• 청정기술
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• 제10권3호
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• pp.159-168
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• 2004

벤젠에 대한 흡착실험이 활성탄과 제올라이트 13X 흡착제에 대하여 수행되었다. 단일 흡착탑과 두 흡착제로 충진된 이중 흡착탑에서 동적흡착특성이 조사되었다. 원료의 유량은 파과시간에 큰 영향을 주지 않았다. 활성탄에 대한 벤젠의 비흡착량이 제올라이트 13X보다 큰 반면, 제올라이트 13X의 밀도가 더 크게 때문에 흡착탑 부피당 흡착량은 제올라이트 13X가 더 컸다. 이중흡착제로 충진된 흡착탑에 대한 동적실험에서 물질전달영역의 길이가 원료의 흐름방향에 따라 달라졌다. 원료 주입구에 활성탄이 충진되고 탑의 출구에 제올라이트 13X가 충진될 때 파과시간은 더 길고 파과곡선은 더 날카롭게 얻어졌다. 또한 두 흡착제의 충진비율에 따라서 파과시간과 파과곡선의 기울기가 영향을 받았다.

• 한국습지학회지
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• 제15권2호
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• pp.265-269
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• 2013

본 연구는 아질산성 질소의 간이분석을 위한 기초 연구로 수행되었다. 수중 질소는 부영양화를 유발하는 암모니아, 아질산 및 질산으로 주로 구성되어 있다. 질소화합물을 제거하기 위한 많은 연구들이 진행되었고, 이에 따른 분석기술도 발달했다. 현장 모니터링을 위한 간이 분석방법의 개발은 수질관리를 위해 필요하므로, 본 연구는 아질산성 질소의 현장 분석법 개발을 위해 진행되었다. BCDMA와 바이페닐로 코팅된 PVC 흡착 칼럼을 이용한 아질산성 질소 분석의 기초 연구를 수행하였다. 흡착칼럼내의 흡착제는 4~20 $mgNO_2-N/L$ 범위내에서 발색길이를 나타내었고, 흡광도는 pH의 영향을 받는 것으로 나타났다.

• Biotechnology and Bioprocess Engineering:BBE
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• 제10권6호
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• pp.552-555
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• 2005

The influence of whole yeast cells $(0{\sim}15%\;w/v)$ on the protein adsorption performance in dye-ligand chromatography was explored. The adsorption of a model protein, bovine serum albumin (BSA), was selected to demonstrate this approach. The UpFront adsorbent $(p=1.5\;g/cm^3)$ derivatised with Cibacron Blue 3GA and a commercially available expanded bed column (20 mm i.d.) from UpFront Chromatography, Denmark, were employed in the batch binding and expanded bed operation. The BSA binding capacity was demonstrated to not be adversely affected by the presence of yeast cells. The dynamic binding capacity of BSA at a $C/C_0=0.1$ biomass concentration of 5, 10, 15% w/v were 9, 8, and 7.5mg/mL of settled adsorbent, respectively.

• 한국응용과학기술학회지
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• 제31권3호
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• pp.394-401
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• 2014

In order to minimize a building energy consumption with ventilation, a development of smart ventilation system is very important. In this study, a dry adsorbent that is main element of smart ventilation system was developed for removing indoor $CO_2$, and evaluate the adsorption performance. Specific surface area, pore characteristic and crystal structure of the modified sorbent was measured to analyze physical properties. From this analysis, it was found that the developed absorbent has a low specific surface area, due to mesopores of substrate was filled with metal contained raw material. Additionally, through analysis of the adsorption properties, the developed adsorbent was shown a adsorption form of mesopore (type IV), which means adsorption amount was rapidly increased at the part of high-pressure. Order to applying for the field, chamber test was performed. Continuous column tests (2,500 ppm) and batch chamber tests ($4m^3$, 5,000 ppm) showed $CO_2$ removal efficiency of 95% and 88% within 1 hour, respectively.

• Environmental Engineering Research
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• 제11권1호
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• pp.1-13
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• 2006

In this study, conventional biofilters packed with flexible synthetic polyurethane (PU) foam carriers were operated to remove toluene from a contaminated air stream. PU foams containing various adsorbents (e.g., zeolite, sepiolite, dolomite and barite) were synthesized for the biofilter media and their adsorption characteristics of toluene were determined. Adsorption capacity of PU-adsorbent foam was in the order of PU-dolomite ${\approx}$ PU-zeolite > PU-sepiolite > PU-barite. During the biofiltration experiment, influent toluene concentration was in the range of 0-160 ppm and EBRT (i.e., empty bed residence time) was 45 seconds. Pressure drop of the biofilter bed was 4-5 mm $H_2O/m$ column height. The maximum removal capacity was in the order of PU-dolomite > PU-zeolite > PU-sepiolite > PU-barite, while the complete removal capacity was in the order of PU-dolomite > PU-sepiolite > PU-zeolite > PU-barite. The better biofiltration performance in PU-dolomite foam was because PU-dolomite foam had lower density and higher porosity than the others providing favorable conditions for microbial growth. The results of biodegradation kinetic analysis showed that PU-dolomite foam had higher maximum removal rate ($V_m\;=\;11.04\;g$ toluene/kg dry material/day) and saturation constant ($K_s\;=\;26.57\;ppm$) than the other PU foams. This supports that PU-dolomite foam was better than the others for biofilteration of toluene.

• 생명과학회지
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• 제13권3호
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• pp.365-373
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• 2003

어유의 탈취장치 대신 컬럼에 활성탄, 활성 알루미나, 실리카겔, 대나무 숯 등 흡착제를 단독 혹은 적당한 비율로 혼합하여 충진시켜 탈색과 동시에 탈취시킴으로서 효율적인 탈취효과를 검토하였다. 대멸치유의 탈검효과는 수산 30%를 어유 100 ml에 대하여 18 ml첨가한 것이, 탈산은 수산화 나트륨을 2.5%로 하여 $40^{\circ}C$에서 30분간 처리한 것이 효과적이었다. 탈취의 경우 흡착제(활성탄, 활성알루미나, 실리카겔)를 농도별로 단독 첨가할 경우는 실리카겔30% 첨가가, 그리고 흡착제를 혼합하여 첨가할 경우는 활성알루미나 30%와 실리카겔 10% 혼합 첨가가 가장 우수하였으나 흡착제에 녹차분말 2%를 첨가할 경우 큰 효과가 없었다. 대멸치유의 탈검, 탈산 및 탈취 후의 주요지방산 조성은 16:0, 20:5n-3, 18:1n, 16:1n-7, 22:6n-3 및 18:0이었다. 대멸치 정제유에 $\alpha$-tocopherol를 첨가하여 $25^{\circ}C$에서 40일간 저장시 산화 안정성은 대조구는 20일까지 항산화제를 첨가한 경우는 30일까지라 생각되며 $\alpha$-tocopherol 0.02%첨가보다 0.01% 첨가가 더 효과적이었다.

• 한국환경농학회지
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• 제6권2호
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• pp.46-52
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• 1987

폐수중(廢水中) 중금속(重金屬)의 제거제(除去劑)로서 천연(天然) Zeolite의 이용(利用) 가능성(可能性)을 조사(調査)하기 위하여 활성탄(活性炭)을 대조(對照)로 하여 흡착실험(吸着實驗) 및 Column 투과실험(透過實驗)을 한 결과(結果)는 다음과 같았다. Freundlich 흡착상수(吸着常數) ${\frac{1}{n}$값이 $0.12{\sim}0.45$, K값 $18.77{\sim}59.48$인 것으로 보아 천연(天然) Zeolite는 활성탄(活性炭)보다 더 효과적(效果的)인 중금속(重金屬) 흡착제(吸着劑)였다. 동일(同一)한 입경(粒徑), 동일(同一)한 투과정도(透過程度)에 있어서 천연(天然) Zeolite는 활성탄(活性炭)보다 더 많은 양(量)의 중금속(重金屬)을 흡착(吸着)하였다. 입자(粒子)가 작을수록 흡착량(吸着量)은 증가(增加)하는 경향(傾向)이었으며 폐수중(廢水中) 중금속(重金屬) 흡착제吸(着劑)로서의 최적입경(最適粒徑)은 $0.5{\sim}2.0mm$ 화분(畵分)이었다. 중김속용액(重金屬溶液)의 Column 투과속도(透過速度)가 느릴수록 또 혼합용액(混合溶液)에서 보다 단일용액(單一溶液)에서 더 많은 량(量)의 중금속(重金屬)이 흡착(吸着)되었다. 혼합용액내(混合溶液內)에서 중금속(重金屬)의 흡착량(吸着量)은 Cu>Zn>Cd의 순(順)이었다.

• Environmental Engineering Research
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• 제19권2호
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• pp.157-163
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• 2014

The adsorption of Cr(VI) from aqueous solutions to activated carbon fiber (ACF) was investigated using both batch and flow-through column experiments. The batch experiments (adsorbent dose, 10 g/L; initial Cr(VI) concentration, 5-500 mg/L) showed that the maximum adsorption capacity of Cr(VI) to ACF was determined to 20.54 mg/g. The adsorption of Cr(VI) to ACF was sensitive to solution pH, decreasing from 9.09 to 0.66 mg/g with increasing pH from 2.6 to 9.9; the adsorption capacity was the highest at the highly acidic solution pHs. Kinetic model analysis showed that the Elovich model was the most suitable for describing the kinetic data among three (pseudo-first-order, pseudo-second-order, and Elovich) models. From the nonlinear regression analysis, the Elovich model parameter values were determined to be ${\alpha}$ = 162.65 mg/g/h and ${\beta}$ = 2.10 g/mg. Equilibrium isotherm model analysis demonstrated that among three (Langmuir, Freundlich, Redlich-Peterson) models, both Freundlich and Redlich-Peterson models were suitable for describing the equilibrium data. In the model analysis, the Redlich-Peterson model fit was superimposed on the Freundlich fit. The Freundlich model parameter values were determined to be $K_F$ = 0.52 L/g and 1/n = 0.56. The flow-through column experiments showed that the adsorption capacities of ACF in the given experimental conditions (column length, 10 cm; inner diameter, 1.5 cm; flow rate, 0.5 and 1.0 mL/min; influent Cr(VI) concentration, 10 mg/L) were in the range of 2.35-4.20 mg/g. This study demonstrated that activated carbon fiber was effective for the removal of Cr(VI) from aqueous solutions.

• Biotechnology and Bioprocess Engineering:BBE
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• 제10권3호
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• pp.280-283
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• 2005

The adsorption of a model protein bovine serum albumin (BSA) in expanded bed chromatography was undertaken by exploiting a commercially available expanded bed column (20 mm i.d.) from UpFront Chromatography and Streamline DEAE $(\rho=1.2g/cm^3)$ from Amersham Pharmacia Biotechnology. The influence of whole yeast cells on the adsorption capacity of column was explored by employing yeast cells in a concentration ranged of 0 to $15\%(w/v)$. Equilibrium isotherms for adsorption of BSA on Streamline DEAE were correlated by using Langmuir equation. The presence of yeast cells resulted in decreased of BSA binding capacity in both batch binding and expanded bed chromatography. Results indicated that the yeast cells act as competitor for proteins to bind to the sites on adsorbents.

• Environmental Engineering Research
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• 제14권3호
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• pp.153-157
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• 2009

Arsenic at abandoned mine sites has adversely affected human health in Korea. In this study, the feasibility of using cationic surfactant-modified activated carbon (MAC) to remove As(V) was evaluated in terms of adsorption kinetics, adsorption isotherms, and column experiments. The adsorption of As(V) onto MAC was satisfactorily simulated by the pseudo-second-order kinetics model and Langmuir isotherm model. In column experiments, the breakthrough point of AC was 28 bed volumes (BV), while that of MAC increased to 300 BV. The modification of AC using cationic surfactant increased the sorption rate and sorption capacity with regard to As(V). As a result, MAC is a promising adsorbent for treating As(V) in aqueous streams.