芬顿试剂预处理杀螟丹农药废水

利用芬顿试剂(Fenton)氧化预处理杀螟丹农药废水,分别考察了H2O2与Fe SO4·7H2O投加量、初始p H、反应时间、温度和摇床转速对Fenton试剂处理杀螟丹废水的影响。结果表明,杀螟丹废水初始COD为676.8 mg/L时,取废水样100 m L,优化反应条件为Fenton试剂的用量1 g Fe SO4·7H2O+4 m L H2O2,初始p H值为3,搅拌强度为160 r/min的摇床转速,反应温度25℃,反应时间60 min。在优化反应条件下COD的去除率达到83.9%。通过Fenton降解,废水可生化性BOD5/COD从0.0745~0.0747上升至0.9066~0.9228,可生化性大幅提高,为后续生化处理创造了条件。考虑到运用于工业废水处理中经济成本等实际问题,建议选取Fenton试剂的用量0.5 g Fe SO4·7H2O+1 m L H2O2,COD去除效率能达到65.5%。     

水体中酮硝基麝香的臭氧氧化降解研究

采用臭氧氧化水体中的酮硝基麝香,考察pH、H2O2等因素对降解程度的影响,结果表明提高初始pH能加快酮硝基麝香的氧化降解,当pH为12时,反应时间1 h,酮硝基麝香几乎完全去除,浓度为2 mol/L和5 mol/L的H2O2存在有利于O3分解生成·OH自由基,使得酮硝基麝香的氧化降解速率加快,当H2O2浓度超过5 mol/L,H2O2会成为·OH的清除剂,降低·OH利用率;无论O3单独作用和O3/H2O2协同作用,酮硝基麝香降解符合准一级动力学规律;酮硝基麝香氧化降解产物包括甲酸、二乙酸和硝酸根等,其中硝基从苯环上脱落降低了硝基麝香对环境的风险.     

强化UV/Fenton法降解水中苯酚的研究

研究了UV/Fenton法处理含苯酚废水时H2 O2 和FeSO4 加入量及苯酚初始浓度对酚去除效果的影响及C2 O2 -4 对UV/Fenton法的增强效果。 [H2 O2 ]=2 0mmol/L ,[FeSO4 ]=5mmol/L ,反应 2 0min ,苯酚初始浓度为 5 0mg/L时 ,酚去除率达 99%。UV/Fenton体系中引入C2 O2 -4 后可有效提高对紫外和可见光的利用率 ,进而提高了对高浓度苯酚废水去除效果     

基于过碳酸钠的类Fenton体系对亚甲基蓝的降解动力学

采用改良低温结晶法制备过碳酸钠(sodium percarbonate,SPC),对其进行XRD表征,并用以作为氧化剂构建类Fenton体系(SPC/Fe~(2+))降解亚甲基蓝(MB),对其降解的影响因素及反应动力学进行了研究。结果表明,在该体系中,当溶液初始pH分别为2~10时,亚甲基蓝的去除率在1 min时均可达到97%以上,说明该体系可高效去除水体中的亚甲基蓝,反应速率快,且过碳酸钠的使用可以拓宽Fenton反应的pH范围。该反应的最佳工艺条件为0.75 g·L~(-1)硫酸亚铁,300 mg·L~(-1)过碳酸钠,亚甲基蓝去除率在反应10 min后可达99.0%。亚甲基蓝在该体系中的降解遵循二级反应动力学方程,反应速率常数分别为64.50×10~(-3)L·(mol·s)~(-1),快于Fenton体系的17.83×10~(-3)L·(mol·s)~(-1)。该体系反应活化能为16.6 kJ·mol~(-1),远小于Fenton体系(46.234 kJ·mol~(-1)),说明以过碳酸钠为氧化剂更有利于非均相类Fenton反应的发生。     

Fenton试剂氧化处理火炸药污染土壤淋洗液

采用Fenton试剂对火炸药污染土壤淋洗液进行氧化处理,研究了Fe SO4·7H2O投加量、H2O2投加量、初始pH、反应时间及温度对处理效果的影响,采用发光细菌发评价处理前后水样的急性毒性变化。结果表明,Fenton试剂氧化可有效去除火炸药污染土壤淋洗液的COD,当Fe SO4·7H2O投加量为8.0 g/L,H2O2投加量为64 m L/L,初始pH为3,反应时间120 min及反应温度30℃时,污染土壤淋洗液的COD由4 553.9 mg/L降至800.1 mg/L,COD去除率82.4%,COD的降解符合二级动力学模型。经Fenton氧化处理后,水样的急性毒性降低94.7%,B/C由0.007升至0.22,可生化性得到明显改善。     

Fenton氧化活性深蓝染料B-2GLN的动力学

为了考查H2O2/Fe2+的摩尔比和H2O2的初始剂量、pH值以及活性深蓝染料B-2GLN(RDB B-2GLN)的初始浓度对活性深蓝染料B-2GLN降解过程的影响,采用在线分光光度法对活性深蓝染料B-2GLN的Fenton氧化过程进行了研究,探讨了其动力学过程,并利用气相色谱-质谱联用分析降解中间产物。结果显示,采用Fenton氧化降解水溶液中活性深蓝染料B-2GLN,在H2O2的剂量为2.635 mmol/L,pH值为2.7,H2O2/Fe2+的摩尔比为37.80和活性深蓝染料B-2GLN的初始浓度16 mg/L的条件下,得到300 s后活性深蓝染料B-2GLN的最大色度去除率为85.04%。水溶液中活性深蓝染料B-2GLN与·OH的反应速率常数为2.62×1011L/(mol·s)。活性深蓝B-2GLN染料的分子结构被Fenton试剂分解而未被完全矿化,同时对活性深蓝染料降解产物进行了分析。在线分光光度法是研究染料色度去除率的一种精确、快速与可行的方法。     

芬顿氧化法处理水中酸性品红的研究

研究了酸性品红在Fenton体系中的降解过程,反应30 min后,在[Fe2+]0=0.06 mmol/L、[H2O2]0=0.3 mmol/L、pH=3、T=30℃的条件下,初始浓度为20 mg/L的酸性品红的去除率达到97%以上。升高反应温度,有利于Fenton体系中酸性品红的降解,但影响并不显著。根据不同温度下的速率常数,并结合Arrhenius方程求出了Fenton试剂降解酸性品红的反应活化能,仅为11.63 kJ/mol。C1?的存在对酸性品红在Fenton体系中的降解表现出明显的阻碍作用,并且随着C1?浓度的增加,抑制作用越来越大;SO24-和NO3-的存在也降低了Fenton试剂的氧化性能。     

UV/Fenton法预处理橡胶促进剂生产废水

采用UV/Fenton法对橡胶促进剂废水进行预处理.当原水COD约为3000 mg/L时,COD去除率可达65%以上,并得到最佳操作条件为:H2O2投加量为8 mL/L,Fe2 投加量为0.8 g/L,反应时间为30 min,pH=5;同时得到Fenton试剂处理该废水的最佳条件为:H2O2投加量为10 mL/L,Fe2 投加量为0.966 g/L,反应时间为30 min,pH=5;单独UV作用的最佳工艺条件为:反应时间为20 min,pH=5;并就3种处理方法进行了比较,发现UV对Fenton试剂处理橡胶促进剂废水具有一定促进作用.反应前后的紫外光谱说明,经UV/Fenton或Fenton反应后原水中的苯胺、硝基苯等物质已得到了彻底的氧化分解.     

光/电Fenton牺牲阳极法降解有机污染物

采用Fe片为阳极和石墨为阴极,在可见光(λ450 nm)照射并外加电压条件下,以有机染料橙Ⅱ(orangeⅡ)及有机无色小分子2,4-二氯苯酚(2,4-dichlorophenol,DCP)为目标化合物,探讨了光/电Fenton牺牲阳极法降解有机污染物的最佳反应条件,结果表明,在电压=3 V,pH=3.0,H2O2浓度为5×10-5mol/L时,orangeⅡ的降解效果最好,反应10 h矿化率可达到78%,210 min内2,4-DCP降解率为91.4%。通过对光/电Fenton体系原位循环伏安参数测定及过氧化物酶催化反应吸光光度法和苯甲酸荧光分析法检测光/电Fenton降解orange II过程中H2O2和羟基自由基(.OH)的变化,表明orangeⅡ降解过程涉及.OH历程。     

光助Ce-Fe/Al2O3催化H2O2降解阳离子红GTL模拟废水

利用Ce-Fe/Al2O3为催化剂的非均相光Fenton体系降解阳离子红GTL模拟废水,考察了H2O2浓度、催化剂用量、初始pH值及不同工艺过程对降解效果的影响,通过紫外-可见漫反射光谱、红外光谱、XPS手段研究铁在反应中的价态变化.结果表明,在11 W低压汞灯照射下,非均相光Fenton体系能够有效地降解结构稳定的阳离子红GTL,在pH 6,反应温度20℃,时间90 min,Ce-Fe/Al2O3 2 g/L,H2O2浓度340 mg/L,含50 mg/L阳离子红GTL模拟废水TOC去除率为92.40%;光Fenton反应中Fe(Ⅲ)转化为Fe(Ⅱ).     

非均相Fenton体系中无机助剂对亚甲基蓝脱色的影响

直接使用有机过渡金属化合物二茂铁作为催化剂，研究了非均相Fenton反应中亚甲基蓝的降解，并考虑了实际排放的印染废水中存在的无机助剂，进一步分析了典型无机助剂CuSO4、NaCl、Na2CO3、Na2SO4、Na2S的存在对该非均相Fenton体系的影响，结果表明：直接使用二茂铁做催化剂反应120min后，亚甲基蓝的剩余率为0．6％，羟基自由基的表观生成率为83．4％。NaCl、Na2CO3、Na2SO4、Na2S的加入会阻碍反应的进行，而CuSO4的加入会促进反应的进行。     

Hydroxyl radical concentration profile in photo-Fenton oxidation process: generation and consumption of hydroxyl radicals during the discoloration of azo-dye Orange II

Dynamic behaviors of hydroxyl (OH) radical generation and consumption in photo-Fenton oxidation process were investigated by measuring OH radical concentration during the discoloration of azo-dye Orange II. The effects of operating parameters for photo-Fenton discoloration, i.e. dosages of H₂O₂ and Fe, initial dye concentration, solution pH and UV irradiation, on the generation and consumption of OH radicals playing the main role in advanced oxidation processes were extensively studied. The scavenger probe or trapping technique in which coumarin is scavenger of OH radical was applied to estimate OH radical concentration in the photoreactor during the photo-Fenton discoloration process. The OH radical generation was enhanced with increasing the dosages of Fenton regents, H₂O₂ and Fe. At the initial stage of photo-Fenton discoloration of Orange II, the OH radical concentration rapidly increased (Phase-I) and the OH radical concentration decreased after reaching of OH radical concentration at maximum value (Phase-II). The decrease in OH radical concentration started when the complete discoloration of Orange II was nearly achieved and the H₂O₂ concentration became rather low. The dynamic behavior of OH radical concentration during the discoloration of Orange II was found to be strongly linked with the change in H₂O₂ concentration. The generation of OH radical was maximum at solution pH of 3.0 and decreased with an increase of solution pH. The OH radical generation rate in the Fenton Process was rather slower than that in the photo-Fenton process.     

微电解-Fenton深度处理制药废水影响因素与参数控制

采用铁炭微电解-Fenton联合工艺深度处理制药废水生化出水,探讨了初始pH、曝气量、反应时间等因素对微电解出水Fe2+和Fe3+变化规律、COD降解速率以及后续Fenton氧化效果的影响,为优化微电解-Fenton氧化联合工艺提出了微电解间歇加酸的理论。间歇加酸可提高微电解系统中COD降解速率和Fe2+含量,使后续Fenton氧化无需投加FeSO4·7H2O即可达到较好的COD去除效果。结果表明,当初始pH=2.5,曝气量为0.6 m3/h,间歇加酸30 min/次,微电解反应2 h,出水投加1 mL/L的H2O2进行Fenton氧化2 h,COD总去除率可达81.33%;间歇加酸30 min/次可将微电解反应2 h出水Fe2+浓度从50 mg/L提高至151 mg/L,COD降解速率从10.6 mg COD/(L·h)提高至22.2 mg COD/(L·h)。     

Fenton法处理垃圾渗滤液MBR-NF浓缩液

采用Fenton法处理MBR-NF浓缩液,考察了FeSO4·7H2O投加量、n(H2O2)/n(Fe2+)投加比、初始pH对渗滤液MBR-NF浓缩液处理效果的影响,并在最佳实验条件下,探讨浓缩液富里酸(FA)、亲水性有机物(HyI)组分在Fenton氧化前后组成的变化。研究结果表明,在FeSO4·7H2O投加量为0.055 mol/L、n(H2O2)/n(Fe2+)投加比为4、初始pH为7.58时,对COD、腐植酸(UV254)、色度(CN)的去除率分别为79.6%、93.7%和97.8%。Fenton氧化后,浓缩液中有机物组分含量发生了较大变化,腐植酸含量下降,HyI成为渗滤液溶解性有机物主要成分。紫外-可见光谱表明,Fenton法对FA去除效果较好,而对HyI氧化效果较差;傅立叶红外光谱显示,经Fenton氧化后,FA的结构发生了明显变化,而HyI则变化不明显。     

Factors that have an effect on degradation of diclofenac in aqueous solution by gamma ray irradiation

Purpose  

Gamma ray irradiation is considered as an effective way to degrade diclofenac. However, due to the extensive coexisting substances in natural waters, the use of gamma ray irradiation for degradation is often influenced by multiple factors. The various factors that affect degradation efficiency, such as initial diclofenac concentration, initial pH, and the concentration of the additives including H₂O₂ (·OH radical promoter), CH₃OH (·OH radical scavenger), thiourea (·OH, H·, and e_aq⁻ scavenger), humic acid, and NO₃⁻ (coexisting substances in natural waters), are investigated. Furthermore, possible intermediate products are identified and corresponding transformation pathways are proposed.     

Effect of ethylenediamine-N,N′-disuccinic acid on Fenton and photo-Fenton processes using goethite as an iron source: optimization of parameters for bisphenol A degradation

The main disadvantage of using iron mineral in Fenton-like reactions is that the decomposition rate of organic contaminants is slower than in classic Fenton reaction using ferrous ions at acidic pH. In order to overcome these drawbacks of the Fenton process, chelating agents have been used in the investigation of Fenton heterogeneous reaction with some Fe-bearing minerals. In this work, the effect of new iron complexing agent, ethylenediamine-N,N'-disuccinic acid (EDDS), on heterogeneous Fenton and photo-Fenton system using goethite as an iron source was tested at circumneutral pH. Batch experiments including adsorption of EDDS and bisphenol A (BPA) on goethite, H₂O₂ decomposition, dissolved iron measurement, and BPA degradation were conducted. The effects of pH, H₂O₂ concentration, EDDS concentration, and goethite dose were studied, and the production of hydroxyl radical (^?OH) was detected. The addition of EDDS inhibited the heterogeneous Fenton degradation of BPA but also the formation of ^?OH. The presence of EDDS decreases the reactivity of goethite toward H₂O₂ because EDDS adsorbs strongly onto the goethite surface and alters catalytic sites. However, the addition of EDDS can improve the heterogeneous photo-Fenton degradation of BPA through the propagation into homogeneous reaction and formation of photochemically efficient Fe-EDDS complex. The overall effect of EDDS is dependent on the H₂O₂ and EDDS concentrations and pH value. The high performance observed at pH 6.2 could be explained by the ability of O ₂ ^?? to generate Fe(II) species from Fe(III) reduction. Low concentrations of H₂O₂ (0.1 mM) and EDDS (0.1 mM) were required as optimal conditions for complete BPA removal. These findings regarding the capability of EDDS/goethite system to promote heterogeneous photo-Fenton oxidation have important practical implications for water treatment technologies.     

Degradation of 1,2-dichloroethane from wash water of ion-exchange resin using Fenton’s oxidation

Background, aim, and scope  

Chlorinated volatile organic compounds (CVOCs), widely used in industry as solvents and chemical intermediates in the production of synthetic resins, plastics, and pharmaceuticals, are highly toxic to the environment and public health. Various studies reported that Fenton’s oxidation could degrade a variety of chlorinated VOCs in aqueous solutions. In acidic conditions, ferrous ion catalyzes the decomposition of H₂O₂ to form a powerful ^•OH radical. In this study, wastewater from wash of ion-exchange resin containing typical CVOC, 1,2-dichloroethane, was treated using Fenton’s oxidation. To reduce environmental load and processing costs of wastewater, Fenton process as a simple and efficient treatment method was applied to degrade 1,2-dichloroethane of wash water.     

Degradation of Acid Orange 7 in aqueous solution by dioxygen activation in a pyrite/H2O/O2 system

Increasing attention has been paid to pyrite due to its ability to generate hydroxyl radicals in air-saturated solutions. In this study, the mineral pyrite was studied as a catalyst to activate molecular oxygen to degrade Acid Orange 7 (AO7) in aqueous solution. A complete set of control experiments were conducted to optimize the reaction conditions, including the dosage of pyrite, the AO7 concentration, as well as the initial pH value. The role of reactive oxygen species (ROS) generated by pyrite in the process was elucidated by free radical quenching reactions. Furthermore, the concentrations of Fe(II) and total Fe formed were also measured. The mechanism for the production of ROS in the pyrite/H₂O/O₂ system was that H₂O₂ was formed by hydrogen ion and superoxide anion (O₂ ^·?) which was produced by the reaction of pyrite activating O₂ and then reacted with Fe(II) dissolved from pyrite to produce ^·OH through Fenton reaction. The findings suggest that pyrite/H₂O/O₂ system is potentially practical in pollution treatment. Moreover, the results provide a new insight into the understanding of the mechanism for degradation of organic pollutants by pyrite.     

Fenton氧化与铁炭微电解组合预处理DMF废水

对COD表征模拟废水中DMF去除率的可行性进行了探讨。在此基础上,分别对铁炭微电解、Fenton氧化-铁炭微电解和铁炭微电解-Fenton氧化组合工艺对DMF废水的处理效果进行分析,结果表明,Fenton氧化-铁炭微电解工艺的处理效果较好。在pH=5,反应时间为1 h,FeSO4·7H2O投加量为1 000 mg/L、H2O2投加量为2.67 mL/L和不曝气的最佳反应条件下,Fenton氧化-铁炭微电解工艺对实际废水和废液中COD的去除率分别达到66.67%和72.22%,从而验证了该工艺处理DMF废水的可行性。此外,Fenton氧化处理DMF废水过程实际上是将酰胺基团和羰基的不饱和双键氧化分解的过程。