• 상하수도학회지
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• 제24권1호
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• pp.109-117
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• 2010

In the present study, the degradation characteristics of Lindane by Advanced Oxidation Processes(UV/$H_2O_2$, Photo-Fenton process) were studied. The degradation efficiency of Lindane in aqueous solution was investigated at various initial pH values, Fenton's reagent concentrations and initial concentrations of Lindane. GC-ECD was used to analyze lindane. Lindane has not been degraded without application of AOPs over two hours. But, approximately 5% of lindane was degraded with UV or $H_2O_2$ alone. Lindane with UV/$H_2O_2$ process showed approximately 7% higher removal efficiency than $H_2O_2$ process. In the UV/$H_2O_2$ process, the pH values did not affect the removal efficiency. The optimal mole ratio of $H_2O_2/Fe^{2+}$ for lindane degradation is about 1.0 in Photo-Fenton process. Also, the experimental results showed that lindane removal efficiency increased with the decrease of initial concentration of lindane. Under the same conditions, the order lindane of removal efficiency is as following : Photo-Fenton process > UV/$H_2O_2$ process > $H_2O_2$ process. In addition, intermediate products were identified by GC-MS techniques. Than PCCH(Pentachlorocyclohexene) was identified as a reaction intermediate of the Photo-Fenton process.

• 한국축산시설환경학회지
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• 제3권2호
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• pp.115-123
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• 1997

This study was conducted to investigate the removal effect of malodorous substances of piggery wastes by air injection. With 7% of TS weight of artificial piggery wastes, this study focused on the changes of the concentration of VFAs, H2S during treatment period of 14 days. As a results of this study, air injection volume for removal of malodorants in this study was 150$m\ell$ / min$.$l$.$Under this condition, we found the concentrations of VFAs, H2S, NH3 have very high relationship with the pH, ORP, BOD, {{{{ { NH}`_{4 } ^{+ } }}-N. Especially, the concentration of Volatile Fatty Acids, one of most offensive odorants and one of BOD compounds were depended on ORP which can be controled by air injection in artificial piggery wastes.

• Journal of Animal Science and Technology
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• 제45권4호
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• pp.641-648
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• 2003

본 연구에서는 돈사 폐수내의 인과 질소를 함께 결정화하여 회수하고 그 상등액을 전기분해 시키는 회분식 돈사 폐수공정에서의 오염물질 부하량과 수처리시간 변화에 따른 처리효율의 변화 및 각 오염물질 제거특성을 파악하였다. Struvite 형성을 위한 Mg원으로는 $MgCl_2$를 사용하였고 주입량은 폐수내 인 기준 1.3 Mole이었다. 총 4개의 운전(Run I, II, III, IV)에서 얻어진 평균 제거효율과 그 제거특성을 분석한 결과 인의 경우 부하량 변화에 따른 처리효율의 변화는 관찰되지 않았으며 제거의 주요 역할을 하는 반응조는 Struvite 반응조로서 적정 Mg원만 제공된다면 pH 조절제 첨가 없이 폭기만으로도 부하량에 관계없이 88% 이상의 제거가 MAP 형성을 통해 얻어지는 것으로 나타났다. 높은 암모니아성 질소 제거효율을 유지하기 위한 적정 부하량은 약 100g/$m^3$.d로서 동 부하량 이하에서는 부하량이 증가함에 따라 제거량도 증가하면서 90% 이상의 높은 효율과 일정한 제거특성을 보인 반면 그 이상에서는 불안정한 제거특성을 나타내면서 제거효율이 감소하였다. TOCs의 경우에는 부하량 변화에 따른 처리효율 변화는 관찰되지 않았으며, 그 제거효율은 수처리 시간에 의존적인 것으로 나타났다 ($r^2$ = 0.97). 색도 제거 효율은 전기분해조 용적기준 수처리시간 2일 이상에서 94%의 매우 높고 일정한 효율을 얻을 수 있었다.

• 한국환경과학회지
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• 제30권2호
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• pp.161-172
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• 2021

This study was initiated to isolate the microorganisms removing phosphorus (P) from domestic sewage and to investigate the effects of environmental factors on the growth and P removal of the isolated bacteria. Microorganisms isolated from the sewage were identified as Chryseobacterium sp., Stenotrophomonas maltophilia, and Bacillus licheniformis. Among them, Bacillus licheniformis was selected as the P removal microorganism. The environmental factors considered in this study included initial phosphorus concentration, temperature, pH, and carbon source. At initial P concentrations of 10, 20, and 30 mg/L, the P removal efficiencies were 100.0%, 84.0%, and 16.5%, respectively. At 20℃, 30℃, and 40℃, the P removal efficiencies were 0%, 75.8%, and 60.6%, respectively. The removal efficiencies of phosphorus according to pH were 1.6%, 91.7%, and 51.1% at pH 5, pH 7, and pH 9, respectively. Using glucose, acetate, and glucose + acetate as carbon sources yielded P removal efficiencies of 80.9%, 33.6%, and 54.1%, respectively. Therefore, the results from the study demonstrated that the P removal efficiencies of Bacillus licheniformis were the highest when the initial P concentration, temperature, pH, and carbon source were 10 mg/L, 30℃, 7, and glucose, respectively.

• 한국에너지공학회:학술대회논문집
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• 한국에너지공학회 2000년도 춘계 학술발표회 논문집
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• pp.19-22
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• 2000

• 한국전기전자재료학회:학술대회논문집
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• 한국전기전자재료학회 2002년도 하계학술대회 논문집 Vol.3 No.2
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• pp.917-921
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• 2002

In this paper, we made different types of non-thermal plasma reactors such as Metal-particle reactor with $Al_2O_3$ to measure NOx removal characteristic and the dielectric effect for NOx removal. NOx removal rate is not so good when we use just dielectric of $Al_2O_3$ at the Metal-particle reactor, also we just put sludge pellets(100%) without Metal-particle reactor with $Al_2O_3$ and dielectric such as $TiO_2$, $BaTiO_3$ to measure the effect of sludge for NOx removal so that NOx removal rate is almost the same. However NOx removal rate is more than 90% in case of the reactor of composition shape used both dielectric of $Al_2O_3$ and sludge pellets at the same time. In case of the shape of plasma reactor with dielectric, the Metal-particle reactor with $Al_2O_3$, and the metal-particle reactor with both $Al_2O_3$ and dielectric such as $TiO_2$, $BaTiO_3$ at the same time, they are almost the same effect for NOx removal, so we made MNPR(Metal-particle Non-thermal Plasma Reactor with $Al_2O_3$) to reduce these kinds of demerits. Finally, we think MNPR should be much better than other reactors for NOx removal.

• 한국미생물·생명공학회지
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• 제36권2호
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• pp.165-172
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• 2008

본 연구에서는 분리균주 LH2를 이용하여 각각의 중금속 (Cr, Cu, Ni, Pb, Zn)에 대한 최적성장조건을 도출하였으며, pH, 온도 및 중금속 농도 변화에 따른 중금속 제거효율을 관찰하였다. 분리균주는 18S rDNA 분석에 의거하여 종 유사성이 100%로서 Exophiala sp.로 동정되었다. 분리균주의 경우 $25^{\circ}C$, pH 7인 진탕배양 조건에서 가장 높은 제거효율을 보였다. 첨가되는 중금속의 농도가 200 ppm이하일 경우 중 금속의 비제거속도를 구한 결과 pH 7인 조건에서 중금속의 종류와 무관하게 10 ppm에서 200 ppm으로 중금속의 농도가 증가함에 따라 0.01에서 4.43 mg-metal $L^{-1}{\cdot}d^{-1}{\cdot}mg^{-1}{\cdot}DCW^{-1}$으로 증가하였다. pH 7로 설정된 배양액에 약 200ppm의 중금속이 첨가될 경우 중금속의 제거효율은 Cr, Cu, Ni, Pb, 및 Zn 이 각각 99.28%, 97.67%, 91.94%, 99.77%, 99.61%로 관찰되었다.

• 상하수도학회지
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• 제29권4호
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• pp.481-491
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• 2015

The aim of this study was to evaluate the chemical quenching system for residual ozone and to determine the operating condition for the quenching system. Hydrogen peroxide ($H_2O_2$) and sodium thiosulfate ($Na_2S_2O_3$) were investigated as quenching reagents for ozone removal, and the tendency of each chemical was notably different. In the case of $H_2O_2$, the degradation rate of ozone was increased as the concentration of $H_2O_2$ increase, and temperature and pH value have a significant effect on the degradation rate of ozone. On the other hand, the degradation rate of ozone was not affected by the concentration of $Na_2S_2O_3$, temperature and pH value, due to the high reactivity between the ${S_2O_3}^{2-}$ and ozone. This study evaluates the decomposition mechanism of ozone by $H_2O_2$ and $Na_2S_2O_3$ with consideration for the water quality and reaction time. Furthermore, the removal test for the quenching reagents, which can be remained after reaction with ozone, was conducted by GAC process.

• 한국기후변화학회지
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• 제8권1호
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• pp.51-56
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• 2017

The objective of the research project is to develop the hybrid deodorizer for the removal of residual harmful gases generating during pretreatment process of biogas. This hybrid deodorizer is capable of treating harmful gases that contains hydrogen sulfide ($H_2S$), ammonia ($NH_3$) and other odor substances. This hybrid deodorizer reduced the hydrogen sulfide content from approximately 150~200 ppm to less than 16 ppm. These residual harmful gases were effectively removed in the effluent, achieving up to 97% removal of $H_2S$ and 94% removal of $NH_3$ after treatment using hybrid deodorizer.

• 한국대기환경학회지
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• 제29권6호
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• pp.811-817
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• 2013

A two-stage bioreactor system using sulfur-oxidizing bacteria was studied to abate high strength hydrogen sulfide ($H_2S$) from biogas. The two-stage bioreactor consisted of a $H_2S$ absorption column (0.5 L) and a microbial oxidation column (1 L) in series, and the liquid medium was continuously recirculated through the columns. The objectives of this study were to determine the feasibility of the bioreactor for biogas desulfurization and to investigate the effect of the medium circulation rate on the system performance. An averaged concentration of $H_2S$ introduced to the bioreactor was 530 ppm, corresponding to an overall loading rate of $44.4g/m^3/hr$. During the initial 20 days period at the medium recirculation rate of 8 reactor volumes per hour (12 L/hr), the dissolved oxygen (DO) concentration in the oxidation column was 6 mg/L, while the DO in the absorption column was 0.5 mg/L showing that the oxygen contents of the biogas stream was not altered. Because of the biological oxidation of $H_2S$ in the oxidation column, the sulfate concentration increased from 200 mg/L to 5,600 mg/L in the liquid medium. The removal efficiency of $H_2S$ was greater than 99% in the initial operation period. After the initial period, the medium recirculation rate between the two columns was stepwise changed eight times from 1.0 to 40 vol/hr (1.5~60 L/hr). At the recirculation rate of faster than 4 vol/hr, the $H_2S$ removal efficiencies were found to be high, but the efficiency declined at the lower recirculation rates than the threshold.