Batch adsorption tests were performed to evaluate the applicability of adsorption kinetic model by using hydrogel chitosan bead crosslinked with glutaraldehyde (HCB-G) for Cu(II) as cation and/or phosphate as anion. Pseudo first and second order model were applied to determine the sorption kinetic property and intraparticle and Boyd equation were used to predict the diffusion of Cu(II) and phosphate at pore and boundary-layer, respectively. According to the value of theoretical and experimental uptake of Cu(II) and phosphate, pseudo second order is more suitable. On comparison with the value of adsorption rate constant (k), phosphate kinetic was 2-4 times faster than that of Cu(II) at any experimental condition indicating the electrostatic interaction between NH3 + and phosphate is dominated at the presence of single component. However, when Cu(II) and phosphate simultaneously exist, the value of k for phosphate was sharply decreased and then the difference was not significant. Both diffusion models confirmed that the sorption rate was controlled by film mass transfer at the beginning time (t < 3 hr) and pore diffusion at next time section (t > 6 hr).

4가지 서로 다른 소재(대나무, 목재, 피탄, 석탄)로 제조된 10가지 활성탄에 대해서, 30% 알코올모델용액에 용해되어 있는 6가지 휘발성화합물(isoamyl alcohol, hexanal, furfural, ethyl lactate, ethyl octanoate, 2-phenyl ethanol)의 흡착효율을 평가하였다. 이들 6가지 휘발성화합물은 알코올음료에서 종종 발견되며, 농도가 높을 경우에는 숙취의 원인이 될 뿐만이 아니라 위스키나 보드카와 같은 술에서 이취의 원인물질이 되기도 한다. 6가지 휘발성화합물이 용해되어 있는 30% 알코올모델용액 200 mL에 0.2 g의 활성탄을 넣고 16시간 일정한 속도로 교반한 후에 처리된 용액을 2가지 시료처리방법(direct liquid injection and headspace-solid phase microextraction)을 이용 GC분석을 수행하여 활성탄의 제거효율을 구하였다. 활성탄의 제거효율은 휘발성화합물의 종류와 활성탄제조의 소재에 따라 차이가 있었으며, ethy octanoate, 2-phenyl ethanol, hexanal에 대한 제거율은 34-100%로 높은 편이나, isoamyl alcohol, ethyl lactate, furfural의 제거율은 5-13%로 비교적 낮은 편이었다. 활성탄의 종류에 따른 제거율은 대나무활성탄인 A가 isoamly alcohol, hexanal, ethyl lactate, furfural 등 대부분의 휘발성화합물에 대해서 유의적으로 높았으며(p < 0.05), 특히 알코올음료에서 숙취와 이취물질이며 fusel oil의 주성분인 isoamyl alcohol, aldehydes(hexanal, furfural), 2-phenyl ethanol에 대한 흡착효율이 높은 것으로 확인되었다.

Basic dyes, Rhodamine 6G(R6G), Rhodamine B(RB), and Methylene Blue(MB), dissolved in water were used to investigate single-component adsorption affinity to the pearl layer fractionated according to the size. Unfractionated pearl layers were also used as adsorbents for the R6G and RB. The Langmuir and the Redlich-Peterson(RP) models were used to fit the adsorption data, and the goodness of fit was examined by using determination coefficient(R2) and standard deviation(SSE). The 3-parameter RP model was found to be better in describing the dye adsorption data than the 2-parameter Langmuir model, as can be expected from the number of parameters involved in the model. The adsorption affinity to the fractionated pearl layer was higher than that to the unfractionated layer. The affinity order to the fractionated Conchiolin layer was found to be R6G > MB > RB. Furthermore, the dye adsorption capacity of the various types of pearl layer was found to be in the order, the fractionated pearl > powdered pearl > unfractionated pearl, exhibiting different adsorption isotherms according to the types of layer used in the study.

Surface complexation models(SCMs) have been performed to predict metal ion adsorption behavior onto the mineral surface. Application of SCMs, however, requires a self-consistent approach to determine model parameter values. In this paper, in order to determine the metal ion adsorption parameters for the triple layer model(TLM) version of the SCM, we used the zeta potential data for Zeolite and Kaolinite, and the metal ion adsorption data for Pb(Ⅱ) and Cd(Ⅱ). Fitting parameters determined for the modeling were as follows ; total site concentration, site density, specific surface area, surface acidity constants, etc. Zeta potential as a new approach other than the acidic-alkalimetric titration method was adopted for simulation of adsorption phenomena. Some fitting parameters were determined by the trial and error method. Modeling approach was successful in quantitatively simulating adsorption behavior under various geochemical conditions.