值等因素对高浓度油田压裂废水的影响进行分析,得出采用该化学预处理方法出水水质清澈,可直接进入生化处理系统进行后续处理。     

Fenton试剂处理六氯苯废水的试验研究

研究了采用Fenton法处理六氯苯模拟废水的方法以及Fenton法处理六氯苯的影响因素。研究结果显示:在H2O2(30%)投加量为500mg/L,Fe2 投加量为1000mg/L,pH=2.5的条件下,经过4h的反应,废水中HCB去除率可达51.65%。     

Treatment of IGCC power station effluents by physico-chemical and advanced oxidation processes

The aim of this work was to improve the quality of aqueous effluents coming from the Gasification Unit in an Integrated Gasification Combined Cycle (IGCC) Thermoelectric Power Station, with the purpose of fulfilling the future more demanding normative. To this end, an integral wastewater treatment including coagulation, flocculation, neutralization, photocatalytic oxidation, and ion-exchange has been studied. A final scheme has been proposed to remove pollutants. All the parameters of the treated wastewater are below pouring specifications. In the first stage, the wastewater was treated with CaCl2 (optimal dose=11 g CaCl2/g F-) as coagulant and a commercial anionic polyelectrolyte (optimal dose=0.02 g/g F-) as flocculant to remove fluoride ions (99%) and suspended solids (92%). The water was then neutralized, improving the degree of transmission of ultraviolet light, allowing the faster photo-degradation of pollutants. The photochemical study included different systems (H2O2, UV/H2O2, Fenton, Fenton-like, UV/Fenton, UV/Fenton-like and UV/H2O2/O2). In the Fenton-like system, the influence of two parameters (initial concentration of H2O2 and amount of Cu(II)) on the degradation of cyanide and formate (taken as the reference of the process) was studied. Experimental results were fit using neural networks (NNs). Results showed that the photocatalytic process was effective for total cyanide destruction after 60 min, while 180 min was needed to remove 80% of formates. However, a more simple system with UV/H2O2/O2 yields similar results and is preferred for industrial application due to fewer complications. Finally, an ion-exchange process with Amberlite IRA-420 was proposed to remove the excess of chlorides added as a consequence of the initial coagulation process.     

油田含油污水高级氧化技术研究

以气浮—过滤预处理后的污水为处理对象,通过臭氧氧化与Fenton氧化两种方法处理油田含油污水。经实验验证:Fenton在pH为4,H2O2初始浓度为0.08mol/L,Fe2+与H2O2的摩尔比为1:10,H2O2与CODCr的质量比为1:1,反应时间为60min的条件下,去除率达54.3%(CODCr100mg/L),可达到GB8978-1996《污水综合排放标准》二级标准。     

Fenton法处理垃圾渗滤液技术的研究及应用

Fenton法是一种非常有效的高级氧化技术,已经逐渐应用于含有难降解有机物废水处理领域中。本文论述了Fenton法、Photo-Fenton法、电-Fenton以及类Fenton技术处理垃圾渗滤液的研究进展;分析了不同技术产生羟基自由基的原理、技术的主要影响因素以及技术的研究方向,并指出了这些技术在工程化应用方面的关键技术要点,旨在为该技术的工程化应用提供实践支持。     

Fenton氧化法处理难降解有机废水的研究进展

Fenton氧化法在处理难降解有机污染物时具有独特的优势，是一种很有应用前景的废水处理技术。在阐述传统Fenton氧化、光Fenton氧化、电Fenton氧化技术的基础上，介绍了三种氧化技术在难降解有机废水处理中的应用现状，并对其在废水处理中的优势、存在问题和研究方向作出了系统评述。     

Regeneration of industrial district wastewater using a combination of Fenton process and ion exchange—A case study

Regeneration studies of wastewater effluent from an organized industrial district (OID) for possible reuse in textile industry as process water was investigated. Advanced treatment methods including Fenton process, polyaluminium chloride (PAC) coagulation and ion exchange were applied on OID effluent. In Fenton process removal efficiencies for suspended solids (SS), chemical oxygen demand (COD), SAC₄₃₆ (spectral absorption coefficient), SAC₅₂₅ and SAC₆₂₀ were determined 61%, 36%, 35%, 49% and 67%, respectively. After Fenton process, wastewater samples were coagulated with PAC. Optimum removal efficiencies for SS, COD, Fe ion, SAC₄₃₆, SAC₅₂₅ and SAC₆₂₀ were determined 83%, 18%, 93%, 32%, 36% and 58%, respectively. Ion exchange experiments were conducted on chemically coagulated wastewater samples to improve the quality of wastewater. Optimum dosage of resins was determined. The experiments revealed that 1:1 resin ratio (20 mL H-type resin:20 mL OH-type resin) gave the best removal rates for the parameters considered in this study. Study results indicated that quality of the wastewater was suitable for the process water characteristics of textile industry and unit wastewater treatment cost was determined as 2.54 €/m³.     

Optimization of Fenton's oxidation of chemical laboratory wastewaters using the response surface methodology

Establishing a treatment process for practical and economic disposal of laboratory wastewaters has become an urgent environmental concern of the Department of Chemical Engineering of the Universidade Estadual de Maringá (State University of Maringá), Brazil. Fenton and related reactions are potentially useful oxidation processes for destroying toxic organic compounds in water. In these reactions, hydrogen peroxide is combined with ferrous or ferric iron in the presence or absence of light to generate hydroxyl radicals (.OH). The feasibility of Fenton's reagent to treat waste chemicals from an academic research laboratory was investigated in this study. A response surface methodology was applied to optimize the Fenton oxidation process conditions using chemical oxygen demand (COD) removal as the target parameter to optimize, and the reagent concentrations, as related to the initial concentration of organic matter in the effluent, and pH as the control factors to be optimized. Maximal COD removal (92.3%) was achieved when wastewater samples were treated at pH 4 in the presence of hydrogen peroxide and iron in the ratios [COD]:[H2O2]=1:9 and [H2O2]:[Fe2+]=4.5:1. Under these conditions, it was possible to obtain simultaneously maximal COD removal and minimal chemical sludge after treatment, which is a residue that needs further processing.