• Journal of the Korean GEO-environmental Society
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• v.11 no.5
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• pp.5-13
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• 2010

The research is intended to develop and verify a biological complex soil treatment process to treat and restore soil and groundwater which is contaminated with oil, heavy metals, and nutrients through experiments with the series of treatment process such as bioreactor, rolled pipe type of contact oxidation system(RPS), and chemical processing system. 5 microbial strains were separated and selected through experiment, whose soil purification efficiency was excellent, and it was noted that anion- and nonion-series of complex agent was most excellent as a surfactant for effectively separating oils from soils. Method to mix and apply selected microbes after treating the surfactant in the contaminated soil was most effective. The removal efficiencies of total petroleum hydrocarbon (TPH)-contaminated soil about 5,000mg/L and above 10,000mg/L were approximatly 90.0% for 28 days and 90.7% for 81 days by soil remediation system and the average removal efficiencies of BOD, $COD_{Mn}$, SS, T-N, and T-P in leachate were 90.6, 73.0, 91.9, 73.8, 65.7% by the bioreactor and RPS. The removal efficiency was above 99.0% by chemical processing system into cohesive agents.

• Journal of Korean Society of Environmental Engineers
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• v.31 no.10
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• pp.919-926
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• 2009

Enrichment of anaerobic ammonium oxidation (ANAMMOX) bacteria is the essential step for operating full-scale ANAMMOX bioreactor because adding a significant amount of seeding sludge is required to stabilize the ANAMMOX reactor. In this study, the enrichment of ANAMMOX bacteria from an activated sludge using sequencing batch reactor was conducted and verified by analyzing changes in the microbial community structure. ANAMMOX bacteria were successfully enriched for 70 days and the substrate removal efficiencies showed 98.5% and 90.7% for $NH_4\;^+$ and $NO_2\;^-$ in the activity test, respectively. The phylogenetic trees of Planctomycetes phylum showed that the diverse microbial community structure of an activated sludge was remarkably simplified after the enrichment. All 36 clones, obtained after the enrichment, were affiliated with ANAMMOX bacteria of Candidatus Brocadia (36%) and Candidatus Anammoxoglobus (64%) genera. The quantification using real-time quantitative PCR (RTQ-PCR) revea ed that the 16S rDNA concentration of ANAMMOX bacteria was 74.8% compared to the granular ANAMMOX sludge obtained from an upflow ANAMMOX sludge bed reactor which had been operated for more than one year. The results of molecular analysis supported that the enriched sludge could be used as a seeding sludge for a full-scale ANAMMOX bioreactor.

• Proceedings of the Korea Air Pollution Research Association Conference
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• 2002.04a
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• pp.307-308
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• 2002

최근 들어 지구환경의 보전 필요성이 그 어느 때보다도 강하게 제기되면서 대류권 내에서 진행되는 광화학적 대기오염 현상과 그에 따른 오존농도의 증가에 대해 많은 관심이 집중되고 있다 광화학적 대기오염현상이란 대기중의 휘발성 유기화합물(Volatile Organic Compounds VOCs)과 질소산화물(NOx)이 햇빛 내의 자외선에 의해 반응하면 오존, 알데히드, peroxyacetyl nitrate 등과 같은 2차 오염물질인 광화학 산화물을 생성하는 것을 의미하는데 이 광화학 산화물은 생물체에 악영향을 주고 아울러 성층권의 오존층을 파괴하여 궁극적으로는 지구 온난화 현상의 원인이 되고 있다. (중략)

• Journal of Korean Society of Environmental Engineers
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• v.35 no.8
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• pp.564-570
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• 2013

Domestic treatment facilities for acid mine drainage (AMD) mostly used a passive treatment process. But some passive treatment facility discharged high manganese concentrations because it is required high pH (>9) for abiotic oxidation of Mn(II) to Mn(IV). This study was focused on the feasibility of biological manganese treatment using the manganese-oxidizing bacteria (Pseudomonas sp. MN5) from AMD and economical application method of it. To investigate the various conditions of water quality the most part of the experiments were based on batch test. And result of it showed that maximum manganese oxidation rate were $10.4mg/L{\cdot}h$ at the pH7. We also performed small column tests in which MOB were attached to the functional polyurethane (FPU) media containing alkaline chemicals. Manganese concentration decreased 42 mg/L to below 6 mg/L. But anaerobic condition formed by excessive bacterial respiration in column resulted in increasing effluent manganese concentration.

• Journal of Korean Society of Water and Wastewater
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• v.20 no.1
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• pp.44-52
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• 2006

Bio-filtration processes using honeycomb tubes (process 1) and aeration and manganese-sand filtration (process 2) were evaluated for the biological manganese removal efficiency. The concentration of manganese at effluent was stabilized after 20days operation in process 1. It was estimated the required time for attaching and growing microorganisms to honeycomb tubes. In long term of operation periods, manganese removal efficiency was dropped for the excessively attached biofilm and manganese dioxide to honeycomb tubes. It took several days for normal operation in process 2, after that manganese removal efficiency was increased to 98% and stabilized for 1.5 years. Microorganisms in process 1 and 2 were isolated and cultured to characterize manganese-oxidizing bacteria. Among the four types of colony, light brown colony was turned blue color by leuco crystal violet spot test. Stenotropomonas genus, known as manganese-oxidizing bacteria, was identified by 16S rDNA partial sequencing analysis which was isolated in process 1 and 2. For the biological treatment to remove manganese, these two considerations are important. One is to choose the proper media attaching manganese oxidant, another one is to define the cultural condition of isolated manganese-oxidizing bacteria.

• KSBB Journal
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• v.14 no.5
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• pp.585-592
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• 1999

This study was aimed to enhance the Fe(II) oxidation rate using immobilized cells of Thiobacillus ferroxidans. For this purpose, a medium for the minimization of jarosite formation was developed first. Secondly, cell immobilization in celite beads was carried out. And then, repeated-batch and continuous operatons of Fe(II) oxidation by using immobilization cells were performed. In a series of flask cultures, three types of media were tested: media with a much lower salt concentration than that of the 9K medium; media which contained different nitrogen sources from that of the 9K medium, that is $(NH_4)_2HPO_4$, $NH_4Cl and HNO$_3$; media which contained $(NH_4)_2HPO_4$ as nitrogen and phosphate source, but without $K_2HPO_4$ as nitrogen and phosphate source in the 9K medium. As a result, the M16 medium which contained 3 g/L of $(NH_4)_2HPO_4$ as nitrogen and phosphate source was found to be the optimal one. It sustained good cell growth allowing no jarosite formation. In the repeated-batch operations, the rate of Fe(II) oxidation gradually increased to reach a maximum value as the batch was repeated. As a result of repeated-batch operations. a maximum Fe(II) oxidation rate was 2.33 g/L . h. In the continuous operations, the iron oxidation rate could be increased to 2.14 g/L .h at a dilution rate of 0.25 $h^{-1}$ which is greater than the maximum specific growth rate (0.12 $h^{-1}$) of the bacteria.

• Journal of environmental and Sanitary engineering
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• v.16 no.3
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• pp.1-13
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• 2001

트리클로로에틸렌 (trichloroethylene, TCE)는 오랜 시간동안 자연환경에서 잔류할 뿐만 아니라 TCE보다 더욱 더 독성이 강한 중간 생성물들을 만들기 때문에 미국과 대부분의 전세계 국가들로부터 주요 1차 환경오염물질로 분류되었다. 그러한 독성물질들은 혐기성 상태에서는 다이클로로 에틸렌(dichloroethylene, DCE)과 바이닐 클로라이드 (vinyl chloride, VC)와 같은 독성물질들이 생성되고 호기성 상태에서는 TCE epoxide계통의 물질들이 생성된다. 또한 훈증제인 메틸 브로마이드 (methyl bromide)는 대기의 오존층을 파괴하는 것으로 알려져 있고, 2001년경에 미국환경보호청 (USEPA)에 의해 사용이 금지될 것이다. TCE는 혐기성 조건하에서 연속적으로 탈염소화되고, 이어서 호기성 조건하에서 완전 산화될 수 있다. 그리하여 연속적인 혐기성 및 호기성 조건하에서 궁극적으로 TCE의 완전분해를 이루게된다. 메틸브로마이드는 화학적으로 가수분해되어 메틸 알콜 (methyl alcohol)로 되거나 유기물에 강하게 결합 (bound)된다. 또한 그것은 생물학적으로 포름알데하이드 (formaldehyde)로 산화되거나 메틸알콜로 가수분해된다. 수많은 연구자들에 의해 행해진 연구들은 TCE와 MeBr은 메탄 혹은 암모니아 산화 세균에 의한 공동대사과정 (cometabolism)을 통해 분해가 증진될 수 있다는 것을 보여주었다. 두 부류의 세균들이 두 화합물들을 분해시킬 수 있는 monooxygenase를 생산한다는 것은 잘 알려져 있다. 이 연구 논문에서 TCE와 MeBr의 생분해와 관련된 가장 최근의 연구논문들로부터 나온 핵심 연구결과들이 요약 검토된다. TCE와 MeBr로 오염된 현장을 정화하기 위해 이러한 기초연구결과들을 토대로 더욱 더 많은 연구가 필요 할 것으로 사료된다.

• Applied Chemistry for Engineering
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• v.21 no.6
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• pp.610-615
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• 2010

In this study ozonation of bis(2-chloroethyl) ether (BCEE) in aqueous solution was performed in a laboratory scale batch reacter. The ozonation process of BCEE was carried out by bubbling ozone at the bottom of reactor containing the BCEE solution. Ozonation was almost complete after 80 min with an ozone concentration of $50{\pm}10mg/L$. Ozonation treatment efficiencies of BCEE were evaluated in terms of $BOD_5$, $COD_{Cr}$, and TOC. In the ozonation of BCEE a 62.79% decrease of the $COD_{Cr}$ and a 57.25% decrease of the TOC lead to biodegradable by-products ($BOD_5/COD_{Cr}$ = 0.39). The results of this research show that wastewaters containing non-biodegradable compounds, such as BCEE can be successfully treated by ozonation followed by bio-treatment. The pseudo first-order rate constants of the ozonation was $2.00{\times}10^{-4}sec^{-1}$ and the activation energy was $10.02kcal{\cdot}mol^{-1}$ at $30^{\circ}C$.

• Journal of the Korea Academia-Industrial cooperation Society
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• v.12 no.9
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• pp.4274-4282
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• 2011

In this study, Fenton reaction was studied for the possibility of applying as advanced treatment and its optimal condition for the removal of refractory organics from the dye wastewater. Fenton reaction was applied to remove refractory organics after the bio-treatment (secondary treatment) inside test laboratory and on-site pilot plant. Wastewater from the secondary treatment was used and its $COD_{Mn}$ was measured as 30~50mg/L. After the Fenton reaction, the optimal condition was found as pH 3~3.5, reaction time 2~2.5hr, chemical input ratio of ($FeCl_2$(33%)/$H_2O_2$(35%)) was 3 : 1. When chemical input ratio of ($FeCl_2$(33%)/$H_2O_2$(35%)) was at its optimal, amount of sludge volume ($SV_{2hr}$) was 21~28%. With pilot plant test, removal rate was heavily influenced by the hydraulic retention time(HRT), and optimum value of HRT was 2.0 hr. When pilot plant($2m^3/d$) was placed on-site and operated continuously, it showed steady and fairly good treatment of COD where COD removal rate was 60~70%, treated water showed below 20mg/L.

• Journal of the Korea Academia-Industrial cooperation Society
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• v.17 no.3
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• pp.86-92
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• 2016

The possibility of the biological treatment of MBT wastewater generated from the vulcanization accelerator manufacturing process was investigated. MBT wastewater is not biodegradable because it hinders the activity of microorganisms, and approximately 10% of the total COD can be removed after a 7 day acclimation period. The optimal conditions of the MBT wastewater for the chemical pre-treatment was pH of 3.5 and the Fenton oxidation with the addition of $Fe^{3+}$ to the wastewater after agitation for 2 hours. The Fenton-treated MBT wastewater showed approximately 20% removal of COD when treated with the activated sludge process for the mixed paper wastewater and Fenton treated wastewater.