• 한국습지학회지
• /
• 제18권1호
• /
• pp.39-44
• /
• 2016

최근 커피 이용량이 증가하면서 폐커피가루의 활용에 대한 관심이 환경공학 분야에서 높아지고 있다. 본 연구에서는 폐커피가루를 재활용하여 오염물질에 대한 흡착제로서의 사용 가능성을 평가하기 위하여 액상의 유기 오염물질(메틸렌 블루)에 대한 흡착평형실험 및 흡착속도실험을 수행하였고, 입상활성탄 및 분말활성탄을 이용한 실험결과와 비교하였다. 실험 결과, 흡착평형의 경우 세 종류의 흡착제 모두 Langmuir 식에 잘 맞는 것으로 확인되었으며, 최대흡착량은 분말활성탄(178.6 mg/g), 폐커피가루(60.6 mg/g), 입상활성탄(15.6 mg/g) 순으로 확인되었다. 흡착속도실험에서도 유사 1차식 및 유사 2차식 모두에서 폐커피가루가 입상활성탄보다 우수한 것으로 확인되었다. 이는 폐커피가루의 입자 크기가 입상활성탄보다 작으며 표면이 입상 및 분말활성탄과 같이 다공성 특성을 띄고 있기 때문인 것으로 판단되었다.

• 한국환경과학회지
• /
• 제20권2호
• /
• pp.241-249
• /
• 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).

• Korean Chemical Engineering Research
• /
• 제53권3호
• /
• pp.309-314
• /
• 2015

야자계 활성탄을 사용하여 수용액으로부터 brilliant blue FCF 염료의 흡착에 대해 조사하였다. 회분식 실험은 흡착제의 양, 초기농도와 접촉시간과 온도를 흡착변수로 사용하여 수행하였다. 흡착평형자료는 Langmuir와 Freundlich 식을 사용하여 해석하였으며, Freundlich 식이 더 좋은 일치도를 나타냈다. 평가된 Freundlich 상수(1/n=0.129~0.212)로부터 활성탄에 의한 brilliant blue FCF의 흡착조작이 적절한 처리방법이 될 수 있음을 알았다. 흡착속도실험자료를 유사일차반응속도식과 유사이차반응속도식에 적용해 본 결과, 흡착동력학은 유사이차반응속도식에 잘 맞는 것으로 나타났다. 음수값의 Gibbs 자유에너지(-4.81~-10.33 kJ/mol)와 양수값의 엔탈피(+78.59 kJ/mol)는 흡착이 자발적이고 흡열공정으로 진행된다는 것을 나타낸다.

• Membrane and Water Treatment
• /
• 제12권2호
• /
• pp.51-58
• /
• 2021

The natural weathered sand of basalt (WSB) has been used for the removal of cadmium from aqueous solution. The influence of various parameters i.e., contact time, pH, weathered sand of basalt dosage, particle size of the weathered sand of basalt, temperature and initial cadmium concentration were analyzed. Cadmium adsorption kinetics was well described by the pseudo second order model. Adsorption equilibrium for cadmium was properly well fitted to Langmuir isotherm model with maximum adsorption capacity 0.50 mg/g. Compared with the other experimental results using various kinds of adsorbents at a low concentration (1.0 mg/L or so) similar to that of this study, the cadmium removal efficiency using weathered sand of basalt was higher. It has been demonstrated that weathered sand of basalt has a available alternative adsorbent for cadmium when its initial concentration is low.

• 한국물환경학회지
• /
• 제27권2호
• /
• pp.141-146
• /
• 2011

Loess, a natural clay, was evaluated as an adsorbent for the decolorization of Acid Orange II, an azo and reactive dye, from aqueous solution. Adsorption studies were performed at $30^{\circ}C$ and the effect of reaction time, loess dosage, initial concentration, loess particle size, pH, agitation rate were investigated to determine the optimum operation conditions. The removal efficiencies of color were measured to evaluate the effectiveness of loess. From this study, it was found that optimal reaction time was 10 min. Color removal efficiencies of Acid Orange II were increased as higher loess dosage, initial concentration and agitation rate. However, color removal efficiencies decreased when pH is high and loess particle becomes large. Adsorption of Acid Orange II fitted to the pseudo-second-order rate kinetics more than first-order rate kinetics. Langmuir and Freundlich adsorption isotherm constants and correlation coefficients were calculated and compared. It was concluded that the adsorption data of Acid Orange II onto loess fitted to the Freundlich model more than Langmuir model.

• Bulletin of the Korean Chemical Society
• /
• 제27권11호
• /
• pp.1819-1824
• /
• 2006

The general objective of the present study was to investigate the potential application of the UV spectroscopic method for determination of the polymeric additives present in papermaking fibrous stock solutions. The study also intended to establish the surface-chemical retention model associated with the adsorption kinetics of additives on fiber surfaces. Polyamide epichlorohydrin (PAE) wet strength resin and imidazolinium quaternary (IZQ) softening agents were selected to evaluate the analytical method. Concentrations of PAE and IZQ in solution were proportional to the UV absorption at 314 and 400 nm, respectively. The time-dependent behavior of polymeric additives obeyed a mono-molecular layer adsorption as characterized in Langmuir-type expression. The kinetic modeling for polymeric adsorption on fiber surfaces was based on a concept that polymeric adsorption on fiber surfaces has two distinguishable stages including initial dynamic adsorption phase and the final near-equilibrium state. The simulation model predicted not only the real-time additive adsorption behavior for polymeric additives at high accuracy once the kinetic parameters were determined, but showed a good agreement with the experimental data. The spectroscopic method examined on the PAE and IZQ adsorption study could potentially be considered as an effective tool for the wet-end retention control as applied to the paper industry.

• 한국물환경학회지
• /
• 제21권1호
• /
• pp.14-20
• /
• 2005

A feasibility study has been conducted regarding the application of waste coffee grounds as an adsorbent for the treatment of nickel ion containing wastewater. The major variables which considered to influence the adsorbability of nickel ion were its initial concentration, reaction temperature, pH, and coexisting ion. The specific surface area of coffee grounds used in the experiment was found to be ca. $39.67m^2/g$, which suggesting its potential applicability as an adsorbent due to its relatively high surface area. In the experimental conditions, more than 90% of the initial amount of nickel ion was shown to adsorb within 15 minutes and equilibrium in adsorption was attained after 3 hours. The adsorption behavior of nickel ion was well explained by Freundlich model and kinetics study showed that the adsorption reaction was second-order. Adsorption was reduced with temperature and its change of enthalpy in standard state was estimated to be -807.05 kJ/mol. Arrhenius equation was employed for the calculation of the activation energy of adsorption and nickel ion was observed to adsorb on coffee grounds exoentropically based on thermodynamic estimations. As pH rose, the adsorption of nickel ion was diminished presumably due to the formation of cuboidal complex with hydroxide ion and the coexistence of cadmium ion was found to decrease the amount of nickel ion adsorption, which was proportional to the concentration of cadmium ion.

• Carbon letters
• /
• 제8권3호
• /
• pp.199-206
• /
• 2007

The activated carbon produced from rubber wood sawdust by chemical activation using phosphoric acid have been utilized as an adsorbent for the removal of Cu(II) from aqueous solution in the concentration range 5-40 mg/l. Adsorption experiments were carried out in a batch process and various experimental parameters such as effect of contact time, initial copper ion concentration, carbon dosage, and pH on percentage removal have been studied. Adsorption results obtained for activated carbon from rubber wood sawdust were compared with the results of commercial activated carbon (CAC). The adsorption on activated carbon samples increased with contact time and attained maximum value at 3 h for CAC and 4 h for PAC. The adsorption results show that the copper uptake increased with increasing pH, the optimum efficiency being attained at pH 6. The precipitation of copper hydroxide occurred when pH of the adsorbate solution was greater than 6. The equilibrium data were fitted using Langmuir and Freundlich adsorption isotherm equation. The kinetics of sorption of the copper ion has been analyzed by two kinetic models, namely, the pseudo first order and pseudo second order kinetic model. The adsorption constants and rate constants for the models have been determined. The process follows pseudo second order kinetics and the results indicated that the Langmuir model gave a better fit to the experimental data than the Freundlich model. It was concluded that activated carbon produced using phosphoric acid has higher adsorption capacity when compared to CAC.

• 공업화학
• /
• 제25권6호
• /
• pp.632-638
• /
• 2014

입상활성탄을 사용하여 new fuchsin 염료를 흡착하는데 필요한 흡착등온선과 흡착동역학 및 열역학 파라미터들에 대하여 조사하였다. 흡착평형은 Langmuir 흡착등온식이 가장 잘 맞았으며, 등온흡착평형관계로부터 Langmuir 식과 Freundlich 식의 분리계수를 평가한 결과, 분리계수값이 각각 $R_L$ = 0.023, 1/n=0.198로 입상활성탄에 의한 new fuchsin 염료의 흡착조작이 유효한 처리방법이 될 수 있음을 알았다. Dubinin-Radushkevich 식으로 구한 흡착에너지값(E = 0.002 kJ/mol)과 Temkin 식으로부터 구한 흡착열상수값(B = 1.920 J/mol)으로부터 흡착공정이 물리흡착공정임을 알았다. 흡착공정에 대한 동력학적 해석을 통해 흡착반응은 유사이차반응속도식이 유사일차반응속도식과 비교하여 일치도가 높은 것으로 나타났으며, 입자 내 확산이 흡착공정의 지배단계이었다. 열역학적 해석을 통해 평가된 엔탈피 변화값(92.49 kJ/mol)과 활성화에너지값(11.79 kJ/mol)으로부터 흡착공정이 흡열반응으로 진행되었다. 또한, 엔트로피 변화값이 313.7 J/mol K로 흡착공정의 무질서도가 증가하였다. 온도가 올라갈수록 자유에너지값이 감소하는 것은 활성탄에 대한 new fuchsin 염료의 흡착반응은 온도가 올라갈수록 자발성이 높아지는 것으로 판단되었다.

• 대한화학회지
• /
• 제16권1호
• /
• pp.1-5
• /
• 1972

The adsorption kinetics on a membrane filter have been studied by an introduction of acid or alkali in yttrium-90 solution. The change of the adsorption in the filtration process was determined by the filtrate activities with using a microsyringe filter holder connected with a syringe. The over all reaction rate obeyed a reversible first order reaction, and the rate constants thus obtained, showed the values of $k_1$ = 0.12 $sec^{-1}$ and $k_1'$ = 0.039 $sec^{-1}$. As a result of the present studies, it would be reasonable that the rate determining step of the adsorption reaction was the hydrolysis reaction of the adsorbed yttrium ions.