• 대한토목학회논문집
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• 제3권2호
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• pp.87-95
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• 1983

본(本) 연구(硏究)에서는 정수처리과정(淨水處理過程)에서 생성(生成)되는 trihalomethane을 제거(除去)하는 방법(方法)으로 활성탄(活性炭)으로 충전(充塡)된 고정층(固定層)에 의한 흡착(吸着)에 관하여 이론적(理論的)인 간단한 모형(模型)을 제시하고 모형(模型)의 simulation을 통하여 얻은 결과(結果)와 고정층(固定層) 흡착실험(吸着實驗)을 통해서 얻은 결과(結果)를 비교(比較), 분석(分析)하였다. 고정층흡착모형(固定層吸着模型)의 simulation 결과(結果)로 흡착효과(吸着効果)에 큰 영향을 미치는 인자(因子)인 물질전달계수(物質傳達係數) K와 Freundlich의 흡착계수(吸着係數)인 $K_F$와 n의 변화(變化)에 따른 전체적인 효율변화(効率變化)를 산정(算定)하였다. 처리효율(處理効率)은 K와 $K_F$가 증가할수록 그리고 n이 감소할수록 유리(有利)한 것으로 나타났다. 실험결과(實驗結果)로부터 얻은 breakthrough curve는 전형적(典型的)인 S자형(字形)으로 나타났으며 break point를 $100{\mu}g/l$로 정할 경우 활성탄(活性炭) 단위무게당(當) 흡착량(吸着量)은 6.3mg/g으로 등온흡착실험(等溫吸着實驗)에서 얻은 결과(結果)보다 훨씬 높았다. 또한 $5^{\circ}C$정도(程度)의 수온차이(水溫差異)는 처리효율(處理効率)에 뚜렷한 영향을 끼치지 못했다. 고정층운전결과(固定層運轉結果)와 잘 부합되는 simulation으로부터 얻은 $K_F$와 n은 등온흡착실험(等溫吸着實驗)에서 얻은 값과 약간의 차이를 나타냈다.

• 방사성폐기물학회지
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• 제1권1호
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• pp.81-92
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• 2003

폐기물 용액의 pH 변화에 따른 고정층에서 우라늄 및 코발트 이온의 흡착거동을 다성분 흡착시스템으로 가정하여 이론적으로 예측하였다. 즉 pH 변화에 따라 존재 분율이 달라지는 각 이온 성분들이 상호 경쟁적으로 흡착한다는 가정 하에서, 평형실험에서 얻어진 결과와 우라늄 및 코발트 이온의 용액특성 (Solution chemistry)을 상호 결합하여 각 이온 성분들의 Langmuir 평형상수 값을 Ideal Adsorbed Solution Theory를 도입하여 구하였으며, 이상의 결과를 이용하여 고정층 파과곡선을 이론적으로 계산한 결과 pH 변화에 따른 흡착거동을 비교적 잘 예측할 수 있었다 따라서 본 연구에서 시도한 방법은 이온 농도와 pH가 높은 경우를 제외하고 pH 변화에 따라 용액 내에 이온의 형태가 다양하게 존재하는 흡착 시스템을 이론적으로 예측하는 데 비교적 유용하게 사용할 수 있을 것으로 판단된다.

• Advances in environmental research
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• 제3권3호
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• pp.231-251
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• 2014

The present study examines the phosphate adsorption potential and behavior of mixture of Ground Burnt Patties (GBP), a solid waste generated from cooking fuel used in earthen stoves and Red Soil (RS), a natural substance in fixed bed column mode operation. The characterization of adsorbent was done by Proton Induced X-ray Emission (PIXE), and Proton Induced ${\gamma}$-ray Emission (PIGE) methods. The FTIR spectroscopy of spent adsorbent reveals the presence of absorbance peak at $1127cm^{-1}$ which appears due to P = O stretching, thus confirming phosphate adsorption. The effects of bed height (10, 15 and 20 cm), flow rate (2.5, 5 and 7.5 mL/min) and initial phosphate concentration (5 and 15 mg/L) on breakthrough curves were explored. Both the breakthrough and exhaustion time increased with increase in bed depth, decrease in flow rate and influent concentration. Thomas model, Yoon-Nelson model and Modified Dose Response model were used to fit the column adsorption data using nonlinear regression analysis while Bed Depth Service Time model followed linear regression analysis under different experimental condition to evaluate model parameters that are useful in scale up of the process. The values of correlation coefficient ($R^2$) and the Sum of Square Error (SSE) revealed the Modified Dose Response model as the best fitted model to the experimental data. The adsorbent mixture responded effectively to the desorption and reusability experiment. The results of this finding advocated that mixture of GBP and RS can be used as a low cost, highly efficient adsorbent for phosphate removal from aqueous solution.

• 한국대기환경학회지
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• 제15권2호
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• pp.191-199
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• 1999

This study evaluated the availability as an alternative adsorbent which is cheaper and more efficient than CuO/${\gamma}$-$Al_2O_3$ which have been studing vigorously to remove $SO_2$. Five adsorbents (CuO/${\gamma}$-$Al_2O_3$, Iron ore, Slag, LD slag, $Fe_2O_3$) was employed in a fixed bed reactor. $SO_2$ breakthrough curves were obtained as a function of temperature, initial gas velocity and particle size. Saturation capacities calculated by the numerical integration of breakthrough curves of $SO_2$ increased with increasing reaction temperature. $SO_2$ breakthrough curve equation of $Fe_2O_3$ for this system can be expressed as Kr=3,914,000 exp(-37,329.86/RT). By means of the breakthrough curve, the influence of bed height on breakthrough time was also estimated.

• 한국안전학회지
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• 제12권3호
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• pp.97-105
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• 1997

Mo-99(Molybdenum) is the only source of Tc-99m(Technetium) which is most frequently used in nuclear medical diagnostics and the demand is on the increase recently. Separation and refining of Mo-99 was investigated by adsorption and desorption on alumina. At pH=0.63, adsorption isotherm of Mo was fitted by Redlich ＆ Peterson equation using the adsorption experimental data. It was found that the pore diffusion model ($D_p=1.4{\times}10^{-6}cm^2/s, K_f/=0.4 cm/s$) agreed well with batch adsorption experimental data. RTDs(Residence Time Distributions ) were measured and axial dispersion coefficients were obtained in the fixed bed absorber according to the changes of the flow rate using 0.05% -NaCl. From the adsorption experimental data, it was shown that the behavior of breakthroughs depended on flow rate. Mo recovery yield was increased as adsorption flow rate was increased and desorption flow rate was decreased.

• 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).

• 한국가스학회:학술대회논문집
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• 한국가스학회 2005년도 춘계학술대회 및 특별심포지움
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• pp.206-206
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• 2005

• 한국가스학회:학술대회논문집
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• 한국가스학회 2003년도 춘계학술발표회 논문집
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• pp.219-223
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• 2003

• 한국원자력학회:학술대회논문집
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• 한국원자력학회 1996년도 춘계학술발표회논문집(3)
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• pp.409-414
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• 1996

Radionuclides such as Cs and Sr were removed from dilute aqueous solutions by means of inorganic adsorbents, 13X and chabazite. The physical adsorption obeyed the DA equation and non-equilibrium dynamic adsorption model, which describes surface diffusion mechanism with the DA equation, simulated the adsorption behavior of cesium and strontium on zeolite in fixed bed adsorbers. The dynamic model simulated the adsorption behavior of cesium and strontium.

• Carbon letters
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• 제2권1호
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• pp.9-14
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• 2001

Adsorption and desorption characteristics of methyl iodide at high temperature conditions up to $250^{\circ}C$ by TEDA-impregnated activated carbon, which is used for radioiodine retention in nuclear facility, was experimentally evaluated. In the range of temperature from $30^{\circ}C$ to $250^{\circ}C$, the adsorption capacity of base activated carbon decreased sharply with increasing temperature but that of TEDA-impregnated activated carbon showed higher value even at high temperature ranges. Especially, the desorption amount of methyl iodide on TEDA-impregnated carbon represented lower value than that on unimpregnated carbon. The breakthrough curves of methyl iodide in the fixed bed packed with base carbon and TEDA-impregnated activated carbon at high temperature were compared. TEDA-impregnated activated carbon would be applicable to adsorption process up to $150^{\circ}C$ for the removal of radioiodine in a nuclear facility.