• 제목/요약/키워드: Kinetic and equilibrium studies

검색결과 89건 처리시간 0.021초

Batch and Flow-Through Column Studies for Cr(VI) Sorption to Activated Carbon Fiber

  • Lee, In;Park, Jeong-Ann;Kang, Jin-Kyu;Kim, Jae-Hyun;Son, Jeong-Woo;Yi, In-Geol;Kim, Song-Bae
    • Environmental Engineering Research
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    • 제19권2호
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    • pp.157-163
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    • 2014
  • The adsorption of Cr(VI) from aqueous solutions to activated carbon fiber (ACF) was investigated using both batch and flow-through column experiments. The batch experiments (adsorbent dose, 10 g/L; initial Cr(VI) concentration, 5-500 mg/L) showed that the maximum adsorption capacity of Cr(VI) to ACF was determined to 20.54 mg/g. The adsorption of Cr(VI) to ACF was sensitive to solution pH, decreasing from 9.09 to 0.66 mg/g with increasing pH from 2.6 to 9.9; the adsorption capacity was the highest at the highly acidic solution pHs. Kinetic model analysis showed that the Elovich model was the most suitable for describing the kinetic data among three (pseudo-first-order, pseudo-second-order, and Elovich) models. From the nonlinear regression analysis, the Elovich model parameter values were determined to be ${\alpha}$ = 162.65 mg/g/h and ${\beta}$ = 2.10 g/mg. Equilibrium isotherm model analysis demonstrated that among three (Langmuir, Freundlich, Redlich-Peterson) models, both Freundlich and Redlich-Peterson models were suitable for describing the equilibrium data. In the model analysis, the Redlich-Peterson model fit was superimposed on the Freundlich fit. The Freundlich model parameter values were determined to be $K_F$ = 0.52 L/g and 1/n = 0.56. The flow-through column experiments showed that the adsorption capacities of ACF in the given experimental conditions (column length, 10 cm; inner diameter, 1.5 cm; flow rate, 0.5 and 1.0 mL/min; influent Cr(VI) concentration, 10 mg/L) were in the range of 2.35-4.20 mg/g. This study demonstrated that activated carbon fiber was effective for the removal of Cr(VI) from aqueous solutions.

활성탄에 의한 아마란스 염료의 흡착동력학에 관한 연구 (Study on Adsorption Kinetic of Amaranth Dye on Activated Carbon)

  • 이종집
    • 청정기술
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    • 제17권2호
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    • pp.97-102
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    • 2011
  • 입상활성탄에 의한 아마란스 염료의 흡착특성을 회분식 실험을 통해 조사하였다. 아마란스 염료의 흡착동력학적 연구는 298, 308, 318 K에서 초기농도 100, 200, 300 mg/L의 수용액을 가지고 수행하였다. 입상활성탄에 의한 아마란스 염료의 흡착 평형관계는 298K에서 Langmuir 등온식이 잘 적용되었다. 유사일차반응속도식과 유사이차반응속도식을 사용하여 동력학 실험값을 평가한 결과, 유사이차반응속도식이 더 잘 맞았으며, 속도상수($k_2$) 값은 아마란스 초기농도 100, 200, 300 mg/L 에 대해 각각 0.1076, 0.0531 및 0.0309 g/$mg{\cdot}h$로 조사되었다. 활성화에너지, 표준엔탈피, 표준엔트로피 및 표준자유에너지를 평가하였다. 조사된 표준자유에너지값은 초기농도 200 mg/L 에서 -5.08 ~ -8.10 kJ/mol로 자발적인 공정임을 알 수 있었다. 엔탈피변화량이 양의 값인 38.89 kJ/mol을 나타내어 활성탄에 대한 아마란스 염료의 흡착이 흡열반응으로 일어난다는 것을 알 수 있었다.

흡착제의 흡착특성 규명을 위한 흡착모델의 적용성 평가(II)-흡착속도론을 중심으로 (Applicability of Theoretical Adsorption Models for Studies on Adsorption Properties of Adsorbents(II))

  • 나춘기;박현주
    • 대한환경공학회지
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    • 제33권11호
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    • pp.804-811
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    • 2011
  • 본 연구는 흡착제의 흡착특성을 이해하는데 이용되는 각종 흡착모델의 적용성을 평가하는데 목적이 있다. 이를 위해 상용의 음이온교환수지(PA-308)를 이용하여 질산성질소에 대한 흡착특성을 회분식 실험을 통해 조사하였다. 음이온교환수지에 의한 질산성질소의 속도실험 결과는 초기의 빠른 흡착과정과 후기의 느린 흡착 과정의 두 가지 단계의 과정으로 이원화되는 경향을 나타내었다. 1차 속도식과 2차 속도식 모두 전체 반응시간에서의 질산성질소에 대한 음이온교환수지의 흡착속도를 수식화 할 수 없었다. 초기의 빠른 흡착반응($t\leq$ 20분)은 1차 속도식에 따르고 외부확산에 의해 거의 지배되는 거동을 보이는 반면, 후기 느린 흡착반응(t > 20분)은 2차 속도 화학반응과 내부확산, 즉 세공 내 확산에 의해서 일어남을 알 수 있었다.

박리-재부착 이후의 재발달 난류경계층 II -난류 모델들에 관한 고찰- (Redeveloping Turbelent Boundary Layer after Separation-Reattachment(II) -A Consideration on Turbulence Models-)

  • 백세진;유정열
    • 대한기계학회논문집
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    • 제13권5호
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    • pp.999-1011
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    • 1989
  • 본 연구의 목적은 첫째, 재발달 경계층에서의 난류에서지 및 난류전단응력에 대한 전달방정식들의 각 항의 측정자료들을 보다 정확히 제시하고 항들간의 균형을 비교 평가함으로써 비평형 유동으로부터 평형유동으로 회복되는 과정을 검토하고, 둘째, 대표적인 난류 모델들로써 표존 k-.epsilon.모델 및 레이놀즈 응력 모델을 사용한 수치계산을 수행함으로써 이와같은 모델들이 비평형 유동을 서술함에 있어 발생될 수 있는 문제점들을 고찰하는데 있다.

Cr(VI) removal using Fe2O3-chitosan-cherry kernel shell pyrolytic charcoal composite beads

  • Altun, Turkan;Ecevit, Huseyin
    • Environmental Engineering Research
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    • 제25권3호
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    • pp.426-438
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    • 2020
  • In this study, cherry kernel shell pyrolytic charcoal was synthesized (CKSC) and composite beads were obtained by blending this pyrolytic charcoal with chitosan and Fe2O3 nanoparticles (Fe-C-CKSC). Cr(VI) adsorption from aqueous solutions by Fe-C-CKSC composite beads and CKSC adsorbents was studied comparatively. The effects of Cr(VI) initial concentration, adsorbent dosage, contact time, pH and temperature parameters on Cr(VI) adsorption were investigated. Adsorption reached an equilibrium point within 120 min for CKSC and Fe-C-CKSC adsorbents. The maximum Cr(VI) removal was obtained at the initial pH value of 1.56 for CKSC and 2.00 for Fe-C-CKSC. The optimum adsorbent dosage was found to be 5 g/L for CKSC and 3 g/L for Fe-C-CKSC. Based on the Langmuir model, the maximum adsorption capacities were calculated as 14.455 mg/g and 47.576 mg/g for CKSC and Fe-C-CKSC, respectively. Thermodynamic and kinetic studies were performed. As a result of adsorption kinetics calculations, adsorption was found to be consistent with the pseudo second order kinetic model. Characterization of the synthesized adsorbents was performed by SEM, BET, FTIR and elemental analysis. This study has shown that low cost adsorbents CKSC and Fe-C-CKSC can be used in Cr(VI) removal from aqueous solutions.

Ni(II)와 D-Penicillamine과의 착물형성반응에 대한 속도론적 및 평형에 관한 연구 (Kinetic and Equilibrium Studies on Complex Formation Between Ni(II) and D-Penicillamine in Aqueous Media)

  • 김용규;최성락
    • 대한화학회지
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    • 제30권5호
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    • pp.475-482
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    • 1986
  • $Ni^{2+}$와 D-penicillamine사이의 착물형성반응에 대한 반응속도 및 평형에 관한 수용액중에서 실시하였다. 속도론적 실험은 압력-급변법을 사용하여 pH8~9범위에서 실시하였다. D-Penicillamine은 질소와 유황원자를 주게로 하여 pH>9.2조건에서 $Ni^{2+}$이온에 배위하나 pH값 8.25∼9.07범위에서 총괄 안정도 상수값이 급격히 감소하며 비해리된 mercapto기가 결합에 참여하지 않는 것으로 밝혀졌다. 또한 이 착물 형성반응에 있어 율속단계는 $Ni^{2+}$이온의 내부 배위권으로 부터 물분자가 유리되는 과정임이 밝혀졌다.

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Equilibrium and kinetic studies for the removal of cationic dye using banana pith

  • El-Maghraby, Azza;Taha, Nahla A.
    • Advances in environmental research
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    • 제3권3호
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    • pp.217-230
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    • 2014
  • The large quantity of green cull bananas has the potential of being used industrially and, thereby, to improve banana economics and eliminate the large environmental problem presented by banana waste. Wastewaters from textile, cosmetics, printing, dying, food colouring, and paper-making industries are polluted by dyes. The adsorption of basic dye by waste banana pith was investigated by varying dye concentrations, adsorbent dose, particle size and agitation rate. The adsorption capacity was found to be maximum value of removal by using 0.1 g of sorbent with particle size 1mm at mixing speed 200 rpm for initial concentration 25 mg/l to reach value of approximate 89%. The Langmuir, Temkin and Freundlich adsorption models were used for mathematical description of the adsorption equilibrium and it was found that experimental data fitted very well to these models except Langmuir model. Adsorption of dye was applied on (pseudo-first and pseudo-second-order kinetics), and the experimental data was more fitted to pseudo second order. The results of this study showed that banana pith could be employed as effective and low-cost materials for the removal of dyes from aqueous solutions.

Developments and applications of a modified wall function for boundary layer flow simulations

  • Zhang, Jian;Yang, Qingshan;Li, Q.S.
    • Wind and Structures
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    • 제17권4호
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    • pp.361-377
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    • 2013
  • Wall functions have been widely used in computational fluid dynamics (CFD) simulations and can save significant computational costs compared to other near-wall flow treatment strategies. However, most of the existing wall functions were based on the asymptotic characteristics of near-wall flow quantities, which are inapplicable in complex and non-equilibrium flows. A modified wall function is thus derived in this study based on flow over a plate at zero-pressure gradient, instead of on the basis of asymptotic formulations. Turbulent kinetic energy generation ($G_P$), dissipation rate (${\varepsilon}$) and shear stress (${\tau}_{\omega}$) are composed together as the near-wall expressions. Performances of the modified wall function combined with the nonlinear realizable k-${\varepsilon}$ turbulence model are investigated in homogeneous equilibrium atmosphere boundary layer (ABL) and flow around a 6 m cube. The computational results and associated comparisons to available full-scale measurements show a clear improvement over the standard wall function, especially in reproducing the boundary layer flow. It is demonstrated through the two case studies that the modified wall function is indeed adaptive and can yield accurate prediction results, in spite of its simplicity.

폐굴껍질을 흡착제로 한 불소폐수 처리특성에 관한 연구 (Studies on the Adsarption Characteristics of Fluoride Ion-Containing Wastewater by Employing Waste Oyster Shell as an Adsorbent)

  • 이진숙;김동수
    • 한국물환경학회지
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    • 제23권2호
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    • pp.222-227
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    • 2007
  • The adsorption features of fluoride ion on the oyster shell have been investigated for the purpose of the employment of waste oyster shell as an adsorbent for the treatment of fluoride ion-containing wastewater. The major component of oyster shell was examined to be Ca with minor components of Na, Si, Mg, Al, and Fe. As the initial concentration of fluoride ion was raised, its absorbed amount was enhanced at equilibrium, however, the adsorption ratio of fluoride ion compared with its initial concentration was shown to be decreased. Also, adsorption of fluoride ion onto the oyster shell resulted in the formation of $CaF_2$ in the morphological structure of adsorbent. Kinetic analysis showed that the adsorption reaction of fluoride ion generally followed a second order reaction with decreasing rate constant with the initial concentration of adsorbate. Freundlich model agreed well with the adsorption behavior of fluoride ion at equilibrium and the adsorption reaction of fluoride ion was examined to be endothermic. Several thermodynamic parameters for the adsorption reaction were calculated based on thermodynamic equations and the activation energy for the adsorption of fluoride ion onto oyster shell was estimated to be ca. 13.589 kJ/mole.

Equilibrium and kinetic studies on the adsorption of copper onto carica papaya leaf powder

  • Varma V., Geetha;Misra, Anil Kumar
    • 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.