UV/Fenton/均相铜类Fenton氧化处理紫菜加工废水COD及色度研究

以COD和色度作为评价指标,采用均相Fenton、Cu-Fenton、UV/Fenton、UV/Cu-Fenton体系处理紫菜加工废水,探究了在室温条件下不同初始pH值、Fe^(2+)和Cu^(2+)投加量、H_(2)O_(2)投加量等因素对出水COD和色度的去除效果,通过正交试验确定了最佳反应条件,同时对反应机理进行了分析。分析显示羟基自由基(·OH)是UV/Fenton/均相铜类Fenton体系去除紫菜废水中COD及色度的主要活性基团。在最佳反应条件下,UV/Fenton体系在100 min时出水COD为40 mg/L,色度为25,比无UV时最佳反应时间缩短了50 min;UV/Cu-Fenton体系,在60 min时出水COD为35 mg/L,色度为20,比无UV时最佳反应时间缩短了一半,UV/Fenton体系和UV/Cu-Fenton体系出水COD及色度均能达标排放。

Oxidation of Partially Hydrolyzed Polyacrylamide from Polymer Flooding Processes Using Fenton Reagents

The degradation of partially hydrolyzed polyacrylamide(HPAM) found in alkaline/surfactant/polymer flooding sewage was investigated using Fenton-type reagents. Different Fenton reagent treatments for HPAM degradation were compared. The effects of pH, hydrogen peroxide(H_(2)O_(2)), ferrous ion(Fe^(2+)), and tartaric ion(C_(4)H_(4)O_(6)^(2-)) concentrations were studied. The degradation reaction occurred within a wide range of pH(3–9). The HPAM degradation performance of photo-Fenton processes using solar light and UV were compared with that of the Fenton process. The degradation rate was found to be strongly dependent on the H_(2)O_(2)/Fe^(2+)/C_(4)H_(4)O_(6)^(2-)molar ratio. The HPAM degradation efficiency was 90%, and the chemical oxygen demand removal efficiency was 85%. HPAM could be degraded into a compound with a lower molecular weight, but it was difficult to achieve complete mineralization to CO_(2). The presence of intermediate products hindered further oxidation in the Fenton process.

Treatment Processes of Leachate from a Landfill by Advanced Oxidation Fenton and Ozone-UV

In this paper it is presented the results of advanced oxidation of leachates from a technified sanitary landfill located in the State of Querétaro, Mexico. One characteristic of already stabilized leachates from sanitary landfills like this case, is their difficult degradation, mainly because the organic matter contained is recalcitrant. For the samples collect, four sites were selected, where three points per site were sampled, measuring at each site the parameters: temperature, pH, conductivity, redox potential (ORP) and dissolved oxygen (DO) and leachate samples were collected. On the other hand, the Chemical Oxygen Demand (COD) of crude leachates, leachates acidified and leachates oxidized by Fenton reagent and Ozone-UV combined were analyzed. COD was used to monitor the degradation kinetics. With the results, the ArcGIS software was applied to study the distribution of temperature, dissolved oxygen and COD mainly in the leachate lagoon. For the application of Fenton reagent in the crude leachate oxidation, the pH was first adjusted and Fe2+/H2O2 ratio was optimized. The efficiency of Ozone-UV treatments was studied through COD degradation kinetics. The graphs of in (Ci/Co) vs time, showed that the kinetic processes are of order one, with very acceptable regression coefficients (R2) and extraordinarily similar speed constants (K). With Fenton oxidation, the highest percentage of COD degradation was achieved and with Ozone-UV oxidation, it was possible to practically degrade all the COD.

UV/Fenton法深度处理含双氯芬酸和锌废水的工艺优化

为研究含药物和重金属复合废水的处理方法,采用UV/Fenton工艺对经过生物处理后的含双氯芬酸(DCF)和Zn^(2+)废水进行处理,通过单因素实验法分析了H_(2)O_(2)浓度、Fe^(2+)浓度和反应时间对废水中COD、DCF和NH_(4)^(+)-N去除效果的影响。结果表明,随着H_(2)O_(2)浓度和Fe^(2+)浓度投加量的升高,COD和DCF的去除率呈先上升后下降的趋势,NH_(4)^(+)-N的去除率则趋于稳定。随着反应时间的增加,COD、DCF和NH_(4)^(+)-N除率均为先上升后趋于平衡。结合成本和效率考虑,得出最佳处理条件为:H_(2)O_(2)的最佳投加量为600 mg/L,Fe^(2+)的最佳投加量为45 mg/L,最佳反应时间应设置为90 min。

紫外光引发Fenton氧化技术协同去除造纸中段废水COD_(Cr)的性能研究

对紫外光引发Fenton氧化技术协同处理造纸中段废水COD_(Cr)进行了研究,探究反应时间、FeSO_(4)·7H_(2)O浓度、H_(2)O_(2)浓度、pH值、紫外光强度等因素对COD_(Cr)去除效率的影响。实验结果表明,在反应时间80min,FeSO_(4)·7H_(2)O浓度0.6 mol/L,H_(2)O_(2)浓度0.3 mol/L,pH值为4,以及紫外光强度为14 mW/cm^(2)的最优条件下,该技术能够实现造纸中段废水74%的COD_(Cr)去除率。紫外光引发Fenton氧化技术能够有效促进Fenton氧化反应中·OH自由基的生成,提高造纸中段废水的COD_(Cr)去除效率。

UV-Fenton工艺的研究进展及其在水环境微污染处理领域的应用

近年来,水环境中的新型难降解污染物受到广泛关注,催生了该领域大量降解、还原及吸附等处理技术的相关研究,尤其是基于强氧化性自由基的高级氧化法(AOPs),典型工艺就是Fenton法。但在传统Fenton氧化体系中,H_(2)O_(2)的利用效率较低,铁泥产量高,且pH限制范围较窄,影响了Fenton反应的整体降解效果及应用。因此,引入了紫外光以提高H_(2)O_(2)的分解效率,即UV-Fenton体系,较传统Fenton可以有效减少Fe^(2+)用量,促进Fe^(3+)向Fe^(2+)的转化,加速H_(2)O_(2)分解,并提高H_(2)O_(2)利用率,进而使有机物矿化更彻底。文章详细对比了传统Fenton与UV-Fenton工艺,介绍UV-Fenton工艺的反应原理,并讨论其影响因素(例如光照强度、Fe^(2+)和H_(2)O_(2)用量等),同时,文章总结了UV-Fenton工艺在水环境领域及微污染处理中的实际应用,包括有机染料、抗生素、农药及全氟化合物等。最后对UV-Fenton工艺的研究改进方向以及实际应用存在问题提出了展望。

Photoassisted fenton oxidation of refractory organics in UASB-pretreated leachate

Nearly 91% of organic pollutants in Hong Kong leachate could be effectively removed by the UASB(upflow anaerobic sludge blanket) process followed by the fenton coagulation. The COD (chemical oxygen demand) of leachate was lowered from an average of 5620 mg/L to 1910 mg/L after the UASB treatment at 37℃, and was further lowered to 513 mg/L after fenton coagulation. The remaining refractory residues could be further removed by photochemical oxidation with the addition of H 2O 2. The BOD/COD ratio was greatly increased from 0.062 to 0.142, indicating the biodegradability of organic residues was improved. The photochemical oxidation for the fenton\|coagulation supernatant was most effective at pH 3\_4, with the addition of 800 mg/L of H 2O 2, and UV radiation time of 30 minutes. The final effluent contained only 148 mg/L of COD, 21 mg/L of BOD(biochemical oxygen demand) and 56 mg/L of TOC (total organic carbon).

三维电极电Fenton处理阿奇霉素制药废水研究

以钛涂钌铱电极(RuO_(2)-IrO_(2)/Ti)为阳极,石墨为阴极,活性炭为粒子电极构建三维电极电Fenton体系,研究三维电极电Fenton处理阿奇霉素制药废水的影响因素,系统性考察活性炭粒子电极类型及投加量对处理效果的影响,并通过改变极板间距、pH、曝气强度、电解电压、反应时间等因素,确定最佳反应条件。进一步通过正交实验比较各因素影响程度大小,优化三维电极电Fenton处理阿奇霉素制药废水实验条件。结果表明,以3 mm柱碳作为粒子电极,当其投加质量浓度为100 g/L时,最佳工艺条件为pH=3、电解电压15 V、曝气强度1.0 L/min、极板间距7 cm、反应时间2 h。此条件下,废水COD平均去除率为72.28%,B/C由初始的0.086上升至0.312,处理效果达最优。此外,各因素对于三维电极电Fenton处理阿奇霉素制药废水效果的影响程度为pH>曝气强度>电解电压>反应时间>极板间距。

Fenton氧化法在工业有机废水处理中的试验研究

工业有机废水具有很高的化学需氧量(COD),潜在污染风险大,已对生态环境构成严重挑战。本研究采用Fenton氧化法处理工业有机废水,通过单因素试验和正交试验分析FeSO_(4)·7H2O用量、H2O2用量和pH对COD去除率的影响。结果表明,Fenton氧化法能够有效去除工业有机废水中的COD,最佳工艺条件下,FeSO_(4)·7H2O用量为0.5 g,H2O2用量为2.0 mL,pH为3,COD去除率最佳。本研究为工业有机废水的高效处理提供有力支持。

Treatment of Landfill Leachate by Fenton Oxidation Process

Central composite design (CCD), the most popular design ofresponse surface methodology (RSM), was employed to investigate theeffect of total organic carbon (TOC) ratio of high molecular weightorganic matter (HMW) to low molecular weight organic matter (LMW),the LMW strength and molar ratio of hydrogen peroxide to ferrous ionon landfill leachate treatment by Fenton process. Based on theexperimental data, a response surface quadratic model in terms ofactual factors was obtained through analysis of variance (ANOVA).

Treatment of 2-phenylamino-3-methyl-6-di-n-butylaminofluoran production effluent by combination of biological treatments and Fenton's oxidation

High strength refractory organic stream is produced during the production of 2-phenylamino-3-methyl-6-di-n-butylaminofluoran （One Dye Black 2, abbr. ODB 2）, a novel heat-sensitive material with a promising market. In this study, a combination of acidificationprecipitation, primary biological treatment, Fenton＇s oxidation and another biological treatment was successfully used for the removal of COD from 18000-25000 mg/L to below 200 mg/L from the ODB 2 production wastewater in a pilot experiment. A COD removal of 70%-80% was achieved by acidification-precipitation under a pH of 2.5-3.0. The first step biodegradafion permitted an average COD removal of 70% under an hydraulic residence time （HRT） of 30 h. By batch tests, the optimum conditions of Fenton＇s oxidation were acquired as： Fe^2＋ dose 6.0 mmol/L; H2O2 dose 3000 mg/L; and reaction time 6 h. The second step biological treatment could ensure an effluent COD below 200 mg/L under an HRT of 10 h following the Fenton＇s treatment.

Several Rules for Treating Phenol Wastewater via Oxidation by O_3/UV-formed Radicals

The treatment of phenol wastewater with an ultraviolet source and an oxone generator by introducing salicylic acid as the capturer is described. The presence of HO during the phenol degradation has been proved. The impacts of factors such as acidity and reaction time on the HO formation are also discussed. The results demonstrate that HO ＇ generated from ozone/UV oxidation under a basic condition is the immediate cause of phenol degradation. At room temperature and a pH value of 9. 93, the degradation of phenol occurs rapidly within 0. 5 rain and the removal of phe- nol（ 100 mg/L） is above 98. 5% within 15 min; in the meantime, the pH value declines gradually with the degradation of phenol. A discussion about the formation and the transformation of the intermediate products during phenol degradation is included.

Degradation of Reactive Brilliant Red X-3B by Fenton Oxidation Method

Abstract [ Objective] The degradation conditions and course of reactive brilliant red X-3B by Fenton oxidation was investigated to understand the feasibility of using Fenton oxidation for dye removal. [Metbed] By using Fenton oxidation, the degradation conditions of reactive brilliant red X-3B wastewater was studied in different initial concentrations, then analyzed its degradation products and process through gas chromatography-mass spectrometer （GC-MS）. [ Remit] When H202：Fe2＋ （molar ratio） =3.1, the removal rate of CODc, was the highest. With the increase of Fe2＋ dos- age, the wastewater became red and more deposits generated. As CODc, of wastewater was 200,400 and 800 mg/L, the dosage of H202 was 0.5, 1.0 and 3.5 ml respectively, and the best initial pH of the wastewater was 4 -5, the removal rate of GODc, reached the maximum values. In addition, Fenton reaction was very fast, that is, most degradation occurred in the first 5 min. [ Cenclmion] Fenton oxidation technology is practical and efficient in the declradation of dves which are mineralized difficultly.

UV-catalytic treatment of spent caustic from ethene plant with hydrogen peroxide and ozone oxidation

The performance of UV/H 2O 2, UV/O 3 and UV/H 2O 2/O 3 oxidation systems for treating spent caustic from an ethylene plant was investigated. In UV/H 2O 2 system, with the increase of H 2O 2 dosage, removal efficiencies of COD and the ratio of biochemical oxygen demand(BOD) to chemical oxygen demand(COD) of the effluent were increased and a better performance was obtained than the H 2O 2 system alone. In UV/H 2O 2 system, removal efficiency of COD reach 68% under the optimum condition, and BOD/COD ratio was significantly increased from 0 22 to 0 52. In UV/O 3 system, with the increase of O 3 dosage, removal efficiency of COD and BOD/COD ratio were increased, and a better performance was obtained than the O 3 system alone. Under the optimum condition, removal efficiency of COD was 54%, and BOD/COD ratio was significantly increased from 0 22 to 0 48. In UV/H 2O 2/O 3 system, COD removal efficiency was found to be 22.0% higher than UV/O 3 system.

Enhanced electrochemical oxidation of phenol by introducing ferric ions and UV radiation

The mineralization of phenol in aerated electrochemical oxidation has been investigated.The results show that a cathodic Fenton process can occur when the Ti-0.3Mo-0.8Ni alloy material is used as cathode in solution containing ferric or ferrous ions; moreover,the reinforcement of cathodic Fenton process on the total organic carbon (TOC) removal rate of phenol is quite distinct.Among the metallic ions investigated,the ferric ion is the best catalyst for the electrochemical mineralization of phenol at initial...

A Molecular Mechanism of Fenton Oxidation Degradation of m-Xylene

Density functional theory（DFT） quantum chemical method was used to study the process of meta-xylene Fenton oxidation. The EHOMO energies of meta-xylene molecules are higher, so they have better ability to provide electron and prone to the nucleophilic reaction. M-xylene mainly reacts with OH free radical in addition reactions. And the position of C（6） is most likely to react with the OH free radical, rather than the C（3）, which is the most difficult to occur. According to all the above results, the most likely reaction mechanism of advanced oxidation degradation of meta-xylene is determined.

Treatment of Oil Field Wastewater after Chemical Flooding by Fenton Oxidation Combined with Biodegradation

Wastewater after chemical flooding is difficult to be treated by biological methods due to the residual chemicals in the wastewater. Fenton oxidation, which has been widely applied to detoxifying hazardous organic compounds and improving the biodegradability of these compounds, can solve this problem. So, in this paper, Fenton oxidation was used to enhance the biodegradability of the wastewater after chemical flooding. The op- timum operating conditions for the Fenton oxidation process were 2.5 g/L Fe2 ＋ , 600 mg/L H202 and 30 rain of treatment time. The wastewater pre- treated by Fenton oxidation was treated by aerobic activated sludge. It was found that a small amount of H202 can significantly increase both the biodegradation rate and extent of the wastewater. The effluent CODc, and HPAM contents were 260 and 94 mg/L respectively after the aerobic bio- logical process with the biodegradation time of 24 h. After Fenton oxidation combining with biodegradation, the total CODc, removal efficiency was up to 90%, and polymer and oil degrading efficiencies were 95% and 92% respectively.

Fenton氧化+水解酸化+接触氧化+MBR工艺处理船舶含油废水实例

针对船舶含油污水所具有的高含油量、高COD、可生化性低的特点,设计“隔油+气浮+Fenton氧化+混凝沉淀+水解酸化+接触氧化+MBR+消毒”的污水处理工艺进行处理。项目运行结果显示,该工艺对船舶含油污水具有较好的处理效果,实际处理污水9.9×10~4 m~3/a,COD、氨氮的去除率达98.00%和98.30%,出水水质满足《城镇污水处理厂污染物排放标准》(GB 18918-2002)一级A标准。

Effects of Influencing Factors on Fenton Oxidation of Antibiotic Pharmaceutical Wastewater by a Statistical Design Approach

A series of batch-scale experiments were completed to investigate the effects of operational parameters on chemical oxygen demand (COD) removal by Fenton reagent for antibiotic pharmaceutical wastewater (APW). The significance of five operational factors including the mass ratio of H2O2/COD (g/g), the mole ratio of H2O2/Fe2+ (mol/mol), initial pH, oxidation temperature T, and reaction time t were evaluated statistically by Box-Behnken design (BBD). It was found that the five parameters were all significant to the COD removal efficiency by t-test, as well as the interactions between mass ratio/reaction time and oxidation temperature/reaction. The optimal COD removal efficiency (89.50%) was achieved when the mass ratio of H2O2/COD and the mole ratio of H2O2/Fe2+ were 3.00 and 5.00 respectively, with pH value of 3.68 at 298K for 72min reaction. A quadratic regression model with 0.9907 regression coefficient (R2) was developed which had good agreement to the experimental data.

电Fenton技术对造纸废水中COD_(Cr)的去除研究

为了提高对造纸废水中COD_(Cr)的去除率,采用电Fenton协同技术处理造纸制浆废水,分别研究影响COD_(Cr)去除效率的因素,优化反应条件.实验结果表明,在反应时间80 min、pH=4、Fe^(2+)浓度为1.0 mol/L、H_(2)O_(2)浓度为0.8 mol/L、极板距离为10 cm、电解电压为10 V、曝气量为1.0 L/min,COD_(Cr)最大去除率为78%.该研究为造纸废水处理提供了理论基础.