• 상하수도학회지
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• 제29권6호
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• pp.609-615
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• 2015

This study was carried out for characterization of MIO synthesized in our laboratory by co-precipitation method and applied isotherm and kinetic models for adsorption properties. XRD analysis were conducted to find crystal structure of synthesized MIO. Further SEM and XPS analysis was performed before and after phosphate adsorption, and BET analysis for surface characterization. Phosphate stock solution was prepared by KH2PO4 for characterization of phosphate adsorption, and batch experiment was conducted using 50 ml conical tube. Langmuir and Freundlich models were applied based on adsorption equilibrium test of MIO by initial phosphate solution. Pseudo first order and pseudo second order models were applied for interpretation of kinetic model by temperature. Surface area and pore size of MIO were found $89.6m^2/g$ and 16 nm respectively. And, the determination coefficient ($R^2$) value of Langmuir model was 0.9779, which was comparatively higher than that of Freundlich isotherm model 0.9340.

• 상하수도학회지
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• 제25권3호
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• pp.359-366
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• 2011

The feasibility of using volcanic ash for lead ion removal from wastewater was evaluated. The adsorption experiments were carried out in batch tests using volcanic ash that was treated with either NaOH or HCl prior to the use. Volcanic ash dose, temperature and initial Pb(II) concentration were chosen as 3 operational variables for a $2^3$ factorial design. Ash dose and concentration were found to be significant factors affecting Pb(II) adsorption. The removal of Pb(II) was enhanced with increasing volcanic ash dose and with decreasing the initial Pb(II) concentration. Pb(II) adsorption on the volcanic ash surface was spontaneous reaction and favored at high temperatures. Calculation of Gibb's free energy indicated that the adsorption was endothermic reaction. The equilibrium parameters were determined by fitting the Langmuir and Freundlich isotherms, and Langmuir model better fitted to the data than Freundlich model. BTV(base-treated volcanic ash) showed the maximum adsorption capacity($Q_{max}$) of 47.39mg/g. A pseudo second-order kinetic model was fitted to the data and the calculated $q_e$ values from the kinetic model were found close to the values obtained from the equilibrium experiments. The results of this study provided useful information about the adsorption characteristics of volcanic ash for Pb(II) removal from aqueous solution.

• Advances in environmental research
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• 제1권3호
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• pp.223-236
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• 2012

Biosorption of methylene blue (MB) from aqueous solution was studied with respect to the point of zero charge of coconut husk, dye concentration, particle size, pH, temperature, as well as adsorbent and NaCl concentration using coconut husk biomass. Amongst Langmuir and Freundlich adsorption isotherms studied, Langmuir adsorption isotherm showed better agreement. Pseudo second order kinetics model was found to be more suitable for data presentation as compared to pseudo first order kinetics model. Also, involvement of diffusion process was studied using intraparticle diffusion, external mass transfer and Boyd kinetic model. Involvement of intraparticle diffusion model was found to be more relevant (prominent) as compared to external mass transfer (in) for methylene blue biosorption by the coconut husk. Moreover, thermodynamic properties of MB biosorption by coconut husk were studied. Desorption of methylene blue from biomass was studied with different desorbing agents, and the highest desorption achieved was as low as 7.18% with acetone, which indicate stable immobilization. Under the experimental conditions MB sorption was not significantly affected by pH, temperature and adsorbent concentration but low sorption was observed at higher NaCl concentrations.

• Membrane and Water Treatment
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• 제12권1호
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• pp.23-35
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• 2021

A POM-membrane was fabricated by immobilizing a keggin type polyoxometalate (POM) H5PV2Mo10O40 onto the surface of microporous flat-sheet polymeric polyvinylidene fluoride (PVFD) membrane using a chemical deposition method. The POM-membrane was characterized by FT-IR, SEM and EDX to confirm existing of the POM onto the membrane surface. The POM-membrane was used to remove an anionic textile dye (Reactive Black 5 named as an RB5) from aqueous phases with a cross-flow membrane filtration and a batch adsorption system. The dye removal efficiency of the POM-membrane using the cross-flow membrane filtration system and the batch adsorption system was about 88% and 98%, respectively. The influence factors such as contact time, adsorbent dosage, pH, and initial dye concentration were investigated to understand the adsorption mechanism of the RB5 dye onto the POM-membrane. To find the best fitting isotherm model, Langmuir, Freundlich, BET and Harkins-Jura isotherm models were used to analyze the experimental data. The isotherm analysis showed that the Langmuir isotherm model was found to the best fit for the adsorption data (R2 = 0.9982, qmax = 24.87 mg/g). Also, adsorption kinetic models showed the pseudo second order kinetic model was found the best model to fit the experimental data (R2 = 0.9989, q = 8.29 mg/g, C0 = 15 ppm). Moreover, after four times regeneration with HNO3 acid, the POM-membrane showed high regenerability without losing dye adsorption capacity.

• Environmental Sciences Bulletin of The Korean Environmental Sciences Society
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• 제2권2호
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• pp.149-158
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• 1998

Biomass of non-living brown seaweed Sargassun fluitans pretreated with NaOH is capable of taking up more than $10\%$ $(q_{max}$ : 3.85 mmol/g for Al and 1.48 mmol/g for Cu) of its dry weight in the Al and Cu at pH of 4.5. However, the maximum Al and Cu uptakes calculated from Langmuir isotherm were 1.58 mmol/g for Al and 1.35 mmol/g for Cu at pH 3.5. Equilibrium batch sorption study was performed using two-metal system containing Al and Cu. The mathematical model of the two-metal sorption system enabled quantitative estimation of one-metal biosorption inhibition due to the influence of a second metal. NaOH-treated S. fluitans contained 2.19 mmol $(43\;wt.\%)$ carboxyl groups per gram of biomass. A modified form of Langmuir, which assumes binding of Cu as $Cu^{2+}$ and Al as $Al(OH)_2^+,$ was used to model the experimental data. This result agrees with the one of mono-valent sorption for Al in single-metal system. The modified Langmuir model gives the following affinity correlated coefficients: 0.196 for Cu and 6.820 for Ah at pH 4.5, and 2.904 for Cu and 3.131 for Al at pH 3.5. The interference of Al in Cu biosorptive uptake was assessed by `cutting' the three dimensional uptake isotherm surfaces at constant second-metal final concentrations. Equimolar final equilibrium concentrations of Cu and Al of 1 mM at pH 4.5 give Cu and hi uptakes reduced by $82.5\%\;and\;5.4\%,$ respectively. However, these values at pH 3.5 were $55\%\;(Cu)\;and\;31\%$ (Al).

• 한국수산과학회지
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• 제34권5호
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• pp.521-525
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• 2001

국내에서 다량 생산되는 갈조류인 미역포자엽, 다시마, 톳, 모자반으로부터 fucoidan을 추출, 분획하여 Pb와 Cd의 흡착 특성을 조사하였다. 4종의 갈조류에서 추출한 fucoidan의 분획물 모두 Pb의 흡착량이 Cd보다 높았으며, 시료간에는 미역포자엽 분획물 (Fr-3.0)이 Pb와 Cd 모두 흡착력이 상대적으로 우수하였다. pH와 농도 변화에 따른 홉착력의 변화는 $C_f$ (잔류농도)가 50mg/L까지는 pH 간 차이가 없었으나, 농로가 증가함에 따라 pH 5.5 처리구가 다른 처리구에 비하여 흡착량이 증가하였다. 실험을 통하여 얻은 Pb 와 Cd의 최대 흡착량은 pH 5.5에서 각각 94mg/g ($C_f$164mg/L), 64mg/g ($C_f$197mg/L)였으며 Langmuir sorption model을 통해 구한 최대 흡착량은 pH 5.5에서 각각 178mg/g, 122mg/g이었다. Cd 공존시 Pb 흘착량은 $C_f$가 낮을 범위에서는 변화가 없었으나 $C_f$가 증가함에 따라 공존 이온의 흡착 방해로 인하여 감소하였다.

• 자원리싸이클링
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• 제17권2호
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• pp.63-69
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• 2008

폐알칼리망간전지 분말에 대한 $Ni^{2+}$의 흡착 거동을 살펴보기 위하여 흡착제의 양, 홉착질의 초기농도 및 반응온도를 변화시켜 가며 그 특성을 조사하였다. $Ni^{2+}$의 흡착반응은 유사이차반응속도를 잘 따르는 것을 알 수 있었으며 $Ni^{2+}$의 초기농도가 증가함에 따라 유사이차반응속도상수($k_2$)는 감소하는 것으로 나타났다. 흡착평형을 표현하는데 널리 이용되는 Langmuir와 Freundlich 흡착 모델에 평형흡착 결과를 적용하였으며 Freundlich isotherm모델에 적합한 것으로 나타났다. 반응온도가 증가함에 따라 평형흡착량이 증가하여 흡착반응은 흡열반응의 양상을 보였으며 온도의 변화에 대한 실험결과로부터 ${\Delta}H^{\circ},\;{\Delta}G^{\circ}$ 그리고 ${\Delta}S^{\circ}$ 열역학적 변수를 도출하였다.

• 한국환경농학회지
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• 제33권3호
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• pp.169-177
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• 2014

본 연구는 철강산업에서 배출되는 산업폐기물의 일종인 페로니켈슬래그와 제강급랭슬래그의 인공습지나 여과시스템에서 인을 효과적으로 흡착 처리하기 위해 페로니켈슬래그와 제강급랭슬래그를 입경별(유효입경: 0.5 mm, 2.5 mm)로 구분하여 Freundlich 및 Langmuir 등온흡착실험을 통해 인에 대한 흡착특성을 조사하였다. Freundlich 등온흡착식에 의한 페로니켈슬래그(FNS)와 제강급랭슬래그(RCS)의 인 흡착능(K)은 RCS 0.5(0.5105) > RCS 2.5(0.3571) > FNS 2.5(0.0545) ${\fallingdotseq}$ FNS 0.5(0.0400) 순이었으며, 본 실험에 사용된 모든 슬래그의 흡착강도(1/n) 값이 0.19954-0.3657범위로 1보다 작으므로 모두 L형의 등온흡착식으로 판단 할 수 있었다. Langmuir 등온흡착식에 의한 인의 최대흡착능(a)은 FNS 0.5, FNS 2.5, RCS 0.5, RCS 2.5가 각각 320, 187, 3,582 및 2,983 mg/kg이었다. 슬래그의 실제 흡착량과 Freundlich와 Langmuir 등온흡착 일반식을 적용한 결과 실제 인의 흡착량은 전반적으로 Langmuir 등온흡착식이 Freundlich 등온흡착식에 비해서 잘 일치하였다. 이상의 결과를 미루어 볼 때, Freundlich와 Langmuir 등온흡착식을 이용한 슬래그의 인 흡착능력은 제강급랭슬래그(RCS)가 페로니켈슬래그(FNS)보다 높았으며, 고로급랭슬래그는 인공습지나 여과시스템에서 인 흡착을 위한 여재로 적용이 가능할 것으로 판단된다.

• 한국환경농학회지
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• 제36권1호
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• pp.22-28
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• 2017

본 연구는 커피찌꺼기의 환경친화적인 재활용 방안을 모색하기 위하여 커피찌꺼기 biochar를 제조하고, 제조된 biochar를 이용하여 구리에 대한 흡착특성을 평가하였다. 커피찌꺼기 biochar에 대한 구리의 흡착은 반응 2시간 이내에 급격하게 일어나는 것을 알 수 있었으며, 2시간 이후부터는 천천히 평형상태에 도달하는 것을 알 수 있었다. 등온흡착 실험의 결과 Langmuir 및 Freundlich 등온흡착식 모두에서 CB600이 CB300에 비해 높은 흡착능을 보였다. 커피찌꺼기 biochar에 대한 구리의 흡착능 예측을 위한 최적모델로는 동적흡착모델의 경우 유사이차속도반응식, 그리고 등온흡착모델의 경우 Langmuir 등온식이 더 적합하였다. 또한 SEM-EDS 분석결과 구리 흡착 후 biochar 표면에 구리가 매우 높은 농도로 흡착되어 있었으며, 이들의 흡착은 biochar 표면의 양이온 교환과 밀접한 관계가 있을 것으로 판단된다. 이상의 결과를 미루어볼 때, 커피찌꺼기는 biochar 제조를 위한 재료로 충분히 활용이 가능하며, 구리 흡착제로 활용이 가능할 것으로 판단된다.

• Advances in environmental research
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• 제4권3호
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• pp.197-210
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• 2015

Hexavalent chromium [Cr (VI)] adsorption on lateritic soil and lateritic soil blended with black cotton (BC) soil, marine clay and bentonite clay were studied in the laboratory using batch adsorption techniques. In the present investigation the natural laterite soil was blended with 10%, 20% and 30% BC soil, marine clay and bentonite clay separately. The interactions on test soils have been studied with respect to the linear, Freundlich and Langmuir isotherms. The linear isotherm parameter, Freundlich and Langmuir isotherm parameters were determined from the batch adsorption tests. The adsorption of Cr (VI) on natural laterite soil and blended laterite soil was determined using double beam spectrophotometer. The distribution coefficients obtained were 1.251, 1.359 and 2.622 L/kg for lateritic soil blended with 10%, 20% and 30% BC soil; 5.396, 12.973 and 48.641 L/kg for lateritic soil blended with marine clay and 5.093, 8.148 and 12.179 L/kg for lateritic soil blended with bentonite clay respectively. The experimental data fitted well to the Langmuir model as observed from the higher value of correlation coefficient. Soil pH and iron content in soil(s) has greater influence on Cr (VI) adsorption. From the study it is concluded that laterite soil can be blended with clayey soils for removing Cr (VI) by adsorption.