• 공업화학
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• 제29권1호
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• pp.28-36
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• 2018

폐감귤박으로 제조한 활성탄(WCAC)을 충전한 고정층 반응기에서 아세톤, 벤젠 및 메틸메르캅탄(MM)의 3종류의 대상가스에 대한 흡착특성을 검토하였다. 단일성분계의 경우에 파과곡선으로부터 구한 파과시간은 유입농도 및 유량이 증가할수록 감소하였으나 형상비(L/D)가 증가할수록 증가하였다. WCAC에 의한 대상가스의 흡착량은 유입농도 및 형상비가 증가할수록 증가하였으나 유량증가에 따른 흡착량은 대상가스에 따라 차이를 나타내었다. 파과시간 및 흡착량 결과에 의하면 WCAC에 대한 친화력은 벤젠이 가장 높고, 다음으로 아세톤 그리고 MM의 순서이었다. 한편, 2성분계 및 3성분계 혼합가스의 흡착 경우에 파과곡선은 WCAC와 친화력이 작은 흡착질은 친화력이 큰 흡착질로 치환되면서 roll-up 현상을 보였다. 그리고 WCAC에 의한 아세톤의 흡착은 황화합물인 MM보다 비극성인 벤젠과 혼합되어 있을 경우에 영향을 크게 받는 것으로 나타났다.

• Preventive Nutrition and Food Science
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• 제3권2호
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• pp.123-127
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• 1998

Fixed-bed adsorption was adapted to separate phenolic acids from diluted phenolic solution. Break-through curve was obtained by nonlinear curve fitting method, and breakpoint, saturation time, and mass transfer coeffi-cient were calculated . Break point and saturation time were reached slower with $\rho$-coumaric acid than ferulic acid .The p-coumaric acid, having small molecular weight, is suposedly traveled longer pathway in characoal than ferulic acid. Fixed-bed adsorption iwht gallic acid having more hydroxyl functional group than other phenolic acids showed break point arrival and the largest saturation time. This fact means that there was bigger electrostatic affinity between gallic acid and charcoal than between other phenolic acids and charcoal.

• 분석과학
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• 제6권4호
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• pp.375-381
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• 1993

생체시료 중 ${\beta}$-blockers의 동시분석을 위한 시료 전처리 과정에서 고상추출법을 사용하기 위해 4가지 흡착제의 흡착 및 탈착 효율을 조사하였다. 용출 용매로서 methanol을 사용하였을 때 Chromosorb 107이 가장 높은 회수율을 보였다. ${\beta}$-Blockers의 breakthrough 조사를 하여 Chromosorb 107 컬럼의 우수한 흡착 및 탈착 성질을 혈청 중 2~8 ppm 농도 범위의 ${\beta}$-blockers를 동시에 고상추출하는 데 Chromosorb 107/methanol의 유용성을 조사하였다.

• 한국지하수토양환경학회:학술대회논문집
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• 한국지하수토양환경학회 2003년도 총회 및 춘계학술발표회
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• pp.217-220
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• 2003

In the case of the remediation studies, push pull test is a more time and cost effective mettled than multi-well tracer test. It also gives Just as much or more information than the traditionally used methods. But the data analysis for the hydraulic parameters, there have been some defections such as underestimation of dispersivity, requirement for effective porosity, and calculation of recovery of center of mass to estimate linear velocity. In this research, Weibull distribution function is proposed to estimate the center of mass of breakthrough curve for Push pull test. The hydraulic parameter estimation using Weibull function showed more exact values of center of mass than those of exponential regression for field test data.

• 한국지하수토양환경학회:학술대회논문집
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• 한국지하수토양환경학회 2005년도 총회 및 춘계학술발표회
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• pp.151-154
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• 2005

Laboratory column experiments for simultaneous removal of Cd and Cr(VI) are conducted using newly developed material, referred to as Fe-loaded zeolite, which has both reduction ability of iron and ion exchange ability of zeolite. Breakthrough curves were obtained from each column experiment, and described with advection-dispersion equation. Apparent parameters including $K_{app}\;and\;D_{app}$ were newly introduced for effectively describing the Cr(VI) breakthrough curve. $K_{app}$ decreased with increasing initial contaminant concentration and with decreasing flow rates. Whereas, $D_{app}$ were not significantly affected by initial contaminant concentration or flow rate.

• 한국환경보건학회지
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• 제37권1호
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• pp.50-56
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• 2011

The adsorption capacity of charcoal is a function of the airborne concentration of the target chemical. To evaluate the adsorption capacity of charcoal packed in the cartridges of air purifying respirators, breakthrough tests were conducted with carbon tetrachloride for three commercial cartridges (3M models #7251, #6000 and AX) at 25, 50, 100, 250 and 500 ppm. Adsorption capacities were calculated using a mass transfer balance equation derived from the curve fitting to the breakthrough curves obtained experimentally. Carbon micropore volumes were estimated by iteration to fit the Dubinin/Radushkevich (D/R) adsorption isotherm. They were 0.6566, 0.5727 and 0.3087 g/cc for #7251, #6000 and the AX cartridge, respectively. Above 100 ppm (at high challenge concentrations), #7251 and #6000 showed higher adsorption capacities. However, as the challenge concentration decreased, the adsorption capacities of #7251 and #6000 sharply dropped. On the other hand, the adsorption capacity of the AX cartridge showed little change with the decrease of the challenge concentration. Thus, the AX showed a higher adsorption capacity than #7251 and #6000 at the 5-50 ppm level. It is concluded that service-life tests of cartridges and adsorption capacity tests of charcoal should be conducted at challenge concentration levels reflecting actual working environmental conditions. Alternatively, it is recommended to use the D/R adsorption isotherm to extrapolate adsorption capacity at low concentration levels from the high concentration levels at which breakthrough tests are conducted, at a minimum of two different concentration levels.

• 한국산업보건학회지
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• 제15권1호
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• pp.8-18
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• 2005

Adsorption capacity for the charcoal were tasted in this study to verify the performance of them for the use of the sampling media in industrial hygiene field. Two set of experiments were conducted. The first experiment was to test performance of the tested charcoal tube that were assembled in the laboratory with the use of the GR grade charcoal. The other tests were investigate the adsorption capacity of the charcoal tested in this study and charcoals embedded in the commercial charcoal tubes. Known air concentration samples for benzene, toluene, and o-xylene were prepared by the dynamic chamber. 1. At low air concentration levels (0.1${\times}$TLV), there was no significant differences between the tested charcoal tubes and the SKC charcoal tubes. This implies that there is no defect with the adsorption capacity of the charcoal. 2. At high concentration with 60 minutes sampling, the breakthrough were found only in the tested charcoal while no breakthrough were shown in the SKC charcoal. 3. From the breakthrough tests for the charcoal, the micropore volume(Wo) were calculated by the curve fitting with the use of Dubinin/Radushkevich(D/R) adsorption isotherm equation. The calculated values were 0.687cc/g for SKC, 0.504cc/g for Sensidyne, and 0.419cc/g for the tested charcoal(Aldrich). 4. Adsorption capacities were obtained from the isotherm curves shown adsorption capacities at several levels of the challenge concentration. All range of the air concentration concerned in industrial hygiene, the SKC charcoal showed approximately two times of adsorption capacity compared to the tested charcoal.

• 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.

• 한국토양비료학회지
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• 제39권1호
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• pp.21-28
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• 2006

본 실험은 포화수분상태에서 두개의 서로 다른 토양의 흡착가능장소에 대한 흡착능과 경쟁에 따른 Cd, Pb, 그리고 Cr 이온의 이동성을 조사하였다. 이 조사를 위하여 수용성상태로 단일, 이중, 삼중의 중금속 조합을 이용하였다. 두개의 토양시료는 밭토양의 지표면으로부터 20 cm 이내에서 채취한 토양을 사용하였다. 그리고 공극수량에 따른 출현과 용출곡선을 중금속용액과 치환용 K 이온용액을 가하여 각각의 곡선이 최대와 최소치에 이은 시점까지 조사하였다. 조사 결과 출현과 용출곡선은 대칭을 이루지 않았으며 용액상태로 존재하는 중금속이온의 종류가 증가됨에 따라 용출곡선의 미행이 증가되었을 뿐만 아니라 공극수량도 증가하는 경향을 보였다. 그리고 출현과 용출곡선을 기준하여 곡선의 위와 아래의 면적을 비교하여 본 결과 출현 후 K에 의한 용출면적은 상대적으로 작아 K에 의한 중금속 탈착은 작은 것으로 조사되었는데 이는 중금속이온이 가지는 전기음성도 차이에 기인한 것으로 추정되었다. 결론적으로 토양내에서 중금속이온의 이동은 토양내에서 존재하는 중금속이온의 종류가 2개 이상 존재하는 한 토양의 물리적 비평형과 용액상태의 화학적평형이 중금속이온 이동에 영향을 미치는 것으로 추정하였다.

• 한국안전학회지
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• 제15권4호
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• pp.88-94
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• 2000

The adsorption characteristics of Tharonil on granular activated carbon were experimentally investigated in an adsorber and in a packed column. It was estabilished that the adsorption equilibrium of Tharonil on granular activated carbon was more successfully fitted by Freundlich isotherm equation than Langmuir isotherm equation in the concentration range from 1 to 1000 mg/1. Intraparticle diffusivities (pore and surface diffusivity) of Tharonil were estimated by the concentration-time curve and adsorption isotherm. The estimated values of pore diffusivity and surface diffusivity are $6.70{\times}10^{-6}$ and $2.0{\times}10^{-9}cm^2/s$, respectively. From comparison of intraparticle diffusivities, it was found that surface diffusion was the limiting step for adsorption rate. The break time and breakthrough curve predicted by constant pattern-linear driving force model were shown to agree with the experimental results.