类Fenton试剂氧化降解土壤中PAHs及其影响因素研究

使用类Fenton试剂可以有效降解土壤中的多环芳烃（PAHs）。选择4种PAHs菲、芘、苯并[a]芘、茚并（1,2,3-cd）芘作为考察对象,研究了类Fenton试剂对土壤中PAHs的降解条件。单因素降解实验结果表明,在H2O2浓度为0.5mol/L,Fe（NO3）3浓度为0.1 mol/L,水土比为3∶1,反应时间为...     

Fenton氧化法深度处理丙烯腈废水的研究

以丙烯腈(AN)废水为研究对象，在正交实验基础上深入研究了Fenton反应体系中pH值、Fe^2 浓度、H2O2浓度、温度、uv和C2O^2-4对降解效果的影响，分析了不同因素作用机理，确定了最佳操作条件：pH=3、[Fe^2 ]=400mg／，L、[H2O2]=400mg／L、反应温度40℃，在此条件下丙烯腈降解率达80％以上。同时发现在紫外光、C2O^2-4对Fenton试剂的协同作用下，降解率可提高10％左右。     

Fenton试剂氧化降解水中的盐酸四环素

利用Fenton试剂对水中盐酸四环素（TC）氧化降解,考察H2O2/Fe2+（摩尔比）、Fenton试剂投加量、溶液pH值对盐酸四环素去除的影响,研究了盐酸四环素降解过程及动力学特征。研究结果表明：对于初始浓度为0.10 mmol·L-1的盐酸四环素,最优反应条件为pH值3.0,H2O2/Fe2+=10：1（物质的量之比）,H2O2施加量1.58 mmol·L-1。在该条件下反应60 min,盐酸四环素降解率达88.47%,对应TOC去除率为18.48%;紫外可见光谱扫描结果表明氧化过程中盐酸四环素的共轭结构被首先破坏;分别采用一级和二级动力学方程拟合降解过程,结果表明反应过程遵循二级动力学模型。     

Fenton试剂催化氧化嘧啶废水的特性

研究了Fenton催化氧化法对废水中嘧啶的去除效能,优化了处理体系中的反应条件,分析了各影响因子的作用机理;并用一元线性回归方程对不同温度下,嘧啶相对残余浓度对反应时间的相关性进行了定量分析。结果表明:温度为25℃,pH为3.5,Fe²⁺的投加量64 mmol/L,H₂O₂投加量为300 mmol/L时,反应2 h,Fenton试剂对嘧啶和COD的去除率分别达90%和50%以上;同时发现Fenton试剂对嘧啶的氧化降解具有相对优先性,且符合一级反应动力学模式,并计算表观反应速率常数和活化能。     

Fenton氧化降解垃圾渗滤液中COD的动力学研究

对絮凝预处理后的垃圾渗滤液进行Fenton氧化处理。通过微分法对Fenton氧化的反应级数进行求解,确定其反应级数为2,并初步建立了Fenton氧化的动力学模型,即1/c=1/c0+kt,由此建立起来的降解的动力学模型与实验数据相吻合;在4个实验基准条件下———初始COD浓度为960 mg/L、pH值4、H2O2投加量0.4 mol/L、nH2O2/nFe2+3∶1,探讨了其中某一变量对反应速率的影响。实验水样为絮凝反应出水,进水COD浓度为912～960 mg/L,出水COD浓度为80～112 mg/L,COD去除率在87%～92%之间,表明Fenton试剂能够有效地处理垃圾渗滤液。     

光助Fenton氧化法降解水中六氯苯的研究

采用光助Fenton氧化法处理六氯苯模拟废水,考察了反应时间、Fe3 与H2O2摩尔比、Fenton试剂用量、初始pH、六氯苯初始浓度、光强对六氯苯降解效果的影响,并初步探讨了六氯苯的降解动力学规律.结果表明.光助Fenton法降解六氯苯的最佳工艺条件为:紫外灯功率为300 W、Fe3 投加量为1.0 mmol/L、H2O2投加量为5.0 mmol/L、反应时间为60 min、初始pH为3,在此条件下,浓度为500μg/L的HCB的去除率可达91.3%.UV辐射与Fenton氧化对HCB的降解具有协同效应.光助Fenton法对HCB的降解符合一级反应动力学方程,表观速率常数为0.04 min-1,与Fenton法相比,提高了近9倍.     

Fenton氧化法对磺胺类抗生素的降解动力学

采用Fenton氧化法同时降解水溶液中磺胺吡啶(SPY)、磺胺二甲基嘧啶(SMZ)和磺胺甲噁唑(SMX)。系统考查了初始H2O2浓度、Fe2+浓度、pH对3种磺胺类抗生素降解性能的影响。结果表明,3种磺胺抗生素被完全降解的最佳Fenton氧化条件是:H2O2浓度为2.0 mmol/L,Fe2+浓度为0.10 mmol/L,pH为3.0~3.5,反应时间为20 min。Fenton试剂对3种磺胺类抗生素的降解符合一级反应动力学,速度常数为0.0318~0.2002 min-1。     

Fenton试剂处理腐殖酸废水影响特性和降解动力学模型

研究了Fenton试剂降解腐殖酸废水的影响特性,并在理论分析反应过程的基础上建立动力学方程,同时根据实验进行动力学方程参数估算。研究表明,Fenton试剂通过氧化和混凝共同作用有效去除腐殖酸。在初始pH=4,40mmol/L FeSO4和160 mmol/L H2O2投量下,腐殖酸60 min氧化去除率、混凝去除率分别达到78.6%和11.5%,其初始氧化速率达到最大59.6 mg/(L.min)。腐殖酸的氧化降解动力学模型值与实验值吻合良好,说明采用该动力学模型能较好预测腐殖酸废水的氧化降解情况,且Fenton氧化降解腐殖酸的机理符合自由基的理论和实践。     

Fenton氧化法深度处理纤维素乙醇废水

采用Fenton氧化法深度处理经生化降解后的纤维素乙醇废水,考察了初始pH值、Fe2+与H2O2的投加比例（物质的量之比）、H2O2投加量与COD的比例（质量之比）以及反应时间对COD和浊度去除的影响,并通过正交实验确定了反应的最佳条件。研究表明：初始pH值、Fe2+/H2O2、H2O2/COD以及反应时间对深度处理效果有不同程度的影响;在初始pH值为3.0、Fe2+/H2O2为2：3、H2O2/COD为2.8、反应时间为3 h的最佳反应条件下,出水COD为45~56 mg·L-1,浊度为2~3 NTU,达到了纤维素乙醇废水的排放标准。     

An unconventional approach to studying the reaction kinetics of the Fenton's oxidation of 2,4-dichlorophenoxyacetic acid

The Fenton's oxidation kinetics of herbicide 2,4-D at various [Fe(II)] and [H(2)O(2)] combinations was investigated and modelled through an unconventional approach. The reaction kinetics of 2,4-D degradation demonstrated a two-stage pattern of decay, where a very fast reactive stage was followed by a retardation stage due to the depletion of oxidants and to the competitive side-reactions of the intermediates (including 2,4-dichlorophenol, chlorohydroquinone and 2,6-dichlororesorcinol). A model characterized by two newly established constants, the initial decay rate and the maximum oxidative capacity, was proposed and proven capable of describing the two-stage process, which cannot easily be described by conventional first- or second-order kinetics approaches.     

Modeling the reaction kinetics of Fenton's process on the removal of atrazine

The degradation of pesticide, atrazine (ATZ), 2-chloro-4-(ethylamino)-6-(isopropylamino)-s-triazine, by Fenton's reagent (FR) was investigated as a function of reagents' concentrations and ratios in a batch reactor. The degradation of ATZ was effectively achieved by hydroxyl radicals, which were generated in the FR process. The decay rates of ATZ and the oxidation capacities of FR were found to depend on the concentrations of hydrogen peroxide and ferrous ion. The removal kinetics of ATZ are initiated by a rapid decay and then followed by a much slower one. After an extended reaction time (5-10 min), the reactions ceased because the Fe(II) and H(2)O(2) were consumed and would be deactivated in the process. A mathematical model was successfully developed to describe the two-stage reaction kinetics by using two simple but critical parameters: the initial ATZ decay rate and the final oxidation capacity of Fenton's process. In general, higher [Fe(II)] or H(2)O(2) concentrations result in faster initial decay rate and higher oxidation capacity. However, the oxidation capacity is more sensitive to the initial [Fe(II)] due to the presence of side reactions as discussed in the paper.     

Citric acid-modified Fenton's reaction for the oxidation of chlorinated ethylenes in soil solution systems

Fenton's reagent, a solution of hydrogen peroxide and ferrous iron catalyst, is used for an in situ chemical oxidation of organic contaminants. Sulfuric acid is commonly used to create an acidic condition needed for catalytic oxidation. Fenton's reaction often involves pressure buildup and precipitation of reaction products, which can cause safety hazards and diminish efficiency. We selected citric acid, a food-grade substance, as an acidifying agent to evaluate its efficiencies for organic contaminant removal in Fenton's reaction, and examined the impacts of using citric acid on the unwanted reaction products. A series of batch and column experiments were performed with varying H2O2 concentrations to decompose selected chlorinated ethylenes. Either dissolved iron from soil or iron sulfate salt was added to provide the iron catalyst in the batch tests. Batch experiments revealed that both citric and sulfuric acid systems achieved over 90% contaminant removal rates, and the presence of iron catalyst was essential for effective decontamination. Batch tests with citric acid showed no signs of pressure accumulation and solid precipitations, however the results suggested that an excessive usage of H2O2 relative to iron catalysts (Fe2+/H2O2<1/330) would result in lowering the efficiency of contaminant removal by iron chelation in the citric acid system. Column tests confirmed that citric acid could provide suitable acidic conditions to achieve higher than 55% contaminant removal rates.     

Kinetic model for phenolic compound oxidation by Fenton's reagent

A kinetic model is developed for the oxidation of phenolic compounds by Fenton's reagent. In the first stage a rigorous kinetic model is applied to calculate the different kinetic rate constants for the oxidation process of p-hydroxybenzoic acid. In a second phase a competitive method is applied to calculate these kinetic constants for another 10 phenolic compounds present in agroindustrial and pulp paper wastewaters. These 10 phenolic compounds were: beta-resorcylic acid, 3-(4-hydroxyphenyl)-propionic acid, ferulic acid, protocatechuic acid, caffeic acid, p-coumaric acid, vanillic acid, syringic acid, veratric acid and 3,4,5-trimethoxybenzoic acid.     

类Fenton氧化-絮凝耦合处理活性艳红K-2BP的研究

以H2O2为氧化剂、聚硅硫酸亚铁(PFSSⅡ)为催化絮凝剂,两者耦合形成类Fenton试剂氧化-絮凝处理活性艳红K-2BP废水.当PFSSⅡ的铁硅摩尔比为1∶3,H2O2和PFSSⅡ的投加量分别为10 mg/L和15 mg/L(以Fe2+计)时,活性艳红的脱色率可达到98%以上,且氧化反应速率符合三级反应速率方程.与传...     

Treatment of reactive dyes and textile finishing wastewater using Fenton's oxidation for reuse

Fenton's oxidation (FO) was used to decolourise and degrade some reactive dyes (Remazol Black 5, Remazol Red, Remazol Blue, Remazol Yellow) and raw textile finishing industry effluents (S1, S2, S3) containing mainly reactive dyes. The operational conditions for pH varied between 2.5 and 4.0 while temperature ranged from 30°C to 50°C. The concentrations of FeSO₄ and H₂O₂ varied to a wide range (200–600 mg/l of FeSO₄, 300–1000 mg/l of H₂O₂) depending on the type of the dyes and their mixture and textile additives used in the process. FO is highly effective for colour removal (>99%) for reactive dyes and (87–94%) for textile finishing wastewater. It can be applied as a pretreatment and the remaining total dissolved solids (TDS) can be removed by an additional advanced process, e.g. membrane process.     

地下水中BTEX的原位生物修复研究进展

BTEX是苯、甲苯、乙苯和二甲苯的统称,存在于原油和石油产品中,其作为化工原料,广泛应用于农药、塑料及合成纤维等制造业.BTEX已成为地下水中普遍存在的污染物,自然衰减或生物修复工程已成功应用于地下水中BTEX的去除.自然衰减受BTEX污染的地下水具有良好的效果,但相比之下,生物修复工程更快、更有效.综述了在好氧和厌氧条件下,地下水中BTEX原位生物修复过程的微生物降解机制.     

异相类Fenton氧化处理T酸废母液的催化剂

为了比较黄铁矿、钛铁矿、磁铁矿、钒钛磁铁矿、零价铁以及亚铁催化双氧水氧化处理T酸废母液的效能,研究了不同体系的催化氧化反应动力学以及pH值变化情况,考察了H2O2投加量、催化剂投加量及循环利用次数的影响.研究结果表明,黄铁矿、钛铁矿催化活性较亚铁离子更好,且受废水pH值变化影响小,T酸废母液TOC去除率高达75%左右,是十分有效的类Fenton反应催化剂.钛铁矿催化活性较黄铁矿好,重复利用5次,TOC去除率依然保持在72%以上,表明钛铁矿有着很好的重复利用性.     

吸附-电化学氧化耦合处理对氯苯酚废水及动力学

以毡状活性炭纤维为阳极,不锈钢为阴极,吸附-电化学氧化耦合降解对氯苯酚废水进行了研究。考察了吸附或耦合电化学氧化过程、电流密度、支持电解质硫酸钠浓度和活性炭纤维重复使用对废水COD去除率的影响,结果表明,采用吸附-电化学氧化耦合方法,当电流密度7.6 mA/cm2支持电解质（硫酸钠）浓度为1 g/L,处理时间为180 min,4-CP废水COD去除率可达97.09%。毡状活性炭纤维对4-CP的静态吸附过程符合Langmiu吸附等温方程。建立了吸附-电化学氧化COD去除动力学模型,动力学模型参数表明,对于COD的去除,电化学氧化作用比吸附作用大。