• Bulletin of the Korean Chemical Society
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• 제24권9호
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• pp.1324-1328
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• 2003

The simultaneous determination of anions ($SO_4 ^{2-},\;Cl^-,\;and\;NO_3^-$) and cations ($Na^+,\;NH^{4+},\;K^+,\;Mg^{2+},\;and\;Ca^{2+}$) in natural water obtained by Nakdong River waters system in Korea were performed by ion-exclusion/cationexchange chromatography with conductimetric detection. The stationary phase was a polymethacrylate-based weakly acidic cation-exchange resin column in the $H^+$-form and a weak-acid eluent. When using only a 1.4 mM sulfosalicylic acid/6 mM 18-crown-6 ether as an eluent, good resolution of both anions and cations, minimum time required for the separation, and satisfactory detection sensitivity were obtained in a reasonable time. The method was successfully applied to the simultaneous determination of anions and cations in natural waters.

• 대한화학회지
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• 제36권5호
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• pp.692-696
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• 1992

$NH_4^+형 양이온 교환수지와 희토류-EDTA 용리액을 사용하여 희토류 원소 혼합물에서 원하는 한 원소를 분리 회수하는 연구를 하였다. NH_4^+형 양이온 교환수지에 희토류 혼합물을 흡착시키고, La-EDTA 용액으로 용리하면 수지에 흡착된 희토류 원소중 La^{3+} 이온 외의 희토류 원소는 용리된다. 수지에 남아있는 La^{3+}은 EDTA 용리액으로 용리하여 분리한다. Ce^{4+}만 선택적으로 분리하고자 할때는 La-EDTA 대신 Ce-EDTA로 용리하고 수지에 남은 Ce^{4+}을 EDTA로 용리하면 된다. 이때 분리 구조는 다음과 같다. 흡착과정 : 3RNH_4 ＋ Ln^{3+} = R_3Ln ＋ 3NH^{4+}, La-EDTA 용리 : R_3Ln ＋ La-Y- = R_3La ＋ Ln-Y^-, EDTA 용리 : R_3La ＋ HY^3- = La-Y ＋ RH ＋ 2R-.$

• 대한화학회지
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• 제29권2호
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• pp.178-182
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• 1985

비철특수합금중 아연(II) 구리(II)와 마그네슘(II)을 양이온 교환수지(Dowex 50w${\times}$8, 80-100 mesh)와 음이온 교환수지(IRA-400)을 이용하여 이온교환크로마토그라프로서 분리하는 방법을 연구 하였다. 이온교환수지는 25 ${\times}$ 2cm ID 칼럼에 넣고 흐르는 속도는 0.30 ml/min으로 조절하였다. 아연(II), 구리(II), 마그네슘(II)와 같은 비철금속 이온들을 분리하기 위한 좋은 용리액의 조건은 다음과 같다. 0.5M $NaNO_3$ (pH 3.1), 0.2~0.5M HCl + 50~90% Acetone과 1M HAc + 0.1M NaAcf(pH 3.7)였으며 0.1M NaAc + 1M NaAc(pH 3.7), 0.5M HCl + 50% Acetone이 가장 좋은 용리액으로 판명되었다. 분리된 용출액은 원자흡광 광도계로 측정하였으며 특히 아연 (II)은 음이온 교환수지에서 0.12N HCl과 1.5N $NH_4OH$ 수용액으로 분리하고 E.D.T.A로 적정하였다.

• 해양환경안전학회:학술대회논문집
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• 해양환경안전학회 2004년도 춘계학술발표회
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• pp.81-84
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• 2004

Control of Sediment is very important in prawn farm due to the eruption of toxic material such as W1ionized H2S, NH3 and NO2-. In this study, column test study, column with filter media such as activated carbon, zeolite, oyster shell and iron chloride to evaluate the reduction of toxicity from sediment ammonia-N(NH3) was effectively removed by Zeolite and oyster shell. It was indicated that ammonium ion(NH4+) was removed by ion exchange of zeolite. And the ammonia in the column of oyster shell was existed as the form of NH4+, which is not toxic for prawn because oyster shell was stably kept around pH 8. Therefore, some of ammonia(NH3) was reduced by oyster shell. Hydrogen sulfide and COD were effectively removed by adsorption of activated carbon and a partial removal of hydrogen sulfide was accomplished by Oyster shell. Phosphorous was removed by activated carbon, oyster shell and iron chloride. In prawn farm, the concentration of ammonia was increased with increase of pH by algae photosynthesis in the column of activated carbon, zeolite and iron chloride, but it was revealed that pH was stably kept in the column of oyster shell.

• 대한화학회지
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• 제35권5호
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• pp.553-559
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• 1991

$NH^{4+}$ retaining 이온으로 치환된 양이온교환 수지관에서 흡착시키는 희토류원소이온의 양, 수지관의 내경, 수지관의 길이 및 용리액의 pH 등을 변화시켜 용리시킨 후 용출액 중의 각 화학종을 분석하여 희토류원소이온의 용리 mechanism과 monazite 광에 포함된 희토류원소들의 분리에 관해 연구하였다. 인접한 희토류원소간의 분리능은 수지의 교환용량 이내에서는 흡착시키는 희토류원소이온의 양을 증가시킬수록 증가하였고, 내경이 같으면 수지관의 높이는 희토류원소이온의 분리능 및 분리시간에 영향을 미치지 않으며 희토류-EDTA 착물은 $NH^{4+}$형 수지에 흡착되지 않음을 알 수 있었다. 용리액의 pH는 수지관 내에서 희토류원소이온과 EDTA와의 반응성에 영향을 미쳐 분리에 큰 영향을 미쳤으며 pH가 낮을수록 분리능은 향상되나 분리시간이 길어짐을 알 수 있었다.

• Journal of Microbiology and Biotechnology
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• 제17권9호
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• pp.1527-1532
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• 2007

Lysine produced during microbial fermentation is usually recovered by an ion-exchange process, in which lysine is first converted to the cationic form (by lowering the pH to less than 2.0 with sulfuric acid) and then fed to a cationexchange column containing an exchanger that has a sulfone group with a weak counterion such as NH;. Ammonia water with a pH above 11 is then supplied to the column to displace the purified lysine from the column and allow its recovery. To enhance the adsorption capacity and for a possible reduction in chemical consumption, monovalent lysine fed at pH 4 was investigated in comparison with conventional divalent lysine fed at pH 1.5. The adsorption capacity increased by more than 70% on a mass basis using pH 4 feeding compared with pH 1.5 feeding. Lysine adsorbed at pH 4 started to elute earlier than that adsorbed at pH 1.5 when ammonia water was used as the eluant solution, and the extent of early elution became more notable at lower concentrations of ammonia. Moreover, the elution of monovalent lysine fed at pH 4 displayed a stiffer front boundary and higher peak concentration. However, when the ammonium concentration was greater than 2.0 N, complete saturation of the bed was delayed during adsorption and the percent recovery yield from elution was lowered., both drawbacks that were considered inevitable features originating from the increased adsorption of monovalent lysine.

• Bulletin of the Korean Chemical Society
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• 제28권10호
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• pp.1683-1688
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• 2007

This paper presents a novel simple method for introducing gold nanoparticles in a poly(4-vinylpyridine) (PVP) polymer layer over a glassy carbon (GC) electrode with the aim of forming a tunable electrochemical interface against a cationic ruthenium complex. Initially, AuCl4 ? ions were spontaneously incorporated into a polymer layer containing positively charged pyridine rings in an acidic media by ion exchange. A negative potential was then applied to electrochemically reduce the incorporated AuCl4 ? ions to gold nanoparticles, which was confirmed by the FE-SEM images. The PVP layer with an appropriate thickness over the electrode blocked electron transfer between the electrode and the solution phase for the redox reactions of the cationic Ru(NH3)6 2+ ions. However, the introduction of gold nanoparticles into the polymer layer recovered the electron transfer. In addition, the electron transfer rate between the two phases could be tuned by controlling the number density of gold nanoparticles.

• 한국해양학회지
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• 제10권1호
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• pp.33-40
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• 1975

본 연구의 결과를 간단히 요약하면 다음과 같다. 가. KCl수용액에서의 Dowex 1-X8, Cl$^{-}$(200-400메쉬)에 의한 Hg(II), Cd(II) 및 Zn(II)의 흡착메카니즘은 고농도의 KCl수용액에서는 모두 음이온의 MCl$_{4}$ $^{2-}$ 착이온 형성에 의한 흡착이며, 저농도에서는 착이온 안정도상수가 큰 Hg(II) 는 역시 착이온 형성에 의한 흡착인데 비해 Cd(II)와 Zn(II)의 경우는 농도에 따라 다르다. 한편 D값의 크기순위는 HCl메디움에서의 MCl$_{4}$$^{2-}$ 착이온의 안정도 상수의 크기순위와 일치한다. 나. KCl-Methonol메디움에서의 Dowex 1-X8, Cl$^{-}$수지에 대한 금속이온의 흡착은 메탄올의 농도증가에 따라 증가되는데, 이것은 메탄올 첨가로 인해 수화현상이 약화되어 착이온 형성이 용이해지기 때문이며 착이온을 잘 형성하는 Hg(II)의 경우는 그 증가율이 크지 않았다. 다. 양이온교환 수지 Dowex50W-X$_{8}$ , $K^{+}$column내에서 KCl-H$_{2}$O 및 KCl-MeOH 용리액에 의한 Zn(II), Cd(II) 및 Hg(II)의 융리메카니즘은 역시 금속이온의 MCl$_{4}$$^{2-}$ 착이온 형성 및 이온쌍 형성의 차이로 용리되는데 그 부피분배 계수의 크기는 Zn(II)>Cd(II)>Hg(II)이며, MeOH의 농도가 증가하면 더욱 빨리 용리되는데 이는 역시 MeOH첨가에 인한 착이온 및 이온쌍 형성이 증대되기 때문이다. 라. MCl(M:K$^{+}$, $Na^{+}$, NH$_{4}$$^{+}$ 및 H$^{+}$) 수용액 메디움에서의 Cd(II), Mg(II) 및 Zn(II)의 Dowex 1-X8, Cl$^{-}$ 수지에 대한 흡착은 역시 어떤 메디움에서도 Cd(II) 흡착이 제일 크며, 다음이 Zn(II) 이고 착이온을 형성않는 Mg(II)이 제일 작았다. 한편 메디움 종류별 D값의 크기순위는 H$^{+}$>K$^{+}$> $Na^{+}$>NH$_{4}$$^{+}$이였다. 메디움의 종류에 따라 D값의 차이가 나는 것은 금속이온의 착이온 형성과 금속이온의 용액내에서의 이온종의 상태와 관련이 있다고 생각된다. 마. MCl(M:K$^{+}$, $Na^{+}$, NH$_{4}$$^{+}$ 및 H$^{+}$)과 MNO$_{3}$ 용리액에 의한 Cd(II), Mg(II) 및 Zn(II)의 용리는 예상한 바와 같이 MCl에서 작은 Dv 값을 갖는데, 이것은 CdCl$_{4}$$^{2-}$ 착이온을 형성하거나 ZnCl$_{4}$$^{2-}$ , ZnCl$_{3}$$^{-}$같은 이온과 MgCl$^{+}$, MgCl$_{2}$같은 이온종을 형성하기 때문인것 같다. 한편 어떠한 용리액에서던지 NH$_{4}$$^{+}$의 경우 Dv값이 제일 작았다. 바. 본 연구의 목적중의 하나인 인체유해 중금속이온인 Hg(II), Cd(II)등이 NaCl같은 염화물이 함유된 시료용액에 공해이온으로 존재할 경우 흡착에 의한 제거가 가능하다. 한편 이같은 중금속이온의 흡착실험은 특히 해수중의 금속이온의 회수연구에도 그 활용이 가능하리라고 믿는다.

• Membrane and Water Treatment
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• 제4권2호
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• pp.109-126
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• 2013

Surface modification by low-pressure ammonia ($NH_3$) plasma on commercial thin-film composite (TFC) membranes was investigated in this study. Surface hydrophilicity, total surface free energy, ion exchange capacity (IEC) and zeta (${\zeta}$)-potentials were determined for the TFC membranes. Qualitative and quantitative analyses of the membrane surface chemistry were conducted by attenuated total reflectance Fourier transform infrared (ATR FT-IR) spectroscopy. Results showed that the $NH_3$ plasma treatment increased the surface hydrophilicity, in particular at a plasma treatment time longer than 5 min at 50 W of plasma power. Total surface free energy was influenced by the basic polar components introduced by the $NH_3$ plasma, and isoelectric point (IEP) was shifted to higher pH region after the modification. A ten (10) min $NH_3$ plasma treatment at 90 W was found to be adequate for the TFC membrane modification, resulting in a membrane with better characteristics than the TFC membranes without the modification for water treatment. The thin-film chemistry (i.e., fully-aromatic and semi-aromatic nature in the interfacial polymerization) influenced the initial stage of plasma modification.

• 한국미생물·생명공학회지
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• 제24권4호
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• pp.472-477
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• 1996

Natural human epidermal growth factor (nhEGF) was purified from pregnant human urine by benzoic acid adsorption, DEAE-Sepharose ion exchange, and immunoaffinity chromatography. The purified nhEGF was further separated into four fractions using Bondapak C$_{18}$ HPLC system. Following characterization by Western blot analysis and double immu- nodiffusion, we found that each fraction corresponds to four derivatives of the nhEGF. For biological analysis of nhEGF, we optimized the labeling time and serum concentration for the incorporatioin of 5-bromo-2'-deoxy uridine (BrdU), a non-radioactive alternative for [$^{3}$H]-thymidine uptake, into NIH 3T3 cells. The DNA synthesis of NIH 3T3 cells was gradually increased at the nhEGF concentrations between 0.1 - 10 ng/ml in the Dulbecco's Modified Eagles Medium (DMEM) containing 0.2% Fetal calf serum (FCS). When we assayed the biological activity of four fractions, the activity of the second fraction was superior to that of the others. Based on the results from the HPLC analysis spiked with recombinant human epidermal growth factor (rhEGF) and amino acid sequencing, we concluded that the second fraction was nhEGF and the other three fractions were the derivatives of nhEGF. In addition, the proportion of nhEGF was approximately 46% is compared with that of the other three derivatives.