• 대한환경공학회지
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• 제22권2호
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• pp.313-321
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• 2000

본 연구는 AFMR(Anaerobic Floating Media Reactor) 공정을 이용하여 폐광산폐수로부터 중금속을 제거하기 위한 연구로서 본 연구에서는 두 개의 AFMR 반응조를 HRT 3일, COD/sulfate 비는 0.3~0.8, 운전온도는 $30^{\circ}C{\sim}35^{\circ}C$, 알칼리도는 1,000 mg/l(as $CaCO_3$)으로 운전하였다. 실험결과 AFMR 반응조는 COD/sulfate 비 0.5, 운전온도 $35^{\circ}C$에서 환원된 $SO{_4}^{2-}$양/제거된 COD양(mg/mg) 비는 약 1를 유지하였으며, 중금속 Cr, Pb, Fe은 99.99%, Cd 98%, Mn 90%의 제거효율을 나타내었다. 운전온도를 $35^{\circ}C$에서 $30^{\circ}C$로 감온시킬 때 AFMR 반응조내의 환원된 $SO{_4}^{2-}$양/제거된 COD양(mg/mg) 비는 1.37배로 증가하였다. 또한 운전온도 $30^{\circ}C$, COD/sulfate 비는 0.4일 때 최대의 황산염 환원을 보였으며 이때 유입되는 중금속인 Fe, Pb, Cr은 99.99%, Zn, Cd, Cu는 99.9%, Mn 97.3%의 중금속 제거효율을 보였다.

• 상하수도학회지
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• 제13권2호
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• pp.47-54
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• 1999

SRB(Sulfate Reducing Bacteria) converts sulfate into sulfide using an organic carbon source as the electron donor. The sulfide formed precipitates the various metals present in the AMD (Acid Mine Drainage). This study is the fundamental research on heavy metal removal from AMD using SRB. Two completely mixed anaerobic reactors were operated for cultivation of SRB at the temperature of $30^{\circ}C$ and anaerobic batch reactors were used to evaluate the effects of carbon source, COD/sulfate($SO_4^=$) ratio and alkalinity on sulfate reduction rate and heavy metal removal efficiency. AMD used in this study was characterized by low pH 3.0 and 1000mg/l of sulfate and dissolved high concentration of heavy metals such as iron, cadmium, copper, zinc and lead. It was found that glucose was an organic carbon source better than acetate as the electron donor of SRB for sulfate reduction in AMD. Amount of sulfate reduction maximized at the COD(glucose)/sulfate ratio of 0.5 in the influent and then removal efficiencies of heavy metals were 97.5% of Cu, 100% of Pb, 100% of Cr, 49% of Mn, 98% of Zn, 100% Cd and 92.4% of Fe. Although sulfate reduction results in an increase in the alkalinity of the reactor, alkalinity of 1000mg/1 (as $CaCo_3$) should be should be added continuously to the anaerobic reactor in order to remove heavy metals from AMD.

• 유기물자원화
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• 제16권3호
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• pp.75-82
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• 2008

상향류 혐기성 슬러지 블랭킷 반응조을 이용한 프로피온산의 처리시 고농도 황산염의 영향을 조사하였다. 반응조의 평균 유기물 부하와 수리학적 체류시간은 $1.2kg \;COD/m^3{\cdot}d$와 1.6일로 유지하였다. 황산염이 없는 조건에서 UASB 반응조의 경우 95%의 COD 제거율을 보였으며 황산염이 $2,000mgSO_4^{2-}/L$로 존재하는 경우 용존 황화물의 영향으로 COD 제거율이 83%로 감소하였다. 메탄 생성균과 황산염 환원균의 경쟁관계를 평가하기 위하여 미생물의 상호작용에 관해 조사하였다. $COD/SO_4^{2-}$ 비가 1인 경우 이용 가능한 전자 수용체의 평균 58%가 메탄 생성균에 의해 이용되며 나머지가 황산염 환원균에 의해 사용되었다. 초산과 프로피온산을 기질로 이용한 비메탄 활성도의 경우 미생물이 기질에 적응함에 따라 증가하였다.

• 한국지구물리탐사학회:학술대회논문집
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• 한국지구물리탐사학회 2003년도 Proceedings of the international symposium on the fusion technology
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• pp.504-510
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• 2003

This study has been carried out to evaluate the passive treatment systems for acid mine drainage in Korea and to suggest, if possible, the method for the improvement. 35 passive treatment systems in 27 mines have been constructed since 1996. SAPS, being the main process, was combined with more than one of processes such as anaerobic wetland, aerobic wetland, and oxidation pond for the construction of passive treatment system. Problems observed during the operation include the poor sulfate removal ratio, overflow, leakage, unusabless of the whole system, and inefficiency. The reasons of the poor sulfate removal ratio are believed that the low temperature during the winter prohibits the SRB activity and HRT for bacterial sulfate reduction is insufficient. An alternative method In Adit Sulfate Reducing System which enables to keep the temperature constant at about $15^{\circ}C$ was suggested. IASRS is the methods of placing the SAPS inside the adit, which enables the temperature around the system constant can be maintained. The experiments using the laboratory scaled model systems made up of four sections showed high efficiencies in pH control and metal removal ratios, but showed still low sulfate removal ratio of about $23\%$ also with high COD at the beginning of the operation.

• 환경위생공학
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• 제13권2호
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• pp.47-56
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• 1998

Effects of sulfate on the anaerobic substrate utilization were evaluated using UASB (Upflow Anaerobic Sludge Blanket) reactor. Effect of sulfate on the organic removal rate was dependent on the relative amount of microorganisms in the reactor, the operational condition, and the characteristics of sludge. When the sulfate shock was applied to 0.0 - 3.0g SO$_{4}$$^{2-}$/d, more than 95% of COD removal efficiency was achieved. Therefore, if F/M ratio was kept to low sufficiently with recirculation, it is shown that operation of the reactor was not affected significantly, though sulfate shock load was doubled compared to the normal operation. Provided that it is shocked by high strength of sulfate or temporary shock load is applied frequently the efficiency of reactor may be disadvantageous as well as the wash-out of sludge will be increased by decreasing the size to the accumulated frequency of granular sludge and the size with maximum frequency.

• 한국지하수토양환경학회:학술대회논문집
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• 한국지하수토양환경학회 2004년도 임시총회 및 추계학술발표회
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• pp.231-234
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• 2004

The experiments on some organic materials used in SAPS are carried out for the better sulfate reduction efficiency and the longer lifetime. Organic materials include spent mushroom compost, sewage sludge, oak chip compost and the combination of there. Reactors with mushroom compost, sewage sludge, the mixture of mushroom compost and sewage sludge, and the mixture of mushroom compost and oak chip compost maintained pH higher than 6.0. Reactors with mushroom compost, the mixture of mushroom compost and sewage sludge, and the mixture of mushroom compost and oak chip compost maintained reduction condition. Reactors with sewage sludge, oak chip compost and the mixture of sewage and oak chip compost produced COD less than 2,000ppm. Reactors with sewage and the mixture of mushroom compost, sewage sludge, oak chip compost showed about 60% of sulfate removal ratios.

• 한국환경보건학회지
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• 제28권1호
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• pp.51-65
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• 2002

This study was carried out to apply some basic physical and chemical treatment options including Fenton's oxidation, and to evaluate the performances and the characteristics of organic and nitrogen removal using lab-scale biological treatment system such as complete-mixing activated sludge and sequencing batch reactor(SBR) processes for the treatment of leachate from a municipal waste landfill in Gyeongnam province. The results were as follows: Chemical coagulation experiments using aluminium sulfate, ferrous sulfate and ferric chloride resulted in leachate CO $D_{Cr}$ removal of 32%, 23% and 21 % with optimum reaction dose ranges of 10,000～15,000 mg/$\ell$, 1,000 mg/$\ell$ and 500～2,000 mg/$\ell$, respectively. Fenton's oxidation required the optimum conditions including pH 3.5, 6 hours of reaction time, and hydrogen peroxide and ferrous sulfate concentrations of 2,000 ～ 3,000 mg/$\ell$ each with 1:1 weight ratio to remove more than 50% of COD in the leachate containing CO $D_{Cr}$ between 2,000 ～ 3,000 mg/$\ell$. Air-stripping achieved to remove more than 97% of N $H_3$-N in the leachate in spite of requiring high cost of chemicals and extensive stripping time, and, however, zeolite treatment removing 94% of N $H_3$-N showed high selectivity to N $H^{+}$ ion and much faster removal rate than air-stripping. The result from lab-scale experiment using a complete-mixing activated sludge process showed that biological treatability tended to increase more or less as HRT increased or F/M ratio decreased, and, however, COD removal efficiency was very poor by showing only 36% at HRT of 29 days. While COD removal was achieved more during Fenton's oxidation as compared to alum treatment for the landfill leachate, the ratio of BOD/COD after Fenton's oxidation considerably increased, and the consecutive activated sludge process significantly reduced organic strength to remove 50% of CO $D_{Cr}$ and 95% of BO $D_{5}$ . The SBR process was generally more capable of removing organics and nitrogen in the leachate than complete-mixing activated sludge process to achieve 74% removal of influent CO $D_{Cr}$ , 98% of BO $D_{5}$ and especially 99% of N $H_3$-N. However, organic removal rates of the SBR processes pre-treated with air-stripping and with zeolite were not much different with those without pre-treatment, and the SBR process treated with powdered activated carbon showed a little higher rate of CO $D_{Cr}$ removal than the process without any treatment. In conclusion, the biological treatment process using SBR proved to be the most applicable for the treatment of organic contents and nitrogen simultaneously and effectively in the landfill leachate.e.

• 도시과학
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• 제9권1호
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• pp.69-73
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• 2020

Sudokwon landfill("Sudokwon" means regions of Seoul, Kyunggi and Incheon metropolitan cities in Korea), the world's largest sanitary landfill, has been systematically managing statistics on the incoming and dumping wastes and satisfactorily controlling pollutants including leachate and LFG. According to our long time experience of LFG field monitoring, the emission of GHG from landfill estimated by the IPCC Guideline showed much difference with our results. C&D waste has high concentration of sulfate compared to other wastes. Increased C&D waste of dumping waste had changed the COD/sulfate ratio in the landfill, which caused the increase of H₂S gas and the decrease of CH₄ gas. But the IPCC estimation method does not consider the effects of sulfate. In addition to that, the oxidation factor of the cover soil is set to the default values of 0.1 but the measured values by the field monitoring, are showing much higher than that, especially in the closed landfill.

• 대한환경공학회지
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• 제22권5호
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• pp.811-817
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• 2000

본 연구에서는 생물학적으로 질산화/탈질 처리한 침출수와 기존 라군 처리한 침출수를 대상으로 응집과 펜톤산화시 최적 처리조건을 탐색하고, 펜톤산화시 알카리도가 COD 처리효율에 미치는 영향을 조사하였다. Jar-Tester를 이용한 응집처리시 염화제이철($FeCl_3$)의 적정 투입농도는 약 $1500mgFe^{3+}/L$로 조사되었으며, 이때 $COD_{Cr}$은 약 55%, $COD_{Mn}$은 약 64%의 처리효율을 나타냈다. 응집처리후($1,500mgFe^{3+}/L$) 펜톤처리시 약품투입비는 $Fe^{2+}/H_2O_2$의 비 1.5에서 COD 처리효율은 약 80%로 최대 처리효율을 나타냈으며, 이때 최적 약품투입농도는 철염 $600mgFe^{2+}/L$, 과산화수소수 $400mgH_2O_2/L$이었다. 펜톤 산화시 유입수의 알카리도가 증가됨에 따라 COD 처리효율이 저하되었다.

• 한국응용과학기술학회지
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• 제15권1호
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• pp.79-90
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• 1998

One of the objectives of this study were to develop a process for manufacturing activated carbons from agricultural by-products(rice shells and saw dust) and another is to measure the iodine number, ash content and removal ratio of COD. The other is to compare those values with those of commercialized activated carbons. Agricultural by-products based activated carbons were manufactured through the steam-reaction method. A rotary kiln type furnace was used for both carbonization and activation. The optimum operating temperatures for carbonization and activation were $650^{\circ}C$ and $900^{\circ}C$, respectively. For the activated carbons produced under these conditions, the iodine number was 1,127mg/g. Especially, removal efficiency of COD was 61.5% for 40mg/L of wastewater and 30% for 150mg/L of SLS(Sodium Lauryl Sulfate).