• 한국환경과학회지
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• 제7권6호
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• pp.773-782
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• 1998

The adsorption experiment of phenol(Ph) from aqueous solution on granular activated carbon was studied in order to design the fixed-bed adsorption column. The experimental data were analyzed by unsteady-state, one-dimensional heterogeneous model. Finite element method(FEM) was applied to analyze the sensitivity of parameter and to predict the fixed-bed adsorption column performance on operation variable changes. The prediction model showed similar effect to mass transfer and intraparticle diffusion coefficient changes suggesting that both parameter present mass transfer rate limits for GAC-phenol system. The Freundlich constants had a greater effect than kinetic parameters for the performance of fixed-bed adsorption column. FEM solution facilitated prediction of concentration history in solution and within adsorbent particle.

• 한국환경농학회지
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• 제16권2호
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• pp.115-118
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• 1997

When the light metals such as $Ca^{++}$ and $Mg^{++}$ were added to heavy metal solution, the adsorption of heavy metals was increased by 20 to 30% more, but there were no differences between species. $Pb^{++}$ was the most adsorbed metal(99.5%), and the adsorption ratio of $Cd^{++}$ was significantly improved. In addition, when the light metal concentration was increased to 100ppm, the adsoption ratios of all four heavy metals were reached to 92 to 99%, while coniferous barks showed only 85 to 92%. On the mixture of four heavy metals, the adsorbed amount of each metal was significantly reduced, compared with that of one heavy metal, while $Zn^{++}$ showed the adsorption improvement to 95%. On the column experiment, $Pb^{++}$ was almost completely adsorbed in the upper part of column, and the adsorbed amount of $Cu^{++}$ was gradually decreased depending on column depth. However, $Cd^{++}$ and $Zn^{++}$ were not influenced by column height, and constantly adsorbed on various column height. Based on the above results, each heavy metal had different adsorption mechanism.

• Journal of Microbiology and Biotechnology
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• 제17권9호
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• pp.1527-1532
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• 2007

Lysine produced during microbial fermentation is usually recovered by an ion-exchange process, in which lysine is first converted to the cationic form (by lowering the pH to less than 2.0 with sulfuric acid) and then fed to a cationexchange column containing an exchanger that has a sulfone group with a weak counterion such as NH;. Ammonia water with a pH above 11 is then supplied to the column to displace the purified lysine from the column and allow its recovery. To enhance the adsorption capacity and for a possible reduction in chemical consumption, monovalent lysine fed at pH 4 was investigated in comparison with conventional divalent lysine fed at pH 1.5. The adsorption capacity increased by more than 70% on a mass basis using pH 4 feeding compared with pH 1.5 feeding. Lysine adsorbed at pH 4 started to elute earlier than that adsorbed at pH 1.5 when ammonia water was used as the eluant solution, and the extent of early elution became more notable at lower concentrations of ammonia. Moreover, the elution of monovalent lysine fed at pH 4 displayed a stiffer front boundary and higher peak concentration. However, when the ammonium concentration was greater than 2.0 N, complete saturation of the bed was delayed during adsorption and the percent recovery yield from elution was lowered., both drawbacks that were considered inevitable features originating from the increased adsorption of monovalent lysine.

• 한국물환경학회지
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• 제23권3호
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• pp.314-318
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• 2007

The feasibility of the employment of waste oyster shell as an adsorbent for fluoride ion has been tested by considering the effect ionic condition on the adsorption of fluoride ion on oyster shell. The adsorption capacity of oyster shell for fluoride ion was found not to be significantly influenced by the ionic strength of aqueous environment. The existence of complexing agent such as nitrilotriacetic acid in wastewater decreased the adsorbed amount of fluoride ion by forming a stable complex of $CaT^-$ and the adsorption reaction of fluoride ion on oyster shell was examined to be endothermic. The coexisting heavy metal ionic adsorbate in wastewater hindered the adsorption of fluoride ion, however, its adsorbed amount was increased as the particulate size of adsorbent was decreased. Finally, a serial adsorption column test has been conducted for a practical application of adsorption process and the breakthrough of the column adsorption was observed in 22 hours under the experimental condition.

• 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.

• 한국지하수토양환경학회지:지하수토양환경
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• 제13권1호
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• pp.52-59
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• 2008

흡착은 비소가 토양에 축적되는 주요 과정이다. 그러므로 토양에서 비소종의 흡착 및 탈착 특성을 이해하는 것은 비소종의 거동을 예측하고 토양으로부터 비소를 제거하는 적절한 정화방법을 수립하기 위해 필수적이다. 본 연구에서는 칼럼을 이용하여 토양에서 As(III)와 As(V)의 흡착 및 탈착실험을 수행하였다. As(III)에 대한 실험은 환원환경에서, 그리고 As(V)에 대한 실험은 산화환경에서 실시했다. 실험이 진행되는 동안 대부분의 As(III)는 그 산화상태를 유지하였다. As(III)의 흡착 및 탈착속도는 As(V)보다 빨랐다. 칼럼실험에서 비소종의 흡착 및 탈착반응은 완전히 가역적은 아니었다. 또한 As(V)는 회분식실험에서보다 칼럼실험에서 더 빠르게 토양에 흡착되었다.

• 자원리싸이클링
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• 제15권3호
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• pp.66-73
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• 2006

망간단괴 제련 과정에서 니켈 이온의 회수량을 높임과 동시에 니켈 폐수를 제거하기 위한 기초 연구를 수행하기 위해 인공니켈 폐수와 실폐수에 대해 흡착제로 망간단괴를 사용하여 고정층 연속 흡착 실험을 하였다. 인공니켈폐수에 대한 고정층 흡착 칼럼의 충전층 높이, 유입수의 유량, 그리고 유입되는 니켈폐수의 농도를 변화시키면서 흡착 특성의 변화양방을 검토하였다. 흡착실험의 결과를 Bohart-Adams식에 적용하여 고정층 칼럼에서의 흡착량 및 흡착속도상수를 계산하여 비교하였다. 또한 고정 흡착층 파과곡선으로부터 유입수의 유량과 흡착질의 초기농도의 변화에 따른 각 칼럼의 흡착량의 변화를 검토하였다. 직렬 연결 칼럼들에 대해 초기 칼럼에서 최종 칼럼으로 흡착이 진행됨에 따라 흡착량은 상승하는 것으로 파악되었다. 실폐수를 고정층 칼럼에 유입하여 흡착특성을 살펴 본 결과, 충전층 높이에 따른 흡착양상의 변화가 인공폐수와 달리 뚜렷하게 관찰되지 않았는데 이는 인공폐수에 비해 실폐수 중의 $Ni^{2+}$의 농도가 현저히 높기 때문인 것으로 판단되었다. 실폐수의 흡착율에 미치는 망간단괴 입자크기의 영향에 대한 검토에서는 흡착제 입자가 작아질수록 니켈 이온의 흡착율이 다소 상승하는 것으로 파악되었다.

• 분석과학
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• 제12권3호
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• pp.196-202
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• 1999

갈조류인 Sargassum horneri를 중금속 흡착제로 사용하여 중금속 Cd(II) 및 Pb(II)이온을 제거하였다. Sargassum horneri는 동해안에서 채취하였고, 풍건 건조시켜 40~60 mesh의 입자 크기로 흡착제를 만들어 사용하였다. batch법은 진탕 시간에 따른 흡착량을 측정함으로써 흡착속도를 조사하였고, column법은 해조 분말을 충진 시킨후 일정농도의 중금속용액을 1 mL/min의 속도로 흘려보내면서 흡착시키고 흡착량을 알아 보았다. 중금석 흡착에 미치는 pH의 영향은 batch법과 column법 모두, pH 10.5>7.0>3.5순으로 나타났다. Pb(II)이온이 Cd(II)이온보다 높은 흡착량을 보였다. 특히 batch법에서는 모든 pH의 조건하에서 5분이내에 최대 흡착량에 도달하였다. 회수율은 batch법에 의해 흡착된 중금속의 회수율이 column법에 의해 흡착된 중금속의 회수율 보다 조금 높게 나타났다.

• 한국환경과학회지
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• 제23권6호
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• pp.1143-1149
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• 2014

The adsorption experiments of lithium ions were conducted in the fixed bed column packed with activated carbon modified with nitric acid. Effect of inlet concentration, bed hight and flow rate on the removal of lithium ions was investigated. The experimental results showed that the removal and the adsorption capacity of lithium ions increased with increasing inlet concentration, and decreased with increasing flow rate. When the bed height increased, the removal and the adsorption capacity increased. The breakthrough curves gave a good fit to Bohart-Adams model. Adsorption capacity and breakthrough time calculated from Bohart-Adams model, these results were remarkably consistent with the experimental values. The adsorption capacity was not changed in the case of 3 times repetitive use of adsorbent.

• 한국환경보건학회지
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• 제19권4호
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• pp.25-32
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• 1993

Granular activated carbon is commonly used in fixed-bed adsorbers to remove organic chemicals. In this experiment organic chemical solutions were prepared by adding the reagent grade organic chemical to distilled water. Isotherm adsorption tests of volatile organic chemicals were conducted using bottle-point technique and column test. Organic chemicals after passing through the column were extracted with hexane and analyzed with gas chromatography (Hewlett-Packard 5890) to check the adsorption capacity and breakthrough curve. The result were as follows: 1. The BET surface area of coconut activated carbon was 658~1,010 m$^2$/g where as coconut shell carbon was 6.6 m$^2$/g. Coconut activated carbon increased the BET surface area and adsorption capacity in bottle-point isotherm. 2. The adsorption capacity of coconut activated carbon for trichloroethylene (TCE) was reduced in the presence of humic substance. 3. A decrease in particle size of activated carbon resulted in higher adsorption capacity and lower intraparticle diffusion coefficient. It is reflected not only as a decrease in Freudlich adsorption capacity value (K) but also as an increase in Freudlich exponenent value (1/n).