• 한국지하수토양환경학회지:지하수토양환경
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• 제11권6호
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• pp.76-82
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• 2006

일반적으로 Fenton 반응 공정을 실제 오염토양에 적용하기에는 다소 무리가 있다. 그 이유로 대표적인 Fenton 반응공정인 고전적인 Fenton 반응은 낮은 pH에서 우수한 처리효율을 보이고 있기 때문이다. 또한, 철이온의 투입을 대신하여 철광석을 이용하는 Fenton-like 반응도 철광석 표면에서 hydroxyl radical을 생성하나 높은 pH에서는 다량의 수산화물과의 경쟁반응으로 인하여 그 활성이 상당히 감소되어진다. 이러한 단점을 보완하기 위하여 중성영역의 pH에서 철이온-chelating agent의 복합체를 촉매로 사용하는 modified Fenton 반응이 제시 되어지고 있다. 이 처리방식의 경우에는 다량의 철이온의 투입이 요구되어진다. 따라서, 본 실험에서는 Fenton-like 반응과 modified Fenton 반응의 효율적인 접목으로 중성영역에서의 chelating agent의 투입으로 철광석으로부터 철이온을 용출하여 복합체를 형성함으로 혼합 Fenton 공정에서 부가적인 촉매로 사용되어짐으로 오염물 처리효율을 크게 향상시킨 기법 개발을 진행하였다. 2,4,6-Trinitrotoluene은 본 실험에서 오염원으로 사용하였으며, chelating agent에 의해 용출된 철이온이 약 0.1 mM 이상일 경우 Fenton-like 반응에 비하여 상당히 좋은 제거효율을 보였다. 혼합 Fenton 공정의 최대제거효율은 magnetite-NTA 시스템으로써 약 76%의 제거효율과 magnetite-EDTA의 경우 약 56%로서 이는 Fenton-like 반응에 비하여 약 40-60% 정도의 제거효율이 향상된 결과이다.

• Journal of Microbiology and Biotechnology
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• 제16권11호
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• pp.1734-1739
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• 2006

The degradation of perchloroethylene (PCE) was investigated with the serial treatment of biological reaction after dechlorination using Fenton's reagent. The dechlorination of PCE was expressed using $D_m$ (dechlorination value), calculated from ${\Delta}Cl^-mol/{\Delta}PCE$ mol, and was 2.58 with 5 mM of $H_2O_2$ and $Fe^{3+}$. The $150{\mu}M$ of PCE was transformed to $37{\mu}M$ of dichloroacetic acid (DCAA). Biological treatment with Delftia sp. N6 was applied after degradation of PCE by the Fenton reaction. The optical densities indicating cell growth were 0.53/0.10 with/without the Fenton reaction after one day, respectively. The N6 strain degraded 95% of the DCAA produced from PCE by the Fenton reaction within one day. Consequently, it seemed that the serial treatment of a Fenton reaction and biological reaction was effective in the removal of not only PCE, but also DCAA, one of the major metabolites of PCE.

• 한국물환경학회지
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• 제18권2호
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• pp.169-187
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• 2002

The effects of important parameters such as reaction time and pH on the Fenton's process were evaluated using a batch reactor. It was proven that organic materials and heavy metals in leachate could be successfully removed by Fenton's reagent. Favorable operation conditions were investigated. It was observed that the reaction between ferrous iron and hydrogen peroxide with the production of hydroxyl radical was almost complete in 10 minutes. That is, the oxidation of organic materials by Fenton's reagent was so fast that it was complete in 30 minutes with batch experiments. With the formation of carbonic acid, pH of the batch reactor decreased to favorable acidic conditions without acid addition. The oxidation of organic materials in the leachate showed a pH dependence and was most efficient in the pH range of 2-3.

• 한국지하수토양환경학회지:지하수토양환경
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• 제11권6호
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• pp.69-75
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• 2006

지하 저장 탱크로부터의 유류 유출로 인하여 전세계적으로 넓은 지역의 토양 및 지하수가 오염되고 있다. Methyl tert-butyl ether(MTBE)는 대기 오염 감소를 위하여 널리 사용되고 있는 유류 첨가제이지만 토양 및 지하수로 유입되어 섭취 되었을 때 발암 가능성이 있는 유독 물질이다. 본 연구는 고도 산화 처리 기법 중 유기 오염물의 분해에 높은 효율을 나타내는 고전적 Fenton reaction의 최대 단점인 강한 산성(pH 2.5-3) 의존성을 극복한 새로운 산화 처리 기법을 개발하여 고농도의 MTBE를 효과적으로 분해 하는 것을 그 목적으로 하여 자연 친화적인 chelating agents를 사용하여 중성 영역에서 Fenton reaction을 가능하게 하는 기법인 Modified Fenton reaction과 Ultra Violet light(UV)를 이용하여 분해효율을 극대화 하는 Photo-assisted Fenton reaction을 응용한 Modified Photo-Fenton reaction system을 개발하여 최적 반응 조건 및 반응 차수, 반응 메커니즘을 밝혀내었다. 낮은 독성과 높은 생분해성을 나타낸 Citrate ion을 chelating agents로 선정하였으며 최적 반응 조건은 [$Fe^{3+}$] : [Citrate] = 1 mM : 4 mM, 3% $H_2O_2$, 17.4 kWh/L UV dose, 초기 pH 6.0이며 이 조건에서 1000 ppm MTBE를 분해한 결과 6시간 후 86.75%, 16시간 후 99.99%의 높은 분해율을 나타냈으며 최종 pH는 6.02로 안정적이었다. 또한 Modified Photo-Fenton reaction을 이용한 MTBE 분해 반응은 유사 1차 반응을 나타내었으며 methoxy group이 ${\cdot}OH$ radical과 주로 반응하여 tert-butyl formate(TBF)가 주요 분해 산물이 되는 분해 경로를 따른 다는 것이 밝혀졌다. 본 연구로 개발된 Modified Photo-Fenton reaction에서 발생되는 산화제인 ${\cdot}OH$ radical의 비선택적 반응성을 고려할 때 본 system은 다른 종류의 유기 오염물 분해에도 효과적일 것으로 판단된다.

• Environmental Sciences Bulletin of The Korean Environmental Sciences Society
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• 제10권S_4호
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• pp.165-172
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• 2001

We investigated the optimal experimental conditions and reaction kinetics for the decompositions of PCE, TCE, naphthalene, and chloroform using conventional Fenton oxidation process. Additionally, the influence of pH on the decompositions of PCE was also evaluated. The results indicated that the optimal pH value was around 3. The dosage of Fenton's reagent and the molar ratio of hydrogen peroxide to ferrous ion for an approximately complete decomposition was found to depend on the properties of the organic compound. Due to their unsaturated structures, the results show that PCE, TCE, and naphthalene could be all effectively decomposed by Fenton's reagent oxidation. Their unsaturated structures could be mostly destoyed within first 1-2 minutes at a low dosage with an certain molar ratio of hydrogen peroxide to ferrous ion. However the saturated compound such as chloroform was more difficult to decompose even with a relatively high dosage of Fenton's reagent.

• 한국환경과학회:학술대회논문집
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• 한국환경과학회 2003년도 가을 학술발표회 발표논문집
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• pp.319-321
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• 2003

This research was carried out to evaluate the removal efficiencies of CODcr and colour for the dyeing wastewater by ferrous solution in Fenton process. The results showed that COD was mainly removed by Fenton coagulation, where the ferric ions are formed in the initial step of Fenton reaction. On the other hand colour was removed by Fenton oxidation rather than Fenton coagulation. The removal mechanism of CODcr and colour was mainly coagulation by ferrous ion, ferric ion and Fenton oxidation. The removal efficiencies were dependent on the ferric ion amount at the beginning of the reaction. However the final removal efficiency of COD and colour was in the order of Fenton oxidation, ferric ion coagulation and ferrous ion coagulation. The reason of the highest removal efficiency by Fenton oxidation can be explained by the chain reactions with ferrous solution, ferric ion and hydrogen peroxide.

• 한국환경보건학회지
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• 제32권5호
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• pp.446-450
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• 2006

In order to treat the wastewater containing organic compound, pre-treatment system connected with MSP(molecular separation process) was investigated. With the aim of selecting an optimum process of Fenton's oxidation, removal efficiency of each process in the optimum reaction condition was recommended. The $Fe/H_{2}O_{2}$(ferric sulfate to hydrogen peroxide)reagent is referred to as the Fenton's regent, which produces hydroxyl radicals by the interaction of Fe with $H_{2}O_{2}$. The powerful oxidizing ability and extreme kinetic reactively of the hydroxyl radical was well established. Increasing dosage of $Fe/H_{2}O_{2}$ increased removal efficiency as molar ratio of $Fe/H_{2}O_{2}$ between 0.2 and 2.5. Optimum dosage of molar ratio was 1. The removal efficiency for reaction condition was increased as pH decreased when the molar ratio of $Fe/H_{2}O_{2}$ was 1.7. Fenton's oxidation was most efficient in the reaction time 35 min for complex wastewater. Also, coagulation aid experiments using kaolin resulted in 3% of kaolin dosage.

• 환경위생공학
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• 제17권4호
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• pp.29-38
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• 2002

Advanced oxidation of wastewater was studied with a purpose to remove TOC and color by the ozone-assisted Fenton reaction. The optimal conditions were determined by hydrogen peroxide and ozone concentrations. Experimental results indicate that the ozone treatment after Fentons process was found to provide very efficient removal efficiency in the process, avoiding the exclusive ozone treatment. The combined process of ozone in the Fenton oxidation respectively was increased removal efficiences of 10.7％ in comparison with exclusive Fenton oxidation. Also, the treatments of ozone after Fenton's oxidation respectively had increased the removal efficiences of 16.％. As a result, the treatment of ozone after Fentons oxidation had the best removal efficiency of approximately 96％. Removal efficiency of color was significantly increased as mush as 26％ by the advanced Fenton's oxidation in comparison with exclusive Fenton's oxidation. The removal efficiencies in the biological treatment using Bacillus subtilis after Fenton's oxidation and after Fenton's and ozone's oxidation were increased by 14％ and 19％ respectively. Although these combined Bacillus subtilis-assisted Fenton's oxidation was determined to be effective method to treat the dyeing wastewater in an economic point of view, the choice of wastewater treatment can be varied depending on water quality.

• 한국환경과학회지
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• 제13권11호
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• pp.987-991
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• 2004

The purpose of this research is to evaluate the removal efficiencies of COD$\_$Cr/ and color for the dyeing wastewater by the different dosages of ferrous solution and H$_2$O$_2$ in Fenton process. In the case of H$_2$O$_2$ divided dosage for the Fenton's reagent 7:3 of H$_2$O$_2$ was more effective than 3:7 to remove COD$\_$Cr/ and color. The results showed that COD$\_$Cr/ was mainly removed by Fenton coagulation, where the ferric ions are formed in the initial step of Fenton reaction. On the other hand color was removed by Fenton oxidation rather than Fenton coagulation. The removal mechanism of COD$\_$Cr/ and color was mainly coagulation by ferrous ion, ferric ion and Fenton oxidation. The removal efficiencies were dependent on the ferric ion amount at the beginning of the reaction. However, the final removal efficiency of COD$\_$Cr/ and color was in the order of Fenton oxidation, ferric ion coagulation and ferrous ion coagulation. The reason of the highest removal efficiency by Fenton oxidation can be explained by the chain reactions with ferrous solution, ferric ion and hydrogen peroxide.

• 대한토목학회논문집
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• 제31권4B호
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• pp.377-382
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• 2011

본 연구에서는 modified fenton 반응에서 과산화수소를 안정화하여 오염토양 정화의 효과를 증대시키고자 하였다. 오염토양을 모사하기 위하여 PAHs 계열의 대표적인 오염물질인 phenanthrene을 사용하였다. 과수안정제로는 음이온 계면활성제인 SDS(Sodium dodecyl Sulfate)를 사용하였다. Modified Fenton 반응에서 phenanthrene의 제거율을 확인하기 위하여 Fe(II) 4 mM, SDS 5~50 mM 및 $H_2O_2$ 102.897 mM를 phenanthrene 125 mg/kg으로 오염된 토양에 주입하였다. 과수안정제인 SDS가 30 mM이 사용된 경우 phenanthrene의 제거 효율이 95%로 가장 높게 나타났으며 30 mM이싱에서는 시스템에서 SDS가 scavenger로 작용하여 오염물질의 제거효율이 SDS 30 mM 일 때 보다 낮게 나타났다. 과수안정제를 사용한 뒤 과산화수소의 농도변화를 분석한 결과 Fe(II) 2 mM에서 48시간 이후 14.6995 mM 이상 남아있어서 가장 안정적이었지만, Fe(III)을 주입한 경우에는 과산화수소가 안정화되지 않았다. Modified Fenton 반응에서 철과 SDS 농도 사이의 최적의 비율을 찾기 위하여 SDS의 농도는 30 mM로 고정하고 철의 농도를 2~8 mM로 변화시켜 실험한 결과 Fe(II) 4 mM 및 SDS 30 mM에서 약 95%의 가장 높은 제거율을 보였다.