• 한국환경과학회지
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• 제11권7호
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• pp.729-735
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• 2002

In order to examine the inhibition effect of other heavy metal ions on the removal of heavy metal ions by crab shell in aqueous solution, 10 heavy metal ions $(Cr^{3+},\;Cd^{2+},\;Ni^{2+},\;Zn^{2+},\;Hg^{2+},\;Cu^{2+},\;Mn^{2+],\;Fe^{2+},\;Fe^{3+},\;Pb^{2+})$ were used as single heavy metal ions and mixed heavy metal ions, respectively. In single heavy metal ions, $Pb^{2+},\;Cr^{3+},\;Cu^{2+}$ were well removed by crab shell, however, $Cd^{2+},\;Ni^{2+},\;Zn^{2+},\;Mn^{2+}$ were not. The heavy metal removal increased as the increase of covalent index (Xm$^2$r), and the relationship classified heavy metal ions as 2 heavy metal groups $(Fe^{3+},\;Fe^{2+},\;Cu^{2+},\; Cr^{3+},\;Mn^{2+},\;Ni^{2+},\;Zn^{2+}\;group\;and\;Pb^{2+},\;Hg^{2+},\;Cd^{2+}\;group)$. In mixed heavy metal ions, the removals of $Fe^{2+},\;Fe^{3+},\;Pb^{2+},\;Cu^{2+}$ as 0.49 m㏖/g, regardless of the existence of other heavy metal ions, were similar to the result of single heavy metal ions experiment. The removals of $Mn^{2+},\;Cd^{2+},\;Ni^{2+}$ decreased as the existence of other heavy metal ions, however, the removal of $Zn^{2+},\;Cr^{3+},\;Hg^{2+}$ increased.

• 자원리싸이클링
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• 제13권2호
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• pp.3-8
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• 2004

석유화학공정에서 발생하는 산화철폐촉매를 이용하여 폐수 중 중금속회수에 관한 기초연구를 실시하였다. Zn, Ni, Cu, 및 Fe의 농도가 200mg/L인 각각의 합성폐수에 폐촉매 첨가량을 변화하여 실험한 바, 각 금속의 98% 회수율을 얻은 폐촉매 첨가량은 Cu 와 Fe 폐수 ：2％ 이상, Zn 폐수：3％ 이상, Ni 폐수 ：7％ 이상이었다. 또한 폐산화철 촉매로서 Zn, Ni, Cu 및 Fe 금속의 98％ 이상 회수할 수 있는 각각의 폐수 pH는 Ni： 10.6 이상, Cu： 8.0 이상, Fe：6.5 이상, Zn：8.5 이상이었다. 따라서 폐산화철 촉매에 의한 폐수 중 중금속 회수는 폐촉매의 알카리성분에 의한 침전이 주 메카니즘이고, 각 금속의 수산화침전 pH이하 폐촉매의 등전점(pH 3.0) 이상의 pH범위에서는 금속이온이 폐촉매 표면에서 물리흡착에 의해 일부 회수된다.

• 대한화학회지
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• 제46권6호
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• pp.502-508
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• 2002

본 실험은 N-Carbamoylglycine의 농도 결정에 PET sensor를 응용한 것이다.N-Carbamoylglycine이 금속 이온에 리간드로 작용하면서 착물을 만들고 있는 fluorophore의 luminescence intensity를 변화시킬수 있고 이를 통해 농도결정에 이용할 수 있다. 사용한 금속이 온은 $Ni^{2+}$, $Cu^{2+}$ 그리고 $Zn^{2+}$이며 비교대상으로 아세트산을 사용하여 선택성을 확인하였다. $Ni^{2+}$ 이온은 음이온 리간드에 의해서 eT mechanism 변화를 보여주었으며 , $Cu^{2+}$이온은 아세트산과 N-Carbamoylglycine을 구별하는 선택성을 가지고 있으며, $Zn^{2+}$이온은 매우 예민한 luminscence intensity 변화를 일으키는 것으로 나타났다.

• KSBB Journal
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• 제16권1호
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• pp.54-60
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• 2001

저품위 광석으로부터 유가 금속을 회수하기 위한 생물용출법의 적용에 있어 미생물의 활성은 매우 중요하며, 제련미생물은 금속이온에 대해 어느 정도 내성을 가지고 있어야 한다. 본 연구에서는 대표적인 제련미생물인 Thiobacillus ferrooxidans의 철산화속도에 미치는 단독 혹은 혼합 금속이온의 영향을 조사하여, T. ferrooxidans의 금속이온에 대한 내성 특성을 조사하였다. 생장 배지에 $Zn^{2+}$, $Cu^{2+}$, $Ni^{2+}$, 및 $Cd^{2+}$를 단독으로 첨가한 경우(첨가농도범위, $Zn^{2+}$ 60g/L이하, $Cu^{2+}$, $Ni^{2+}$, 및 $Cd^{2+}$ 6 g/L 이하)에는 T. ferrooxidans에 의한 철산화속도는 금속이온의 첨가량에 크게 저해 받지 않았다. $Zn^{2+}$를 제외한 $Cu^{2+}$, $Ni^{2+}$, 및 $Cd^{2+}$의 2 성분 혹은 3 성분의 혼합금속이온을 첨가한 경우에는 T. ferrooxidans의 철산화 활성에 대한 혼합 금속이온의 저해 효과는 최대 50% 정도로 크게 나타나지는 않았다. 그러나, $Zn^{2+}$을 타 금속이온과 2 성분 혹은 3 성분을 혼합하여 생장 배지에 첨가한 경우에는 T. ferrooxidans의 철산화 활성 저해에 대한 혼합 금속이온의 상승 효과가 큰 것을 밝혔다.

• 대한화학회지
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• 제30권6호
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• pp.526-531
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• 1986

95% 메탄올 용액에서 코발트(II), 니켈(II), 구리(II)와 아연(II)이온들과 1,15-diaza-3,4:12,13-dibenzo-5,8,11-trioxacycloheptadecane (NenOdien H$_4$, L)리간드와의 안정도 상수를 전위차 적정법으로 25$^{\circ}$C 에서 결정하였다. 그 결과 착물의 형성은 리간드내의 주게원자의 영향을 받으며 안정도 상수의 크기는 Co(II) < Ni(II) < Cu(II) > Zn(II)의 순위이였다. 한편 고체착물의 구조를 분광광도법, 원소분석 및 전기전도도법의 결과로부터 논의하였다. 그 결과 고체상태의 화학조성과 기하구조는 팔면체의 $[CoL_2(OH_2)Cl]Cl{\cdot}2H_2O$, 팔면체의 $[NiL_2(OH_2)Cl]Cl{\cdot}2H_2O$, 사각피라밋형의 [CuLCl]Cl, 그리고 팔면체의 $[ZnLCl_2]{\cdot}\frac{1}{2}H_2O$임을 알 수 있었다.

• Bulletin of the Korean Chemical Society
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• 제31권6호
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• pp.1633-1637
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• 2010

The UV-vis absorption spectrum of protoporphyrin IX shows a very sharp and strong absorption maximum peak at 398 nm in acetonitrile-water mixture solution (1:1 v/v). When divalent metal ions such as $Cu^{2+}$, $Zn^{2+}$, and $Ca^{2+}$ ion were added to protoporphyrin IX, metal protoporphyrin IX complexes were thereby produced. Cu-protoporphyrin IX complexes have the largest formation constant ($K_f$) among them. The fluorescence intensity of protoporphyrin IX was diminished by the presence of $Cu^{2+}$, $Zn^{2+}$, $Ca^{2+}$, $Mn^{2+}$, and $Ni^{2+}$ ions as quenchers. However, $Mg^{2+}$, $Mn^{2+}$, and $Ni^{2+}$ ions are hardly combined with protoporphyrin IX. $Mg^{2+}$ ion does not take part in the fluorescence quenching process of protoporphyrin IX in acetonitrile-water mixture solution. According to the Stern-Volmer plots, fluorescence quenching by $Cu^{2+}$, $Zn^{2+}$, and $Ca^{2+}$ ions involves static quenching, which is due to complex formation. On the contrary, dynamic quenching has a large influence on the overall quenching process, when $Mn^{2+}$ and $Ni^{2+}$ ions were added to protoporphyrin IX in acetonitrile-water mixture solution.

• Applied Biological Chemistry
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• 제20권3호
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• pp.300-309
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• 1977

The information related to the heavy metal pollution in the environment was obtained from studies on the effects of pH, phosphate and soil properties on the adsorption of metal ions (Cd, Cu, Ni, and Zn) by soils. Three soil materials; soil 1 with low CEC (8.2 me/100g) and low organic carbon content (0.34%); soil 2 with high CEC (36.4 me/100g) and low organic carbon content (1.8%) and soil 3 with high CEC (49.9 me/100g) and high organic carbon content (14.7%) were used. Soils were adjusted to several pH's and equilibrated with metal ion mixtures of 4 different concentrations, each having equal equivalents of each metal ion (0.63, 1.88, 3.12 and 4.38 micromoles per one gram soil with and without 10 micromoles of phosphate per one gram soil). Reported here are the results of the equilibrium study on soil I. The rest of the results on soil 2 and soil 3 will be repoted subsequeutly. Generally higher metal ion concentration solution resulted in higher final metal ion concentrations in the equilibrated solution and phosphate had minimal effect except it tended to enhance removal of cadmium and zinc from equilibrated solutions while it tended to decrease the removal of copper and nickel. In soil 1, percentages of added metal ions removed at pH 5.10 were; Cu 97, Ni 69, Cd 63, and Zn 55, while increasing pH to 6.40, they were increased to Cu 90.9, Zn 99, Ni 96, and Cd 92 per As initial metal ion concentration increased, final metal ion concentrations in the equilibrated solution showed a relationship with pH of the system as they fit to the equation $p[M^{++}]=a$ pH+b where $p[M^{++}]=-log$[metal ion concentration in Mol/liter]. The magnitude of pH and soil effects were reflected in slope (a) of the equation, and were different among metal ions and soils. Slopes (a) for metal ions in the aqueous system are all 2. In soil 1 they were; Zn 1.23, Cu 0.99, Ni 0.69 and Cd 0.59 at highest concentration. The adsorption of Cd, Ni, and Zn in soil 1 could be represented by the Iangmuir isotherm. However, construction of the Iangmuir isotherm required the correction for pH differences.

• Bulletin of the Korean Chemical Society
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• 제17권9호
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• pp.790-793
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• 1996

The azacrown compound, 1,7-dioxa-4,10,13-triazacyclopentadecane-N,N',N"-tri(methyl-acetic acid)(N3O2-tri(methylacetic acid)) was synthesized by modified procedure of Krespan. Potentiometric method has been used to determine the protonation constants of N3O2-tri(methylacetic acid) and stability constants of complexes on the divalent transition metal ions (Co2+, Ni2+, Cu2+, and Zn2+) and trivalent metal ions (Ce3+, Eu3+, Gd3+, and Yb3+) with N3O2-tri(methylacetic acid). The stability constants for the complexes of the divalent transition metal ions studied in the present work with N3O2-tri(methylacetic acid) were 11.4 for Co2+, 11.63 for Ni2+, 13.51 for Cu2+, and 11.65 for Zn2+, respectively. Thus, the order of the stability constants for complexes on the transition metal ions with N3O2-tri(methylacetic acid) was shown Co2+ < Ni2+ < Cu2+ > Zn2+ as same as the order of Irving-Williams series. The stability constants of Ce3+, Eu3+, Gd3+, and Yb3+ trivalent lanthanide metal ion complexes of N3O2-tri(methylacetic acid) were, respectively, 11.26 for Ce3+, 11.56 for Eu3+, 11.49 for Gd3+, and 11.80 for Yb3+. The values of the stability constants on trivalent metal ions with the ligand are increasing according to increase atomic number, due to increase acidity. But the value of stability constant of Gd3+ ion is less than the value of Eu3+ ion. This disordered behavior is also reported by Moeller.

• 대한화학회지
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• 제66권5호
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• pp.416-419
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• 2022

• Membrane and Water Treatment
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• 제11권4호
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• pp.283-294
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• 2020

This work aims at studying the feasibility of continuous removal of mixed heavy metal ions from simulated zinc plating wastewaters by coupling a microbial fuel cell and a microbial electrolysis cell in batch and continuous modes. The discharging voltage of MFC increased initially from 0.4621 ± 0.0005 V to 0.4864 ± 0.0006 V as the initial concentration of Cr⁶⁺ increased from 10 ppm to 60 ppm. Almost complete removal of Cr⁶⁺ and low removal of Cu²⁺ occurred in MFC of the MFC-MEC-coupled system after 8 hours under the batch mode; removal efficiencies (REs) of Cr⁶⁺ and Cu²⁺ were 99.76% and 30.49%. After the same reaction time, REs of nickel and zinc ions were 55.15% and 76.21% in its MEC. Cu²⁺, Ni²⁺, and Zn²⁺ removal efficiencies of 54.98%, 30.63%, 55.04%, and 75.35% were achieved in the effluent within optimum HRT of 2 hours under the continuous mode. The incomplete removal of Cu²⁺, Ni²⁺ and Zn²⁺ ions in the effluent was due to the fact that the Cr⁶⁺ was almost completely consumed at the end of MFC reaction. After HRT of 12 hours, at the different sampling locations, Cr⁶⁺ and Cu²⁺ removal efficiencies in the cathodic chamber of MFC were 89.95% and 34.69%, respectively. 94.58%, 33.95%, 56.57%, and 75.76% were achieved for Cr⁶⁺, Cu²⁺, Ni²⁺ and Zn²⁺ in the cathodic chamber of MEC. It can be concluded that those metal ions can be removed completely by repeatedly passing high concentration of Cr⁶⁺ through the cathode chamber of MFC of the MFC-MEC-coupled system.