• 한국원자력학회:학술대회논문집
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• 한국원자력학회 2001년도 춘계학술발표회요약집
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• pp.390.2-390
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• 2001

• Journal of Microbiology and Biotechnology
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• 제20권4호
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• pp.763-766
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• 2010

An efficient and simple fermentation process was developed for the production of ${\gamma}$-aminobutyric acid (GABA) by Lactobacillus sakei B2-16. When the L. sakei B2-16 was cultivated in the rice bran extracts medium containing 4% sucrose, 1% yeast extract, and 12% monosodium glutamate, the maximum GABA concentration reached 660.0 mM with 100% conversion yield, showing the 2.4- fold higher GABA concentration compared with the modified MRS medium without the rice bran extracts. The GABA production was scaled-up from a laboratory scale (5 l) to a pilot (300 l) and a plant (5,000 l) scale to investigate the application possibility of GABA production to industrial fields. The production yields at the pilot and plant scales were similar to the laboratory scale using rice bran extracts medium, which could be effective for the low-cost production of GABA.

• 상하수도학회지
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• 제28권3호
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• pp.305-314
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• 2014

A pilot plant (Q=5 $m^3/d$) study was implemented for small and medium sized personal wastewater treatment plant effluent to evaluate MBR and A/O processes utilizing self-sufficient energy composed of wind and solar energy. The removal efficiencies of BOD, SS, turbidity and color were sufficient for legal water quality standards for gray water. However, those of nitrogen and phosphorus could not meet legal regulations which suggested that further removal of those contaminants were needed for reuse of the treated water. Self-sufficient energy rate was 100 % for the pilot plant due to excessive design capacity. In this research, wind and solar energy system was applied considering geological characteristics, which significantly improved energy self-sufficiency. Substantial improvement on energy self-sufficiency can be obtained by optimized investment and operation at a full scale wastewater treatment plant.

• 대한전자공학회:학술대회논문집
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• 대한전자공학회 2001년도 The 6th International Symposium of East Asian Resources Recycling Technology
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• pp.281-285
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• 2001

This technology Provides an economical Production of high value added goods applicable to electro chemicals by recycling of waste products in EGL(Electro Galvanizing Line). The waste products produced in EGL contain potassium chloride (KCI), nickel and zinc. Highly pure KCI and Zinc Chloride which are raw material of electro plating, can be produced by the development of the recycling process. The scope of this study ranges from laboratory experiments to pilot test in plant. We have developed the whole process of recycling technology such as purification method of waste products, fabrication methods of electro chemicals, basic design of plant, pilot scale production and evaluation of pilot goods, Developed electro chemicals were pure enough to satisfy the specification of steel company.

• Korean Chemical Engineering Research
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• 제49권2호
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• pp.200-205
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• 2011

직경 1.0 m인 파일럿 규모 슬러리 기포탑에서 기포체류량의 축방향, 반경방향분포를 고찰하였다. 기체의 유속, 연속 액상의 표면장력 그리고 슬러리상에 포함된 고체입자의 분율이 기포탑 내부 기포의 축방향 및 반경방향 분포에 미치는 영향을 검토하였다. 본 연구의 실험조건 모두에서 체류량은 기포탑의 중심으로부터 반경방향 무차원 거리가 증가함에 따라 감소하였으며, 기포탑의 분산판으로부터 축방향의 무차원의 거리가 증가함에 따라 증가하였다. 기포체류량의 반경방향 불균일도는 기체의 유속이 증가함에 따라 연속 액상의 표면장력이 감소함에 따라 증가하였으나 슬러리상에 포함된 고체입자 분율에는 크게 영향을 받지 않았다. 본 연구의 범위에서 축방향과 반경방향 기포체류량의 분포는 각각의 실험변수의 상관식으로 나타낼 수 있었다.

• 한국에너지공학회:학술대회논문집
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• 한국에너지공학회 2006년도 에너지.가스.기후변화학회 연합춘계학술대회 및 특별심포지움
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• pp.180-183
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• 2006

• 한국방재안전학회논문집
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• 제12권1호
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• pp.23-34
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• 2019

농촌지역 하천이나 호소수 수질 개선을 위한 비점오염원의 관리 및 저감은 시급한 현안이다. 본 연구에서는 농촌지역의 비점오염 저감을 위하여, 개비온 매트리스호안공에 혐기/호기의 구역을 적용한 자연형 비점오염처리 하천호안을 제안하고, 이의 축소모형 실험(1/6 축적) 및 현장 적용(가로2.0 m 세로 3.0 m 높이 0.4 m의 3단 격벽의 호안)을 통하여 활용성을 평가하였다. 개비온 매트리스 내부에 골재를 채운후 차수 격벽을 설치하고, 호안 법면의 자연 경사를 활용하여 혐기/호기 조건의 여과대를 조성하여 오염물질을 다단으로 처리하였다. 또한 호안공의 표면에 식생을 활착시켜, 토사의 표면 유입을 차단하고, 추가적으로 식생에 의한 정화 기능을 도모하였다. 본 호안공의 축소모형 및 현장 적용에서의 화학적산소요구량(COD) 및 질소성분(T-N, $NH_4{^+}-N$, $NO_3{^-}-N$)의 모니터링 결과, Lab Scale에서는 TCOD 17%, SCOD 35%, TN 14%, $NH_4{^+}-N$ 62%, $NO_3{^-}-N$ 33%의 제거효율을 나타내었고, pilot plant 시운전에서는 TCOD 24%, SCOD 29%, TN 47%, $NH_4{^+}-N$ 50%, $NO_3{^-}-N$ 33%의 제거효율을 나타내었으며, pilot plant 시운전에서는 29%의 TP 제거효율도 달성하였다.

• 한국물환경학회지
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• 제25권5호
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• pp.764-767
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• 2009

For a more effectively designed gravity thickener, thickening experiments were conducted for residuals produced by a ceramic membrane water treatment plant (WTP). Two kinds of residuals, one from backwashing (BW) and the other from chemically enhanced backwashing (CEB) procedure, were separately collected during a pilot plant experiment and their limiting solid flux ($SF_L$) measured. Batch thickening experiments showed that the BW and CEB residual had $SF_L$ of 10 and $25kg/m^2{\cdot}d$, respectively. Continuous operation of a pilot-scale gravity thickener proved that a mixed BW and CEB residual could be successfully thickened at the solid loading rate (SLR) of $12kg/m^2{\cdot}d$, allowing the concentration of the thickened residual to be about $15kg/m^2{\cdot}d$. From the experimental results and consideration of the seasonal thickening characteristics of the residual, SLR of $15kg/m^2{\cdot}d$ was proposed as a design parameter for full-scale gravity thickeners.

• 상하수도학회지
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• 제29권1호
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• pp.65-75
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• 2015

In this study, cation and anion exchange process for performance evaluation was conducted. A pilot plant for the ultrpure water production was installed with the capacity of $25m^3/d$. The various production rate and regeneration of ion exchange rate were tested to investigate the design parameters. The test resulst was applied to calculate the operating costs. Changing the flow rate of the ion exchange capacity of the reproduction reviewed the cation exchange process as opposed to the design value is 120 to 164% efficiency, whereas both anion exchange process is 82 to 124% efficiency, respectively. This results can be applied for more large scale plant if the scale up parameters are consdiered. The ion exchange capacity of the application in accordance with the design value characteristic upon application equipment is expected to be needed. In this study, the performance of cation and anion exchange resin process was evaluated with pilot plant($25m^3/d$). The ion exchange capacity along with space velocity and regeneration volume was evaluated. In results, the operation results was compared with design parameters.

• 한국물환경학회지
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• 제23권5호
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• pp.600-606
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• 2007

Livestock wastewater containing concentrated organic matters and nutrients has been known as one of the major pollutants. It is difficult to apply the conventional activated sludge process to treat livestock wastewater because of high Non-biodegradable (NBD) matter and ammonia. The objectives of this study are to remove NBD matters including aromatic compounds and ammonia in livestock wastewater using Coagulation-Fenton oxidation-Zeolite (CFZ) processes and ascertain applicable feasibility in the field through pilot plant experiment. NBD matters and color remained in the treated water were removed over 92% by Fenton oxidation as the second treatment process. Ammonia was removed by over 99.5% in the zeolite ion exchange process as the last treatment method. From $UV_{254}$, $E_2/E_3$ ratio and GC/MS analyses of treated water at each process, the aromatic compound was converted to aliphatic and aromaticity was decreased. In pilot scale test, organics and ammonia removal efficiencies were not much different from the result of lab-scale test at various operation conditions. Furthermore, reaction time and dosage of Fenton reagent in pilot scale experiment reduced by 40 min and 50% rather than in lab-scale test. $BOD_5$, $COD_{Mn}$, SS, T-N and T-P of treated water in the pilot-scale experiment also met the effluent standards.