• 한국식품과학회지
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• 제22권1호
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• pp.88-93
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• 1990

GLC를 이용 N-TFA n-butyl ester유도제화에 의한 아미노산 분석시 stainless steel packed column으로 효과적인 분리를 할 수 있는 고정상을 찾기 위하여 다음과 같은 2개의 column을 개발하여 표준 아미노산의 N-TFA n-butyl ester 유도체를 분석하였다. Column 1;3.36% OV-17+3.0% SE-30 on chromosorb W HP 100-120 mesh. Stainless steel column $(2m{\times}3mm\;I.D.)$ Column 2;1% NPGS+0.5% OV-17+0.5% SE-30 on chromosorb W HP 100-120 mesh. Stainless steel column $(2m{\times}3mm\;I.D.)$ Column 1에서 histidine을 제외한 19개의 아미노산 peak가 나타났으나 alanine과 valine peak는 분리되지 않았다. Colume 2에서는 15개의 아미노산이 좋은 분리를 이루었고 column 1에서 분리되지 않은 alanine과 valine.이 잘 분리되었으나 column 1에서 분리된 tryptophan, arginine 및 tyrosine이 나타나지 않았다. 분리된 모든 아미노산은 column 1, 2를 막론하고 아미노산 주입량 $1.25{\times}10^{-3}{\mu}mole-1.0{\times}10^{-2}{\mu}mole$의 범위에서 각 아미노산 peak의 높이와 내부표시제 peak 높이와의 비에 대한 주입량으로 나타낸 검정선이 선형을 나타내었고 모두 원점을 지났다. Glutamine, asparagine 및 cystine은 column 1,2에서 모두 glutamic acid, aspartic acid 및 cysteine peak와 일치하는 것으로 보아 N-TFA n-butyl ester 유도체를 만드는 과정에서 염산에 의해 각각 glutamic acid, aspartic acid 및 cysteine으로 전환되는 것으로 사료된다.

• KSBB Journal
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• 제24권4호
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• pp.353-360
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• 2009

본 연구에서는 혐기조 및 무산소조, 호기조로 구성된 상향류식 고정상 담체 반응장치와 호기조로 고정상 담체 대신에 유동상 담체를 사용한 Loop Reactor로 이루어진 장치에서 생활하수를 이용하여 성능실험을 수행한 후 HRT에 따른 유기물 및 T-N, T-P 등 오염물질의 제거 특성을 비교 분석하였다. 두 반응기 모두 평균 BOD 제거율과 SS 제거율은 HRT가 증가함에 따라 증가하다가 HRT 16 h 이상에서는 일정한 수치를 나타내고 있으며 HRT 16 h에서 고정상 담체 반응기와 Loop Reactor의 평균 BOD 제거율은 각각 86.6%, 90.9%이었으며 평균 SS 제거율은 각각 78.0%, 88.2%로 Loop Reactor의 경우가 각각 4.3%, 10.2%의 더 높은 BOD와 SS 제거율을 나타내었다. 또한 평균 $COD_{Cr}$, 제거율 및 평균 $COD_{Mn}$ 제거율은 BOD와 SS 제거율과 마찬가지로 HRT가 증가함에 따라 증가하다가 HRT 16 h에서 일정한 수치를 나타내고 있으며 고정상 담체 반응기와 Loop Reactor의 평균 $COD_{Cr}$, 제거율은 각각 63.5%, 75.2%이었으며 평균 $COD_{Mn}$ 제거율은 각각 60.7%, 73.6%로 Loop Reactor의 경우가 11.7%, 12.9% 더 높은 제거율을 나타내었다. 반면에 평균 T-N 제거율 및 T-P 제거율은 두 반응기 모두 HRT가 증가함에 따라 제거율은 계속 증가하는 양상을 보여주고 있으며 HRT 16 h에서 Loop Reactor의 경우 평균 T-N 제거율 및 평균 T-P 제거율은 각각 33.6%, 54.5%로 고정상 담체 반응기보다 14.1%, 10.8%의 더 높은 제거율을 나타내었다. 이상의 결과에서 Loop Reactor가 성능이 훨씬 더 우수하였으며 최적 HRT는 16 h임을 알 수 있었다.

• 한국물환경학회지
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• 제26권3호
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• pp.454-459
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• 2010

This study investigated the applicability of manganese coated media such as manganese coated sand (MCS), manganese coated sericite (MCSe) and manganese coated starfish material calcined at $550^{\circ}C$ (MCSf) to remove Mn(II) in synthetic wastewater. Manganese coated media prepared at different pH was applied in the treatment of soluble Mn(II) in batch and column experiments at various Mn(II) concentrations. The amount of Mn coated on three different media was approximately 800~1100 mg/kg. From the stability test, negligible dissolution of Mn was observed above pH 3.0. In batch test, more than 40% of Mn(II) was removed by all sand media at various manganese concentrations. In order to see the effect of additional oxidant for the removal of Mn(II), 4 mg/L of hypochlorite was added in Mn(II) solution during column experiment. Breakthrough of Mn(II) was greatly retarded in the presence of hypochlorite in all column reactors packed with different media. Among the manganese coated media, MCSf prepared at pH 4 indicated the highest removal capacity. The removal efficiency of Mn(II) was also increased in the multi-layer system (0.5 g of MCS, MCSe, and MCSf each).

• 한국환경과학회지
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• 제9권3호
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• pp.261-266
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• 2000

A kinetic study for nitrate removal by anion exchange resin was performed using continuous column reactors. Kinetic approach from the packed bed showed the reaction rate constant k$_1$ was 0.07~0.17 $\ell$/mgㆍhr and maximum exchange quantity q$_{o}$ was 27.75~31.81 mg/g. The results from the continuous column well agreed with that from the batch reactor. An economic analysis of the water treatment plant by anion exchange resin with a regenerating system was performed to design plant and process. Based on the treatment of 20 mg/$\ell$ nitrate-contained wastewater of 10,000 gallons per day to 2 mg/$\ell$, total capital cost and total annual cost are estimated to be 836 million wons and 211 million wons, respectively.y.

• 한국지하수토양환경학회:학술대회논문집
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• 한국지하수토양환경학회 2006년도 총회 및 춘계학술발표회
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• pp.20-28
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• 2006

Partitioning tracer tests were conducted to quantify the saturation degree of diesel and water in unsaturated soil, respectively. The use of partitioning tracers that partition into diesel, water, and air (i.e., three-phase partitioning), is in attractive alternative to traditional coring and analysis method. These gaseous partition tracers not global warming gas like CFC's are Butane, Acetylene, Ethylene, Methylene chloride, and Methane. The glass column packed with sandy soil was prepared, in which a three-phase system of air, water, and diesel was maintained. Conservative and partition gas tracers were injected into the columns and detected easily using a single GC detector(FID). For each tracer, a method of moments was used to estimate partition coefficient between water, diesel. and the air, respectively. The results from the column studies showed that the diesel/air tracer partition coefficient ranged from 8.2 to 868 and 9.2 for water/air. Saturation degree of diesel and water in the column, predicted by the partition coefficients obtained from tests, was underestimated up to 66% and 23% respectively.

• Biotechnology and Bioprocess Engineering:BBE
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• 제6권6호
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• pp.376-385
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• 2001

Considerable attention has been focused in recent years upon the field of biosorption for the removal of metal ions from aqeous effluents. Compared to other technologies, the advan-tages of biosortption are the high purity of the treated waste water and the cheap raw material. Really, the first major challenge for the biosorption field is to select the most promising types of biomass. Abundant biomass types either generated as a waste by-product of large-scale industrial fermentations particularly fungi or certain metal-binding seaweeds have gained importance in re-cent years due to their natural occurrence, low cost and, of course good performance in metal biosorption. Industrial solutions commonly contain multimetal systems or several organic and in organic substances that form complexes with metals at relatively high stability forming a very complex environment. When several components are present, interference and competition phe-nomena for sorption sites occur and lead to a more complex mathematical formulation of the process. The most optimal configuration for continuous flow-biosorption seems to the packed-bed column which gets gradually from the feed to the solution exit end. Owing to the com-petitive ion exchange taking place in the column, one or more of the metals present even at trace levels may overshot the acceptable limit in the column effluent before the breakthrough point of the trargeted metal. Occurrence of 'overshoot's and impact on havey metal removal has not been analyzed enough. New trends in biosorption are discussed in this review.

• Nuclear Engineering and Technology
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• 제55권12호
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• pp.4395-4407
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• 2023

Bubble columns are widely encountered in several industries, especially in the field of nuclear safety. The Eulerian-Eulerian and the Eulerian-Lagrangian methods are commonly used to investigate bubble columns. Eulerian approaches require additional tasks such as strict volume conservation at the interface and a predefined well-structured grid. In contrast, the Lagrangian approach can be easily implemented. Hence, we introduce a fully Lagrangian approach for the simulation of bubble columns using the discrete bubble model (DBM) and moving particle semi-implicit (MPS) methods. Additionally, we propose a rigorous method to estimate the volume fraction accurately, and verified it through experimental data and analytical results. The MPS method was compared with the experimental data of Dambreak. The DBM was verified by analyzing the terminal velocity of a single bubble for each bubble size. It agreed with the analytical results for each of the four drag correlations. Additionally, the improved method for calculating the volume fraction showed agreement with the Ergun equation for the pressure drop in a packed bed. The implemented MPS-DBM was used to simulate the bubble column, and the results were compared with the experimental results. We demonstrated that the MPS-DBM was in quantitative agreement with the experimental data.

• Biotechnology and Bioprocess Engineering:BBE
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• 제5권3호
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• pp.174-180
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• 2000

Cyclodextrin glucanotransferase (CGTasa) from Thermoanaerobacter sp. was adsorbed on the ion exchange resin Amberlite IRA-900. The optimum conditions for the immobilization of the CGTase were pH6.0 and 600 U CGTase/g resin, and the maximum yield of immobilization was around 63% on the basis of amount ratio of the adsorbed enzyme to intial amount in the solution. Immobilixation of CGTase shifted the optimum temperature for the enzyme to peoduce transglycosylated xylitol from 7$0^{\circ}C$ to 9$0^{\circ}C$ and improved the thermal stability of immobilized CGTase, especially after the addition of soluble starch and calcium ions. Transglycosylated xylitol was continuoncly produced using immobilized CGTase in the column type packed bed reactor, and the operating conditions for maximum yield were 10%(w/v) dextrin (13 of the dextrose equivalent) as the glycosyl donor, 10%(w/v) dextrin (13 of the dextrose equivalent) as the glycosyl donor, 10%(w/v) xylitor as the glycosyl acceptor, 20mL/h of medium fiow rate, and 6$0^{\circ}C$. The maximum yield of transglycosylated xylitol and productivity were 25% and 7.82 g.L-1.h-1, respectively. The half-life of the immobilized CGTase in a column type packed bed reactor was longer than 30 days.

• 공업화학
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• 제9권4호
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• pp.475-480
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• 1998

본 연구에서는 고밀집 glassy carbon (GC) 섬유 다발체 전극 전해계를 사용하여 우라늄 (VI)를 함유한 유기상과 질산 수용상의 혼합상에서 전해 역추출시 우라늄 (VI) 환원 전해특성 연구가 수행되었고, 이에 관한 전해 역추출 모델을 제시하였다 우라늄 (VI) 전해환원 반응은 혼합상 내의 수용상에서 보다 혼합상 내의 유기상에서 빨리 일어났다. 유기상의 유속이 증가하는 경우 역추출 과정에서 유기상 내 우라늄 이온의 확산 저항 증가에 의해서 수용상으로의 역추출은 증가하다 일정하게 되었으며, 수용상 유속 변화는 총 우라늄 (VI) 환원전류에는 영향을 주지 않았다. 전해반응이 없는 경우보다 전해 반응이 동반되는 경우 우라늄 역추출이 보다 효과적으로 이루어 짐을 알 수 있었다.

• 청정기술
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• 제20권2호
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• pp.166-170
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• 2014

강산성 양이온 교환수지를 충전한 고정층 컬럼을 사용하여 수중의 리튬이온을 제거하는 연속식 실험을 수행하였다. 층 높이, 유입 유량 및 유입 농도와 같은 파라미터들을 살펴보았으며, 파과곡선으로부터 파과시간($t_{0.05}$), 포화시간($t_{0.95}$) 및 제거된 리튬이온의 총량(mtotal)을 구하였다. 실험 결과 $t_{0.05}$와 $t_{0.95}$는 층 높이가 감소함에 따라 감소하였고, 유입 농도와 유입 유량이 증가함에 따라 감소하였다. mtotal은 유입 유량과 층 높이가 증가함에 따라 증가하였지만, 유입 유량이 증가함에 따라서는 감소하였다. 실험자료를 토마스 모델식과 윤-넬슨 모델식을 적용한 결과, 토마스 모델식이 파과 데이터에 잘 부합하였다.