• Bulletin of the Korean Chemical Society
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• 제19권2호
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• pp.218-222
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• 1998

Removal of Cd(Ⅱ), Zn(Ⅱ) and Cu(Ⅱ) from aqueous solutions using the adsorption process on magadiite has been investigated. It was found that the removal percentage of metal cations at equilibrium increases with increasing temperature, and follows the order of Cd(Ⅱ) > Cu(Ⅱ) > Zn(Ⅱ). Equilibrium modeling of adsorption showed that the adsorptions of Cd(Ⅱ), Cu(Ⅱ), and Zn(Ⅱ) were fitted to Langmuir isotherm. Kinetic modeling of the adsorption showed that first order reversible kinetic model fitted to experimental data. From kinetic model and equilibrium data, the overall rate constant (k) and the equilibrium constant (K) for the adsorption process were calculated. The overall rates of adsorption of metal ions follow the order of Cd(Ⅱ) > Cu(Ⅱ) > Zn(Ⅱ). From the results of thermodynamic analysis, standard Gibbs free energy (ΔG°), standard enthalpy (ΔH°), and standard entropy (ΔS°) of adsorption process were calculated.

• 한국환경과학회지
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• 제20권2호
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• pp.241-249
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• 2011

In this research, equilibrium of adsorption and kinetics of As(V) removal were investigated. The coal mine drainage sludge(CMDS) was used as adsorbent. To find out the physical and chemical properties of CMDS, XRD (X-ray diffraction), XRF (X-ray fluorescence spectrometer) analysis were carried out. The CMDS was consist of 70% of goethite and 30% of calcite. From the results, an adsorption mechanism of As(V) with CMDS was dominated by iron oxides. Langmuir adsorption isotherm model was fitted well more than Freundlich isotherm adsorption model. Adsorption capacities of CMDS 1 was not different with CMDS 2 on aspect of amounts of arsenic adsorbed. The maximum adsorption amount of two CMDS were respectively 40.816, 39.682 mg/g. However, the kinetic of two CMDS was different. The kinetic was followed pseudo second order model than pseudo first order model. Concentrations of arsenic in all segments of the polymer in CMDS 2 does not have a constant value, but the rate was greater than the value of CMDS 1. Therefore, CMDS 2, which is containing polymer, is more effective for adsorbent to remove As(V).

• 한국환경과학회지
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• 제29권12호
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• pp.1261-1274
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• 2020

The characteristics of ammonia-nitrogen (NH4+-N) adsorption by a zeolitic material synthesized from Jeju scoria using the fusion and hydrothermal method was studied. The synthetic zeolitic material (Z-SA) was identified as a Na-A zeolite by X-ray diffraction, X-ray fluorescence analysis and scanning electron microscopy images. The adsorption of NH4+-N using Jeju scoria and different types of zeolite such as the Z-SA, natural zeolite, and commercial pure zeolite (Na-A zeolite, Z-CS) was compared. The equilibrium of NH4+-N adsorption was reached within 30 min for Z-SA and Z-CS, and after 60 min for Jeju scoria and natural zeolite. The adsorption capacity of NH4+-N increased with approaching to neutral when pH was in the range of 3-7, but decreased above 7. The removal efficiency of NH4+-N increased with increasing Z-SA dosage, however, its adsorption capacity decreased. For initial NH4+-N concentrations of 10-200 mg/L at pH 7, the adsorption rate of NH4+-N was well described by the pseudo second-order kinetic model than the pseudo first-order kinetic model. The adsorption isotherm was well fitted by the Langmuir model. The maximum uptake of NH4+-N obtained from the Langmuir model decreased in the order of Z-CS (46.8 mg/g) > Z-SA (31.3 mg/g) > natural zeolite (5.6 mg/g) > Jeju scoria (0.2 mg/g).

• Environmental Engineering Research
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• 제20권4호
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• pp.342-346
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• 2015

Haloacetonitriles (HANs) are nitrogenous disinfection by-products (DBPs) that have been reported to have a higher toxicity than the other groups of DBPs. The adsorption process is mostly used to remove HANs in aqueous solutions. Functionalized composite materials tend to be effective adsorbents due to their hydrophobicity and specific adsorptive mechanism. In this study, the removal of dichloroacetonitrile (DCAN) from tap water by adsorption on thiol-functionalized mesoporous composites made from natural rubber (NR) and hexagonal mesoporous silica (HMS-SH) was investigated. Fourier-transform infrared spectroscopy (FTIR) results revealed that the thiol group of NR/HMS was covered with NR molecules. X-ray diffraction (XRD) analysis indicated an expansion of the hexagonal unit cell. Adsorption kinetic and isotherm models were used to determine the adsorption mechanisms and the experiments revealed that NR/HMS-SH had a higher DCAN adsorption capacity than powered activated carbon (PAC). NR/HMS-SH adsorption reached equilibrium after 12 hours and its adsorption kinetics fit well with a pseudo-second-order model. A linear model was found to fit well with the DCAN adsorption isotherm at a low concentration level.

• 한국재료학회지
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• 제23권8호
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• pp.462-468
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• 2013

We study and describe-from the point of view of the interactions of the adsorbed particles-three types of the adsorption isotherms, namely, Langmuir type adsorption isotherms, phase transition type adsorption isotherms, and adsorption limited type adsorption isotherms, which are observed by experiments. By introducing and using a one dimensional statistical occupancy model, we derived analytical adsorption isotherms for the no force, the attractive force, and the repulsive force exerted on the other adsorbed particles. Our derived adsorption isotherms qualitatively pretty well agree with the experimental results of the adsorption isotherms. To specify each adsorption type, Langmuir type adsorption is a phenomenon that occurs with no forces between the adsorbed particles, phase transition type adsorption is a phenomenon that occurs with the strong attractive forces between the adsorbed particles, and adsorption limited type adsorption is a phenomenon that occurs with the repulsive forces between the adsorbed particles. The theoretical analysis-only using fundamental thermodynamics and occupancy statistics though-qualitatively quite well explains the experimental results.

• Membrane and Water Treatment
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• 제11권1호
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• pp.69-77
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• 2020

Former studies revealed that sepiolite thermally treated at high temperature have high adsorption capacity for phosphate. However, its micron size (75 ㎛) limits its application to water treatment. In this study, we synthesized sepiolite impregnated polysulfone (PSf) beads to separate it easily from an aqueous solution. PSf beads with different sepiolite ratios were synthesized and their efficiencies were compared. The PSf beads with 30% impregnated sepiolite (30SPL-PSf bead) possessed the optimum sepiolite ratio for phosphate removal. Kinetic, equilibrium, and thermodynamic adsorption experiments were performed using the 30SPL-PSf bead. Equilibrium adsorption was achieved in 24 h, and the pseudo-first-order model was suitable for describing the phosphate adsorption at different reaction times. The Langmuir model was appropriate for describing the phosphate adsorption onto the 30SPL-PSf bead, and the maximum adsorption capacity of the 30SPL-PSf bead obtained from the model was 24.48 mg-PO₄/g. Enthalpy and entropy increased during the phosphate adsorption onto the 30SPL-PSf bead, and Gibb's free energy at 35 ℃ was negative. An increase in the solution pH from 3 to 11 induced a decrease in the phosphate adsorption amount from 27.30 mg-PO₄/g to 21.54 mg-PO₄/g. The competitive anion influenced the phosphate adsorption onto the 30SPL-PSf bead was in the order of NO₃^- > SO₄^2- > HCO_3^-. The phosphate breakthrough from the column packed with the 30SPL-PSf bead began after ~2000 min, reaching the influent concentration after ~8000 min. The adsorption amounts per unit mass of 30SPL-PSf and removal efficiency were 0.775 mg-PO₄/g and 61.6%, respectively. This study demonstrates the adequate performance of 30SPL-PSf beads as a filter for phosphate removal from aqueous solutions.

• Korean Chemical Engineering Research
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• 제57권2호
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• pp.210-218
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• 2019

실로퓨트를 이용한 식물세포 Taxus chinensis 유래 주요 타르성분인 2-피콜린 흡착 실험을 수행하였다. 2-피콜린 초기농도, 흡착 온도 및 시간을 달리한 회분식 흡착 평형 데이터를 Langmuir, Freundlich, Temkin, Dubinin-Radushkevich 등온흡착식에 적용하였다. 실로퓨트를 이용한 2-피콜린의 흡착은 Langmuir 흡착등온식에 가장 적합함을 알 수 있었다. 흡착온도가 증가함에 따라 흡착용량이 감소하는 경향을 보였으며 실로퓨트를 이용한 2-피콜린 흡착 공정이 적합함을 알 수 있었다. 동역학적 해석을 통하여 본 흡착 공정은 유사 이차 반응속도식에 잘 따름을 알 수 있었으며, 입자 내 확산과 경계층 확산이 율속 단계에 거의 영향을 미치지 않았다. 열역학적 해석을 통해 흡착 과정이 발열이며, 비가역적 비자발적으로 수행되었다. 흡착량이 증가함에 따라 등량흡착열은 감소하는 경향을 보여 흡착제의 표면 에너지가 불균일함을 알 수 있었다.

• 청정기술
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• 제14권1호
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• pp.47-52
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• 2008

흡착공정의 흡착속도를 표현하는 여러 가지 물질전달 모델들 가운데, 식의 형태가 비교적 간단한 선형추진력(Linear Driving Force, LDF) 모델이 많이 사용된다. 본 연구에서는 벤젠을 분리 및 제거하기 위한 실제 흡착공정에서 이 물질전달모델의 적용가능성을 알아보고자 하였다. LDF모델에 의한 전산모사 결과와 동적실험에서 구한 실험 값을 비교함으로써 흡착공정의 물질전달 계수를 구하였다. 여러 다른 값의 온도 및 압력에서 얻은 파과곡선을 이용하여 물질전달계수의 온도 및 압력에 대한 의존관계를 알아보았다. 물질전달계수의 온도와 압력에 대한 의존성은 각각, 아레니우스함수와 지수함수 형태의 경험식으로 표현할 수 있었다.

• 청정기술
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• 제27권3호
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• pp.261-268
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• 2021

석탄계 입상 활성탄(CGAC)에 의한 acid black 1 (AB1) 염료의 평형, 동력학 및 열역학적 특성을 초기농도, 접촉 시간, 온도 및 pH 를 흡착변수로 하여 조사하였다. 활성탄에 의한 AB1의 흡착반응은 산성에서는 활성탄의 표면(H⁺)과 AB1이 가지고 있는 sulfite ion (SO₃^-), nitrite ion (NO₂^-) 사이의 정전기적 인력에 의해 일어났고, 최고 흡착률은 pH 3에서 97.7%였다. AB1의 등온 데이터는 Freundlich 등온식에 가장 잘 맞았으며, 계산된 분리계수(1/n) 값으로부터 활성탄에 의한 AB1의 흡착이 효과적인 처리과정이 될 수 있음을 알았다. Temkin 식의 흡착열 관련상수의 값은 물리 흡착 공정(< 20 J mol^-1)임을 나타냈다. 동역학 실험에서는 유사 2차 모델이 유사 1차 모델보다 더 일관성이 있었으며 추정된 평형 흡착량은 오차 백분율의 9.73% 이내에서 잘 일치하였다. 입자내 확산이 흡착 과정에서 속도 조절 단계였다. 활성화 에너지와 엔탈피 변화값으로부터 흡착반응이 물리흡착으로 진행되는 흡열반응임을 확인하였다. 엔트로피 변화는 활성탄 표면에서 AB1의 흡착이 일어나는 동안 고-액 계면에서 활발한 반응에 의해 엔트로피가 증가하는 것으로 나타났다. 자유에너지 변화는 온도증가와 함께 흡착반응의 자발성이 더 커지는 것을 나타냈다.

• 한국지반공학회지:지반
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• 제11권2호
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• pp.121-138
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• 1995

여러종류의 화합물질들이 동시에 토양에 유출되었을 때 이들이 토양에 흡착하는 정도를 예측 함에는 Langmuir Competitive Model과 IAS(Ideal Adsorption Model) 등이 널리 사용되고 있 는데, 5개의 유기화합물질(Phenol, 2,4-Dichlorophenol, 2,4,6-Trichlorophenot Brucine, Thiourea)과 2종류의 토양을 이용한 흡착실험을 통해서 이 Model들의 예측도를 비교분석하였다. 흡착실험은 이 화합물질들이 독자적인 상태에서 그리고 혼합상태에서 각각 구분하여 실헙하였다. 일반적으로 IAS Model이 Langmuir Model보다 혼합상태에서 각 구성 화합물질들의 흡착을 더 정확히 예측하였다. Langmuir Model은 Phenol과 함께 섞여있는 다른물질의 농도가 높을 때 Phenol의 흡착을 낮게 예측하였다. 두가지 Model모두 Thiourea가 혼합상태에 있을때 흡착정도를 만족스럽게 예측하지 못했는데 Thiourea는 Aliphatic화합물이고 나머지 4개는 Aromatic화합물이다.