• 한국생물공학회:학술대회논문집
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• 한국생물공학회 2005년도 생물공학의 동향(XVI)
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• pp.65-66
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• 2005

Anaerobic digestion is one of the well-known methods for biological treatment handling of concentrated organic matter such as swine $wastewater.^{1)} The anaerobic digestion can reduce organic loading but also hydrolyze non-biodegradable organic $matter.^{2)}$ The feces from the scrapper-type barn are usually collected to make compost and the urine is discarded with swine-slurry wastewater by ocean-dumping or treated by biological methods. The lagoon, aerobic digestion, anaerobic digestion, SBR, $A^{2}/O$, and UCT have been applied for treating swine $wastewater.^{3)} In this study, as a result of the analysis of swine wastewater, the total and soluble chemical oxygen demand was 130g/L and 60g/L, respectively. And the volatile fatty acid as chemical oxygen demand equivalent was 45g/L, which was 75% of soluble chemical oxygen demand. Before everything else, ammonia nitrogen concentration was 6.5 g/L. From biochemical acidogenic potential test, it was concluded that the enhanced acidification process to manage swine waste should be operated in the ammonia nitrogen concentration of less than 1.2 g/L. In the result of seeding ratio experiments with artificial $wastewater^{4)}, the lag period of acidogens was taken the long time because of the inhibition by the $ammonia^{5)}$, however no difference of period by the seeding ratio was not shown. The Haldane-based biokinetics were also evaluated using a method of fourth order Runge-Kutta $approximation.^{6,7)}$ The nonlinear least squares (NLLS) method with a 95% confidence interval was also used. The ranges of maximum microbial growth rate, ${/mu_{max}}$, and half saturation coefficient, $K_{s}$, for acidogenesis of various seeding ratio with artificial wastewater were 6.1 ~ 12.6 $d^{-1}$ and 45,000 ~ 53,500 mg glucose/L, respectively. Also, the methanogenic microbial yield coefficient, Y, and microbial decay rate coefficient, $k_{d}$, and inhibition substrate concentration, $K_{si}$, for the reactors were determined to be 0.32 ~ 0.465 ${/mu}g$/mg glucose; 0.42 ~ 1.01 $d^{-1}$ and 51,500 ~ 55,600 mg glucose/L, respectively.

• 한국물환경학회지
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• 제28권6호
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• pp.917-922
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• 2012

In order to improve applicability of a microbial fuel cell the laboratory-scaled study has been performed by adopting an air-cathode MFC system with high concentrated anaerobic slugies in this study. The concentrations of microbes are grouped into three types, Type A (TS 1.7%), Type B (TS 1.1%) and Type C (TS 0.51%). The open circuit voltage $(V_{oc})$ characteristics showed that the medium microbes concentration of 1.10% (Type B) kept a constant voltage of 1.0 V for 150 hours, which showed the longest time among three types (Type A and Type C). The discharge charge curves for a closed circuit with $500 \Omega$ also showed that Type B generated a stable discharge voltage of 0.8 V for a longer time as in the open circuit voltage case. This could be explained by the relatively large amount of the attached microbes. Under the $V_{oc}$condition the COD removal efficiency of Type B was found to be low for a long time, but those of Type A and C were found to be high for a short period of time. Therefore, the suspended microbes could decrease the coulombic efficiency. It was concluded that the high $V_{oc}$ was caused by low COD and the $V_{oc}$ became low after the COD removal. The COD reduction resulted in an unstable and low working voltage. From the polarization characteristics Type A was found to show the highest power density of $193\;mW/m^2$ with a fill factor of 0.127 due to the relatively high remaining COD even after the MFC reaction.

• 상하수도학회지
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• 제23권6호
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• pp.735-741
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• 2009

This study intends to evaluate the efficiency of non-point source reduction technique by using the porous lightweight and recycled aggregate which microorganism is seeded. In case of infiltration velocity 30~70 mm/hr in high concentration of influent, it is indicated that SS was 40~94%, COD 44~91%, BOD 4~91%, TN 1.2~66%, TP 7~70% of removal efficiency. Removal efficiency is good in infiltration velocity 30 > 50 > 70㎜/hr order. Therefore, the non-point source treatment facility filled with lightweight and recycled aggregate using microbial seeding shows higher removal efficiency than a conventional sand and gravel. We confirm that the function and efficiency are improved significantly and applied to treat non-point sources.

• 대한환경공학회지
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• 제37권6호
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• pp.332-339
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• 2015

질소화합물은 부영양화 등 수질을 악화시키는 결과를 초래하므로 질소 제거는 수처리에 있어 가장 중요한 문제들 중 하나이다. 본 연구에서는 독립영양탈질 공정인 CANON (Completely Autotrophic Nitrogen-removal Over Nitrite)을 이용하여 암모니아성 질소 제거 효율을 평가하고, 미생물 군집 분석을 수행하였다. AOB (Ammonium Oxidizing Bacteria)와 ANAMMOX(ANaerobic AMMonium OXidation)균을 동시에 식종하고, $37^{\circ}C$에서 유입 암모니아성 질소농도 100 mg-N/L와 아질산성 질소 농도 100 mg-N/L 조건으로 운전한 결과, 성공적인 CANON 반응이 유도되었다. 유입수에서 아질산성 질소를 제외시키고 암모니아성 질소(100 mg-N/L)만을 공급하였을 때, DO농도 0.4 mg/L 이상에서는 CANON의 성능이 악화되었지만, DO농도를 0.3 mg/L으로 낮추자 71.3%의 총 질소제거효율을 나타내었다. 유입 암모니아성 질소 농도를 50 mg-N/L로 낮추었을 때, 질소 제거효율이 급격히 악화되었다. 그러나 유입농도를 다시 100 mg-N/L로 증가시키자 14일 만에 이전의 질소제거성능을 회복하였고, 이후 $76.1{\pm}4.9%$의 총 질소제거효율을 나타냈다. 온도를 상온($20{\pm}1^{\circ}C$) 조건으로 전환하자 초기에는 불안정한 CANON 반응이 일어났지만, 23일 이후에는 안정적인 총 질소제거효율($70.0{\pm}2.6$%)을 유지하였다. PCR-DGGE를 이용한 미생물군집 분석 결과, 식종원과 CANON의 미생물군집은 확연한 차이를 나타냈지만, CANON의 각 조건에 따른 미생물군집은 크게 다르지 않았다. 따라서 질소제거 성능의 악화는 미생물군집을 구성하는 미생물종의 변화에 기인하기 보다는 구성 미생물종들의 질소제거 활성의 저하에 기인하는 것으로 생각된다. 이러한 결과는 AOB와 ANAMMOX균을 식종하여 CANON 반응을 성공적으로 유도한다면, 이후 농도나 온도의 변화에도 안정적인 미생물군집을 유지할 수 있다는 것을 의미한다.

• 대한환경공학회지
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• 제31권10호
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• pp.919-926
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• 2009

혐기성 암모늄 산화공정을 안정화시키기 전에 많은 양의 식종 미생물 투여가 필요하므로 혐기성 암모늄 산화균의 농후배양은 실규모의 혐기성 암모늄 산화 반응기를 운영할 때 필수적인 과정이다. 본 연구에서는 활성슬러지 미생물을 식종한 연속 회분식 반응기를 이용하여 혐기성 암모늄 산화균을 농후배양하고, 미생물 군집구조의 변화를 관찰하여 농후배양 결과를 검증하였다. 혐기성 암모늄 산화균의 농후배양은 70일간 시행되었고, 농후배양 후 활성시험에서 $NH_4\;^+$와 $NO_2\;^-$의 기질제거효율이 각각 98.5%와 90.7%로 관찰되어 혐기성 암모늄 산화균의 배양이 성공적으로 수행된 것으로 판단되었다. 계통분류학적 분지도 작성 결과, 다양하였던 Planctomycetes 문(phylum)의 미생물 군집구조가 농후배양 이후에 현저하게 단순해졌다는 것이 밝혀졌다. 농후배양 이후 발견된 36개의 clone들 모두가 혐기성 암모늄 산화균이었으며, Candidatus Brocadia (36%) 와 Candidatus Anammoxoglobus (64%) 속(genus)에 속하였다. RTQ-PCR (real-time quantitative PCR)을 통해 혐기성 암모늄 산화균을 정량한 결과, 혐기성 암모늄 산화 상향류식 연속 배양기에서 1년 이상 선택 배양된 붉은색 혐기성암모늄 산화 입상 슬러지에 비해 혐기성 암모늄 산화균의 16S rDNA 농도가 74.8%인 것으로 나타났다. 상기의 분자생물학적 분석을 통해 70일간 농후배양된 활성슬러지가 혐기성 암모늄 산화 실용화 공정의 접종 미생물로 활용 가능할 것으로 판단되었다.

• 한국수소및신에너지학회논문집
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• 제26권5호
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• pp.409-415
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• 2015

This study was performed to optimize the integrated anaerobic digestion (AD) and microbial electrolysis cells (MECs) for the enhanced hydrogen production. The optimum operational conditions of integrated AD and MECs were obtained using response surface methodology. The optimum substrate concentration and operational pH were 10 g/L and 6.8, respectively. In the confirm test, 1.43 mol $H_2/mol$ hexose was achieved, which was 2.5 times higher than only AD. After 40 to 60 hour at seeding, the volatile fatty acids (VFAs) in reactor of AD were not changed. However the VFAs of reactor of AD-MECs were reduced by 61.3% (acetate: 76.4%, butyrate: 50.0%, lactate: 55.0%).

• 한국수소및신에너지학회논문집
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• 제22권3호
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• pp.326-332
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• 2011

The authors examined the effects of operating parameters on the $H_2$ production by dark fermentation of the wastewater generated from food waste recycling facilities, in short "food waste wastewater (FWW)". Central composite design based response surface methodology was applied to analyze the effect of initial pH (5.5-8.5) and substrate concentration (2-20 g Carbo. COD/L) on $H_2$ production. The experiment was conducted under mesophilic ($35^{\circ}C$) condition and a heat-treated ($90^{\circ}C$ for 20min)anaerobic digester sludge was used as a seeding source. Although there was a little difference in carbohydrate removal, $H_2$ yield was largely affected by the experimental conditions, from 0.38 to 1.77 mol $H_2$/mol $hexose_{added}$. By applying regression analysis, $H_2$ yield was well fitted based on the coded value to a second order polynomial equation (p = 0.0243): Y = $1.78-0.17X_1+0.30X_2+0.37X_1X_2-0.29X_1{^2}-0.35X_2{^2}$, where $X_1$, $X_2$, and Y are pH, substrate concentration (g Carbo. COD/L), and hydrogen yield (mol $H_2$/mol $hexose_{added}$), respectively. The 2-D response surface clearly showed a high inter-dependency between initial pH and substrate concentration, and the role of these two factors was to control the pH during fermentation. According to the statistical optimization, the optimum condition of initial pH and substrate concentration were 7.0 and 13.4 g Carbo. COD/L, respectively, under which predicted $H_2$ yield was 1.84 mol $H_2$/mol $hexose_{added}$. Microbial analysis using 16S rRNA PCR-DGGE showed that $Clostridium$ sp. such as $Clostridium$ $perfringens$, $Clostridium$ $sticklandii$, and $Clostridium$ $bifermentans$ were main $H_2$-producers.