• Journal of Korean Society of Environmental Engineers
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• v.27 no.11
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• pp.1168-1173
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• 2005

Pilot scale vertical-type membrane bioreactor was operated to examine the effect of $FeCl_3$ injection on the removal of organics, nitrogen and phosphorous, and additionally trans-membrane pressure (TMP) was observed. The membrane type was hollow fiber membrane with pore size of $0.25\;{\mu}m$, and the material was polytetrafluoroethylene (PTFE). The membrane permeate was continuously removed by a pump under a constant flux ($25\;L/m^2/h$). Air back-flushing technique were adopted to reduce fouling. As a result, TMP was increased more slowly than that of the operation without air back-flushing, During long-term operation, approximately 310 days, the injection of $FeCl_3$ was effective not only in removing phosphorous chemically but also in reducing TMP increase. Furthermore, while the average COD and T-N concentration of the effluent without $FeCl_3$ injection was 14.3 mg/L and 6.0 mg/L respectively, that of effluent with $FeCl_3$ was 11.3 mg/L and 6.0 mg/L respectively, which confirmed the effects of $FeCl_3$.

• Clean Technology
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• v.5 no.1
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• pp.49-61
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• 1999

Fenton's oxidation can improve the biodegradability of refractory organic wastewater by generating $OH{\cdot}$ which is one of the most reactive species. Fenton's reagent is used to treat a variety of industrial waste containing a range of toxic organic compounds. But this process cannot be economical because of high chemical cost of $H_2O_2$, ferrous ion solution and high sludge disposal cost. In this study, we proposed a modified Fenton's oxidation process which can reduce the reagent cost and obtain better removal efficiencies with less Fenton's reagents, and have a good potential of sludge recycling. In modified Fenton reaction, ferrous ion solution is adjusted to optimal pH with NaOH. Then it added to the sample and reacted to $H_2O_2$. For the experiment, synthetic wastewater made of phenol, which is one of the typical water pollutants, was used and the ionic strength of this wastewater was controlled by adding $NaHCO_3$. The effects of DO, ionic strength, and $H_2O_2$ dosing methods were investigated. As a result, modified Fenton's treatment efficiencies are better than conventional Fenton's reaction treating leachate and dyeing wastewater. And modified Fenton's treatment efficiencies combined to the sludge recycling for a half of Iron dosage are as good as the conventional Fenton's for a normal Iron dosage.

• Proceedings of the Korean Environmental Sciences Society Conference
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• 1993.10a
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• pp.36-36
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• 1993

• Proceedings of the Korean Environmental Sciences Society Conference
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• 1998.10a
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• pp.119-120
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• 1998

• Proceedings of the Korean Environmental Sciences Society Conference
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• 1998.04a
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• pp.157-159
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• 1998

• Proceedings of the Korean Environmental Sciences Society Conference
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• 2000.05a
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• pp.126-127
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• 2000

Fe(III) 응집제는 pH 5～9범위에서 Al(III)계 응집제보다 보다 우수한 응집효과를 보였으며 또한 pH의 영향을 거의 받지 않는 것으로 나타났다. 잔류 Fe의 경우 응집제 주입농도와 pH 증가에 영향을 거의 받지 않고 저농도의 잔류 Fe농도를 나타낸 반면, Al(III) 응집제는 잔류 Al의 급격한 증가를 나타내었다.

• Journal of Korean Society of Environmental Engineers
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• v.32 no.1
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• pp.79-86
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• 2010

Effects of operating parameters such as applied voltage, solution conductivity, ferrous ion concentration, electrode material on phenol degradation by pulsed corona discharges were investigated in laboratory scale experiments. The increase of applied voltage enhanced the phenol degradation by generating more energetic electrons. The solution conductivity inversely affected phenol removal rate in the tested ranges because the increase of conductivity decreased the electric field strength through the liquid phase. The addition of ferrous sulfate promoted the phenol degradation through the OH radical production by the Fentonlike reactions between ferrous ion and hydrogen peroxide generated by pulsed corona discharges. Catechol and hydroquinone were detected as primary intermediates of phenol degradation and the decrease of pH and the increase of conductivity were observed probably due to the generation of organic acids. Almost all of the initial phenol was disappeared and 29% of total organic corbon (TOC) was removed in the condition of 0.5 mM of ferrous sulfate after approximately 230 kJ of discharge energy transferred to the reactor.

• Proceedings of the Korean Environmental Sciences Society Conference
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• 2006.11a
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• pp.345-349
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• 2006

수용성 안료인 RhB를 대상으로 광-펜톤 공정의 최전 운전조건을 구하고, 광-펜톤 공정을 구성하는 개별 공정을 비교한 결과 다음의 결론을 얻었다. 광-펜톤 공정의 최적 $Fe^{2+}$와 $H_2O_2$ 투입량은 각각 0.0031 mmol과 0.625 mmol이었으며, 최적 pH는 3으로 나타났으나, 7이하의 pH 범위에서는 RhB 색 감소에 큰 영향을 미치지 않는 것으로 나타났다. 초기 반응 속도에 가장 큰 영향을 주는 인자는 UV 광 전력 > $H_2O_2$> 철염의 순으로 나타났다. 80분간의 반응시간 경과 후 최종 RhB 농도를 고찰한 결과 UV 광 전력이 낮을 경우 색도가 다 제거되지 않기 때문에 광-펜톤 공정에서 UV 광 전력이 색 제거에 대한 가장 큰 인자라고 사료되었다. 광-펜톤 공정의 개별 공정인 UV, $H_2O_2$, 펜톤을 이용하여 RhB의 농도감소를 고찰한 결과 초기 반응속도상수는 펜톤 공정의 빠른 초기 반응로 인해 펜톤 > UV >$H_2O_2$로 나타났으나, 최종 RhB 농도를 고려할 경우 UV> 펜톤 > $H_2O_2$로 나타났다.

• 수도
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• v.24 no.4 s.85
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• pp.39-46
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• 1997

실험실 규모의 연구를 확대한 Pilot-Plant연구는 Bromate 감소에 대한 다양한 수질 문제에 대응할 수 있었다. 이러한 연구를 통해 산성하에서 $Fe^{2+}$을 주입시 Bromate가 감소됨을 확인하였다. 그러나 이러한 반응은 느린 반응이었으며, 온도에 의존하는 반응이었다. 단독응집제로서 $Fe^{2+}$은 탁도를 증가시켰다. 따라서 탁도를 제어하기 위해 $Fe^{2+}$를 주입하였다. $Fe^{2+}$/$Fe^{3+}$응집제의 조합으로 TOC를 제거할 수 있었다. 초기 결과를 통해 이러한 공정은 매우 면밀히 추진되어야 하며, 모든 온도에서 적용될 수 없었다. 현재까지 얻어진 결과에 의하면 오존처리함으로서 발생되는 Bromate를 최소화하는 방안은 낮은 pH조건과 $Fe^{2+}$의 주입이다. 최종 처리수에서 입자상물질과 철을 최소화하기 위해서는 pH 등과 같은 조건들을 변화시켜 여과공정 이전에 잔류 $Fe^{2+}$를 산화시킬 수 있도록 초기에 최적화가 이루어 져야 한다.

• Journal of Environmental Health Sciences
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• v.35 no.1
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• pp.58-63
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• 2009

This study investigated improvement to sludge dewaterability and coagulation for sewage treatment plant sludge by using sodium hypochlorite solution (NaOCl), ferric sulfate [$Fe_2(SO_4)_3$] and zeolite. The specific resistance to filtration(SRF), chloride, pH and turbidity were used to evaluate the sludge dewatering behaviors. The results of study were as follows: By varying the amount of NaOCl added the optimum result in terms of enhancement for pretreatment occurred when 34 mg/l of NaOCl was injected. When the total solids concentration of the sludge was 10,000 mg/l, the optimum ferric sulfate dosage for the sludge dewaterability was 150 mg/l and the corresponding SRF was $1.7{\times}10^7sec^2/g$. It was observed that injecting zeolite into sludge was effective in improving the dewaterability of sludge.