• 한국농공학회:학술대회논문집
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• 한국농공학회 2001년도 학술발표회 발표논문집
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• pp.431-434
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• 2001

This study was carried oui to investigate tile filtering performance of using fresh compost as a biofilter. Three biofilter vessels were made using fresh compost as a biofilter media. A mixtures of dairy manure, soy sludge, rice hulls and sawdust were composted in a pilot scale reactor of 605L to generate tile ammonia emission. The ammonia emission from the compost reactor was passed through three biofilters and collected in the boric acid trap to measure the ammonia emission. Filtering performance was influenced by the depth of biofilter media. Efficient filtering effect was acquired for the depth above 40 cm.

• Environmental Engineering Research
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• 제19권1호
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• pp.47-57
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• 2014

The aim of this paper was to study the effect of five different waste combinations (C/N 15, C/N 20, C/N 25, C/N 30, and control) of sewage sludge coupled with sawdust and cattle manure in a pilot scale rotary drum reactor, during 20 days of the composting process. Our results showed that C/N 30 possesses a higher temperature regime with higher % reduction in moisture content, total organic carbon, soluble biochemical oxygen demand and chemical oxygen demand; and higher % gain in total nitrogen and phosphorus at the end of the composting period implying the total amount of biodegradable organic material is stabilized. In addition, $CO_2$ evolution and oxygen uptake rate decreased during the process, reflecting the stable behavior of the final compost. A Solvita maturity index of 8 indicated that the compost was stable and ready for usage as a soil conditioner. The results indicated that composting can be an alternate technology for the management of sewage sludge disposal.

• 환경위생공학
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• 제16권1호
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• pp.34-39
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• 2001

Submerged Membrane Bio-Reacter(SMBR) process was used to food wastewater treatment. From laboratory pilot-scale experiment data, it was confirmed that this process was very effective process for organics, suspended solid, and N, P treatment. It was found that BOD and COD removal rate were obtained 90% and 92%, respectively, for 150 days operation. Organics loading rate did not affect to the removal efficiency because MLSS concentration in aerobic tank was highly maintained. IN the case of first reactor operated with anoxic and second reactor operated as aerobic, T-N, T-P removal rate were obtained 93% and 95%, respectively. It was shown that removal efficiency could be maintained stable due to the complete removal of SS and sludge production decreased with increasing of sludge retention time.

• Journal of Microbiology and Biotechnology
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• 제15권3호
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• pp.455-460
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• 2005

A pilot-scale sulfur particle autotrophic denitrification (SPAD) process for the treatment of municipal wastewater was operated for 10 months at Shihwa, Korea, and higher than $90\%\;NO^{-}_{3}-N$ removal efficiency was observed. Plate counting showed that the lower part of the denitrifying column reactor had the most autotrophic denitrifiers. The biofilm thickness formed on sulfur particles from the SPAD reactor was approximately $25-30\;{\mu}m$, measured by DAPI (4,6-diamidino-2-phenylindole) staining. The presence of bacteria inside the highly porous sulfur particle was also monitored by SEM observation of the internal surfaces of broken sulfur particles. Biofilm extracellular polymeric substances (EPS) analysis showed that the ratio of carbohydrate to protein decreased with the reactor heights at which biofilm-formed sulfur particles were obtained.

• KSBB Journal
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• 제7권1호
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• pp.79-83
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• 1992

Erwinia rhapontici를 Ca-alginate에 고정화시켜 고정화 세포의 반응특성을 고찰하고, STR, PBR을 이용하여 Palatinose의 생산을 검토하였다. Free cell과 고정화 세포의 반응최적 pH는 5.5-6.0, 반응 최적온도는$30-35^{\circ}C$로 동일하였으나 고정화에 의해 pH 및 온도 범위가 보다 넓어졌고, 이때 Free cell및 고정화 세포의 겉보기 Km갑슨 각각 0.13, 0.28M이었다. STR을 이용한 Palatonose 생산시 고정화 세포의 반감기는 약 380 시간으로 낮았으나, PBR을 통해 30일까지 안정운전이 가능하였다. PBR 운전시의 운전온도 30, $33^{\circ}C$에서 Palatinose수율 및 고정화 세포의 안정성은 거의 동일한 결과를 나타내었으며 이때 PBR생산성은 약 120g/l$\cdot$h이었고, Pilot scale인 50L 까지 성공적으로 Scale up 되었다.

• Korean Chemical Engineering Research
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• 제56권6호
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• pp.878-883
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• 2018

A circulating fluidized bed (CFB) has been used in various chemical industries because of good heat and mass transfer. In addition, the methanol to olefins (MTO) process requiring the CFB reactor has attracted a great deal of interest due to steep increase of oil price. To design a CFB reactor for MTO pilot process, therefore, we has examined the hydrodynamic properties of spherical catalysts with different particle size and developed a correlation equation to predict catalyst holdup in a riser of CFB reactor. The hydrodynamics of micro-spherical catalysts with average particle size of 53, 90 and 140 mm was evaluated in a $0.025m-ID{\times}4m-high$ CFB riser. We also developed a model described by a decay coefficient to predict solid hold-up distribution in the riser. The decay coefficient developed in this study could be expressed as a function of Froude number and dimensionless velocity ratio. This model could predict well the experimental data obtained from this work.

• 한국표면공학회지
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• 제55권6호
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• pp.441-447
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• 2022

Silicon-based materials are one of the most promising anode active materials in lithium-ion battery. A carbon layer decorated on the surface of silicon particles efficiently suppresses the large volume expansion of silicon and improves electrical conductivity. Carbon coating through chemical vapor deposition (CVD) is one of the most effective strategies to synthesize carbon- coated silicon materials suitable for mass production. Herein, we synthesized carbon coated SiOx via pilot scale CVD reactor (P-SiO_x@C) and carbon coated SiO_x via industrial scale CVD reactor (I-SiO_x@C) to identify physical characteristic changes according to the CVD capacity. Reduced size silicon domains and local non-uniform carbon coating layer were detected in I-SiO_x@C due to non-uniform temperature distribution in the industrial scale CVD reactor with large capacity, resulting in increased surface area due to severe electrolyte consumption.

• 한국원자력학회:학술대회논문집
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• 한국원자력학회 2003년도 춘계학술발표대회 요약집
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• pp.148-148
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• 2003

• 대한지하수환경학회지
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• 제4권3호
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• pp.116-121
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• 1997

정화 효율과 운영상의 문제점을 파악하였다. 반응조 유입수 및 방류수에 대하여 현장에서 pH 및 Eh(산화환원전위)를 측정하였고 Cd, Pb, As, Zn, Cu, Fe, Al 및 Mn 등을 실험실에서 분석 하였다. 반응조 방류수에 대한 수질분석 결과 우분 및 석회석이 섞인 볏짚 반응조의 Cu, Zn, Fe, Cd, Al, Mn및 Pb의 정화효율(최대)은 98%, 100%, 99%, 100%, 97%, 61% 및 100%였고 이때 반응조의 수질환경은 pH 6 그리고 Eh 값이 -300 mV부근의 환원환경이었다. 그러나 시간이 경과함에 따라 Eh 값은 상승하였고 Al을 제외한 금속성분의 정화효율도 낮아져 반응조의 혐기환경유지는 금속성분의 정화에 매우 중요하였다. 반응조 시설을 운영한 결과 배관내의 산화물 Scale 및 기질물질의 부피 변화는 광산배수의 흐름을 방해하는 요소로 나타났다.

• Korean Chemical Engineering Research
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• 제47권4호
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• pp.446-452
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• 2009

최근 청정대체에너지로 각광을 받고 있는 dimethyl ether(DME)를 천연가스를 이용하여 직접 생산하는 1단계법의 고정층 촉매 반응기를 모사하였다. 1단계법의 고정층 반응기의 경우, 발열 반응인 메탄올 합성반응과 메탄올 탈수 반응이 동시에 일어나기 때문에 촉매의 비활성화를 일으킬 수 있는 hot spot의 발생을 막는 것이 가장 중요하다. 따라서 향후 상용공정에 적용 가능한 향류 냉각방식(count-current cooling system)과 포화액체 풀비등 방식(pool boiling system)을 적용하여 반응기 거동을 모사하고 이를 비교하였다. CO 전환율과 DME 생산성 면에서 향류 냉각방식이 더 효과적이었다. 하지만 포화비등액체 풀비등 방식이 더 작은 온도 범위에서 운전되어 hot spot(국소 고온점)의 가능성을 낮추고 더 안정적인 반응기 운전범위를 확보할 수 있었다.