• Journal of the Korea Organic Resources Recycling Association
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• v.11 no.1
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• pp.127-128
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• 2003

본 연구는 퇴비화 과정 중 난용성 인산의 가용화와 무기태 인산의 변화를 알아보기 위하여 수행하였다. 비료와 퇴비중의 인산형태는 다른 성분들보다 토양에 흡착 또는 고정되거나 불용화 되는 양이 많아 작물의 흡수량이 적다. 시비된 인산의 흡수율은 낮고, 그 대부분은 난용화되기 때문에 토양에 축적되거나 세탈과 용탈에 의해 수질을 오염화시키는 주원인이 되고 있다. 퇴비화 과정중의 인산형태별 함량변화를 분석조사하여 작물에 시비되는 인산비료와 퇴비의 시용량을 적절하게 조절하여 인산의 과잉 시비량을 저감시키기 위한 연구이다. 돈분을 원료로 한 퇴비화 과정에서 단계별로 퇴비시료를 채취하여 총인산(T-P), 유효인산(Avail. -P)과 무기태인산분획별(Ca-P, Al-P, Fe-P)로 분석한 결과는 다음과 같다. 퇴적더미의 초기부피는 570L였으며, 약 2개월간의 퇴비화를 통해서 시료채취와 미생물등의 분해작용으로 최종부피는 430L정도로 감소하였다. 이는 초기의 부피보다 25% 감소하였다. 퇴적더미의 분해로 인한 용적밀도의 변화를 고려하면, 총인산 함량은 초기 약 17,500mg/kg에서 최종시료는 22,500mg/kg로 증가되었다. 또한 퇴비화가 진행됨에 따라 인산의 가용태가 증가하는 결과를 보였으며, 초기의 유효인산이 4,500mg/kg에서 최종시료에서는 8,900mg/kg으로 증가되었다. 그리고 무기태 인산분획별 인산의 형태별 변화를 조사한 결과, 퇴비화 과정 중 Ca-P의 경우 pH와의 중요한 상관관계를 갖고 있었다. 유기물분해를 통해 유리된 인산과 Ca은 난용태로 전환되는데, 초기의 약 10일 동안 Ca-P의 감소원인은 pH의 감소로 인한 Ca이 유리되는 정도가 낮기 때문인 것으로 해석된다. 초기 Ca-P형태의 인산함량은 11,900mg/kg으로 Fe-P와 Al-P보다 많았다. 또한 퇴비화가 안정화되어 부숙된 최종시료의 무기태 인산분획물 중 Ca-P는 18,000mg/kg로 증가하였으며, Ca-P>Al-P>Fe-P의 순 이었다. 그러나 Al-P와 Fe-P 형태의 무기태인산은 초기의 함량비율보다 다소 감소한 결과를 보였다. 결론적으로, 퇴비화과정 중 단계별 인산함량의 형태전환을 분석한 결과 총인산의 함량은 퇴비화가 안정화될수록 부피감소로 인한 인산함량이 증가하는 경향을 보였지만, 유기물질의 분해로 인한 원료내 인산의 형태가 불용태와 난용태에서 가용태 인산으로 전환되는 것을 도출하였다. 또한 무기태 인산분획물에서는 Ca-P 인산형태가 퇴비화가 진행될수록 증가한다는 결과를 얻었으며, Fe-P와 Al-P는 분해된 유기물의 킬레이트작용으로 감소되었다고 판단되며, 그 존재형태가 경쟁적임을 알 수 있었다. 따라서 화학비료와 퇴비의 시용이 병행될 경우에는 퇴비의 가용태 인산함량뿐만 아니라 무기태 인산의 함량을 분석한 후 인산질비료의 시비량을 조절해야할 것으로 판단된다.

• Journal of Korean Society of Environmental Engineers
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• v.32 no.12
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• pp.1126-1133
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• 2010

A two-stage biofilter was constructed and utilized to determine the removal efficiency when treating dynamic loading of a mixture of odorous compounds including benzene, toluene, p-xylene, ammonia and hydrogen sulfide. A yeast strain, Candida tropicalis, and a sulfur oxidizing bacterial (SOB) strain, Acidithiobacillus caldus sp., were immobilized in polyurethane media and packed in the two-stage biofilter. The experiment of dynamic loading variation was composed of (1) stepwise loading variation of all the odorous compounds (total EC test), (2) stepwise loading variation of each odorous compound, and (3) intermittent loading variation with 2-day-off and 3-day-on. The total EC test showed that the maximum elimination capacity was $61\;g/m^3/hr$ for total VOCs, and 5.2 and $9.1\;g/m^3/hr$ for ammonia and hydrogen, respectively. In addition, the inhibition between VOCs was observed when the loading of each individual VOC was varied. Especially the stepwise increase in toluene loading resulted in decreases of benzene and p-xylene removal efficiencies about 30% and 25%, respectively. However, the inhibition between organic and inorganic compounds was not observed. The intermittent loading variation with 2-day-off and 3-day-on showed that greater than 95% of the overall removal efficiency was restored in two days after the loading resumed. Consequently, the two-stage biofilter packed with immobilized microorganisms showed advantages over conventional biofilters for the simultaneous treatment of the mixture of organic and inorganic odorous compounds.

• Journal of the Korea Organic Resources Recycling Association
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• v.8 no.4
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• pp.138-146
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• 2000

This study was performed to determine the best fermentation soil in vanishing composting of individual residence garbage. At the result, temperature, weight, water content, volatile solid were reduced gradually by reaction of microorganism in the reactors after food was inserted for 9 days. The vanishing possibility was observed in all reactors. The best reactor was F and 4 that seeded microorganisms which were provided at S University. In addition it was possible to shorten cycle of putting in food waste. Inactivated reactors will be bad because of increased water content for long reaction time. Sodium chloride was accumulated and not vanished as time passed. But reactor was not insulated, the activities of microorganism in the reactor were affected highly by cold weather(about less than $12^{\circ}C$). When the study was extended to find out the feasibility of application, the retention time could be shortened to 3days form 9 days, when the microorganism reactor that used the fermentation soil seeded microorganisms which were provided at S University was maintained about $20^{\circ}C$.

• Journal of Korean Society of Environmental Engineers
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• v.29 no.9
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• pp.997-1002
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• 2007

The objectives of this research are to remove dissolved organic matter and nitrogen compounds by using aerated submerged bio-film(ASBF) reactors in batch systems and improve understanding of dissolved organic matter and nitrogen compounds removal rates with dynamic relationships between heterotrophic and autotrophic bacteria in the fixed-film reactor. This research explores the possibility of enhancing the performance of shallow wastewater treatment lagoons through the addition of specially designed structures. These structures are designed to encourage the growth of a nitrifying bacterial bio-film on a submerged surface. Specially, the effects of cold temperatures on the dissolved organic matter and ammonia nitrogen performance of the ASBF pilot plant was investigated for the batch system. It is anticipated thai the ASBF would be used for a design of biological treatment for removing of dissolved organic matter and nitrogen compounds in new wastewater treatment plants as well as existing wastewater treatment plants.

• Microbiology and Biotechnology Letters
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• v.15 no.6
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• pp.430-435
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• 1987

A chitin-immobilized enzyme amyloglucosidase(AMG) and a bacterium Zymomonas mobilis were coentrapped in alginate gel beads. Ethanol production was performed in a packed bed column reactor in a simultaneous saccharification and fermentation(SSF) mode using liquefied sago starch as a substrate. It was found that this process eliminated product inhibition and reverse reaction of glucose enhancing the rate of saccharification and ethanol production. At a low dilution rate of D = 0.11 hr$^{-1}$, the steady-state ethanol concentration was 46.0g/$m\ell$ (96.8 % of theoretical yield). The maximum ethanol productivity was 17.7g/$m\ell$, h at D = 0.83 hr$^{-1}$ when the calculation was based on the total working volume. The continuous production of ethanol was maintained stably over 40 days without problems in this reactor system.

• Proceedings of the Korean Environmental Sciences Society Conference
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• 2006.11a
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• pp.255-260
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• 2006

천수만의 수리 역학 및 수질 모델을 위하여 3차원 수리역학 모델(EFDC)과 21개 수질 변수에 대한 수질 모델이 접합된 3차원 수리역학-부영양화 모델(HEM-3D)을 이용하였다. 관측 자료에 대한 모델 검증 결과, 조위는 관측치에 비해 5% 정도, 유속은 10% 정도 작은 값을 보였으며, 지각은 모델 결과치가 고정항에서 늦고 간월도에서 빠르게 나타났다. 수질 항목, 특히 용존산소의 관측치에 나타난 전반적인 분포 양상을 잘 재현하고 있었으며, 항목별 기여도 분석에서는 수질 모델이 퇴적물에 의한 산소 소비에 민감하게 반응하고 있으며, 용존산소 변화에 있어서 퇴적물에 의한 영향이 중요한 역할을 하고 있음을 보여주었다. 본 모델 결과는 기존의 모델들과 비교하여 천수만 해역의 해수 유동 특성을 잘 재현하고 있으며, 본 모델과 연계된 수질 모델의 오염물 확산과 수질 항목들의 거동을 이해할 수 있는 정보를 제공하였다. 그럼에도 불구하고 본 연구를 통하여 나타난 문제점은, 수질 예측 모델에 필요한 수질 변수들의 관측 자료와 양식장에 의한 오염 부하량 자료가 충분하지 못하며, 퇴적물에 의한 수질 변화를 정량화할 수 있는 모델의 개발이 시급하다는 것이다. 특히 퇴적물에 의한 산소 요구량은 유기퇴적물이 미생물 등에 의해 분해되는 과정에서 요구되는 산소량으로서, 해수 유동 조건의 변화와 오염부하에 의한 유기퇴적물의 집적이 주된 요인이다. 방조제 건설 이후 해수유동 조건의 변화와 더불어 지속적으로 오염물이 유입되고, 담수 및 천수만의 수질이 점점 악화되고 있다. 따라서 이러한 오염부하와 퇴적물에 대한 관리대책이 시급한 것으로 판단되며, 향후 정확한 수질 예측을 위해서는 본 연구에서 나타난 문제점들에 대한 재고가 필요할 것으로 사료된다.

• KSBB Journal
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• v.14 no.1
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• pp.82-90
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• 1999

In order to eventually fabricate an analytical system for infectious microorganisms, we synthesized major immunochemical components, utilized them for the construction of model system, and investigated an assay concept for bacterial whole cells. For the preparation of system components, a polyclonal antibody, against Salmonella thompson as model analyte, purified by immuno-affinity chromatography was used to chemically link to streptavidin or an enzyme, horseradish peroxidase(HRP). The antibody and streptavidin was modified with sulfosuccinimidyl 4-[N-maleimidomethyl]cyclohexane-1-carboxylate and N-succinimidyl-3-[2-pyridyldithio]propionate(subsequently activated by dithiotheritol), respectively. The modified components were reacted to synthesize antibody-streptavidin conjugates which were then purified on a two-layer chromatography column of diaminobiotin gel and Sephadex G-100. For antibody-HRP conjugates, HRP molecules were activated by $NalO_4$ oxidation and then coupled to immunoglobulin. After stabilizing with ($NaCNBH_3$, the conjugates were purified by size exclusion chromatography on Biogel A5M column. To devise a model system, such produced components were combined with a dot-blotter in which a nitrocellulose membrane($12{\mu}m$ pre size) with immobilized biotin was already located. The analyte (S. thompson cells) was reacted with the both antibody conjugates in a liquid phase, and the complexes formed were captured on the membrane surfaces by applying vacuum in the bottom compartment of the blotter to invoke biotin-streptavidin reaction. Under optimal conditions, the system enabled to identify the analytical concept for bacterial whole cells, and the lower limit of detection was approximately $1{\mu}g/m{\ell}$($10^5-10^6$ cells/m$m{\ell}$). The controlling factors were the concentrations of each antibody conjugate that caused agglutination in the presence of analyte as they increased.

• Food Science and Preservation
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• v.24 no.7
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• pp.885-890
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• 2017

For the construction of the microbial monitoring method, anti-Salmonella polyclonal antibodies (pAbs) were produced from a rabbit and purified by saturated ammonium sulfate precipitation and protein A affinity column. The reactivity of anti-Salmonella pAbs was compared to that of commercial ones by using an indirect ELISA. The specificity of anti-Salmonella pAbs was investigated using 20 Salmonella serotypes and 20 non-Salmonella strains. A capturing ability of anti-Salmonella pAbs was investigated by exposing antibody-immobilized gold biosensor to different concentration of Salmonella mixture. Anti-Salmonella pAbs were successfully produced and purified with an antibody concentration of 2.0 mg/mL The reactivity of purified anti-Salmonella pAbs was greater than that of commercial one at all tested concentrations. All Salmonella serotypes, except S. Diarizonae, showed excellent binding efficiency with purified anti-Salmonella pAbs. Moreover, the purified anti-Salmonella pAbs showed excellent specificity against all non-Salmonella strains. The anti-Salmonella pAbs immobilized on the gold biosensor demonstrated the successful capturing capability against Salmonella with a dose-response manner. Therefore, the anti-Salmonella pAbs exhibited sufficient reactivity, specificity, as well as capturing capability against Salmonella to be considered as a bio-recognition element.

• Korean Journal of Microbiology
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• v.45 no.4
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• pp.419-424
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• 2009

To provide the basis of biosensor based on the lux genes from bioluminescent bacteria of Photobacterium leiognathi and Vibrio harveyi, we test the expression of lux genes in several strains of Escherichia coli. The expression of the recombinant plasmid of PlXba.pT7-3, containing all lux genes requiring for light emission without adding substrate, in E. coli 43R was so strong to see the blue-green light in single colony as well as in the alginate immobilized cell. In addition, the light intensity was decreased by adding heavy metal ion such as cadmium and zinc ions. These result raise the possibility that a biosensor can be developed using the lux genes system.

• Journal of the Korea Organic Resources Recycling Association
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• v.31 no.2
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• pp.53-61
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• 2023

Most of the sewage sludge is organic waste containing a large amount of organic substances decomposable by microorganisms by biological treatment. As for existing sewage sludge treatment methods, reduction and fuel conversion are being carried out using technologies such as drying, incineration, torrefaction, carbonization. However, the disadvantage of high energy consumption has been pointed out as latent heat of 539 kcal/kg is consumed based on drying. Therefore, in this study, we intend to produce solid fuel through hydrothermal carbonization(HTC), which is a thermochemical treatment. To evaluate the value of solid fuel, the characteristics of carbonization and fuel ratio were analyzed. As a result, as the hydrothermal carbonization reaction temperature increased, the lower heating value also increased by about 500 kcal/kg due to the increase in the degree of carbonization. H/C, O/C, ratio showed a decreasing trend from 1.78, 0.46 to 1.57, 0.32. When the ratio of ash to combustible content (fixed carbon + volatile) of dry sludge was 0.25 or more, it was derived that the degree of carbonization and calorific value did not increase even when hydrothermal carbonization was performed.