• Journal of the Korean Chemical Society
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• v.54 no.3
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• pp.300-309
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• 2010

The ability of sodium-exchanged clay particles as an adsorbent for the removal of commercial dyes, Methylene blue (MB) and Malachite green oxalate (MG) from aqueous solutions has been investigated under various experimental conditions. The effect of the experimental parameters, such as pH solution, agitation time, adsorbate concentration and adsorbent dose were examined. Maximum adsorption of dyes, i.e. >90% has been achieved in aqueous solutions using 0.03 g of clay at a pH of 7 and 298 K for both dyes. The adsorption process was a fast and the equilibrium was obtained within the first 5 min. For the adsorption of both MB and MG dyes, the pseudo-second-order reaction kinetics provides the best correlation of the experimental data. The adsorption equilibrium results follow Langmuir and Dubini-Radushkevich (D-R) isotherms with high regression coefficients $R^2$ > 0.98. The mean free energies $E_a$ of adsorption from D-R model were 3.779 and 2.564 kj/mol for MB and MG respectively, which corresponds to a physisorption process.

• Proceedings of the Korean Institute of Surface Engineering Conference
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• 2017.05a
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• pp.131-131
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• 2017

알루미늄은 내식성, 내마모성과 같은 물리적, 화학적 성질이 우수하지 못하여 이를 향상시키기 위해서 양극산화법이 산업적으로 널리 사용되고 있다. 알루미늄 양극산화법을 적용하면 강도, 내마모성 및 내식성이 향상될 뿐만 아니라 알루미늄 표면에 규칙적으로 배열된 30nm~100nm 크기의 pore에 염료를 흡착시켜 다양한 색상의 외관을 가지는 양극산화피막을 형성시킬 수 있다. Pore간의 간격은 수십nm~수백nm 정도이며, pore의 크기와 간격 및 깊이는 양극산화조건(양극산화 전압, 전해액의 종류와 농도 및 온도)에 의해 크게 변화된다. 또한 염료의 농도와 착색 시간에 따라서 양극산화 피막의 색조가 변화되는 것으로 알려져 있다. 따라서 본 연구에서는 양극산화피막의 색조에 미치는 전해조건의 영향을 조사하고, 분광측색계를 사용하여 산화피막의 색조를 정량적으로 분석하고 또한 산화피막의 pore에 흡착된 염료를 정량분석하기 위해서 UV-visible을 사용하여 분석하였다. Al5052 합금을 이용하여 에칭, 양극산화, 착색처리, 봉공(sealing)처리를 실시하였다. $55^{\circ}C$ 100g/L NaOH 용액에서 에칭을, $25^{\circ}C$ 10 vol.% $HNO_3$ 용액에서 디스머트를 실시한 다음, $25^{\circ}C$ 10 vol.% $H_2(SO_4)$ 용액에서 15V의 정전압으로 양극산화를 실시하였다. 이후, $55^{\circ}C$ 5~8g/L의 오렌지, 블랙 착색염료(일본 OKUNO 사(社)의 TAC-LH(301), TAC-BLH(411))를 사용하여 착색처리를, $85^{\circ}C$ 초산니켈 수용액에서 봉공처리를 실시하였다. 착색조건으로는 양극산화 시간(5분, 10분, 15분, 20분), 착색 시간(15초, 1분, 2분, 5분) 및 착색 농도(오렌지 -2.5g/L, 5g/L, 7.5g/L, 블랙 - 4g/L, 8g/L, 12g/L)를 변화시켰으며, 산화피막의 색조를 정량 분석하기 위해 분광측색계를 사용하였고 흡착된 염료의 농도를 정량 분석하기 위해서 $55^{\circ}C$, 1M NaOH에 재용해하여 UV-visible로 흡광도를 측정하였다. 양극산화피막의 색조는 양극산화 시간이 길어질수록, 착색시간이 길어질수록, 착색농도가 진할수록 산화피막에 흡착되는 염료의 양이 증가하며 색조가 더 선명해지고 진해지는 것을 확인하였다. 이를 분광측색계로 분석하였을 때 각 전해조건하에서 경향성을 나타내었다. 또한 흡광도 측정을 통해 계산한 염료의 양과 전해조건의 상관관계를 조사하였다. 양극산화 시간이 길어지면 산화피막의 두께가 증가하여 염료가 흡착될 수 있는 표면적이 넓어지고, 착색 시간이 길어지면 동일한 산화피막에 더 많은 염료가 흡착이 된다. 그리고 착색 농도가 진할수록 동일면적, 동일시간 하에서 더 많은 염료가 흡착되어 결과적으로 전해조건이 강해질수록 산화피막의 색조가 진해지는 것으로 판단된다.

• Textile Coloration and Finishing
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• v.7 no.2
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• pp.86-91
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• 1995

탄소 섬유란 높은 강도, 높은 탄성률 등을 갖고 잇는 소재로서, 복합 재료에 이용되고 있다. 최근에는 스포츠 용품에 대해서도 장식성이 필요한 시대가 되어서 탄소 섬유도 착색할 필요가 있게 되었다. 일반 의류용 섬유를 염색할 때 염료가 섬유를 구성하는 분자에 단분자상으로 흡착한다. 섬유란 사실상 투명하기 때문에 빛이 섬유 내부에 흡착된 염료까지 도달하고, 염료는 빛을 흡수하여 발색한다. 그러나 탄소 섬유의 색은 검고, 빛이 섬유 내부까지 미치지 못하기 때문에 만약 탄소 섬유에 염료를 흡착시키더라도 염료는 발색하지 않게 된다. 한편 검은 탄소 섬유를 표백해서 백색으로 만들기 위해 예를 들어 불소와 반응시키면 검은 탄소 섬유가 백색이 되기는 하지만, 이 불소와 반응한 탄소섬유는 대단히 부서지기 쉬워서, 섬유로 사용할 수 없게 된다. 따라서 탄소섬유는 검은 색 그대로 착색시키지 않으면 안된다. 즉 탄소 섬유는 섬유의 표면에 도료와 같은 색소 층을 붙여서 착색하게 된다.

• Proceedings of the Korean Society of Dyers and Finishers Conference
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• 2009.11a
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• pp.41-42
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• 2009

천연가죽 제조 공정에서 유해성 금속성 성분인 크롬이 전혀 함유되지 않은 비크롬 가죽을 제조한 후에 염색 공정에서 다색성 염료인 오배자와 소목을 각각 원료피 무게대비 5%를 사용하고, 매염제를 2~3% 사용하여 염료의 흡착성 증대, 음이온성 가지제 10~12%를 사용하여 가죽에 유연성 및 매염제의 표면 흡착성 증대를 통해서 천연염료에는 존재하지 않는 블랙색상의 가죽을 제조하였다.

• Applied Chemistry for Engineering
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• v.25 no.6
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• pp.632-638
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• 2014

Batch adsorption studies including equilibrium, kinetics and thermodynamic parameters for the adsorption of new fuchsin dye using granular activated carbon were investigated with varying the operating variables such as initial concentration, contact time and temperature. Equilibrium adsorption data were fitted into Langmuir, Freundlich, Dubinin-Radushkevich and Temkin isotherms. Adsorption equilibrium was mostly well described by Langmuir Isotherm. From the estimated separation factor of Langmuir ($R_L$ = 0.023), and Freundlich (1/n = 0.198), this process could be employed as an effective treatment for the adsorption of new fuchsin dye. Also based on the adsorption energy (E = 0.002 kJ/mol) from Dubinin-Radushkevich isotherm and the adsorption heat constant (B = 1.920 J/mol) from Temkin isotherm, this adsorption is physical adsorption. From kinetic experiments, the adsorption reaction processes were confirmed following the pseudo second order model with good correlation. The intraparticle diffusion was a rate controlling step. Thermodynamic parameters including changes of free energy, enthalpy, and entropy were also calculated to predict the nature of adsorption. The change of enthalpy (92.49 kJ/mol) and activation energy (11.79 kJ/mol) indicated the endothermic nature of adsorption processes. The change of entropy (313.7 J/mol K) showed an increasing disorder in the adsorption process. The change of free energy found that the spontaneity of process increased with increasing the adsorption temperature.

• Proceedings of the KIEE Conference
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• 2011.07a
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• pp.1586-1587
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• 2011

염료 감응 태양전지(DSCs)는 최근 큰 발전을 이루고 있지만, 효율개선과 비용절감 등의 과제를 여전히 안고 있다. 염료 감응 태양전지(DSCs)의 효율 상승을 위해 염료, $TiO_2$ 산화물, 투명전극, 전해질 및 Pt 전극에 관한 연구가 활발히 진행 되고 있다. 본 연구에서는 염료 감응 태양전지(DSCs)의 특성 분석을 위해 $TiO_2$ 두께를 $20{\mu}m$로 지정하고 면적을 $0.5{\times}0.5\;Cm^2$에서 $1.5{\times}1.5\;Cm^2$까지 증가시켜 개방전압($V_{oc}$), 단락전류밀도($J_{sc}$), 충진률 FF(%), 광전변환효율(${\eta}$)등의 특성을 분석해 보았다. 또한 염료가 흡착되는 시간을 12시간과 24시간으로 변화시켜 최적의 특성을 가지는 DSCs를 연구해 보았다.

• Korean Chemical Engineering Research
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• v.55 no.6
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• pp.771-777
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• 2017

Adsorption characteristics of Eosin Y dye by carbon nano tubes (CNTs) were examined through batch experiments. CNTs used in the study had specific surface area of $106.9m^2/g$, porosity volume of $1.806cm^3/g$, and porosity diameter of $163.2{\AA}$, respectively. Adsorption experiments were carried out as function of contact time, initial solution pH (2~10), dye concentration (100, 150 and 200 mg/L), adsorbent dose (0.05~1.0 g) and temperature (293, 313 and 333 K). The adsorption was favoured at lower pHs and temperatures. Adsorption data were well described by the Langmuir model. The adsorption process followed the pseudo-second order kinetic model. The adsorption capacity decreased with increase in temperature. The results of the intraparticle diffusion model suggested that film diffusion and particle diffusion were simultaneously occured during the adsorption process. Thermodynamic studies suggested the spontaneous and endothermic nature of adsorption of Eosin Y dye onto CNTs.

• Clean Technology
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• v.20 no.3
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• pp.290-297
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• 2014

Batch adsorption studies were carried out for equilibrium, kinetics and thermodynamic parameters for adsorption of coomassi brilliant blue G (CBBG) using activated carbon with varying the operating variables like initial concentration, contact time and temperature. Equilibrium adsorption data were fitted into Langmuir, Freundlich and Dubinin-Radushkevich isotherms. From estimated separation factor of Langmuir and Freundlich, this process could be employed as effective treatment for removal of CBBG. Also from Dubinin-Radushkevich isotherm model, adsorption energy (E) indicated adsorption process is physical adsorption. From kinetic experiments, the adsorption reaction was found to confirm to the pseudo second order model with good correlation. Intraparticle diffusion was rate controlling step. Thermodynamic parameters like change of free energy, enthalpy, and entropy were also calculated to predict the nature of adsorption. The change of enthalpy (406.12 kJ/mol) indicated endothermic nature of the adsorption process. The change of entropy (1.66 kJ/mol K) showed increasing disorder in process. The change of free energy found that the spontaneity of process increased with increasing adsorption temperature.

• Journal of the Korean Chemical Society
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• v.54 no.1
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• pp.110-114
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• 2010

The equilibrium of adsorption of basics dyes RB 5 and BG 4 from a single dyes in the mixtures on the sodium-exchanged clay of the Maghnia (Algeria) was studied. The maximum adsorption capacities of BR5 and BG4 in single dyes were 465.13 and 469.90 mg/g respectively. In the simultaneous adsorption of BR5 and BG4 from mixture solutions, three different initials concentrations ratios R (R=$C_{(BR5)}/C_{(BG4)}$) were tested: 2.5/1, 1/1 and 1/2.5 using ADMI method. The isotherms adsorptions of dyes from the mixtures are characteristics of competition phenomenon. A very strong interaction between BR5 and BG4 for the active sites of adsorption of surface of clay is obtained for R = 1/1. The ratio R' (R'=$Qe_{(mixture)}/Qe_{(single)}$) of the adsorption capacity of BR5 and BG4 in the mixture were reduced by factor of 0.86, 0.74 and 0.84 for the initials concentrations ratios R (R=$C_{(BR5)}/C_{(BG4)}$) of 2.5/1, 1/1 and 1/2.5 respectively. The variation of the ratio of the adsorption capacity R‘ of BR5 and BG4 in the mixture solutions with initial concentration ratios R indicates that BR5 dye is slightly favourable in the competition adsorption than BG4. Langmuir and Freundlich models fit very well with adsorption behaviour of single dyes as well as the dyes in mixture solutions.

• Applied Chemistry for Engineering
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• v.23 no.5
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• pp.450-455
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• 2012

The paper includes the utlization of an activated carbon as a potential adsorbent to remove a hazardous fluorescein dye from an aqueous solution. Batch adsorption experiments were carried out for the removal of fluorescein dyes using a granular activated carbon as an adsorbent. The effects of various parameters such as pH, amount of adsorbent, contact time, initial concentration and temperature of the adsoprtion system were investigated. The experimental results revealed that activated carbon exhibit high efficiencies to remove fluorescein dyes from the aqueous solution. The equilibrium process can be well described by Freundlich isotherm in the temperature range from 298 K to 318 K. From adsorption kinetic experiments, the adsorption process followed a pseudo second order kinetic model, and the adsorption rate constant ($k_2$) decreased with increasing the initial concentration of fluorescein. The free energy of adsorption ${\Delta}G^0$), enthalpy ${\Delta}H^0$), and entropy (${\Delta}S^0$) change were calculated to predict the nature adsorption. The estimated values for ${\Delta}G^0$ were -17.11~-20.50 kJ/mol over an activated carbon at 250 mg/L, indicated toward a spontaneous process. The positve value for ${\Delta}H^0$, 33.2 kJ/mol, indicates that the adsorption of fluorescein dyes on an activated carbon is an endothermic process.