Pretreatment of Olive Oil Mill Wastewater by Two Different Applications of Fenton Oxidation Processes

The removal of chemical oxygen demand (COD) and phenol from olive oil mill wastewaters (OOMW) was investigated experimentally by using conventional Fenton (CFP) and Fenton type processes (FTP) with zero valent iron (ZVI). Different operational parameters such as initial pH, Fe²⁺, Fe⁰, and H₂O₂ concentrations were examined. Kinetic studies in terms of COD and phenol removals for both CFP and FTP were performed. The original pH value (4.6) of OOMW for CFP was found as the optimum pH. The determined optimum conditions are [Fe²⁺] = 1500 mg L^?1, [H₂O₂] = 1750 mg L^?1, and pH = 4.6 for CFP; [Fe⁰] = 2000 mg L^?1, [H₂O₂] = 2000 mg L^?1, and pH = 3 for FTP. 82.4% COD and 62% phenol removals were performed under the optimum conditions by CFP, while 82% COD and 63.4% phenol were removed by FTP. According to the results of kinetic studies, it was observed that COD and phenol were removed by FTP more rapidly, compared to CFP. Consequently, it was determined that both CFP and FTP were effective processes for the pretreatment of OOMW.     

Fe-ZSM-5分子筛催化降解染料废水的研究

传统的Fenton均相亚铁盐催化剂处理染料废水,具有难以避免的二次污染和亚铁离子流失问题。分子筛催化剂相比传统催化剂具有高效环保的特点,在催化氧化染料废水领域有着良好的前景。本文通过液相离子交换法制备了Fe-ZSM-5非均相分子筛催化剂,替代传统的亚铁盐催化剂,应用X射线衍射对制备的Fe-ZSM-5分子筛催化剂进行表征,表明随离子交换次数的增加,Fe-ZSM-5催化剂负载的铁量上升,且较好地保持了分子筛结构,有利于提高亚铁离子的催化能力。通过实验确定了Fe-ZSM-5催化剂催化反应的最佳温度、pH值、Fe-ZSM-5的用量、反应时间等工艺参数,比较了Fe-ZSM-5催化剂和传统Fenton均相催化剂降解染料废水的脱色率和废水中铁离子的残留量,结果表明Fe-ZSM-5的脱色率达到98.5%,相比于Fenton均相催化剂的脱色率提升约3%;两种催化剂的铁离子残留量差别显著,Fe-ZSM-5催化剂处理的废水中只产生微量的Fe离子,可以认为Fe-ZSM-5非均相分子筛催化剂有效地解决了催化剂损耗和二次污染问题。     

Pilot‐Scale Degradation of Organic Contaminants in a Continuous‐flow Reactor by the Helielectro‐Fenton Method

The feasibility of pilot‐scale mineralization of organic pollutants in wastewaters using the Electro‐Fenton® process is demonstrated. The treatment was applied in a continuous‐flow reactor, to solutions of nitrobenzene, 2,4‐D and benzoic acid and to actual wastewaters from a fine chemicals company along with a pulp and paper company. The results showed mineralization yields from 60 to 84% by simply applying the Electro‐Fenton® process. When a subsequent exposure to sunlight was carried out (Helielectro‐Fenton method), this mineralization almost went to completion, except for the effluent from the fine chemicals industry.     

Optimization of a Photo‐assisted Fenton Oxidation Process: A Statistical Model for MDF Effluent Treatment

In the present study, the effects of initial COD (chemical oxygen demand), initial pH, Fe²⁺/H₂O₂ molar ratio and UV contact time on COD removal from medium density fiberboard (MDF) wastewater using photo‐assisted Fenton oxidation treatment were investigated. In order to optimize the removal efficiency, batch operations were carried out. The influence of the aforementioned parameters on COD removal efficiency was studied using response surface methodology (RSM). The optimal conditions for maximum COD removal efficiency from MDF wastewater under experimental conditions were obtained at initial COD of 4000 mg/L, Fe²⁺/H₂O₂ molar ratio of 0.11, initial solution pH of 6.5 and UV contact time of 70 min. The obtained results for maximum COD removal efficiency of 96% revealed that photo‐assisted Fenton oxidation is very effective for treating MDF wastewater.     

Fenton氧化膜-生物反应器出水中丙烯腈的实验研究

采用膜-生物反应器和Fenton氧化组合工艺对丙烯腈废水进行处理。从GC/MS测量结果来看,膜-生物反应器出水中主要物质为2,6双（二甲基-乙基）-4-酚、苯二甲酸和硝基苯二甲酸,均为生物难降解有机物,使出水不能达标。后续Fenton氧化工艺处理膜生物反应器出水,可以使COD含量等指标达到所要求的排放标准。经过膜-生物处理与Fenton法结合的优化工艺,COD去除率达到80%~88%,去除率达到98%,出水水质可达排放标准。Fenton氧化工艺的最佳工艺条件为：pH值为3.4,硫酸亚铁的投加量为700mg/L,双氧水的投加量为600mg/L。     

Fenton体系处理黑臭河道沉积物的效果初探

沉积物中有机质的削减是黑臭水体治理的关键.Fenton(Fe^2++H2O2)试剂在有机污染废水和土壤原位修复中的应用广泛且效果良好;Fenton试剂也能很好地去除黑臭水体中的色度和浊度,但其氧化沉积物有机质的研究未见报道.为探究Fenton试剂对黑臭水体沉积物的氧化效果,本研究通过室内模拟实验用Fenton氧化法对黑臭河道沉积物进行处理,考察氧化过程沉积物特征和性质的变化;分析覆水后沉积物中污染物的释放特征,并和H2O2体系(无Fe^2+)进行比较.结果表明:Fenton体系显著提高了沉积物与上覆水的氧化还原电位,对黑臭河道沉积物中的有机质具有很强的氧化效率.在温度为28℃、H2O2为20%Q(Q为体系中沉积物有机质完全矿化的理论H2O2用量)和Fe^2+∶H2O2(摩尔比)为0.5∶1时,反应1 d,酸挥发性硫化物去除率为70.13%,沉积物总有机碳减少了22.14%,总有机氮减少了87.60%,生成了较多的铵态氮和硝态氮;由于铁对磷的钝化,沉积物中溶解性反应磷含量大幅减少.H2O2体系的氧化速度较Fenton体系慢,覆水后对体系中的Eh提高不明显.值得注意的是,Fenton体系会降低上覆水的pH,释放较多的铵态氮.需要联合其他技术(如微生物法),强化水体中有机质和氨氮的降解,以取得理想的修复作用.     

高盐强酸性地下水中复合苯系污染物原位芬顿氧化实验研究

在原位氧化过程中,实际场地地下水和含水介质的物化特征是影响氧化效果的重要因素,而目前对此影响的研究较少。以某场地实际高盐强酸性复合苯系污染地下水为研究对象,以地下水中2-硝基-4-甲氧基苯胺(2-nitro-4-methoxyaniline,2-N)和3-硝基-4-甲氧基苯胺(3-nitro-4-methoxyaniline,3-N)为特征污染物,探究芬顿(Fenton)试剂原位氧化特征,并研究液相环境因素(初始H2O2浓度、初始Fe2+浓度、初始pH值、初始醋酸(Acetic acid,HAc)浓度、初始SO4^2-浓度)以及含水层介质对Fenton法去除2-N和3-N的影响。结果显示:(1)Fenton法去除2-N和3-N效果显著,且在初始液相条件为c(H2O2)=7 mmol/L、c(Fe²⁺)=4 mmol/L、pH=4、c(HAc)=0 mg/L和c(SO4^2-)=0 mmol/L时去除效果最佳;(2)各因素对Fenton法氧化2-N和3-N的影响不同,加入H₂O₂和Fe²⁺使2-N和3-N去除率上升,增大HAc浓度使2-N和3-N去除率下降;(3)含水层介质对2-N和3-N具有一定吸附性,且对3-N的吸附性强于2-N,二者在本实验中最大吸附态占比分别为29%和42%,而吸附态的存在会抑制Fenton法对2-N和3-N的去除;(4)矿物分析结果显示介质含有少量黄铁矿,在硫酸环境下,介质腐蚀溶解释放Fe²⁺,在达到一定浓度后,无需额外添加Fe²⁺即可完成Fenton反应进而去除2-N和3-N。