• 한국물환경학회지
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• 제21권1호
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• pp.29-33
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• 2005

In order to recycle the waste material and to develop the thickening unit of waste activated sludge from wastewater treatment facilities, the filtration bio-reactor equipped with a shadow mask filter module was employed for this work from which the operating properties and parameters were drawn. The sludge thickening and filtration unit is made of cylindrical acryl tank(12cm i.d. ${\times}$ 58cm height: working volume of 6L), where the flat-sheet type of shadow mask filter module(pore size: 220~250um, opening area: 34.8~39.6%) was installed and the effluent was withdrawn from the effluent port at the lowest point of the reactor, and the filtration was performed only by the hydraulic pressure. For evaluating the operating performance of this reactor, some parameters such as the solid-liquid separation of different biomass concentrations, the water quality of filtrate, the aeration cleaning time and the cleaning effect were investigated. Depending on the MLSS concentrations, the different time to withdraw 3L of filtrate was required in which the longer filtration time was necessary for the higher MLSS concentrations caused by the thicker formation of cake layer: 40 minutes for 5,000 mg/L, 70 minutes for 10,000 mg/L and 100 minutes for 15,000 mg/L, where the concentrations of SS were 8.9, 6.7 and 6.5 mg/L, respectively. Under the same operating conditions (the intensity of aeration cleaning: 80 L/min, MLSS: 10,000 mg/L), the proper aeration cleaning time was revealed 30 seconds, and the stable formation of cake layer was in the range of 10 to 15 minutes. Therefore, the shadow mask considered as a waste material can be of use as a filter material for the sludge thickening system.

• 공업화학
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• 제22권3호
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• pp.249-254
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• 2011

Ferroelectric의 강유전체 소구들을 충전한 원통형의 비열 방전 플라즈마 반응기를 설계 제작하였으며, 강유전체 층방전 구조를 구성하는 평판(20 mm 간격) 금속망 전극 사이에 직경 2.0 mm인 $SrBiTaO_9$ (SBT) 소구들을 위치시키고 고압의 교류 전원을 인가하였다. SBT 소구는 상온($25^{\circ}C$)에서 150, 큐리온도($335^{\circ}C$)에서 500의 유전상수를 가졌다. 플라즈마 반응기에서 오존 생성속도는 거의 인가전압의 증가에 비례하였으며, SBT 소구들이 충전된 경우, 20 kV 이상의 인가전압에서 오존 생성속도는 급격하게 증가하였다. 부코로나 방전에서 오존 생성속도가 정코로나 방전에서의 경우보다 높았다. 그러나 톨루엔 및 메틸렌클로라이드의 분해율은 생성된 오존 농도에 비례하여 증가하지 않았다.

• 대한환경공학회지
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• 제22권10호
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• pp.1869-1879
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• 2000

혐기성 소화공정 중 생성되는 주요 중간대사산물인 프로피온산의 분해대사에 대한 연구중 에탄올과의 산화 환원 반응인 coupling 반응으로써 혐기성 소화공정에서 프로피온산 축적을 저감시킬 수 있는 연구를 수행하였다. 따라서, 본 연구는 혐기성 공정에서 프로피온산의 전환에 따른 동력학적 반응과 에탄올과의 상호 반응에 따른 특정기질 선호영향을 모델에 적용하여 살펴보았다. 본 연구는 4단계의 실험으로 수행되었다. 1, 2, 3단계는 각기 다른 기질에 순화된 미생물들을 이용하여 프로피온산 1 g COD/L와 에탄올의 농도를 각각 0, 100, 200, 400과 1,000 mg/L로 주입하여 프로피온산과 에탄올의 혐기성 분해과정을 비교 연구하였으며, 4단계에서는 Glu-MCR과 HPr-MCR의 순화미생물의 혼합비를 조절하여 프로피온산 1 g COD/L를 주입하였을 때의 혐기성 분해를 연구하였다. 본 연구에서는 수정된 경쟁적 모델을 이용하여 특정기질 선호현상을 규명하였고, 에탄올 농도의 증가에 따라 아세트산 형성반응의 $K_{s2}$값의 증가와 메탄화 과정에서의 아세트산 생성 및 분해과정에 해당되는 $K_3$값이 일부 증가하는 결과를 얻을 수 있었다. 또한 순화미생물들에 따라 프로피온산과 에탄올의 분해에 미치는 영향이 다른 결과를 얻을 수 있었다.

• 한국식품과학회지
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• 제30권1호
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• pp.110-117
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• 1998

고정화 transglucosidase (TG)를 이용한 충진형 반응기를 만들어 isomaltooligosaccharides (IMO)의 연속생산 가능성을 살펴보고 기질용액의 농도와 유속에 따른 반응산물의 생성패턴과 운전안정성을 조사하였다. 고정화 TG에 의한 IMO의 생성패턴은 soluble TG의 경우와 동일하였다. 충진형반응기에 의해 생성된 포도당과 isomaltose의 농도는 기질인 maltose 용액의 농도와 종류에 관계없이 유속의 증가에 따라 지속적으로 감소되는 경향을 보였고 isomaltotriose 역시 10% 기질용액을 사용한 경우를 제외하고 같은 경향을 보였다. 반면, panose의 농도는 유속의 증가에 따라 증가하다가 감소하는 경향을 보였다. 기질농도가 10% 일 때, IMO의 최대수율은 2 mL/min 유속에서 52.1%였고, 20%와 30% (w/v)일 때는, $0.5{\sim}1.0\;mL/min$ 유속에서 각각 $39.0{\sim}38.0%,\;12.1{\sim}14.2%$의 최대수율을 보였다. 20%의 maltose를 함유한 조제당화액을 사용했을 때의 수율은 유속이 0.5 mL/min일 때 36.3%였다 본 충진형반응기는 $55^{\circ}C$에서 안정되게 운전되었다. 144시간 운전후에 초기 활성의 85%, 288시간 경과후에도 약 65%의 활성이 잔존하였다. 본 실험결과로 보아 IMO를 생산하기 위해 고정화 TG를 이용한 충진형반응기를 적용하는 것은 가능성이 클 것으로 예상되었다.

• JSTS:Journal of Semiconductor Technology and Science
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• 제5권3호
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• pp.149-158
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• 2005

This paper describes design, fabrication, and application of the silicon based temperature controllable micro reactor. In order to achieve fast temperature variation and low energy consumption, reaction chamber of the micro reactor was thermally isolated by etching the highly conductive silicon around the reaction chamber. Compared with the model not having thermally isolated structure, the thermally isolated micro reactor showed enhanced thermal performances such as fast temperature variation and low energy consumption. The performance enhancements of the micro reactor due to etched holes were verified by thermal experiment and numerical analysis. Regarding to 42 percents reduction of the thermal mass achieved by the etched holes, approximately 4 times faster thermal variation and 5 times smaller energy consumption were acquired. The total size of the fabricated micro reactor was $37{\times}30{\times}1mm^{3}$. Microchannel and reaction chamber were formed on the silicon substrate. The openings of channel and chamber were covered by the glass substrate. The Pt electrodes for heater and sensor are fabricated on the backside of silicon substrate below the reaction chamber. The dimension of channel cross section was $200{\times}100{\mu}m^{2}$. The volume of reaction chamber was $4{\mu}l$. The temperature of the micro reactor was controlled and measured simultaneously with NI DAQ PCI-MIO-16E-l board and LabVIEW program. Finally, the fabricated micro reactor and the temperature control system were applied to the thermal denaturation and the trypsin digestion of protein. BSA(bovine serum albumin) was chosen for the test sample. It was successfully shown that BSA was successfully denatured at $75^{\circ}C$ for 1 min and digested by trypsin at $37^{\circ}C$ for 10 min.

• 한국지하수토양환경학회지:지하수토양환경
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• 제20권3호
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• pp.1-6
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• 2015

The rapid industrial development is facing problem due to energy depletion in Korea. So that, it can be necessary to develop alternative energy sources. Alternative energy like biofuels can be produced by using waste fuel, which is ecofriendly. As we know, the organic waste was banned to dump in landfill and ocean dumping. The most practicable method usually used to reduce organic waste is getting feedstuff or composting, considering the discharge characteristics of agricultural by-products waste treatment were selected. In this study, bio-coal was made using agriculture by product. Biocoal was prepared by adding 50 g of uniformly mixture into reactor and was carbonized at low temperatures 210, 220, and 230℃. The time of reaction was 1, 2 and 3 hours. Bio-coal approximately was similar to the standard of solid fuels. Other characteristics of fuel were also studied. The experiments which were analyzed were moisture content and calorific value, ash, chlorine, sulfur and heavy metals analysis as mercury, cadmium, lead, arsenic, and chromium. As a result, bio-coal 220℃, 2 hours was the optimal conditions while heating.

• 한국막학회:학술대회논문집
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• 한국막학회 2000년도 추계 총회 및 국제학술발표회
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• pp.127-130
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• 2000

• Journal of Plant Biotechnology
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• 제5권3호
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• pp.187-191
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• 2003

This paper reported the establishment of mass production system of adventitious roots of Eleutherococcus sessiliflorus through the shake flask and bio-reactor culture. Induction of adventitious roots was started from the explants of germinated somatic embryos on half-strength Murashing and Skoog (MS) solid medium. The frequency of adventitious root formation was better in the explants comprising the basal hypocotyl parts than root explants alone. Among the different auxins tested (NAA, IBA and IAA), frequency of adventitious root induction was highest on medium with 0.5 mg/L NAA, and produced $16.3\pm1.9$ roots per explant. In shake-flask culture, deletion of $NH_4NO_3$ of MS medium was effective for induction of adventitious root compared with both full and half-strength MS media. Fresh weight increase of induced adventitious roots was performed well in medium with 0.5 mg/L IBA. When adventitious roots produced in shake-flask culture were transferred to 10-liter bioreactor, 5.5 times of fresh weight increase was gained after one month of culture. HPLC analysis revealed that the amount of eleutheroside E and E1 was higher in in vitro cultured adventitious roots than the 3 year-old field cultivated root barks of Eleutherococcus sessiliflorus. The content of eltutheroside B was much lower in adventitious roots than that of field cultivated one.

• 상하수도학회지
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• 제20권1호
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• pp.27-34
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• 2006

This study was conducted to evaluate the performance of a membrane bioreactor filled with high concentration of powdered activated carbon (HCPAC-MBR) to reduce DBPs at the drinking water treatment. The pilot system was installed after the rapid sand filtration process whose plant was the conventional treatment process. The removal efficiencies of DBPs were measured during pilot operation period of 2 years. HAA and THM removal rates could be maintained around 80~90% without any troubles and then tremendous reduction of HAA and THM reactivity were observed more than 52%. The average removal rate of HAA formation potential (FP) and THM formation potential (FP) were 70.5% and 67.6% respectively. It is clear that the PAC membrane bioreactor is highly applicable for advanced water treatment to control DBPs.

• Environmental Engineering Research
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• 제21권2호
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• pp.180-187
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• 2016

In the present work, bael shell (aegle marmelos) is used as the feedstock for pyrolysis, using a fixed bed reactor to investigate the characteristics of the pyrolysis oil. The product yields, e.g., liquid, char and gases are produced from the biomass at different temperatures with the particle size of 0.5-1.0 mm, at the heating rate of $150^{\circ}C/min$. The maximum liquid yield, i.e., 36.23 wt.%, was found at $5500^{\circ}C$. Some physical properties of the pyrolysis oil such as calorific value, viscosity, density, pH, flash point and fire point are evaluated. The calorific value of the bael shell pyrolysis oil was 20.4 MJ/kg, which is slightly higher than the biomass, i.e., 18.24 MJ/kg. The H/C and O/C ratios of the bio-oil were found as 2.3 and 0.56 respectively, which are quite higher than some other bio-oils. Gas Chromatography and Mass Spectroscopy (GC-MS) and Fourier Transform Infra-red (FTIR) analyses showed that the pyrolysis oil of bael shell is mostly composed by phenolic and acidic compounds. The results of the properties of the bael shell pyrolysis oil reveal the potential of the oil as an alternate fuel with the essential upgradation of some properties.