• Korean Chemical Engineering Research
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• 제59권1호
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• pp.21-34
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• 2021

본 연구에서는 Chitosan nanoparticles (CNPs) 와 Lactococcus lactis (L. lac.) 를 흡착제로 사용하여 phthalates의 흡착 실험을 진행하였다. CNPs는 Tripolyphospate (TPP)와의 가교 결합을 통하여 제조되었으며, 제조과정 중에 L. lac.의 도입을 통하여 L. lac.-CNPs를 제조하였다. 모든 흡착제는 Fourier transform infrared spectroscopy (FTIR)을 사용하여 특성을 측정하여 다양한 작용기의 존재를 확인하였다. Adsorption isotherm 과 adsorption kinetic 을 통하여 CNPs, L. lac. 및 L. lac.-CNPs 의 흡착 거동 및 메커니즘을 확인하였다. 모든 입자에 대하여 DBP 및 DEP 의 흡착 거동은 Langmuir adsorption isotherm model 보다는 Freundlich adsorption isotherm model 에 적합하였으며, 이는 입자의 표면이 이질적 (heterogeneous) 라는 것을 의미한다. 흡착 메커니즘은 Pseudo-1st-order model 보다는 Pseudo-2nd-order model 에 적합하였으며, 이는 DBP 및 DEP 의 흡착이 입자 표면의 다양한 작용기들에 의하여 물리적 흡착보다는 정전기적 인력과 수소 결합 등에 의한 화학적 흡착이 지배적임을 나타낸다. 최종적으로, 쉽고 빠른 방법으로 CNPs 및 L. lac-CNPs 의 제조가 가능하며, 유기성 오염 물질을 효과적으로 제거할 수 있는 저비용의 흡착제로서 사용할 수 있음을 확인하였다.

• 콘크리트학회논문집
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• 제29권4호
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• pp.389-397
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• 2017

시멘트내 $C_3A$상과 $C_4AF$상은 염소이온과 반응하여 프리델염을 생성한다. 프리델염은 구조체에서 염소를 포함하기 때문에 염소이온의 흡착에 매우 중요하다. 외부에서 염소이온이 침투하면, 칼슘 알루미네이트 수화물은 염소이온을 고정하므로, $C_3A$상과 $C_4AF$상 및 AFm상의 염소 흡착 거동을 고찰하는 것은 고정화 현상을 이해하는데 매우 중요하다. 한편, 흡착 등온은 시멘트와 프리델염의 상호관계에서 정량적인 지식을 제공할 뿐만 아니라 그 상호관계의 특성을 이해하는데 매우 중요하다. 본 연구의 목적은 $C_3A$상, $C_4AF$상 및 AFm상의 염소이온 흡착 거동을 고찰하는데 있다. $C_3A$상과 $C_4AF$상의 흡착등온은 이론적 화학당량보다 다소 낮았으며 Langmuir 흡착등온식으로 표현할 수 있었다. AFm상의 흡착등온은 이론적 화학당량보다 매우 낮았으며, Freundlich 흡착등온식으로 표현하였다. 또한 흡착등온 모델에서 온도의 영향 매개변수를 실험범주내에서 온도의 함수로 제안하였다.

• 한국환경과학회지
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• 제9권2호
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• pp.145-149
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• 2000

The purpose of this study was to determine whether Vermi Cast could be used effectively to remove $SO_2$ from flue gas, and then to investigate optimum adsorption conditions. The Vermi Cast used as adsorbent was mechanically screened with 8~20 mesh sieve. The adsorption data for $SO_2$ were regressed using the Freundlich isotherm. The fit was generally satisfactory ($R^2$=0.945~0.982). With the temperature changes from 2$0^{\circ}C$ to 4$0^{\circ}C$, the constant k in Freundlich isotherm qe= $kCe^{1/n}$, decreased from 1.409 at 2$0^{\circ}C$to 0.297 at 4$0^{\circ}C$, and the exponent 1/n were decreased from 0.343 to 0.134. With the bed depth changes from 10cm to 30cm, the adsorption capacity expressed as mmol of $SO_2$ adsorbed per g of Vermi Cast increased from 0.247 to 0.381. Moisture content is an important parameter in the $SO_2$ adsorbed were observed over 0.3mmol $SO_2$ /g Vermi Cast. The best adsorption capacity was 0.487mmol $SO_2$ /g Vermi Cast, and it was obtained with moisture content 37%, temperature 2$0^{\circ}C$. From the above results, ti might be concluded that Vermi Cast is effectively as a good adsorbent to remove $SO_2$ from flue gas.

• 한국물환경학회지
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• 제25권6호
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• pp.943-950
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• 2009

Cadmium (Cd) adsorption onto the activated carbon containing hydroxyapatite (HAP) was investigated in batch experiments and response surface methodology (RSM) using the Box-Behnken methods were applied to the experimental results. Cd adsorption with different HAP mass ratio of from 10% to 30%. With more HAP, Cd was more adsorbed. These results suggest that the higher HAP mass causes an increase of the ion exchange potential of the HAP sorbent. Equilibrium experimental results from Cd adsorption was fitted to Langmuir and Freundlich isotherm models. Cd adsorption on HAP sorbent were found to follow the Freundlich isotherm model well in the initial adsorbate concentration range. Also, Cd adsorption was a function of the HAP mass ratio ($x_1$), initial Cd concentration ($x_2$), and initial pH ($x_3$) from the application of the RSM. Statistical results showed the order of significance of the independent variables to be initial Cd concentration > HAP mass ratio > initial pH.

• Korean Chemical Engineering Research
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• 제58권2호
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• pp.301-306
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• 2020

We investigated the individual biosorption removal of lead, copper, and nickel ions from aqueous solutions using Chara sp. algae powder in a batch mode. The impact of several parameters, such as initial concentration of the metal ions, contacting time, sorbent dose, and pH on the removal efficiency, was investigated. The maximum removal efficiency at optimum conditions was found to be 98% for Pb(II) at pH = 4, 90% for Cu(II) at pH = 5, and 80% for Ni(II) at pH = 5. The isotherm study was done under the optimum conditions for each metal by applying the experimental results onto the well-known Freundlich and Langmuir models. The results show that the Langmuir is better in describing the isotherm adsorption of Pb(II) and Ni(II), while the Freundlich is a better fit in the case of Cu(II). Similarly, a kinetic study was performed by using the pseudo-first and second-order equations. Our results show that the pseudo-second-order is better in representing the kinetic adsorption of the three metal ions.

• 한국수처리학회지
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• 제26권6호
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• pp.143-152
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• 2018

The process parameters of ethyl violet from aqueous solution by activated carbon adsorption were carried out as a function of pH, temperature, contact time, initial concentration and temperature. The adsorption equilibrium data can be described well by the Langmuir and Freundlich isotherm models. Base on Langmuir constant ($R_L=0.0343{\sim}0.0523$) and Freundlich constant (1/n=0.1633~0.1974), This process could be employed as effective treatment for adsorption of ethyl violet. The kinetic experimental results showed that the adsorption process can be well described with the pseudo second order model. Based on the positive enthalpy (6.505 kJ/mol), the adsorption of ethyl violet onto granular activated carbon is endothermic. The negative Gibbs free energy (-1.169~-1.681 kJ/mol) obtained indicates that the adsorption process is spontaneous and physisorption.

• Bulletin of the Korean Chemical Society
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• 제34권8호
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• pp.2358-2366
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• 2013

Iron oxide (ferrihydrite, hematite, and magnetite) coated silica gels were prepared using a low-cost, easily-scalable and straightforward method as the adsorbent material for arsenic removal application. Adsorption of the anionic form of arsenic oxyacids, arsenite ($AsO^{2-}$) and arsenate ($AsO{_4}^{3-}$), onto hematite coated silica gel was fitted against non-linear 3-parameter-model Sips isotherm and 2-parameter-model Langmuir and Freundlich isotherm. Adsorption kinetics of arsenic could be well described by pseudo-second-order kinetic model and value of adsorption energy derived from non-linear Dubinin-Radushkevich isotherm suggests chemical adsorption. Although arsenic adsorption process was not affected by the presence of sulfate, chloride, and nitrate anions, as expected, bicarbonate and silicate gave moderate negative effects while the presence of phosphate anions significantly inhibited adsorption process of both arsenite and arsenate. When the actual efficiency to remove arsenic was tested against 1 L of artificial arsenic-contaminated groundwater (0.6 mg/L) in the presence competing anions, the reasonable amount (20 g) of hematite coated silica gel could reduce arsenic concentration to below the WHO permissible safety limit of drinking water of $10{\mu}g/L$ without adjusting pH and temperature, which would be highly advantageous for practical field application.

• 대한화학회지
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• 제61권5호
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• pp.238-243
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• 2017

본 연구에서, 400도에서 탄화시킨 정수 슬러지를 수중의 납과 카드뮴의 제거를 위한 흡착제로서 시험하였다. 탄화된 슬러지는 열중량 분석, 주사 전자 현미경, X-선 형광분광기, 표면적 분석에 의해 특성화 하였다. 탄화 슬러지는 정수 슬러지 자체보다도 대단히 높은 비표면적과 총 세공부피를 나타내었다. 회분식 흡착 과정에서 탄화 슬러지는 카드뮴보다는 납에 대하여 더 나은 흡착성능을 보였으며, 실험에서 행한 농도에서 90~98%의 흡착 능력을 달성하였다. 흡착의 평형 데이터는 Freundlich와 Langmuir와 흡착등온선 모델을 이용하여 평가하였고, Freundlich와 Langmuir 흡착 등온선 둘 다 0.95보다 큰 상관계수($R^2$) 값을 나타내었다. 연구의 결과들은 열처리 된 탄화 정수 슬러지가 수중으로부터 납과 카드뮴을 제거하는데 효율적인 흡착제로 사용될 수 있다는 것을 보였다.

• 청정기술
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• 제7권2호
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• pp.141-149
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• 2001

본 연구는 활성탄이 충진된 고정 흡착층에서 흡착특성에 영향을 줄 수 있는 다양한 변수들, 흡착온도, 흐름속도, 흡착질의 종류와 농도, 형상비(L/D)에 따른 영향이 조사되었다. 고정층내의 파과시간은 흡착온도, 흐름속도와 흡착질의 농도가 증가함에 따라 감소하였다. 또한 고정 흡착층의 파과곡선으로부터 얻어지는 물질전달영역(mass transfer zone)과 미사용길이(length of unused bed)는 흡착가스 유속, 흡착가스의 농도 및 흡착온도에 영향을 많이 받는 반면 고정 흡착층의 형상비에 대한 영향은 상대적으로 작았으며, 이 중에서 흡착가스의 농도에 대한 영향이 가장 큰 것으로 나타났다. 단일성분에 대한 흡착평형실험 데이터를 가장 잘 예측할 수 있는 모델식을 구하기 위해 Langmuir, Freundlich 및 Langmuir-Freundlich 모델식을 적용하여 실험결과와 비교해 보았을 때 세가지 이론식 모두 benzene과 toluene의 흡착평형을 잘 표현하는 것을 알 수 있었다.

• 한국환경과학회지
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• 제29권8호
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• pp.827-835
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• 2020

Zeolite material having XRD peaks of Na-A zeolite in the 2θ range of 7.18 to 34.18 can be synthesized from the waste catalyst using a fusion/hydrothermal method. The adsorption rate of Mn ions by a commercial Na-A zeolite and the synthesized zeolitic material increased as the adsorption temperature increased in the range of 10 ~ 40℃. The adsorption of Mn ion were very rapid in the first 30 min and then reached to the equilibrium state after approximately 60 min. The adsorption kinetics of Mn ions by the commercial Na-A zeolite and the zeolitic material were found to be well fitted to the pseudo-2^nd order kinetic model. Equilibrium data by the commercial Na-A zeolite and the zeolitic material fit the Langmuir, Koble-Corrigan, and Redlich-Peterson isotherm models well rather than Freundlich isotherm model. The removal capacity of the Mn ions by the commercial Na-A zeolite and the zeolitic material obtained from the Langmuir model was 135.2 mg/g and 128.9 mg/g at 30℃, respectively. The adsorption capacity of Mn ions by the synthesized zeolitic material was almost similar to that of commercial Na-A zeolite. The synthesized zeolitic material could be applied as an economically feasible commercial adsorbent.