• Carbon letters
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• 제22권
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• pp.14-24
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• 2017

Carboxylated multi-wall carbon nanotubes (MWCNTs-COOH) have been used as efficient adsorbents for the removal of picric acid from aqueous solutions under stirring and ultrasound conditions. Batch experiments were conducted to study the influence of the different parameters such as pH, amount of adsorbents, contact time and concentration of picric acid on the adsorption process. The kinetic data were fitted with pseudo-first order, pseudo-second-order, Elovich and intra-particle diffusion models. The kinetic studies were well described by the pseudo-second-order kinetic model for both methods. In addition, the adsorption isotherms of picric acid from aqueous solutions on the MWCNTs were investigated using six two-parameter models (Langmuir, Freundlich, Tempkin, Halsey, Harkins-Jura, Fowler-Guggenheim), four three-parameter models (Redlich-Peterson, Khan, Radke-Prausnitz, and Toth), two four-parameter equations (Fritz-Schlunder and Baudu) and one five-parameter equation (Fritz-Schlunder). Three error analysis methods, correlation coefficient, chi-square test and average relative errors, were applied to determine the best fit isotherm. The error analysis showed that the models with more than two parameters better described the picric acid sorption data compared to the two-parameter models. In particular, the Baudu equation provided the best model for the picric acid sorption data for both methods.

• 한국환경과학회지
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• 제30권9호
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• pp.719-726
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• 2021

In this study, zeolitic materials were synthesized from Jeju Volcanic Rocks (JVR) using a fusion/hydrothermal method at NaOH/JVR ratios of 0.6 and 1.2. The crystallinities of the zeolitic materials at NaOH/JVR ratios of 0.6 and 1.2 were 25.5% and 59.0%, respectively. It was confirmed through the SEM image that the zeolitic materials covered the zeolite particle with a cube-shaped crystals. The Co ions adsorption by the zeolitic materials were to reach the adsorption equilibrium at 120 min. It could be better simulated in the pseudo-second order adsorption kinetic equation than in the pseudo-first order adsorption kinetic equation. The adsorption capacities (q_m) of Co ions could be to estimate Langmuir isotherm better than Freundlich isotherm. The maximum adsorption capacities (q_m) at NaOH/JVR ratios of 0.6 and 1.2 were 55.3 mg/g and 68.7 mg/g, respectively. It was found that there was a high correlation between the crystallinity of zeolitic materials and the adsorption capacity of Co ions adsorption.

• 한국지반환경공학회 논문집
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• 제12권10호
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• pp.23-28
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• 2011

본 연구에서는 생계면활성제, SWA 1503, Triton X-100 및 SDS를 포함하는 다양한 계면활성제의 토양에 대한 흡착 특성을 조사하였다. 프로인드리히 흡착 등온 모델이 계면활성제의 실험 결과를 가장 잘 설명하는 것으로 나타났다. 실험결과 점토 함량의 증가에 따라 계면활성제의 토양에 대한 흡착량이 증가하였다. 이와 같은 결과는 점토가 모래에 비해 표면적이 넓어 점토의 토양표면과 공극에 계면활성제의 흡착이 많이 이루어지는 것에 기인한다. 시간에 따른 흡착실험의 경우 biosurfactant > SWA 1503 > Triton X-100 > SDS 순으로 흡착량이 높은 것으로 나타났다.

• Membrane and Water Treatment
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• 제7권5호
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• pp.403-416
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• 2016

The possibility of using carica papaya leaf powder for removal of copper from wastewater as a low cost adsorbent was explored. Different parameters that affect the adsorption process like initial concentration of metal ion, time of contact, adsorbent quantity and pH were evaluated and the outcome of the study was tested using adsorption isotherm models. A maximum of 90%-94.1% copper removal was possible from wastewater having low concentration of the metal using papaya leaf powder under optimum conditions by conducting experimental studies. The biosorption of copper ion was influenced by pH and outcome of experimental results indicate the optimum pH as 7.0 for maximum copper removal. Copper distribution between the solid and liquid phases in batch studies was described by isotherms like Langmuir adsorption and Freundlich models. The adsorption process was better represented by the Freundlich isotherm model. The maximum adsorption capacity of copper was measured to be 24.51 mg/g through the Langmuir model. Pseudo-second order rate equation was better suited for the adsorption process. A dynamic mode study was also conducted to analyse the ability of papaya leaf powder to remove copper (II) ions from aqueous solution and the breakthrough curve was described by an S profile. Present study revealed that papaya leaf powder can be used for the removal of copper from the wastewater and low cost water treatment techniques can be developed using this adsorbent.

• 한국재료학회지
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• 제26권9호
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• pp.498-503
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• 2016

The characteristics of aqueous lithium recovery by ion exchange were studied using three commercial cation exchange resins: CMP28 (porous type strong acid exchange resin), SCR-B (gel type strong acid exchange resin) and WK60L (porous type weak acid exchange resin). CMP28 was the most effective material for aqueous lithium recovery; its performance was even enhanced by modifying the cation with $K^+$. A comparison to $Na^+$ and $H^+$ form resins demonstrated that the performance enhancement is reciprocally related to the electronegativity of the cation form. Further kinetic and equilibrium isotherm studies with the $K^+$ form CMP28 showed that aqueous lithium recovery by ion exchange was well fitted with the pseudo-second-order rate equation and the Langmuir isotherm. The maximum ion exchange capacity of aqueous lithium recovery was found to be 14.28 mg/g and the optimal pH was in the region of 4-10.

• 공업화학
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• 제30권5호
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• pp.562-568
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• 2019

Cylindrical shape extrudates of calcium silicate hydrate (CSH) were prepared using different percentages of polyvinyl alcohol (PVA) / sodium alginate (SA) mixtures as binders and an aqueous solution containing 6% $H_3BO_3$ and 3% $CaCl_2$ was used as a cross linking agent. As the quantity of alginate increases, the phosphate removal efficiency and capacity were decreased. Among four different extrudate samples, the sample prepared by 8% PVA + 2% SA showed the highest phosphate removal efficiency (59.59%) and capacity (29.97 mg/g) at an initial phosphate concentration of 100 ppm and 2.0 g/L adsorbent dosage. Effects of the adsorbent dosage, contact time and initial phosphate concentration on the sample were further studied. The removal efficiency and capacity obtained by a 4.0 g/L adsorbent dose at an initial phosphate concentration of 100 ppm in 3 h were 79.38% and 19.96 mg/g, respectively. The experimental data of kinetic and isotherm measurements followed the pseudo-second-order kinetic equation and Langmuir isotherm model, respectively. These results suggested that the phosphate removal was processed via a chemisorption and a monolayer coverage of phosphate anions was on the CSH surface. The maximum adsorption capacity ($q_{max}$) was calculated as 23.87 mg/g from Langmuir isotherm model.

• 한국산학기술학회논문지
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• 제15권4호
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• pp.2029-2035
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• 2014

본 논문은 입상활성탄에 의해서 합성폐수에서의 용존유기탄소의 흡착평형과 회분식 실험을 통해 흡착성질을 파악하고자 하였다. 흡착평형의 새로운 모델식을 제안하였고 이 식을 바탕으로 회분식 실험데이터를 모사하였다. 합성폐수의 유기성분은 Beef extract, Peptone, Humic acid, Tannic acid, Sodium lignin sulfonate, Sodium lauryle sulfate, Arabic gum powder, Arabic acid (polysaccharide), $(NH_4)_2SO_4$, $K_2HPO_4$, $NH_4HCO_3$, $MgSO_4{\cdot}7H_2O$ 등으로 구성되었다. 농도가 낮은 영역 (0~2.5 mg/L)에서는 선형적인 흡착평형을 보여주었고, 농도가 높은 영역 (2.5~6mgl/L)에서는 우호적인 흡착평형을 보여주었다. 사용되어진 생물학적 처리방법에서 나오는 유출수의 합성폐수는 알려진 양으로 준비되어졌다. 흡착평형 모델링은 Freundlich, Langmuir, Sips 및 하이브리드 식을 이용하여 모사하였다. 특히, 선형과 Sips를 이용한 하이브리드 흡착평형식은 낮은 농도와 높은 농도 역에서 매우 좋은 흡착평형식이었다. 용수 및 폐수처리에 활성탄 흡착에 있어서, 선형식과 Sips식을 합친 새로운 하이브리드 식은 새로운 흡착평형식이 될 수 있었다. 하이브리드 흡착평형식 (선형+Sips)을 이용하여 LDFA 운동학적식을 통하여 다양한 흡착제 양에 따른 회분식 반응조에서의 실험데이터를 잘 모사할 수 있었다.

• 공업화학
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• 제31권2호
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• pp.164-171
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• 2020

석탄계 활성탄을 사용한 Reactive Red 120 (RR 120) 염료의 흡착특성을 활성탄의 양, pH, 초기농도, 접촉시간 및 온도를 흡착변수로 사용하여 조사하였다. 등온흡착평형관계는 Langmuir 식이 Freundlich 식보다 더 잘 맞았다. 흡착 메카니즘은 균일한 에너지 분포를 가진 단분자층 흡착이 우세하다고 판단되었다. 평가된 Langmuir 분리계수(R_L = 0.181~0.644)로부터 이 흡착공정이 효과적인 처리영역(R_L = 0~1)에 속하는 것을 알았다. Temkin 식과 Dubinin-Radushkevich 식에 의해 구한 흡착에너지는 각각 E = 15.31~7.12 J/mol과 B = 0.223~0.365 kJ/mol로 흡착공정은 모두 물리흡착(E < 20 J/mol, B < 8 kJ/mol)으로 나타났다. 흡착속도실험결과는 유사 1차 반응속도식에 잘 맞았다. CGAC에 대한 RR 120 염료의 흡착반응은 온도가 올라갈수록 자유에너지 변화값이 감소하였기 때문에 온도 증가와 함께 자발성이 높아지는 것으로 나타났다. 엔탈피 변화(12.747 kJ/mol)는 흡열반응임을 알려주었다. CGAC에 의한 RR 120의 흡착반응의 등량흡착열은 9.78~24.21 kJ/mol로 물리흡착(< 80 kJ/mol)임을 밝혔다.

• 상하수도학회지
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• 제19권4호
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• pp.404-410
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• 2005

A series of batch type adsorption experiments were performed to remove aquatic phosphorus, where the layered double hydroxide (HTAL-CI) was used as an powdered adsorbent. It showed high adsorption capacity (T-P removal: 99.9%) in the range of pH 5.5 to 8.8 in spite of providing low adsorption characteristics (pH<4). The adsorption isotherm was approximated as a modified Langmuir type equation, where the maximum adsorption amount (50.5mg-P/g) was obtained at around 80mg-P/L of phosphorus concentration. A phosphate ion can occupy three adsorption sites with a chloride ion considering the result that 1 mol of phosphate ion adsorbed corresponded to the 3 moles of chloride ion released. Although the chloride ion at less than 1,000mg-CI/L did not significantly affect the adsorption capacity of phosphate, carbonate ion inhibited the adsorption property.

• 한국식품저장유통학회지
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• 제4권1호
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• pp.33-38
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• 1997

In order to provide informations for designing packaging and storage condition of dry jujube (Zizyphus jujuba MILLER), moisture sorption isotherm was determined for temperatures of 20, 30 and 4$0^{\circ}C$, and quality changes were evaluated as function of temperature and water activity. Dry jujube at a given water activity showed higher equilibrium moisture content for lower temperature. Moisture isothem could be fitted by GAB model equation, giving higher C value, lower m0 and relatively constant k value with increase in temperature. Ascorbic acid was lost more highly at higher temperature and water activity, and showed negligible retention for whole range of water activity and temperature studied after 141 days. Browning increased with water activity up to 0.73 at 30 and 4$0^{\circ}C$. Dry jujube of high water activity had high L value in surface color, which represent brightness of surface color. Considering quality retention in the storage, dry jujube is desired to be dried to water activity of 0.42 and be stored at temperature below 3$0^{\circ}C$