• 한국환경보건학회지
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• 제34권2호
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• pp.175-182
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• 2008

This study investigates the optimal conditions for electrogenerated hydrogen peroxide production and the application of the electro-Fenton process using DSA electrodes. The influences of parameters for the hydrogen peroxide generation such as electrode materials, electrolyte concentration, current, pH, air flow rate and electrode distance were investigated using a laboratory scale batch reactor. The relative performance for hydrogen peroxide generation of each of the six electrodes is : Ru-Sn-Ti > Ru-Sn-Sb > Ru > Ir > Pt > Sn-Sb. Optimum NaCl dosage, current and air flow rate were 2.0 g/l, 12.5 A and 2 l/min, respectively. When the pH is low, hydrogen peroxide concentration was high. Electrode distance dos not effect to a hydrogen peroxide generation. A complete color removal was obtained for RhB (200 mg/l) at the 8 min mark of the electro-Fenton process under optimum operation conditions of $Fe^{2+}$ 0.105 g/l and 5.0 A. The electro-Fenton process increased initial reaction and decreased final reaction time. However the effect was not high.

• 한국물환경학회지
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• 제30권6호
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• pp.653-657
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• 2014

Effects of $H_2O_2$ addition for fenton oxidation on iron coagulation for treatment of phosphorus species, such as orthophosphate, metaphosphate, pyrophosphate, organic phosphate, were investigated. The effects of coagulant dosage, hydrogen peroxide dosage and the combined sequence ferric coagulation and $H_2O_2$ addition for fenton oxidation and coagulation were studied. The characteristics of floc growth rate were monitored using the PDA. The removal efficiencies of phosphorus species by iron coagulation were increased as Fe/P molar ratio increased. However, the removal efficiencies of metaphosphate, pyrophosphate, organic phosphate by a ferric coagulation were not increased as Fe/P molar ratio increased. The removal efficiency of metaphosphate, pyrophosphate, organic phosphate was increased by using iron coagulation and $H_2O_2$ addition for fenton oxidation. The result indicated that non-reactive phosphorus after iron coagulation was changed to reactive phosphorus by $H_2O_2$ addition for fenton oxidation and the oxidized iron enhanced the coagulation efficiencies.

• Environmental Engineering Research
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• 제17권4호
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• pp.217-225
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• 2012

In this study, the treatability of two target contaminants during the Fenton reaction, n-hexadecane and 1-methylnaphthalene, was evaluated as a function of the amounts of $FeCl_2$ and $H_2O_2$ injected into open and closed reaction systems. In the Fenton reaction of n-hexadecane and 1-methylnaphthalene, the mass recovery of the target contaminants was above 95% in the closed system. However, when the Fenton reaction was performed with high amounts of $H_2O_2$ and $FeCl_2$ injected in the open system, a reduction of approximately 40% of the initial mass of 1-methylnaphthalene was observed. This trend may be explained by the unique physical properties of 1-methylnaphthalene, which has higher volatility than n-hexadecane. Further, this trend was well correlated with the rise in high temperature at the initial reaction stage. Considering the mass recovery of the two target contaminants, the reaction temperature, and the residual concentration of $H_2O_2$ at different amounts of $FeCl_2$ and $H_2O_2$ injected, it can be suggested that the Fenton reaction should be performed with controlled conditions that can provide a suitable reaction environment between oxidant and contaminants.

• 한국물환경학회지
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• 제21권3호
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• pp.284-288
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• 2005

In this study, photochemical advanced oxidation processes (AOPs) utilizing the Photo Fenton reaction ($Fe^{2+}+H_2O_2+UV$) were investigated in lab-scale experiments for the treatment of livestock wastewater. For the experimets, the livestock wastewater was pretreated by coagulation with $3,000mg/L\;FeCl_3$. The optimal conditions for Photo-Fenton processes were determined: pH was 5, the concentration of ferrous ion (Fe II) was 0.01 M. The concentration of hydrogen peroxide was 0.1 M, and molar ratio ($Fe^{2+}/H_2O_2$) was 0.1. The optimal reaction time was 80 min. Under the optimal condition of Photo-Fenton process, chemical oxygen demand (COD), color and fecal coliform removal efficiencies were about 79, 70, and 99.4%, respectively and sludge production was 7.5 mL from 100 mL of solution.

• 청정기술
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• 제5권1호
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• pp.49-61
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• 1999

펜턴산화는 산화력이 매우 우수한 $OH{\cdot}$을 생성하여, 난분해성 유기폐수의 생분해성을 향상시킬 수 있으므로 다양한 용존 유기오염물질을 함유하고 있는 산업폐수의 처리에 널리 이용되고 있지만, 철염과 과산화수소 등의 약품비용과 Sludge 처분비용 때문에 현재로서는 그리 경제적인 공정이라고 볼 수 없다. 본 연구에서는 펜턴산화의 약품비용을 줄이고, 적은 약품으로 처리효율을 향상시키기 위한 변형 펜턴산화법과 혼합한 슬러지 재이용의 가능성을 제시하고자 하였다. 본 연구는 펜턴산화에서 사용되는 철염용액에 NaOH용액을 첨가하였더니 철염용액의 폭발적인 반응을 보고 이를 펜턴산화에 응용하게 되었다. 본 연구에서 제안하는 변형 펜턴산화 공정이란 펜턴산화에서 사용되는 철염용액에 NaOH를 넣어 적정 pH로 조정하여, 수산화물을 형성시킨 후 처리대상 시료에 주입하여 과산화수소와 반응시켜 $OH{\cdot}$을 형성시키는 방법이다. 이 때 대상시료로서는 대표적인 오염물질인 페놀을 사용하였고 자연수의 이온강도와 유사한 수준으로 맞추기 위하여 $NaHCO_3$를 적량 첨가하여 페놀 인공폐수를 조제하였다. 이를 이용하여, DO의 영향, 이온강도의 영향, 과산화수소 주입횟수에 따른 영향을 알아보았다. 또한, 침출수와 염색폐수에 적용시켜 본 결과 기존의 펜턴산화보다 더 나은 처리효율을 얻을 수 있었으며, 변형 펜턴산화법과 슬러지 반송을 조합하여 실험한 결과 철염을 50%만 주입하여도 기존의 펜턴산화와 유사한 수준의 처리효율을 얻을 수 있었다.

• 한국지구물리탐사학회:학술대회논문집
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• 한국지구물리탐사학회 2003년도 Proceedings of the international symposium on the fusion technology
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• pp.493-500
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• 2003

The effect of reductive treatment with elemental iron on the extent of mineralization by Fenton oxidation was studied for the explosive 2,4,6-trinitrotoluene (TNT) and hexahydro-l,3,5-trinitro-l,3,5-triazine (RDX) using a completely-stirred tank reactor (CSTR). The results support the hypothesis that TNT and RDX are reduced with elemental iron to products that are oxidized more rapidly and completely by Fenton's reagent. Iron pretreatment enhanced the extent of TOC removal by approximately $20\%\;and\;60\%$ for TNT and RDX, respectively. Complete TOC removal was achieved for TNT and RDX solutions with iron pretreatment under optimal conditions. On the other hand, without iron pretreatment, complete mineralization of TNT and RDX solutions were not achieved even with much higher $H_2O_2$ and $Fe^{2+}$ concentrations. The bench-scale iron treatment-Fenton oxidation integrated system showed more than $95\%$ TOC removal for TNT and RDX solutions under optimal conditions. The proposed zero-valent iron-Fenton process was evaluated with pink water from the Iowa Army ammunition plant. Results from batch and column experiments show that TNT, RDX, and octahydro-l,3,5,7-tetranitro-l,3,5,7-tetrazocine (HMX) were completely removed from the pink water and that triaminotoluene (TAT) and ${NH_4}^+$ were recovered as products in reduction with zero-valent iron. By using an integrated system, $83.3\pm4.2\%$ of TOC was removed in a CSTR with 10 mM of $Fe^{2+}$ and 50 mM of $H_2O_2$. These results suggest that the reduction products of TNT and RDX are more rapidly and completely mineralized by Fenton oxidation and that a sequential iron treatment-Fenton oxidation process may be a viable technology for pink water treatment.

• Environmental Engineering Research
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• 제10권3호
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• pp.138-143
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• 2005

Laboratory batch experiments were conducted to evaluate the Fenton degradation rates of phenanthrene. Fenton reactions for the degradation of phenanthrene were carried out with aqueous and slurry phase, to investigate the effects of sorption of phenanthrene onto solid phase. Various types of surfactants and electrolyte solutions were used to evaluate the effects on the phenanthrene degradation rates by Fenton's reaction. A maximum 90% removal of phenanthrene was achieved in aqueous phase with 0.9% of $H_2O_2$ and 300 mg/L of $Fe^{2+}$ at pH 3. In aqueous phase reaction, inhibitory effects of synthetic surfactants on the removal of phenanthrene were observed, implying that surfactant molecules acted as strong scavenger of hydroxyl radicals. However, use of $carboxymethyl-{\beta}-cyclodextrin$ (CMCD), natural surfactant, showed a slight enhancement in the degradation of phenanthrene. It was considered that reactive radicals formed at ternary complex were located in close proximity to phenanthrene partitioned into CMCD cavities. It was also show that Fenton degradation of phenanthrene were greatly enhanced by addition of NaCl, indicating that potent radical ion ($OCI^-$) played an important role in the phenanthrene degradation, although chloride ion might be acted as scavenger of radicals at low concentrations. Phenanthrene in slurry phase was resistant to Fenton degradation. It might be due to the fact that free radicals were mostly reacting with dissolved species rather than with sorbed phenanthrene. Even though synthetic surfactants were added to increase the phenanthrene concentration in dissolved phase, low degradation efficiency was obtained because of the scavenging of radicals by surfactants molecules. However, use of CMCD in slurry phase, showed a slight enhancement in the phenanthrene degradation. As an alternative, use of Fenton reaction with CMCD could be considered to increase the degradation rates of phenanthrene desorbed from solid phase.

• 한국지하수토양환경학회지:지하수토양환경
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• 제21권1호
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• pp.86-93
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• 2016

Fenton is the reaction using the OH· radicals generating by interaction between hydrogen peroxide and Fe²⁺ which can oxidize the contaminants. Fe²⁺ ions are oxidized to Fe³⁺ ions by reaction with H₂O₂ and formed OH· radicals. UV-Fenton process includes the additional reaction that generates the OH· radicals by photodegradation of H₂O₂. In methylorange (MO) decolourization experiment with UV-Fenton, optimal Fe²⁺: H₂O₂ ratio was obtained at 1 : 10. Based on the obtained condition (H₂O₂= 10mM, Fe²⁺ = 1 mM) with/without UV-fenton experiment was carried out. Removal efficiency and sludge production were measured at 30 min. The case of w/o UV irradiation and only H₂O₂ was hardly treated and only Fe²⁺ showed 65% removal owing to coagulation. When UV-Fenton process in optimal ratio (Fe²⁺: H₂O₂ = 1 : 10), UV irradiation showed better removal efficiency than of w/o UV irradiation. Also, MO decolourization was a function of the hydrogen peroxide concentration (x₁), Fe²⁺:H₂O₂ ratio (x₂), and numbers of UV lamp (x₃) from the application of the response surface methodology. Statistical results showed the order of significance of the independent variables to be hydrogen peroxide concentration > numbers of UV l amp > Fe²⁺: H₂O₂ ratio.

• Korean Chemical Engineering Research
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• 제59권4호
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• pp.508-513
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• 2021

고분자전해질 연료전지(PEMFC)의 내구성을 향상시키기 위해서는 필수적으로 고분자막의 내구성이 향상되어야한다. 고분자막의 내구성을 향상시키기 위해서 e-PTFE 지지체와 라디칼 제거제(Radical Scavenger)가 첨가된다. 본 연구에서는 e-PTFE 지지체가 들어간 강화막(Reinforced Membrane)과 비강화막(Non-reinforced Membrane)의 화학적 내구성을 Fenton 반응에 의해 비교하고자 하였다. 라디칼 제거제가 첨가되지 않은 고분자막의 Fenton 실험에서는 작게 절단한 시편의 단면을 통한 과산화수소 용액과 철이온의 흡수율이 강화막에서 더 높아 불소유출농도가 더 높게 나타났다. 라디칼 제거제의 종류와 첨가량에 따라 강화막의 불소유출농도가 3배 이상의 큰 차이가 발생해서 라디칼 제거제의 영향이 지지체의 영향보다 강한 것을 알 수 있었다.

• 대한토목학회논문집
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• 제29권2B호
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• pp.207-212
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• 2009

광물촉매에 의한 Fenton 산화에서 모래에 흡착된 phenanthrene을 대표적인 계면활성제인 SDS와 Tween 80을 사용하여 물질이동 영향을 조사하였다. 계면활성제 주입에 따라 액상과 고체상 사이 또는 산화물 표면으로 phenanthrene이 물질이동하였으며, 계면활성제 농도가 증가할수록 phenanthrene의 apparent solubility는 증가하는 경향을 나타내었다. Tween 80은 apparent solubility가 증가 하더라도, 계면활성제가 분해에 scavenger 작용을 하여 모래에 흡착된 phenanthrene 산화에는 영향을 주지 않았다. SDS를 주입하였을 때, Fenton-like 반응에서 SDS와 goethite가 착물을 형성하여 과산화수소 소모량을 지연시켰의며, 계면활성제를 주입 하지 않았을 때 보다 SDS 32 mM를 주입하였을 때 phenanthrene 처리효율이 증가하였다. 그러므로 최적농도의 SDS 주입은 액상과 고체상 사이 또는 산화물 표면에 phenanthrene 산화를 위한 적당한 조건을 제공 해주며, 과산화수소 소모량을 줄이고, phenanthrene 처리효율을 개선시킬 것이다.