• Korean Chemical Engineering Research
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• 제43권1호
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• pp.153-160
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• 2005

본 실험은 TNT 오염토양의 효율적 제거를 위한 화학적 처리기술 개발을 목적으로 다양한 Fenton reaction 적용성에 관해 고찰하였다. 기존 Fenton reaction은 낮은 pH 요구성을 가지는 단점이 있고 천연토양은 pH에 대한 buffering capacity를 가지고 있으므로 그 적용성이 미약하였다. 이에 중성 pH에서도 효율적으로 Fenton reaction을 유도할 수 있는 modified Fenton reaction을 본 실험에 적용하였다. 또한, 천연 토양 내 다양한 철광석을 철이온 대신 사용함으로써 철슬러지의 발생의 최소화를 위한 Fenton-like reaction의 적용 가능성에 대하여 검토하여 보았다. 실험결과는 오염토양의 기존 Fenton reaction 제거효율은 약 20시간 후 pH 3에서 93%이며 반면 pH 7에서는 21%임을 보였다. 한편, TNT 오염 수용액 처리에 철이온과 5종의 chelating agent를 투입한 실험에서는 24시간 반응 후 pH 7에서 NTA-Fe의 경우가 87%로 그 효율이 가장 우수하였고 citrate-Fe 46%, EDTA-Fe 71%, oxalate-Fe 64%, acetate-Fe 37%의 각각의 제거효율을 나타내었다. 또한, TNT 오염 수용액 처리에 3종의 철광석으로 Fenton-like reaction을 적용한 경우, pH 3에서 24시간 후 goethite 33%, hematite 40%, magnetite 40%의 처리효율을 보였고, pH 7인 경우 goethite 28%, hematite 34%, magnetite에서는 36%의 처리효율을 보였다. 게다가, 성능이 우수한 chelating agent 3종과 2종의 철광석을 이용한 복합처리 실험에서는 magenetite 경우 pH 7에서 NTA 79%, oxalate 59%, EDTA 14%의 제거효율이 측정되었고, hematite 경우 NTA 73%, oxalate 25% 그리고 EDTA 19%의 처리효율을 얻었다. 결론적으로 철광석과 modified fenton reaction의 복합처리의 경우 처리 기간 등의 운영인자를 확보할 경우 효율적으로 TNT 오염토양에 적용될 수 있을 것으로 기대된다.

• Advances in environmental research
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• 제3권1호
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• pp.29-43
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• 2014

Pharmaceutical wastewater effluents are well known for their difficult elimination by traditional biotreatment methods and their important contribution to environmental pollution due to its fluctuating and recalcitrant nature. OTC is one of the nonbiodegradable antibiotics that makes antibiotic-resistant, so it can make be high risk for environment. NZVI can be a good choice for removal of OTC in aqueous solution. Response surface methodology (RSM) was used to optimize the amounts of NZVI and OTC to be used at pH 3 and under 200 W, UV-A irradiation. The responses were removal percent of absorption at 290 and 348 nm, TOC and COD of OTC. In the optimum condition, Linear model was performed 155 ppm of OTC were removed by 1000 ppm NZVI after 6.5 hours and the removal efficiency of absorption at 290 and 348 nm, TOC and COD were 87, 95, 85 and 89 percent, respectively. In the similar process, there is no organic compound after 14 hours. The parameters ORP, DO and pH were investigated for 6:30 hours to study the type of NZVI reaction in process. In the beginning of reaction, oxidation was the dominant reaction after 3 hours, photocatalytic reaction was remarkable. The mechanism of OTC degradation is proposed by HPLC/ESI-MS and four by products were found. Also the rate constants (first order kinetic chain reaction model) were 0.0099, 0.0021, 0.0010, 0.0049 and $0.0074min^{-1}$, respectively.

• 유기물자원화
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• 제14권1호
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• pp.160-168
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• 2006

본 연구에서는 PAHs 오염토양의 펜톤처리시 식물성 식용유와 폐식용유의 첨가가 처리효율에 미치는 영향을 알아보고자 실시하였다. 토양 중 철성분 때문에 철용액을 첨가하지 않고 과산화수소만을 첨가한 경우에도 펜톤반응이 진행되었으며, 과산화수소는 3%에서 최대 효율을 나타내었다. 3%의 과산화수소만을 첨가한 경우에는 총 PAHs가 약 19% 제거되었는데 여기에 17.5 mM $FeSO_4$(III)를 첨가한 경우에는 25%가 제거되어 6% 정도의 효율증진을 나타내었다. 올리브유 1%를 펜톤반응과 동시 또는 전에 첨가한 경우 제거효율은 37~38%로써 펜톤처리만을 한 경우의 22.3% 보다 약 15%정도 제거효율을 증가시킬 수 있었다. 올리브유, 콩식용유, 그리고 폐식용유 농도를 1%와 5%로 하여 주입한 결과 대부분 35% 이상의 처리효율을 나타내었으며, 오일의 종류와 농도에 따른 영향은 크지 않았다. 폐식용유를 사용하였을 때 고가의 올리브유를 사용한 경우와 큰 효율차이를 나타내지 않았으므로 폐식용유 사용시 추가비용이 거의 소요되지 않는 장점이 있을 것으로 판단된다. 3% 과산화수소와 2.5 mM $FeSO_4$에서 1% 올리브유 첨가 후 15분이 지나서 펜톤반응을 실시한 경우 벤젠고리 3~4개와 5~6개인 화합물의 제거율은 펜톤반응만을 실시한 경우 보다 각각 13%와 17% 정도 증가하였다.

• 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.

• 상하수도학회지
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• 제26권6호
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• pp.779-786
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• 2012

The degradation of 2-chlorophenol(2-CP) by various AOPs(Advanced Oxidation Processes) including the photo-Fenton process has been examined. In sole $Fe^{2+}$, UV or $H_2O_2$ process without combination, low removal efficiencies have been achieved. But the photo-Fenton process showed higher removal efficiency for degradation of 2-chlorophenol than those of other AOPs including the Fenton process and the UV processes. In the photo-Fenton process, the optimal experimental conditions of 2-chlorophenol degradation were obtained at pH 3 and the $Fe^{2+}/H_2O_2$molar ratio of 1. Also the 2-chlorophenol removal efficiency increased with decreasing of the initial 2-chlorophenol concentration. 3-chlorocatechol and chlorohydroquinone were identified as photo-Fenton reaction intermediates, and a degradation pathway of 2-chlorophenol in the aqueous phase during the photo-Fenton reaction was proposed.

• 한국지하수토양환경학회:학술대회논문집
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• 한국지하수토양환경학회 2003년도 추계학술발표회
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• pp.379-381
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• 2003

Metal sorption onto the ICS (Iron oxide coated sand) was studied in batch experiments. Heavy metal cations such as Cd, Pb, and Cu, and a metal anion, As, which sporadically exist in mine sites, were tested for the sorptive removal by ICS. In low pH conditions As showed the highest removal efficiency compared to the other metal cations. And the sorption removal of As was apparently pH-independent reaction. However, removal of metal cations increased with pH and above pH 7 most metal cations showed very low soluble concentrations after treatment. Such a high removal ratio of metal cations above the neutral pH appeared predominantly due to precipitation.

• 한국환경보건학회지
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• 제21권1호
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• pp.21-28
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• 1995

The removal of heavy metals from synthetic wastewater containing Pb, Cr, Cd using previously washed and dried exhausted coffee was studied varying cohcentration, pH and temperature. All the heavy metals were removed in 3.0 minutes and the removal efficiency was maximum 80~90% with different pH and temperature conditions. The differences in removal efficiency between exhausted coffee and activated carbon under the same conditions were not seen. The removal efficiency was slightly increased with increasing pH in Cd and increasing temperature in Cr, respectively. The batch adsorption kinetics and adsorption equilibrium were examined and described by a first order reversible reaction and Freundlich isotherm, respectively. And the removal of Pb was found to have the best removal efficiency.

• 상하수도학회지
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• 제27권1호
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• pp.31-38
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• 2013

The degradation of 4-chlorophenol(4-CP) by various AOPs(Advanced Oxidation Processes) with continuous feeding of $H_2O_2$, including the ultraviolet/hydrogen peroxide, the Fenton and the photo-Fenton process has been investigated. The photo-Fenton process showed the highest removal efficiency for degradation of 4-chlorophenol than those of other AOPs including the Fenton process and the combined UV process with continuous feeding of $H_2O_2$. In the photo-Fenton process, the optimal experimental condition for 4-CP degradation was obtained at pH 3. Also the 4-CP removal efficiency increased with decreasing of the initial 4-CP concentration. 4-chlorocatechol and 4-chlororesorcinol were identified as photo-Fenton reaction intermediates, and the degradation pathways of 4-CP in the aqueous phase during the photo-Fenton reaction were proposed.

• 한국물환경학회지
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• 제20권5호
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• pp.488-493
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• 2004

The effects were examined from several conditions of $TiO_2$ photocatalysis reaction to phenols degradation by changing it's reacting conditions such as phenol concentration, pH, $TiO_2$ concentration, $H_2O_2$ concentration, flow rate, and intensity of ultraviolet rays. Phenol degradation was more efficient in low concentration of phenol, neutral pH. Phenol degradation appeared to increase as concentration of $TiO_2$ photocatalyst, that of $H_2O_2$ and intensity of ultraviolet rays increased. As $TiO_2$ dosage increased, initial rate constant k linearly increased. When $H_2O_2$ was injected more than optimum, phenol removal rate didn't increase in proportional to the change of $H_2O_2$ concentration as OH radicals was being consumed. When flow rate is less than $4.75m^3/m^2$ day, phenol removal efficiency appeared to decrease as ultraviolet rays transmission rate becomes low by $TiO_2$ suspension coated in photo reaction column. Meanwhile, initial rate constant according to light intensity change in less than $25mW/cm^2$ appeared to be in proportion to light intensity ($mW/cm^2$) Removal efficiency decreased about 12% after 180 minutes of reaction time while showed stable removal efficiency of 100% after 300 minutes when using regenerated $TiO_2$.

• 상하수도학회지
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• 제21권6호
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• pp.745-753
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• 2007

By struvite and hydroxyapatite crystallization, was high concentration of nitrogen and phosphorus in wastewater simultaneously. Particularly, removal of nitrogen and phosphate for crystallization have been applied to landfill leachates and animal wastewater. The purpose of this study is to decide the optimum struvite crystallization factors, sequence of $Mg^{2+}$ addition, pH control and the molar ratio of $Mg^{2+}$ over $PO_4^{3-}$. In conclusion, dosage of the magnesium followed by pH control formed magnesium hydroxide, so pH was decreased. Therefore, pH adjustment should followed by after magnesium dosage and then pH should be adjusted to 11. Over pH 10, it was not good for struvite crystallization efficiency by side reaction. Following of the $Mg^{2+}$ and the $PO_4^{3-}$ are dosed excessively, the removal efficiency of the $NH_4^+$ increased. A molar ratio of $Mg^{2+}:NH_4^+:PO_4^{3-}$, 1.3:1:1.3 was the most on effective for $NH_4^+$ removal at pH 9.5. But for the perfect removal $NH_4^+$, it is thought to be that molar ratio should be 2:1:2.