Degradation of 2,4,6-trinitrotoluene in water and soil slurry utilizing a calcium peroxide compound

The degradation of 2,4,6-trinitrotoluene was examined in pure water and contaminated soil slurry using calcium peroxide as a source of solid hydrogen peroxide and oxygen. The extent of TNT oxidation was compared with that obtained by using hydrated lime, which is normally generated by slurrying CaO2 in water and contained in CaO2 technical formulation (approximately 50%, w/w). Complete TNT degradation occurred between 280 min, 0.1% CaO2/Ca(OH)2 and 20 min, 1% CaO2/Ca(OH)2. A large part of the generated oxidation products, 80-90%, were absorbed on the solid calcium hydroxide, whereas the remaining 10-20% was detected in solution until 48 h. Removal of nitro groups was extremely effective in CaO2 slurry, where all the nitrogen (3 mol per mol of TNT) was removed from TNT within 240 min. Respect to calcium hydroxide, the peroxy compound liberated H2O2 in solution, 370 mg l-1 at 0.2% CaO2, w/v, which then decomposed within 480 min. Most of the 14C-TNT was retained more strongly on the calcium hydroxide generated by slurrying CaO2. This pool remained adsorbed on the solid until pH dropped below 5.8. The treatment of a contaminated soil slurry, 700 mg TNT kg-1, reduced CH3CN extractable TNT below 20 mg kg-1 at very low concentration of CaO2/Ca(OH)2, approximately 0.2%, w/w. Both oxidants do not lead to soil sterilization as the phosphorus added to neutralize the pH serves as a source of nutrient for the soil biomass.     

Removal of TNT and RDX from water and soil using iron metal

Contaminated water and soil at active or abandoned munitions plants is a serious problem since these compounds pose risks to human health and can be toxic to aquatic and terrestrial life. Our objective was to determine if zero-valent iron (Fe(0)) could be used to promote remediation of water and soil contaminated with 2,4,6-trinitrotoluene (TNT) and hexahydro-1,3,5-trinitro-1,3,5-triazine (RDX). As little as 1% Fe(0) (w/v) removed 70 mg TNT litre(-1) from aqueous solution within 8 h and removed 32 mg RDX litre(-1) within 96 h. Treating slurries (1:5 soil:water) of highly contaminated soil (5200 mg TNT and 6400 mg RDX kg(-1) soil) from the former Nebraska Ordnance Plant (NOP) with 10% Fe(0) (w/w soil) reduced CH(3)CN-extractable TNT and RDX concentrations below USEPA remediation goals (17.2 mg TNT and 5.8 mg RDX kg(-1)). Sequential treatment of a TNT-contaminated solution (70 mg TNT litre(-1) spiked with (14)C-TNT) with Fe(0) (5% w/v) followed by H(2)O(2) (1% v/v) completely destroyed TNT and removed about 94% of the (14)C from solution, 48% of which was mineralized to (14)CO(2) within 8 h. Fe(0)-treated TNT also was more susceptible to biological mineralization. Our observations indicate that Fe(0) alone, Fe(0) followed by H(2)O(2), or Fe(0) in combination with biotic treatment can be used for effective remediation of munitions-contaminated water and soil.     

超声波/紫外线-Fenton反应联用去除克拉玛依土壤中石油类污染物

研究了超声波(ultrasonic)和紫外线(ultraviolet)-Fenton反应联用处理干旱区老化石油污染土壤。土壤TPH含量为30 470 mg/kg,pH值为3,H2O2与Fe比例为50∶1时,H2O2浓度为0.37%、0.74%、1.11%和1.85%在超声波处理6 h土壤TPH去除量分别为4 495、11 983、15 470和19 800 mg/kg;TPH去除量随H2O2/Fe2+增大而增大,H2O2/Fe2+为100∶1时,TPH去除量为12 699 mg/kg。溶液pH值接近中性,H2O2浓度为0.74%,H2O2/Fe2+为50∶1,超声波与UV共同作用2 h和4 h,TPH去除量分别达到14 824和21 821 mg/kg;UV单独作用2 h、4 h对土壤TPH去除量为9 253和12 845 mg/kg。超声波-Fenton反应对1,2-二甲苯降解效果最好,其次为C17-C28的直链及支链烷烃,最低为烃类衍生物。     

Fenton氧化/高浓度泥浆法处理矿山废水

为了解决某大型铜矿废水COD不达标问题，采用Fenton氧化对原有高浓度泥浆（HDS）工艺进行改进。探讨了Fenton氧化矿山废水各指标的去除效果以及H₂O₂浓度对出水COD去除效果的影响，结果表明，Fenton氧化-电石乳中和絮凝沉淀工艺处理矿山废水是可行的，最优实验条件为：pH稳定在3.0～4.5，H₂O₂投加量0.5 mL/L，电石乳投加量8.5 g/L，PAM投加量1.5 mg/L；系统对废水COD的去除机理是加入的H₂O₂和矿山酸性废水中的Fe²⁺离子在低pH下形成Fenton试剂；系统对TFe、Zn²⁺、Cu2+ 的去除效果比Mn²⁺的去除效果更稳定。     

Conditioning of aluminium-based water treatment sludge with Fenton's reagent: effectiveness and optimising study to improve dewaterability

Alternative conditioning of aluminium-based drinking water treatment sludge using Fenton reagent (Fe2+/H2O2) was examined in this study. Focuses were placed on effectiveness and factors to affect such novel application of Fenton process. Experiments have demonstrated that considerable improvement of alum sludge dewaterability evaluated by capillary suction time (CST) can be obtained at the relative low concentrations of Fenton reagent. A Box-Behnken experimental design based on the response surface methodology was applied to evaluate the optimum of the influencing variables, i.e. iron concentration, hydrogen peroxide concentration and pH. The optimal values for Fe2+, H2O2, and pH are 21 mg g(-1)DS(-1)(dry solids), 105 mg g(-1)DS(-1) and 6, respectively, at which the CST reduction efficiency of 48+/-3% can be achieved, this agreed with that predicted by an established polynomial model in this study.     

Fe/C微电解和Fenton氧化联合处理印刷电路板废水

研究了Fe/C微电解和Fenton氧化处理印刷电路板废水的最佳条件和联合工艺的处理效果。结果表明,Fe/C微电解最佳工艺条件为：pH=2,Fe/C质量比为2∶1,投加药剂量为30 g/L,停留时间为30 min;Fenton氧化最佳工艺条件为：pH=3,H2O2投加量为6 mL/L,停留时间为2 h。将2种方法联用并进行中试实验,结果表明,对原水的COD去除率可达80%,而且Fenton反应可利用微电解产生的Fe2＋,节约成本,运行稳定,效果良好。     

Fenton/絮凝工艺深度处理制浆造纸废水的工程应用分析

以某制浆造纸厂生化出水Fenton/絮凝深度处理工艺长期运行数据为依据,系统分析了H2O2、废酸液（FeSO4含量约8%）、硫酸铝、PAM及氧化钙等处理药剂用量与水量、进水负荷和COD去除量之间的关系。结果表明,H2O2、废酸液、硫酸铝、PAM及氧化钙的单位水量平均投加量分别为0.05、2.18、0.07、0.0075和0.27 kg/m3,而去除单位COD的药剂平均消耗量分别为0.20、8.48、0.27、0.029和1.06 kg/（kg COD）;H2O2、废酸液、硫酸铝和氧化钙的用量随进水负荷的增大而增加,而PAM随进水负荷的变化较小。H2O2和FeSO4的投加摩尔比（MH2O2/Fe2＋）主要集中在1.0-2.0之间,其中在1.0-1.6之间的累积频率达到93%。该工艺的出水COD和SS分别为65-100 mg/L和20-30 mg/L,达到《制浆造纸工业水污染物排放标准》（GB 3544-2008）排放要求。废水深度处理成本约为1.01元/m3,其中药剂费用约0.58元/m3,占56.98%。     

Accelerated remediation of pesticide-contaminated soil with zerovalent iron

High pesticide concentrations in soil from spills or discharges can result in point-source contamination of ground and surface waters. Cost-effective technologies are needed for on-site treatment that meet clean-up goals and restore soil function. Remediation is particularly challenging when a mixture of pesticides is present. Zerovalent iron (Fe0) has been shown to promote reductive dechlorination and nitro group reduction of a wide range of contaminants in soil and water. We employed Fe0 for on-site treatment of soil containing > 1000 mg metolachlor, > 55 mg alachlor, > 64 mg atrazine, > 35 mg pendimethalin, and > 10 mg chlorpyrifos kg(-1). While concentrations were highly variable within the windrowed soil, treatment with 5% (w/w) Fe0 resulted in > 60% destruction of the five pesticides within 90 d and increased to > 90% when 2% (w/w) Al2(SO4)3 was added to the Fe0. GC/MS analysis confirmed dechlorination of metolachlor and alachlor during treatment. Our observations support the use of Fe0 for ex situ treatment of pesticide-contaminated soil.     

Efficient use of Fe metal as an electron transfer agent in a heterogeneous Fenton system based on Fe0/Fe3O4 composites

In this work a novel heterogeneous Fenton system based on Fe(0)/Fe3O4 composites is described. The composites with several Fe(0)/Fe3O4 ratios were prepared by two different methods, i.e. mechanical alloying of Fe(0) and Fe3O4 powders and controlled reduction of Fe3O4 with H2. Reaction studies and detailed Conversion Electron M?ssbauer surface characterization of the composites Fe(0)/Fe3O4, Fe(0), Fe3O4, alpha-Fe2O3 and gamma-Fe2O3 suggested that Fe2+surf species are essential to produce an active Fenton system. Kinetic studies for the oxidation of the dye methylene blue, used as an organic model molecule, and for the peroxide decomposition suggest that the reactions proceed via HO* radicals generated from Fe2+surf species and H2O2 in a Fenton like mechanism. The increase in activity caused by the addition of Fe(0) is discussed in terms of a creation of Fe2+surf species during the preparation of the composite and by an electron transfer mechanism from Fe(0) to Fe3+surf during the Fenton reaction to regenerate the Fe2+surf active species.     

吸附饱和活性炭的Fenton试剂再生

颗粒活性炭吸附有机废水中二异丙基苯等有机物后，采用Fenton试剂对活性炭进行氧化再生。研究H2O2与Fe2＋的摩尔配比及投加量、pH、温度、再生时间等因素对活性炭再生效果的影响。实验结果表明，Fenton体系中Fe2＋和H2O2的摩尔比为1：20，H2O2投加量为120mmol／L，pH为3，再生温度为25℃，再生时间为70min时，为最佳再生条件，再生率可达85．6％，且6次连续再生的平均效率仍能达到84．9％。Fenton试剂再生活性炭的方法表现出较高的经济和环境效益。     

Oxidation of chlorophenols in soil at natural pH by catalyzed hydrogen peroxide: the effect of soil organic matter.

This investigation reports on the effects of soil organic matter (SOM) during the oxidation of chlorophenols with Fe2+-catalyzed H2O2 (Fenton oxidation) system. The soil pH was 7.1 and was not altered. Sorption experiments of soil pre-treated under various oxidation conditions were performed. Concentrations of organic matter in the liquid phase and soil before and after oxidation were analyzed. The results were correlated to the observation in batch Fenton oxidation tests. They showed that the oxidation of chlorophenols at natural soil pH depended on the dose of H2O2 and Fe2+. The soil organic content did not vary significantly after various Fenton treatments, while the sorption of chlorophenols was 10-25% less by the oxidation. The concentration of chlorophenols in the liquid phase exhibited a "decrease and rebound" phenomenon in the batch Fenton oxidation tests. It appeared that the oxidation of SOM resulted in the release of sorbed chlorophenols which were then oxidized by the excess H2O2. An "oxidation-desorption-oxidation" scheme was proposed to describe one of the interaction mechanisms among the oxidant, SOM, and chlorophenols during oxidation.     

垃圾填埋场渗滤液物化深度处理研究

通过Fenton法和结合聚合硫酸铁的混凝作用，实现垃圾渗滤液氧化塘出水COD的深度处理；并利用水泥水化产物的凝胶物质，强化COD去除率。30％H2O2投加量为0．75mL／L、七水硫酸亚铁投加量为1．5g／L、n（H2O2）：n（Fe^2＋）=1．2：1（摩尔比）时，Fenton法对渗滤液COD的去除率可达52％；水灰比为2：1、搅拌24h的水泥水化物将Fenton法的出水pH值从4调至10，该工艺流程总的COD去除率为73．6％，较普通的Ca（OH）2调节法提高9．3％，出水COD可以从进水的1200mg／L降至315mg／L。     

Oxidation of TNT by photo-Fenton process

A series of photo-Fenton reactions have been performed for the degradation of 2,4,6-trinitrotoluene (TNT) in a 4.2-l reactor. The degradation reaction rate of TNT followed a pseudo-first-order behavior; and the rate constants for 2.4mW cm(-2)UV only, 2.4mW cm(-2)UV/H(2)O(2), Fenton, photo-Fenton (2.4mW cm(-2)) and photo-Fenton (4.7mW cm(-2)) were 0.002min(-1), 0.007min(-1), 0.014min(-1), 0.025min(-1) and 0.037min(-1), respectively. Increasing the intensity of UV light, and the concentrations of ferrous ions and hydrogen peroxide promoted the oxidation rate under the experimental conditions in this study. The weighting factor (f), the Fe(II)-promoted efficiency (r) and the promoted-UV light efficiency (p) were calculated to clarify their effects on the TNT oxidation. Moreover, the inhibition effect of hydroxyl radical was also observed in both Fenton and photo-Fenton oxidation when the concentration of Fe(II) were higher than 2.88mM. Solid phase micro-extraction was first applied to the separation of the organic byproducts from TNT oxidation. GC/MS was employed to identify the byproducts during the Fenton and photo-Fenton oxidation of TNT. These compounds were clarified as 1,3,5-trinitrobenzene, 1-methyl-2,4-dinitrobenzene 2,5-dinitrobenzoic acid and 1,3-dinitrobenzene. By these byproducts, the mechanisms of the methyl group oxidation, decarboxylation, aromatic ring breakage, and hydrolysis can be recognized and demonstrated. The pathway of TNT oxidation by photo-Fenton process was also proposed in this study.     

Enhanced degradation of polycyclic aromatic hydrocarbons by biodegradation combined with a modified Fenton reaction

A study has been conducted to enhance degradation of a mixture of polycyclic aromatic hydrocarbons (PAHs) by combining biodegradation with hydrogen peroxide oxidation in a former manufactured gas plant (MGP) soil. An active bacterial consortium enriched from the MGP surface soil (0-2 m) biodegraded more than 90% of PAHs including 2-, 3-, and 4-ring hydrocarbons in a model soil. The consortium was also able to transform about 50% of 4- and 5-ring hydrocarbons in the MGP soil. As a chemical oxidant, Fenton's reagent (H2O2 + Fe2+) was very efficient in the destruction of a mixture of PAHs (i.e., naphthalene (NAP), fluorene (FLU), phenanthrene (PHE), anthracene (ANT), pyrene (PYR), chrysene (CHR), and benzo(a)pyrene (BaP)) in the model soil; noticeably, 84.5% and 96.7% of initial PYR and BaP were degraded, respectively. In the MGP soil, the same treatment destroyed more than 80% of 2- and 3-ring hydrocarbons and 20-40% of 4- and 5-ring compounds. However, the low pH requirement (pH 2-3) for optimum Fenton reaction made the process incompatible with biological treatment and posed potential hazards to the soil ecosystem where the reagent was used. In order to overcome such limitation, a modified Fenton-type reaction was performed at near neutral pH by using ferric ions and chelating agents such as catechol and gallic acid. By the combined treatment of the modified Fenton reaction and biodegradation, more than 98% of 2- or 3-ring hydrocarbons and between 70% and 85% of 4- or 5-ring compounds were degraded in the MGP soil, while maintaining its pH about 6-6.5.     

Mineralization of dinitrotoluenes and trinitrotoluene of spent acid in toluene nitration process by Fenton oxidation

Fenton's reagent, UV/H2O2 and UV/Fenton's reagent were employed to mineralize dinitrotoluene (DNT) isomers and 2,4,6-trinitrotoluene (TNT) of spent acid in toluene nitration process. The bench-scale experiments were conducted to elucidate the influence of various operating variables on the performance of removal of total organic compounds (TOC) from spent acid, including reaction temperature, concentration of ferrous ion and H2O2 dosage. It is remarkable that organic compounds were completely mineralized by Fenton oxidation, of which removal efficiency is superior to that of UV/H2O2. Nevertheless, it makes slight difference between Fenton oxidation and UV/Fenton oxidation. According to the spectra identified by gas chromatograph/mass spectrometer (GC/MS), it is proposed that oxidative degradation of DNT isomers leads to o-, m-, p-mononitrotoluene (MNT) and 1,3-dinitrobenzene respectively. Besides, the oxidation of 2,4,6-TNT gives the 1,3,5-trinitrobenzene intermediate. Apparently, Fenton oxidation is promising for purification of spent acid industrially.     

Fe<Superscript>0</Superscript>-based system as innovative technology for degrading trichloromethane: Redox removal characteristics

BACKGROUND: The spent waste of aliphatic chlorinated solvents has caused severe deterioration of groundwater quality. Trichloromethane (TCM), which shows health and toxicological effects on human beings, was selected as a model compound to be dechlorinated through a redox system. METHODS: The Fe0-based system including Fe0/H2O, Fe0/UV, Fe0/H2O2, and Fe0/UV/H2O2 was explored to evaluate its performance in dechlorinating TCM. H2O2 was dosed at later reaction time points to initiate Fenton or photo-Fenton reactions. The first two systems demonstrate the reductive dechlorination of TCM by Fe0-released electrons, while the latter two show dechlorination of TCM by both electron reduction and hydroxyl radical oxidation. The system parameters of TCM remaining, Cl- buildup, Fe2+ accumulation, H2O2 residue, and ORP were measured to describe different redox characteristics of TCM dechlorination. The Cl- buildup was used as a way to describe the degree of TCM dechlorination in an open reaction system. RESULTS: Reductive dechlorination efficiencies of TCM were 5% and 6% for the systems of Fe0/H2O and Fe0/UV, respectively. In contrast, the Fe/H2O2 and Fe0/UV/H2O2 systems were capable of dechlorinating TCM reductively and oxidatively by 14% and 15%, respectively. The presence of UV light was found to retard the dissolution of Fe2+, but it enhanced the rate of chloride buildup, based on the comparison of Fe0/H2O and Fe0/UV systems. In addition, WV irradiation plays only a minor role in the Fe0/UV/H2O2 system, in view of TCM dechlorination. Application of small amount of H2O2 results in the increase of Fe2+ accumulation rate in the Fe0/H2O2 system. CONCLUSIONS: TCM was dechlorinated mostly through post Fenton oxidation; reductive reaction represents a less efficient way to dechlorinate TCM. The efficiencies of overall TCM dechlorination for the two systems of Fe0/H2O2 and Fe0/UV/ H2O2 are comparable to each other, and this implies that the presence of UV irradiation imposes no significant enhancement. RECOMMENDATIONS AND OUTLOOKS: It is highly recommended to initiate effective redox dechlorination of TCM with the system of Fe0/H2O2, where the H2O2 in excess is applied at a later reaction time point.     

Catalytic oxidation of pentachlorophenol in contaminated soil suspensions by Fe+3-resin/H2O2

Pentachlorophenol (PCP) is a wood preserving agent that is commonly found in contaminated soils at wood treatment sites. The catalytic properties of Fe+3-resin for the oxidation of PCP in aqueous solution and soil suspension with H2O2 were tested. Batch tests in aqueous solution were performed at various dosages of catalyst and H2O2, and reaction temperatures. The results showed that the oxidation of PCP in aqueous solution depends on the dose of H2O2 and the temperature. Essentially complete oxidation of 100 mgl(-1) PCP was obtained with 0.5% Fe+3-resin catalyst, 0.1 M H2O2 and at a reaction temperature of 80 degrees C. The oxidation of PCP achieved in three different soil suspensions was more than 94% within 30-50 min. Moreover, it was demonstrated that the same Fe+3-resin could be reused for at least six cycles of PCP oxidation in soil solutions without loss in efficiency unless the pH of the reaction falls below 5. It was proposed that the loss in used Fe+3-resin catalyst activity could be related to the leaching of Fe+3 at low pH.     

Fenton组合工艺处理焦化厂生化出水的应用研究

比较了Fenton氧化、Fenton氧化+活性炭及Fenton氧化+生物活性炭工艺对焦化厂生化出水的处理效果.结果表明,Fe2+、H2O2的投加量分别为56、27.2 mg/L时,Fenton氧化工艺对水样的UV254、颜色度(VIS380)、COD和总氰均有较好的去除效果;Fenton氧化+活性炭工艺在有效去除UV254、VIS380、COD和总氰的同时,能强化活性炭的吸附效果,并能显著提高水样的生化性能;Fenton氧化+生物活性炭工艺能有效去除UVM254,VIS380、COD与总氰,使出水达到<污水综合排放标准>(GB 8978-1996)一级标准.     

Effects of operating parameters on advanced oxidation of diuron by the Fenton's reagent: a statistical design approach

Advanced oxidation of diuron in aqueous solution by Fenton's reagent using FeSO(4) as source of Fe(II) was investigated in the absence of light. Effects of operating parameters namely the concentrations of pesticide (diuron), H(2)O(2) and Fe(II) on oxidation of diuron was investigated by using Box-Behnken statistical experiment design and the surface response analysis. Diuron oxidation by the Fenton reagent was evaluated by determining the total organic carbon (TOC), diuron, and adsorbable organic halogen (AOX) removals. Concentration ranges of the reagents resulting in the highest level of diuron oxidation were determined. Diuron removal increased with increasing H(2)O(2) and Fe(II) concentrations up to a certain level. Diuron concentration had a more profound effect than H(2)O(2) and Fe(II) in removal of diuron, TOC and AOX from the aqueous solution. Nearly complete (98.5%) disappearance of diuron was achieved after 15min reaction period. However, only 58% of diuron was mineralized after 240min under optimal operating conditions indicating formation of some intermediate products. Optimal H(2)O(2)/Fe(II)/diuron ratio resulting in the maximum diuron removal (98.5%) was found to be 302/38/20 (mgl(-1)).     

The use of amino compounds for binding 2,4,6-trinitrotoluene in water

Sites polluted with 2,4,6-trinitrotoluene (TNT) constitute a worldwide problem. In this work, chemical reactions for binding TNT to amino-compounds are proposed as an initial step for developing new remediation techniques to clean-up groundwater and soils contaminated with TNT. Indeed, addition of aniline and an amino acid-like cysteine caused a decrease in free TNT of 86% and 68-100%, respectively. Using 13C-NMR spectroscopy, it was shown that TNT chemically forms a Meisenheimer complex with cysteine and aniline in 1/1 (by vol.) H2O/d6-acetone.