Fenton试剂氧化降解微囊藻毒素-LR

研究了Fenton试剂氧化降解微污染水体中微囊藻毒素MC-LR的效果,在H2O2浓度1.5mmol·l-1,Fe2 浓度0.10 mmol·l-1,反应温度为25±1℃,pH值为4.18及反应时间为30min的条件下,浓度为0.41mg·l-1的MC-LR去除率可以达到92.4%,降解过程符合准一级反应动力学.Fenton试剂氧化体系能有效地降解MC-LR,特别是在紫外光的照射下,MC-LR的降解速率得到大幅度提高.紫外光能促进Fe3 还原为Fe2 ,所以光助Fenton试剂氧化反应中可以使用Fe3 代替Fe2 .     

Fenton氧化法修复石油污染土壤的研究进展

传统的Fenton氧化法（Fe2＋/H2O2）因反应速度过快、需要定期补充Fe2＋、控制pH值≤3等方面的限制而影响到石油烃类污染土壤的修复效果.本文综述了近年来Fenton反应中氧化剂、催化剂的改进及其对土壤中石油污染物的去除效率,揭示了土壤性质、反应条件、污染物结构及非均相催化剂比表面积等因素对去除效率的影响,介绍了超声波前置处理后,Fenton试剂与土壤上解吸的石油污染物接触几率的增加及石油烃类可生物降解性的提高,促进了微生物的后续处理效果,并对该领域的研究趋势进行了展望.     

地下水水化学成分对类Fenton法氧化硝基苯的影响

实验主要研究了地下水水化学成分对类Fenton法氧化去除硝基苯的影响。采用天然细砂模拟地下含水层介质,利用砂样中的原位铁做催化剂进行类Fenton氧化硝基苯实验。通过不同硝基苯和过氧化氢摩尔比的类Fenton实验,确定两者的最优物质的量比。然后模拟配制Na-SO4、Na-Cl、Ca-HCO3和Ca-SO4型4种水化学成分不同的地下水,在硝基苯和过氧化氢最优物质的量比情况下,研究了地下水水化学成分对类Fenton法氧化去除地下水中硝基苯的影响。反应在棕色瓶中进行,并用20℃恒温培养振荡器,以120 r.min-1的频率对其振荡。分别在10、30、60、90和120 min时取样,用气相色谱法检测硝基苯的质量浓度。结果表明：硝基苯和过氧化氢的最佳物质的量比为1∶200;地下水的水化学成分对类Fenton反应有重要影响,Na-SO4、Na-Cl、Ca-HCO3和Ca-SO4型地下水中硝基苯的最终去除率分别约为91%、92%、75%、82%,反应所需的时间大约为90、30、120和30 min。因此,类Fenton法对硝基苯污染地下水的原位化学修复具有较好效果,研究结果可为硝基苯污染地下水的原位化学修复提供一定的理论依据。     

垃圾渗滤液的Fenton氧化预处理研究

采用Fenton氧化法对垃圾渗滤液进行预处理,考察了渗滤液初始pH值、H2O2和FeSO4.7H2O投加量、H2O2/Fe2＋投加的物质的量比及氧化反应时间等对Fenton氧化处理效果的影响,获得Fenton氧化处理垃圾渗滤液的最佳工艺条件：初始pH=3.0,H2O2投加量为5.0 mL.L-1,FeSO4.7H2O投加量为3.48 g.L-1,H2O2/Fe2＋物质的量比为4-1,反应时间为1.5 h。最佳条件下处理后垃圾渗滤液COD为5 220 mg.L-1,COD去除率达57.8%。凝胶渗透色谱和三维荧光光谱分析结果表明,垃圾渗滤液中主要含有腐殖酸类大分子物质,经Fenton氧化后降解变成小分子化合物。     

Fenton氧化处理垃圾膜滤浓缩液

本文以混凝预处理后的上海老港垃圾填埋场渗滤液纳滤浓缩液为研究对象,采用混凝预处理、Fenton氧化法和生化法相结合的工艺对其进行处理,将其出水COD从2930 mg·L~(-1)降至100 mg·L~(-1)以下.采用响应曲面法研究了Fenton氧化法处理经过混凝预处理纳滤浓缩液过程中,各个影响因素之间的相互作用关系,并确定了最佳实验条件,即FeSO_4·7H_2O投加量为62.5 mmol·L~(-1)、H_2O_2投加量为121.8 mmol·L~(-1)、初始pH 3.0.在此条件下,Fenton氧化法可使混凝预处理出水的COD降低39.0%.进一步研究表明,Fenton氧化后纳滤浓缩液中芳香环类污染物减少、腐殖化程度降低.经过3 h的Fenton氧化法处理后,BOD5/COD从纳滤浓缩液原液的0.02上升到0.29.将垃圾渗滤液纳滤浓缩液Fenton氧化法处理后出水与垃圾填埋场渗滤液的纳滤出水1∶1混合,进行序批式活性反应器(SBR)处理,在水力停留时间为2 d时,出水COD可降低至96.0 mg·L~(-1).     

H_2O_2分次投加对Fenton氧化修复石油污染土壤及后续生物降解的影响

Fenton化学氧化和生物联合修复可以有效提高土壤有机污染物的去除效率.本文考察了H_2O_2分次投加对Fenton氧化过程中,土壤有机物(SOM)氧化量、石油烃(TPH)去除量、营养物质释放情况以及后续生物修复过程中的营养利用情况和修复效果的影响.结果表明,H_2O_2分次投加可以有效减少SOM的氧化、提高TPH去除率并能促进后续生物修复.实验发现,当900 mmol·L~(-1) H_2O_2分4次投加时,Fenton氧化阶段SOM氧化率最低(1.86%)、TPH去除率最高(32.14%),且土著细菌的残余量也最高(5.0×10~6 CFU·g~(-1)),这使得该体系营养物质在生物修复阶段得以充分利用,生物去除率高达38%,总TPH去除率达到70%,在4种投加方式下是最高的.H_2O_2分次投加的Fenton氧化方式是提高TPH去除率并促进后续生物降解的有效方法.     

环糊精的Fenton氧化特性及产物分析

环糊精因其具有包合增溶特性,单独或与高级氧化技术(如Fenton氧化)耦合可应用于有机污染物的土壤污染修复,然而环糊精的稳定性不清楚.本研究考察了环糊精在Fenton体系中的降解动力学及转化产物,评估了环糊精的稳定性.结果表明,β-环糊精(β-CD)在Fenton体系中反应速率随着过氧化氢浓度的升高而线性增加,符合二级动力学过程.环糊精与羟基自由基反应的绝对速率常数在酸性条件下(p H=3)分别为3.9×10~9L·(mol·s)~(-1)(β-CD和甲基β环糊精),6.5×10~9L·(mol·s)~(-1)(羟丙基β环糊精),7.2×10~9L·(mol·s)~(-1)(γ-环糊精),中性条件下(p H=7)为2.9×10~9L·(mol·s)~(-1)(β-CD),3.1×10~9L·(mol·s)~(-1)(MCD),3.2×10~9L·(mol·s)~(-1)(HPCD),3.3×10~9L·(mol·s)~(-1)(γ-CD),显示环糊精在酸性条件下降解加快,且绝对速率常数的种类差别较大,而在中性条件下比较稳定,且种类之间差别不大.产物质谱分析表明,环糊精空腔骨架上的羟基被氧化,生成了含有醛基和羧基氧化产物;反应前后总有机碳含量无明显差别,表明环糊精及产物的空腔结构稳定,未被开环破坏.     

Fenton氧化4-氯酚降解机制研究

为了深入探讨4-氯酚（4-CP）在Fenton氧化体系中的降解机制,利用高效液相色谱（HPLC）等多种手段系统分析了反应过程中Fe2＋、Cl-、氧化中间产物对苯二酚、1,4-苯醌、4-氯邻苯二酚和4-氯间苯二酚的浓度以及氧化还原电位（ORP）的变化规律.研究结果表明,Fe2＋浓度经历了短暂的下降之后迅速上升到接近初始的...     

化学沉淀结合Fenton法预处理脱硫废液的原理与效果分析

脱硫废液因含有高浓度氰化物、硫氰化物、硫化物等有毒组分而影响焦化废水处理的生物工艺.以焦化企业产生的实际脱硫废液为研究对象,选用化学沉淀-Fenton氧化的串联方法尝试预处理及分析方法的可行性,通过单因素实验,考察了硫酸亚铁投加剂量、反应前后溶液pH值、反应时间3种条件对脱硫废液中总氰及易释放氰去除效果的影响,在优化条件下对经硫酸亚铁沉淀后的脱硫废液残液进行Fenton氧化实验.结果表明,当硫酸亚铁投加量为理论值的1.2倍,H2O2投加量为COD当量的0.3倍时,可使脱硫废液的COD去除率达到76.65%,使初始浓度分别为327.7、704.6和2087.3 mg.L-1的氰化物、硫氰化物及硫化物基本得到去除,为后续生物处理创造了有利条件.化学沉淀结合Fenton法是脱硫废液预处理效率高且实用的方法.     

Fenton氧化对印染污泥脱水性能的影响

采用Fenton氧化法对印染污泥进行预处理,研究印染污泥中TSS、VSS、CST、SRF等脱水性能指标的变化规律.结果表明,当pH值为2.0,H2O2和Fe2+投加量分别为428 mg.g-1(干泥)和42.8 mg.g-1(干泥),反应时间1.5 h、反应温度80℃时,Fenton氧化后印染污泥的脱水效果最佳.在该条件下,TSS由18.66 g.L-1下降至4.82 g.L-1,去除率为74.17%;CST和SRF分别由98.6 s和6.03×1011s.2g-1下降至18.9 s和8.42×1010s.2g-1;污泥的平均粒径和中值粒径分别由53.8μm和42.9μm下降至19.8μm和16.2μm.     

Up to 95 % reduction of chemical oxygen demand of slaughterhouse effluents using Fenton and photo-Fenton oxidation

Meat industries produce effluents containing high concentrations of organic and inorganic compounds, which must be removed before being discharged or reused. Advanced oxidation processes using Fenton reaction coupled with UV, solar radiation, and electrochemical oxidation are promising methods. Here, we treated the effluent from an anaerobic digester using: (a) the photoelectro-Fenton process, using a system with a Ti-RuO₂ anode and a carbon felt cathode, (b) the solar photo-Fenton process, using a batch reactor and a compound parabolic collector, and (c) a combination of Fenton and solar photo-Fenton processes. The effluent had an initial chemical oxygen demand (COD) of 1159 mgL^?1, and we obtained high removal efficiencies of COD, up to 95 %, using the combination of Fenton and solar photo-Fenton processes.     

Degradation of the herbicide imazapyr by Fenton reactions

The degradation of the herbicide imazapyr has been carried out by three advanced oxidation processes involving iron ions as catalysts: Fentons reagent, photo-Fenton and electro-Fenton. We show that all processes are rapid and efficient. The kinetic rate constant was found to be k=5.4×10⁹ M^–1 s^–1. The mineralization of imazapyr is almost complete using the photo-Fenton and electro-Fenton processes.     

Experimental and computational assessment of 1,4-Dioxane degradation in a photo-Fenton reactive ceramic membrane filtration process

• 1,4-Dioxane was degraded via the photo-Fenton reactive membrane filtration. • Degradation efficiency and AQY were both enhanced in photocatalytic membrane. • There is a tradeoff between photocatalytic degradation and membrane permeation flux. • Degradation pathways of 1,4-Dioxane is revealed by DFT analysis. The present study evaluated a photo-Fenton reactive membrane that achieved enhanced 1,4-Dioxane removal performance. As a common organic solvent and stabilizer, 1,4-Dioxane is widely used in a variety of industrial products and poses negative environmental and health impacts. The membrane was prepared by covalently coating photocatalyst of goethite (α-FeOOH) on a ceramic porous membrane as we reported previously. The effects of UV irradiation, H₂O₂ and catalyst on the removal efficiency of 1,4-Dioxane in batch reactors were first evaluated for optimized reaction conditions, followed by a systematical investigation of 1,4-Dioxane removal in the photo-Fenton membrane filtration mode. Under optimized conditions, the 1,4-Dioxane removal rate reached up to 16% with combination of 2 mmol/L H₂O₂ and UV₃₆₅ irradiation (2000 µW/cm²) when the feed water was filtered by the photo-Fenton reactive membrane at a hydraulic retention time of 6 min. The removal efficiency and apparent quantum yield (AQY) were both enhanced in the filtration compared to the batch mode of the same photo-Fenton reaction. Moreover, the proposed degradation pathways were analyzed by density functional theory (DFT) calculations, which provided a new insight into the degradation mechanisms of 1,4-Dioxane in photo-Fenton reactions on the functionalized ceramic membrane.     

Photocatalytic treatment of dimethoate by solar photocatalysis at pilot plant scale

Titanium dioxide photocatalysis, using 200 mgl⁻¹ of TiO₂, and photo-Fenton, using 20 mg l⁻¹ of iron, were applied to the treatment of dimethoate dissolved in water at 50 mg l⁻¹. A heterogeneous photocatalysis test was performed in a 35-l solar pilot plant with Compound Parabolic Collectors (CPCs) under natural illumination. A homogeneous photocatalysis test was performed in a different solar pilot plant with four CPC units and a total volume of 75 l. In this work total disappearance of dimethoate and 90% of mineralization were attained in both solar treatments. Treatment time, hydrogen peroxide consumption and ferric phosphate precipitation during photo-Fenton treatment were discussed. An erratum to this article can be found at     

Degradation of bisphenol A by photo-fenton processes

The photo-Fenton reactions, which could yield hydroxyl radicals via the catalytic degradation of H₂O₂ by Fe(II), were focused as one of the abiotic degradation processes of bisphenol A (BPA) in surface waters. At pH 6, in the presence of H₂O₂ only, 32% of BPA was degraded after 120?min of irradiation. However, 97% of BPA was degraded in the presence of both H₂O₂ and Fe(II). Without light irradiation, no BPA degradation was observed even in the presence of Fe(II) and H₂O₂. These results show that photo-Fenton processes are effective in the natural attenuation of BPA in surface water. In addition, the presence of humic acids (HAs), which were of more aliphatic nature, resulted in enhancing BPA degradation via the photo-Fenton processes. Therefore, HAs can be one of the important factors in enhancing the degradation of BPA in surface water via the photo-Fenton processes.     

Treatment of organic pollutants by homogeneous and heterogeneous Fenton reaction processes

Nowadays, the water ecosystem is being polluted due to the rapid industrialization and massive use of antibiotics, fertilizers, cosmetics, paints, and other chemicals. Chemical oxidation is one of the most applied processes to degrade contaminants in water. However, chemicals are often unable to completely mineralize the pollutants. Enhanced pollutant degradation can be achieved by Fenton reaction and related processes. As a consequence, Fenton reactions have received great attention in the treatment of domestic and industrial wastewater effluents. Currently, homogeneous and heterogeneous Fenton processes are being investigated intensively and optimized for applications, either alone or in a combination of other processes. This review presents fundamental chemistry involved in various kinds of homogeneous Fenton reactions, which include classical Fenton, electro-Fenton, photo-Fenton, electro-Fenton, sono-electro-Fenton, and solar photoelectron-Fenton. In the homogeneous Fenton reaction process, the molar ratio of iron(II) and hydrogen peroxide, and the pH usually determine the effectiveness of removing target pollutants and subsequently their mineralization, monitored by a decrease in levels of total organic carbon or chemical oxygen demand. We present catalysts used in heterogeneous Fenton or Fenton-like reactions, such as H₂O₂–Fe³⁺(solid)/nano-zero-valent iron/immobilized iron and electro-Fenton-pyrite. Surface properties of heterogeneous catalysts generally control the efficiency to degrade pollutants. Examples of Fenton reactions are demonstrated to degrade and mineralize a wide range of water pollutants in real industrial wastewaters, such as dyes and phenols. Removal of various antibiotics by homogeneous and heterogeneous Fenton reactions is exemplified.     

Iron-doped copper 1,4-benzenedicarboxylate as photo-Fenton catalyst for degradation of methylene blue

Abstract

A metal-organic framework of iron-doped copper 1,4-benzenedicarboxylate was synthesized and, for the first time, utilized as a heterogeneous photo-Fenton catalyst for degradation of methylene blue dye in aqueous solution under visible light irradiation. The synthesized materials were characterized by scanning electron microscopy, Fourier-transform infrared spectroscopy, X-ray diffraction and energy-dispersive X-ray spectroscopy. The influence factors, kinetics, and stability of the synthesized catalysts were investigated in detail. Iron-doped copper 1,4-benzenedicarboxylate showed higher degradation efficiency than pure copper 1,4-benzenedicarboxylate. An almost complete degradation was achieved within 70?min under visible light irradiation at a solution pH of 6, a catalyst loading of 1?g?L^?1, a H₂O₂ dosage of 0.05?mol L^?1 and methylene blue concentration of 50?mg?L^?1. Recycling studies demonstrated that the iron-doped copper 1,4-benzenedicarboxylate is a promising heterogeneous photo-Fenton catalyst for long-term removal of methylene blue dye from industrial wastewater.     

Degradation of dye rhodamine B under visible irradiation with Prussian blue as a photo-Fenton reagent

Rhodamine B can be degraded using Prussian blue as a photo-Fenton like reagent under λ > 420 nm visible irradiation. Kinetic studies show ln(C _o/C _t ) is linearly proportional to the reaction time during the photo-degradation process; thus, the degradation reaction obeys a pseudo-first order kinetic law. It is very interesting that the presence of salinity such as 0.1 M KCl can speed up greatly the degradation rate: the time to achieve 90.0% degradation ratio is shortened from 120.0 to 40.0 min under comparable conditions, which is very useful in the treatment of wastewaters with high content of salinity.     

Solar photo-oxidation of recalcitrant industrial wastewater: a review

Conventional methods to clean wastewater actually lead to incomplete treatments, calling for advanced technologies to degrade recalcitrant pollutants. Herein we review solar photo-oxidation to degrade the recalcitrant contaminants in industrial wastewater, with focus on photocatalysts, reactor design and the photo-Fenton process. We discuss limitations due to low visible-light absorption, catalyst collection and reusability, and production of toxic by-products. Photodegradation of refractory organics by solar light is controlled by pH, photocatalyst composition and bandgap, pollutant properties and concentration, irradiation type and intensity, catalyst loading, and the water matrix.