The adsorption process using GAC is one of the most secured methods to remove of phosphate from solution. This study was conducted by impregnating Cu(II) to GAC(GAC-Cu) to enhance phosphate adsorption for GAC. In the preparation of GAC-Cu, increasing the concentration of Cu(II) increased the phosphate uptake, confirming the effect of Cu(II) on phosphate uptake. A pH experiment was conducted at pH 4-8 to investigate the effect of the solution pH. Decrease of phosphate removal efficiency was found with increase of pH for both adsorbents, but the reduction rate of GAC-Cu slowed, indicating electrostatic interaction and coordinating bonding were simultaneously involved in phosphate removal. The adsorption was analyzed by Langmuir and Freundlich isotherm to determine the maximum phosphate uptake(qm) and adsorption mechanism. According to correlation of determination(R2), Freundlich isotherm model showed a better fit than Langmuir isotherm model. Based on the negative values of qm, Langmuir adsorption constant(b), and the value of 1/n, phosphate adsorption was shown to be unfavorable and favorable for GAC and GAC-Cu, respectively. The attempt of the linearization of each isotherm obtained very poor R2. Batch kinetic tests verified that ~30% and ~90 phosphate adsorptions were completed within 1 h and 24 h, respectively. Pseudo second order(PSO) model showed more suitable than pseudo first order(PFO) because of higher R2. Regardless of type of kinetic model, GAC-Cu obtained higher constant of reaction(K) than GAC.

In this study, Bacillus sp. SRCM 112835 was isolated from soybean paste (Doenjang, Korean Fermented Soy Paste). Bacillus sp. SRCM 112835 showed biosorption of the Cu (II) in aqueous solution. The strain effectively absorbed 30.2% of the Cu (II) from a 52.3 mg/L within 60 min. The properties of the Bacillus sp. SRCM 112835 were investigated by Fourier transform infrared spectroscopy (FT-IR), point of zero charge (pHpzc), and phylogenetic analysis. The influence of initial pH (2.08-9.98) and biomass dosage (0.005-0.07 g) were likewise probed. Isotherm and kinetic experiment results suggested that the Langmuir isotherm and pseudo-second-order kinetic models well-fitted the experimental data, respectively.

탄소전극과 이온교환막을 결합한 축전식 탈염(CDI)을 이용하여 셀 구조와 셀 전위에 따른 구리 이온의 제거 특성을 연구하였다. 탄소전극과 이온교환막의 결 합 방식에 따라 4종류의 셀에 대해 실험한 결과 양이온, 음이온교환막을 결합한 셀(MCDI)에서 구리 이온의 제거율과 전하효율이 가장 높은 것으로 나타났다. 셀 전위에 따른 영향을 분석한 결과 0.6 V 이하에서는 전기이중층에 의한 전기 흡착(electrosoprtion)에 의해, 그리고 0.6 V 이상에서는 구리 이온의 전착 (electrodepostion)반응에 의해 구리 이온이 제거됨을 확인하였다. 또한 1.2 V 이상에서는 물이 전기분해되어 전하효율이 감소하였다. MCDI 셀의 운전결과 전하효율은 80% 정도로 구리 이온을 포함한 중금속 이온을 제거하는데 효과적인 것으로 판단되었다.

탄소전극과 이온교환막을 결합한 막결합 축전식 탈염(MCDI) 셀을 이용하여 환원전위가 다른 Na+과 Cu2+ 이온 혼합용액에서 Cu2+ 이온의 제거 특성을 연구 하였다. MCDI 셀에 일정한 전류밀도(1.5 mA/cm2)를 공급하면서 탈염을 실시한 결과 Cu2+ 이온은 일정한 제거속도를 유지하였지만 Na+ 이온의 제거량은 시간에 따라 감소하였다. 이는 Cu2+ 이온은 전착반응에 의해, Na+ 이온은 전기흡착 반응에 의해 제거되기 때문인 것으로 판단된다. Cu2+ 이온의 당량비가 0.14, 0.38, 0.50인 혼합용액을 탈염한 결과 제거된 이온 중 Cu2+ 이온의 당량비는 각 각 0.27, 0.60, 0.79로 나타났다. 이를 통해 Cu2+ 이온의 전착반응에 의해 혼합용 액에서 Cu2+ 이온의 제거율을 증가시킬 수 있음을 알 수 있었다.

The oxygen and nitrogen enriched activated carbons were obtained from modification of commercial activated carbon by using nitric acid, sodium hydroxide and urea. Zeta-potentials of modified activated carbons were investigated in relation to copper ion adsorption. The structural properties of modified activated carbons were not so much changed, but the zeta-potentials and isoelectric points were considerably changed. The zeta-potential of nitric acid modified activated carbon was the most negative than other activated carbons in the entire pH region, and the pHIEP was shifted from pH 4.8 to 2.6, resulted in the largest copper ion adsorption capacities compare with other activated carbons in the range of pH 3~6.5. In case of urea modified activated carbon, copper ion adsorption was larger than that of the as-received activated carbon from pH 2 to pH 6.5 even though the pHIEP was shifted to pH 6.0, it was due to the coordination process operated between nitrogen functional groups and copper ion. The adsorption capacity of copper ion was much influenced by zeta-potential and pHIEP of carbon adsorbent.

In this work, activated carbon fibers (ACFs) were plated with copper metal using electroless plating method and the effects of surface properties and pore structures on chromium adsorption properties were investigated. Surface properties of ACFs have been characterized using pH and acid/base values. BET data with N2 adsorption were used to obtain the structural parameters of ACFs. The electroless copper plating did significantly lead to a decrease in the surface acidity or to an increase in the surface basicity of ACFs. However, all of the samples possessed a well-developed micropore. The adsorption capacity of Cr(III) for the electroless Cu-plated ACFs was higher than that of the as-received, whereas the adsorption capacity of Cr(VI) for the former was lower than that of the latter. The adsorption rate constants (K1, K2, and K3) were also evaluated from chromium adsorption isotherms. It was found that K1 constant for Cr(III) adsorption depended largely on surface basicity. The increase of Cr(III) adsorption and the decrease of Cr(VI) adsorption were attributed to the formation of metal oxides on ACFs, resulting in increasing the surface basicity.

폐-광석으로부터 금속구리분말을 회수하기 위하여 더미 미생물용출, Fe 제거와 전기분해실험을 수행하였다. Cu가 0.034% 함유된 폐-광석시료에 대하여 더미 용출실험을 수행한 결과, Cu 용출률은 박테리아 용출-용액에서 61%, 황산 용출-용액에서 62%로 나타났다. Fe를 효과적으로 제거하기 위하여 더미 용출-용액에 NaOH, H2O2 및 Ca(OH)2를 각각 적용한 결과 H2O2가 가장 효과적인 Fe 제거제로 선정되었다. 전해질 용액을 준비하기 위하여 H2O2를 더미 용출-용액에 처리한 결과 박테리아 용출-용액에서 Fe가 99%, 황산 용출-용액에서 60%로 제거된 반면에 Cu 제거율은 각각 5%와 7%로 나타났다. 이 용액에 대하여 전기분해 실험을 수행한 결과 Cu 회수율이 박테리아 용출-용액에서 98%, 황산 용출-용액에서 76%로 나타났다. 모수석 형태의 금속구리분말이 양쪽 용출-용액에서 회수되었다.

PVA-D2EHPA/TOPO beads containing two extractants, di-(2-ethylhexyl) phosphoric acid (D2EHPA) and trioctylphoshine oxide (TOPO) were prepared for the removal of copper ions from aqueous solution. The prepared PVA-D2EHPA/TOPO beads were characterized by SEM and FT-IR. The removal characteristics of copper ions by PVA-D2EHPA/TOPO beads was investigated using batch and continuous systems. In batch experiments, the maximum removal capacity calculated from Langmuir isotherm model was 18.6 mg/g and the optimal pH was in the range of 4.5 ∼6. The continuous experiments showed that the removal capacity of copper ions increased with increasing inlet copper ion concentrations and bed heights, but decreased with increasing inlet flow rates.