Fenton氧化联合人工湿地处理污泥中的重金属

针对单独应用Fenton氧化技术处理污泥的不足以及人工湿地在处理污水污泥方面的优势,以污水处理厂污泥浓缩池中含重金属污泥为对象,研究其依次经过Fenton氧化和人工湿地处理后重金属的去除效果及形态变化,以及污泥pH、TN和TP的变化情况。结果表明,Fenton氧化提高了污泥重金属的生物有效性,并促进了人工湿地对重金属的去除。Fenton氧化污泥经人工湿地处理后,Cu、Zn、Ni和Mn的去除率分别为67.2%、79.7%、37.0%和17.0%,与对照相比重金属的平均去除率提高了27.5%。经人工湿地处理后Fenton氧化污泥和原污泥重金属的生物有效性均降低。Fenton氧化污泥pH为4.4～4.6,经人工湿地处理后为6.2～7.1。人工湿地对Fenton氧化污泥和原污泥中TN的影响较小,而对TP表现出较高的去除率,2系统TP的去除率分别为51.1%和45.5%。     

可用于去除高盐废水中有机污染物的混凝-Fenton氧化联合工艺

以某环氧树脂生产厂产生的高盐有机废水为对象,对比研究了Fenton、Fenton-混凝、混凝-Fenton等工艺去除废水中有机污染物的效能。考察了Fenton反应中Fe2+、H2O2投加比、初始pH、反应时间以及混凝反应中混凝剂种类、投加量等参数对处理效果的影响。结果表明：Fenton工艺的最佳条件为亚铁和过氧化氢投加比1：20,投加量分别为25 mmol·L-1和500 mmol·L-1,初始pH 3,反应时间120 min,TOC去除率为62.50%;混凝工艺选择FeSO4混凝剂,投加量为300 mg·L-1,TOC去除率为23.78%;废水经过Fenton-无混凝剂混凝、Fenton-混凝剂混凝、混凝-一级Fenton氧化和混凝-二级Fenton氧化工艺处理,TOC去除率分别为68.32%、71.51%、80.69%和89.27%。     

Fenton试剂氧化法处理染料结晶废母液

采用Fenton试剂氧化法处理分散橙、分散紫和分散蓝3种染料结晶废母液。研究了H₂O₂加入量、n（H₂O₂）#x02236;n（Fe²⁺）和废母液pH对COD去除率或TOC去除率的影响。对TOC去除反应分段进行了动力学方程拟合,并探讨了反应机理。实验得到的分散橙、分散紫和分散蓝的废母液处理工艺条件：H₂O₂加入量分别为264.4,352.9,441.2mmol/L;n（H₂O₂）#x02236;n（Fe²⁺）分别为20,10,20;废母液pH=3。3种废母液在0~20min和20~120min两个阶段的反应与二级动力学拟合方程的相关性最好。3种废母液经Fenton试剂氧化处理后,部分有机物降解为小分子有机酸,部分有机物完全矿化。     

混凝-Fenton-BAF深度处理垃圾渗滤液中试研究

针对经过SBR处理后,难以再进一步生化降解的垃圾渗滤液,提出混凝-Fenton-曝气生物滤池(BAF)工艺进行深度处理.首先利用混凝去除SBR出水的悬浮性有机物,降低Fenton试剂的处理成本;然后采用Fenton试剂进行氧化处理,既降低垃圾渗滤液的COD值,又提高其可生化性,最后通过BAF工艺去除有机物,实验结果表明,在SBR出水COD为600～800 mg/L的情况下,最终出水的COD低于80 mg/L,处理成本仅为2.6元/t.     

Fenton氧化-序批式膜生物反应器耦合处理干法腈纶废水

采用Fenton氧化-序批式膜生物反应器(SBMBR)组合工艺处理干法腈纶废水。结果表明,在废水初始pH值为3.0,H2O2投加量为90.0 mmol/L,Fe2+投加量为20.0 mmol/L,反应时间为2.0 h的条件下,Fenton氧化预处理对腈纶生产废水的COD去除率达到47.0%以上,COD由1 091 mg/L降至560 mg/L,废水的BOD5/COD由0.32升至0.69,废水的可生化性得到显著提高。Fenton处理出水与丙烯腈废水等比例混合后,采用SBMBR进行生化处理,在水力停留时间为24 h,90 min缺氧/150 min好氧交替运行的条件下,COD、NH4+-N和TN的平均去除率分别为71.7%、97.2%和47.4%,碳源不足是限制TN去除效果的主要影响因素。在无外加碳源的条件下,组合工艺处理后出水COD和NH4+-N浓度分别为117 mg/L和1.7 mg/L,出水水质可以稳定达到国家一级排放标准(GB8978-1996)。     

铁碳微电解-Fenton法预处理苯胺基乙腈生产废水的动力学研究

通过采用铁碳微电解-Fenton法预处理苯胺基乙腈生产废水的实验研究,分析了处理过程的COD降解动力学;同时研究了单纯活性炭吸附和微电解过程中COD去除率的变化。结果表明,铁碳微电解的初期COD降解过程近似符合一级反应动力学,并且得到微电解与活性炭吸附对铁碳微电解降解COD的关系式;Fenton反应中通过研究有机物浓度和过氧化氢初始浓度与反应进程的关系,建立了反应动力学模型;单纯吸附实验COD去除率在24h内快速下降,而微电解在相应时间内COD去除率波动较小,为实际应用提供了数据经验和理论依据。     

某化工园区污水处理厂Fenton处理方案的比较研究

利用GC-MS分析了某化工园区污水厂一期（化工）进水中的有机物组分,并通过活性污泥呼吸抑制实验评估其微生物毒性及对现有生化处理系统的影响。在此基础上,对Fenton试剂后置深度处理和前置预处理2个方案开展比较研究。结果表明,一期进水含多种难降解有机物,对生活污泥表现出微生物毒性,但对园区污水厂污泥无明显呼吸抑制作用。Fenton试剂后置处理生化出水,当进水COD-1,在pH为3.5左右,H2O2投加量为5 mmol·L-1,Fe2+/H2O2摩尔比为1：2的条件下,出水COD可稳定低于60 mg·L-1,处理成本不含污泥处置费低于1.8元·t-1水,难降解组分从18种减少为4种。而Fenton试剂前置预处理化工废水时,废水B/C在几种Fenton药剂组合下均未能达到0.3以上,无法得到理想的可生化性提高效果。因此推荐该化工园区污水厂采用Fenton试剂后置处理工艺为主的提标改造方案。     

Multi-response optimization of Fenton process for applicability assessment in landfill leachate treatment

Fenton process, as a pretreatment method, was found to be effective in the primary treatment of mature/medium landfill leachate. However, the main problem of the process is the large amount of produced sludge that requires an accurate feasibility evaluation for operational applications. In this study, the response surface methodology was applied for the modeling and optimization of Fenton process in three target responses, (1) overall COD removal, (2) sludge to iron ratio (SIR) and (3) organics removal to sludge ratio (ORSR), where the latter two were new self-defined responses for prediction of sludge generation and applicability assessment of the process, respectively. The effective variables included the initial pH, [H₂O₂]/[Fe²⁺] ratio and Fe²⁺ dosage. According to the statistical analysis, all the proposed models were adequate (with adjusted R² of 0.9116–0.9512) and had considerable predictive capability (with prediction R² up to 0.9092 and appropriate adequate precision). It was found that all the variables had significant effects on the responses, specifically by their observed role in dominant oxidation mechanism. The optimum operational conditions obtained by overlay plot, were found to be initial pH of 5.7, [H₂O₂]/[Fe²⁺] ratio of 17.72 and [Fe²⁺] of 195 mM, which led to 69% COD removal, 2.4 (l sludge/consumed mole Fe²⁺) of SIR and 16.5 (gCOD removed/l produced sludge) for ORSR in verification test, in accordance with models-predicted values. Finally, it was observed that [H₂O₂]/[Fe²⁺] ratio and Fe²⁺ dosage had significant influence on COD removal, while Fe²⁺ dosage and [H₂O₂]/[Fe²⁺] ratio had remarkable effects on SIR and ORSR responses, respectively.     

Ethanol washing of PAH-contaminated soil and Fenton oxidation of washing solution

As a means to remediate soil contaminated by polycyclic aromatic hydrocarbons, we investigated a combined process involving ethanol washing followed by a Fenton oxidation reaction. Artificial loamy soil was contaminated with various representative polycyclic aromatic hydrocarbons (i.e., fluorene, anthracene, pyrene, benzo(b)fluoranthene, or benzo(a)pyrene) at concentrations ten times higher than regulatory soil standards of The Netherlands or Canada, and then washed four times in ethanol, which reduced the concentration of polycyclic aromatic hydrocarbon contamination to below the regulatory standard. Fenton oxidation of ethanol solutions containing anthracene, benzo(a)pyrene, pyrene, acenaphthylene, acenaphthene, benz(a)anthracene, benzo(j)fluoranthene, or indeno(1,2,3-cd)pyrene showed a removal efficiency of 73.3%–99.0%; by contrast, solutions containing naphthalene, fluorene, fluoranthene, phenanthrene, or benzo(b)fluoranthene showed a removal efficiency of 9.6%–27.6%. Since each of the nonremediated polycyclic aromatic hydrocarbons, excluding benzo(b)fluoranthene, are easily biodegradable, these results indicate that the proposed treatment can be successfully applied to polycyclic aromatic hydrocarbon-contaminated soil that does not contain high concentrations of benzo(b)fluoranthene. The main reaction products resulting from Fenton oxidation of ethanol solutions containing anthracene or benz(a)anthracene were anthraquinon or benz(a)anthracene-7,12-dione, respectively; while 1,8-naphthalic anhydride was produced by solutions of acenaphthylene and acenaphthene, and 9-fluorenone by a fluorene solution. Received: June 9, 1998 / Accepted: March 24, 1999     

Electro-Fenton法的影响因素及研究进展

Electro-Fenton法是一种新型的电催化氧化技术,具有"环境友好"的特点,是一种高级氧化技术(AOPs)。结合国内外Electro-Fenton法的研究近况,阐述Fenton法的作用机理及主要影响因素,主要受pH值、O2流量、温度、电流密度、Fe2+离子浓度、电极间距离、电解质及电极材料等因素影响,结合具体的废水对主要反应参数进行总结,分析作用机理。对Electro-Fenton法的研究发展趋势提出了一些观点。