• 한국화재소방학회논문지
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• 제20권4호
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• pp.98-104
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• 2006

원자력발전소 화재방호 규정에서 방화벽 관통부는 방화벽과 동등한 내화성능을 갖는 구조로 시공할 것을 요구하고 있다. 화재방호 규정이 제정되기 이전에 설계되어 방화벽 관통부 내화성능 인증되지 않은 'K' 원자력발전소에 대해서 내화성능을 평가하였다. 내화성능 평가는 육안점검에 의한 방법과 시공된 관통부 데이터와 시험체 데이터를 비교하여 판단하는 한계접근법을 적용하였다. 내화성능 평가 결과, 전체 관통부의 50%에 해당하는 관통부가 성능기준에 미달하는 것으로 나타났다. 본 연구에서는 성능평가 결과와 더불어 관통부 내화성능을 확보하기 위한 설비 개선, 유지관리 방안 등을 제시하였다. 본 연구는 가동중인 발전소를 대상으로 한 실증평가로서 본 연구에서 적용한 평가방법, 연구결과 등은 향후 타원전의 관통부 성능평가에 유용하게 활용될 것으로 기대된다.

• 원자력산업
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• 9_10호통권3호
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• pp.50-50
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• 1981

• 한국대기환경학회:학술대회논문집
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• 한국대기환경학회 1995년도 한국대기보전학회 추계학술대회 요지집
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• pp.169-170
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• 1995

• 한국상하수도협회지
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• 통권7호
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• pp.112-118
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• 2004

• 한국원자력학회:학술대회논문집
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• 한국원자력학회 2002년도 추계학술발표회요약집
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• pp.354.1-354
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• 2002

• 한국지반환경공학회 논문집
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• 제10권5호
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• pp.33-39
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• 2009

본 연구는 정읍시에서 배출되는 하수 슬러지, 축산 분뇨, 음식물 쓰레기를 대상으로 Pilot Scale($100m^3$) 초고온 호기성 퇴비화 공정에서의 복합 악취 및 12개 지정 악취물질을 평가하였다. 각각의 대상 물질은 종균과 혼합하였고 1차 50일, 2차 60일 기간동안 운전하였다. 호기성 퇴비화가 진행됨에 따라 1차, 2차 퇴비화공정에서 온도가 상승하여 약 $90{\sim}95^{\circ}C$가 되었다. 악취 분석을 위한 시료는 1차의 경우 퇴비상부에서, 2차의 경우 Pilot Plant 경계지점에서 채취하였다. 지정 악취 물질 12개 항목의 기기 분석에서 악취의 주요 원인으로는 암모니아, 메틸머캅탄, 디메틸다이설파이드, 트리메틸아민이었다. 초기 복합악취의 농도는 퇴비화 공정이 끝난 후의 농도보다 높았지만 규제기준을 넘지 않았다. 초고온 호기성 퇴비화 공정에서는 적절한 교반시점과 발효 온도가 악취 발생의 중요한 인자라고 판단된다.

• 한국환경과학회지
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• 제23권4호
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• pp.681-695
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• 2014

In a pilot-scale dyeing wastewater treatment using two-type fluidizing media, each thickness of biofilm was 15 and 30 ${\mu}m$, respectively. The numbers of protozoa inhabited in small-size (PEMT A) and big-size (PEMT B) media were $7.5{\times}10^4$ and $1.25{\times}10^5$ cells/ml, respectively, and dominant species were Entosiphon sulcatus var sulcatus in PEMT A and Chlamydomonas reinhardtii in PEMT B, respectively. Flask experiments using the two media revealed that the percentages of color removal were 25.8% in PEMT A and 27.1% in PEMT B after 72-h cultivation, indicating the necessity of bioaugmentation. Experiments for bioaugmentation effect on color removal were carried out in the pilot-scale treatment for 75 d by three-step operation under the control of wastewater loading rate and microbial input rate. Dye degradation occurred mainly in the second reaction tank, and the attachment of augmented dye-degrading microorganisms to media took at least 35 d. Final value of chromaticity in effluent was 227, meeting the required standard. Therefore bioaugmentation onto media was good for color treatment. In summary, thickness of biofilm formed on the media depended upon the size of media, resulting in different ecosystem inside the media. Hence, this affected microbial community and color treatment further. Accordingly, the reduction of operation cost is expected by efficient color-treatment process using bioaugmented media.

• 청정기술
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• 제9권2호
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• pp.71-79
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• 2003

화력발전소에서 배출되는 질소산화물 제어를 위한 선택적 촉매 환원 공정은 안정적이며 고효율 설계가 가능하여 범용적으로 사용되고 있는 기술이다. 선택적 촉매 환원 공정의 최적 설계를 위해서는 촉매 특성에 따른 설계기술이 정립되어야 하며, 다양한 조건에 대한 설계경험이 필요하다. 본 연구에서는 SCR 공정의 설계자료 도출을 위해 설계/제작된 $1,000Nm^3/hr$급 SCR 파일럿 플랜트를 이용하여 반응온도, $NH_3/NO$ 몰비, 공간속도, 선속도 및 압력손실 등의 설계변수에 대한 성능실험을 수행하고, 도출된 실험 결과를 통한 설계과정을 기술하였다.

• 한국생물정보학회:학술대회논문집
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• 한국생물정보시스템생물학회 2005년도 BIOINFO 2005
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• pp.151-155
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• 2005

Recently, systems biology has been increasingly applied to gain insights into the complexity of living organisms. Many inaccessible biological information and hidden evidences fur example flux distribution of the metabolites are simply revealed by investigation of artificial cell behaviors. Most bio-models are models of single cell organisms that cannot handle the multi-cellular organisms like plants. Herein, a structured and multi-cellular model of potato was developed to comprehend the root starch biosynthesis. On the basis of simplest plant cell biology, a potato structured model on the platform of Berkley Madonna was divided into three parts: photosynthetic (leaf), non-photosynthetic (tuber) and transportation (phloem) cells. The model of starch biosynthesis begins with the fixation of CO$_2$ from atmosphere to the Calvin cycle. Passing through a series of reactions, triose phosphate from Calvin cycle is converted to sucrose which is transported to sink cells and is eventually formed the amylose and amylopectin (starch constituents). After validating the model with data from a number of literatures, the results show that the structured model is a good representative of the studied system. The result of triose phosphate (DHAP and GAP) elevation due to lessening the aldolase activity is an illustration of the validation. Furthermore, the representative model was used to gain more understanding of starch production process such as the effect of CO$_2$ uptake on qualitative and quantitative aspects of starch biosynthesis.

• 상하수도학회지
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• 제25권3호
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• pp.383-390
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• 2011

In this study, a process combined biofiltration with sulfur-utilizing autotrophic denitrification and membrane separation was proposed to examine the efficiency of nitrogen removal. As an experimental device, hollow-fiber module was installed in the center of reactor to generate the flux forward sulfur layer in the cylinder packed with granular sulfur. In addition, a simple module was installed in activated sludge aeration tank which inside and outside of sulfur-using denitrification module was covered with microfilter and the module was considered as an alternative of clarifier. The experiment for developing new MBR process was carried out for three years totally. As the results of first two-year experiment, successful nitrogen removal performance was revealed with lab-scale test and pliot scale plant using artificial wastewater and actual plating wastewater. In this year, pilot scale test using actual domestic wastewater was performed to prove field applicability. As the results, high-rate nitrogen removal performance was confirmed with about 0.19 kg ${NO_3}^--N/m^3$ day of rate. Also significant fouling and pressure increase were not found during the experiment. And, the production ratio of sulfate and the consumption ratio of alkalinity showed a slightly higher value about 311 mg ${SO_4}^{2-}/L$ and 369 mg $CaCO_3$/L, respectively. In conclusion, the developed MBR process can be utilized as an alternative for retrofiting existing wastewater plants as well as new construction of advanced sewage wastewater treatment plants, with cost-effective merit.