• 상하수도학회지
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• 제29권5호
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• pp.565-573
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• 2015

The influencing factors to remove phosphate were evaluated by converter slag (CS). Experiments were performed by batch tests using different CS sizes and column test. Solutions were prepared at the different pH and concentrations. The maximum removal efficiency was obtained over 98% with the finest particle size, $CS_a$ within 2 hours in batch tests. The removal efficiency was increased in the order of decreasing size with same amount of CS for any pH of solutions. The adsorption data were well fitted to Freundlich isotherm. From the column experiment, the specific factors were revealed that the breakthrough removal capacity (BRC) $x_b/m_{cs}$, was decreased by increasing the influent concentration. The breakthrough time, tb was lasted shorter as increasing the influent concentration. The pH drop simultaneously led to lower BRC drop during the experimental hours. The relation between the breakthrough time and the BRC to influent concentration was shown in the logarithmic decrease. Results suggested that the large surface area of CS possessed a great potential for adsorptive phosphate removal. Consequently particle size and initial concentration played the major influencing factors in phosphate removal by converter slag.

• 상하수도학회지
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• 제28권4호
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• pp.453-459
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• 2014

The excessive concentration of phosphorus in the river and reservoir is a deteriorating factor for the eutrophication. The converter slag was used to remove the phosphate from the synthetic wastewater. Influencing factors were studied to remove soluble orthophosphate with the different particle sizes through the batch and the column experiments by continuous flow. Freundlich and Langmuir adsorption isotherm constants were obtained from batch experiments with $PS_A$ and $PS_B$. Freundlich isotherm was fitted better than Langmuir isotherm. Regression coefficient of Freundlich isotherm was 0.95 for $PS_A$ and 0.92 for $PS_B$, respectively. The adsorption kinetics from the batch experiment were revealed that bigger size of convert slag, $PS_A$ can be applied for the higher than 3.5 mg/L of phosphate concentration. The pilot plant of continuous flow was applied in order to evaluate the pH variation, breakthrough points and breakthrough adsorption capacity of phosphate. The variation of pH was decreased through the experimental hours. The breakthrough time was 1,432 and 312 hours to 10 mg/L and 50 mg/L for the influent concentration, respectively. The breakthrough adsorption capacity was 3.54 g/kg for 10 mg/L, and 1.72 g/kg for 50 mg/L as influent phosphate concentration.

• 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.

• 대한환경공학회지
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• 제22권7호
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• pp.1193-1203
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• 2000

본 연구는 흡착에 의한 Cd(II)의 제거를 위하여 일본 Diaion사에서 제조되고 있는 강산성양이온 교환수지(SK1B)를 흡착제로 사용하여 흡착평형실험, 탈착실험 및 흡착속도실험을 수행하였다. 흡착평형실험에서는 흡착능에 미치는 pH와 온도의 영향을 알아보았고 흡착등온식을 산출하였으며, 탈착실험에서는 재생회수에 대한 수지의 재생율의 변화에 대해서 알아보았다. 흡착속도실험에서는 수지를 미분층 반응기에 채워 유량별로 초기제거속도를 구하여 경막저항이 최소가 되는 최적유량을 구하였으며, 이 최적유량에서 흡착속도실험을 수행하여 총괄흡착속도식을 구하였다. 용액의 pH를 변화(2~7)시켜 제조하여 수지를 투여한 결과 pH가 증가할수록 흡착능이 증가하였으며 pH 6 이상에서는 흡착능이 일정한 경향을 나타내었다. 흡착능에 미치는 온도의 영향은 $10{\sim}50^{\circ}C$ 범위에서 온도가 증가할수록 흡착능도 증가함을 알 수 있었다. 회분식실험을 통해 얻은 자료를 각 흡착등온식에 적용해 본 결과 본 실험의 농도 영역(5~15ppm)에서는 Freundlich 흡착등온식과 Sips 흡착등온식이 Langmuir 흡착등온식보다 더 %편차가 적었다. 탈착제로서 0.01~2N 농도의 HCl 수용액을 사용할 경우에는 탈착제의 농도가 진할수록 흡착제의 재생율이 높았으며 재생 반복회수가 늘어날수록 재생율이 약간씩 감소하였다. 미분층 반응기를 이용한 연속공정실험($25{\pm}5^{\circ}C$)에서 경막확산저항이 최소가 되는 최적유량 $564m{\ell}/min$에서 수행한 수지에 대한 Cd(II) 수용액의 총괄흡착속도식은 다음과 같이 표현될 수 있다. $r=1.3785C_{fc}^{1.2421}-2.0907{\times}10^{0.0746C_i}\;q_e^{0.0121C_i-0.0301}$

• 한국대기환경학회지
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• 제23권5호
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• pp.575-584
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• 2007

The adsorption capability of iron phthalocyanine derivatives were investigated by means of X-ray diffractometor (XRD), IR (infrared) spectroscopy, scanning electron microscopy (SEM) and temperature programmed desorption (TPD). According to TPD results, iron phthalocyanine derivatives showed two desorption peaks at low temperature ($100{\sim}150^{\circ}C$) and high temperature ($350{\sim}400^{\circ}C$) indicating that there were two kinds of acidities. Tetracarboxylic iron phthalocyanine (Fe-TCPC) have a stronger desorption peak (chemical adsorption) at the high temperature and a weaker desorption peak (physical adsorption) at the low temperature than iron phthalocyanine (Fe-PC). The specific surface areas of Fe-TCPC and Fe-PC were $26.46\;m^2/g\;and\;11.77\;m^2/g$, respectively. The pore volumes of Fe-TCPC and Fe-PC were $0.14\;cm^3/g\;and\;0.06\;cm^3/g$, respectively. The adsorption capability of triethyl amine calculated by breakthrough curve at 220 ppm of equilibrium concentration was 29.2 mmoL/g for Fe-TCPC and 0.8 mmoL/g for Fe-PC. The removal efficiency of dimethyl sulfide of Fe-TCPC and Fe-PC in batch experiment of 225 ppm of initial concentration were 44.9% and 28.9%, respectively. The removal efficiency of trimethyl amine of Fe-TCPC and Fe-PC in batch experiment of 118 ppm of initial concentration were approximately 100.0% and 33.9%, respectively.

• 동력기계공학회지
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• 제17권1호
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• pp.71-76
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• 2013

This study is experimentally performed for using the oyster shell as a desiccant in the batch type system. The peltier element(thermoelectric device) is used for absorbing and releasing the adsorption and desorption heat generation. The cooling and heating effects of peltier element exist in this experiment and these effects are generally known phenomena among some references. The increase in electric current induced into peltier element is effectively release the heat generation of adsorption and desorption. Consequently, the non-dimensional adsorption and desorption amount would increase with increase in electric current. However, in the case of adsorption, the increase of induced current into peltier element, the heat of cold side can not release sufficiently. So the heat of hot side of peltier is transferred into the cold side.

• 한국인쇄학회지
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• 제6권1호
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• pp.59-66
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• 1988

One of the rising problems in the field of environmental engineering is the eutrophic phenomenon which appears in the closed water basin. This study is the elimination orthophosphate by adsorption, which is indispensible nutritive element for eutrophication Ziriconium(IV) oxide hydrate-activatedcarbon complex. which has excellent adsorptivity for orthophosphate and can easily be reused after desorption process has been made and used as adsorbents. The main purpose of this study is to obtain intraparticle diffusivity which is basic data for the design of adsorption operation the experimental results were as follows. 1. Optimum condition which gave maxinum adsorption of orthophosphate was ph5 2. Equilibrium adsorption showed good consistency with Freundlich type. q=10.80C1/2.08 3. Pore diffusivity and surface diffusivity obtained the kinetic experiment of batch adsorption were respectivity 5.38 and 2.06 ($\textrm{cm}^2$/sec)

• 한국광물학회지
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• 제20권4호
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• pp.327-337
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• 2007

흰색, 노란색, 정제된 노란색 등 3 가지 종류의 영동 일라이트에 대하여 정량 X선 회절분석법에 의하여 광물조성을 구하였으며, 레이저 입도분석기를 이용하여 입자 크기 및 입도 분포를 측정하였다. 영동 일라이트의 인산염 흡착 특성을 규명하기 위하여 배치(batch) 흡착 실험을 실시하였다. 흰색 일라이트는 노란색 일라이트에 비하여 적은 양의 일라이트를 포함하고 있지만, 입자 크기는 더 작다. 정제된 노란색 일라이트는 정제하지 않은 시료에 비하여 월등히 많은 일라이트를 포함하며, 입자 크기도 훨씬 미세하다. 일라이트의 양이 많아짐에 따라 인산염의 흡착률은 대체로 증가하는 경향을 보이는데 반하여, pH가 증가하면 인산염의 흡착량은 감소하는 경향을 나타낸다. 일반적으로 일라이트의 함량이 많고, 입자 크기가 미세할수록 인산염의 흡착량이 증가하지만, 일라이트의 함량이 적은 흰색일라이트가 노란색 일라이트보다 더 많은 인산염을 흡착하는 이유는 작은 입자 크기, 높은 층간 전하, 낮은 사면체 자리의 치환에 기인한 것으로 여겨진다. 흰색 일라이트는 랑미어 흡착등온선, 노란색 일라이트는 프로인드리히 흡착등온선에 더욱 잘 부합하는 경향을 보여주고 있다.

• 한국환경과학회지
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• 제20권12호
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• pp.1607-1615
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• 2011

The adsorption performance of cupper and zinc ions($Cu^{2+}$ and $Zn^{2+}$) in aqueous solution was investigated by an adsorption process on reagent grade Na-A zeolite(Z-WK) and Na-A zeolite (Z-C1) prepared from coal fly ash. Z-C1 was synthesized by a fusion method with coal fly ash from a thermal power plant. Batch adsorption experiment with Z-C1 was employed to study the kinetics and equilibrium parameters such as initial metal ions concentration and adsorption time of the solution on the adsorption process. Adsorption rate of metal ions occurred rapidly and adsorption equilibrium reached at less than 120 minutes. The kinetics data of $Cu^{2+}$ and $Zn^{2+}$ ions were well fitted by a pseudo-second-order kinetics model more than a pseudo-first-order kinetics model. The equilibrium data were well fitted by a Langmuir model and this result showed $Cu^{2+}$ and $Zn^{2+}$ adsorption on Z-C1 would be occupied by a monolayer adsorption. The maximum adsorption capacity($q_{max}$) by the Langmuir model was determined as $Cu^{2+}$ 99.8 mg/g and $Zn^{2+}$ 108.3 mg/g, respectively. It appeared that the synthetic zeolite, Z-C1, has potential application as absorbents in metal ion recovery and mining wastewater.

• 한국환경과학회지
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• 제22권12호
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• pp.1651-1660
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• 2013

The adsorption of lithium ion onto zeolite was investigated depending on contact time, initial concentration, cation forms, pH, and adsorption isotherms by employing batch adsorption experiment. The zeolite was converted into different forms such $K^+$, $Na^+$, $Mg^{2+}$, $Ca^{2+}$, and $Al^{3+}$. The zeolite had the higher adsorption capacity of lithium ion in $K^+$ form followed by $Na^+$, $Ca^{2+}$, $Mg^{2+}$, and $Al^{3+}$ forms, which was in accordance with their elctronegativities. The lithium ion adsorption was explained using the Langmuir, Freundlich, and Dubinin-Radushkevich adsorption isotherms and kinetic models. Adsorption rate of lithium ion by zeolite modified in $K^+$ form was controlled by pseudo-second-order and particle diffusion kinetic models. The maximum adsorption capacity obtained from Langmuir isotherm was 17.0 mg/g for zeolite modified in $K^+$ form. The solution pH influenced significantly the lithium ions adsorption capacity and best results were obtained at pH 5-10.