• 한국방사성폐기물학회:학술대회논문집
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• 한국방사성폐기물학회 2004년도 Proceedings of the 4th Korea-China Joint Workshop on Nuclear Waste Management
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• pp.245-256
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• 2004

The extraction of three kinds of amido podands, N,N,N'N'-tetrabutyl-3-oxa-pentanedi- amide (TBDGA), N,N,N'N'-tetra-isobutyl-3-oxa-pentanediamide(TiBDGA) and N,N,N'N'-tetra- butyl-3,6-dioxa-oct-anediam- ide(TBDOODA) on U(VI),Pu(IV), Am(III), Eu(III) and other metal ions is studied in nitric acid solutions. 40%octanol-kerosene is chosen as diluents to eliminate third phase and emulsion. TBDGA and TiBDGA show extraction selectivity to An(III) and Ln(III) much higher than to U(VI) and Pu(IV). Fe, Ru and Mo is poorly extracted by the three kinds of amid podands in 2~3mol/L $HNO_3$ solutions. Aiming to eliminate interface crude when using simulated HLLW solution in the system of 0.2mol/L TBDGA/Octanol＋kerosene, acetohydroxyamic acid was adapted. Distribution ratio of zirconium was decreased when adding acetohydroxyamic acid in aqueous solution, and interface crude disappeared as mixing extractant with HLLW. The counter-current extraction test is carried out in a set of miniature mixer-settler, with 0.2mol/L TBDGA/ 40% octanol-kerosene as extractant to separate U(VI), Pu(IV), Am(III) and Eu(III) from simulated high level liquid waste(HLLW) solution. In battery A, lanthanides and actinides are coextracted into organic phase with the recovery of 99.98% for U(Ⅵ), >99.99% for Pu(IV), and >99.99% for Am(III) and Eu(III) respectively. In battery R1, 99.99% U, 86.2% Pu and a part of Am or Eu are stripped into aqueous phase by 0.2mol/L acetohydroxyamic acid (AHA) in 0.01mol/L $HNO_3$ solution. In battery $R_2$, Am, Eu and remained Pu are completely back-extracted by 0.2mol/L AHA. This separation process contains no salt reagent, and it is not necessary to dilute HLLW feed.

• 자원리싸이클링
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• 제28권1호
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• pp.55-61
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• 2019

묽은 염산용액의 pH를 2에서 9까지 변화시켜 아민계(Alamine 308과 TEHA)와 중성추출제(TOP)로 몰리브덴(VI)과 텅스텐(VI)의 용매추출거동을 조사하였다. 텅스텐(VI)이 몰리브덴(VI)보다 상기 세 추출제에 선택적으로 추출되었으며, TEHA로 추출시 가장 높은 분리인자를 얻었다. 수소화처리하지 않은 3차 아민에 의한 두 금속의 추출율은 용액의 pH에 따라 지속적으로 감소하여 pH 9에서는 전혀 추출되지 않았다. 본 논문의 실험조건에서 용매추출거동을 금속의 농도분포곡선을 이용하여 설명하였다. Alamine 308과 TEHA는 TOP에 비해 두 금속의 추출과 분리에 효과적이다.

• Bulletin of the Korean Chemical Society
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• 제30권7호
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• pp.1526-1530
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• 2009

Solvent extraction reaction of Zn(II) by Alamine336 from strong HCl solution up to 10 M was identified by analyzing the data reported in the literature. The equilibrium constant of this reaction was estimated by considering the complex formation between zinc and chloride ion. The necessary thermodynamic parameters, such as equilibrium constant for the formation of complexes and the interaction parameters, were evaluated from the thermodynamic data reported in the literature. The following solvent extraction reaction and the equilibrium constant was obtained by considering the activity coefficients of solutes present in the aqueous phase with Bromley equation. $Zn^{2+}\;2Cl^{-}\;+\;R_3NHCl_{org}\;=\;ZnCl_3R_3NH_{org},\;K_{ex}\;=\;6.33\;{\times}\;10^2$ There was a good agreement between measured and calculated distribution coefficients of Zn(II).

• 자원환경지질
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• 제36권3호
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• pp.159-170
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• 2003

전주시 하천 퇴적물시료, 호남고속도로 주변의 토양과 퇴적물 시료, 광산주변 광미 및 토양시료를 대상으로 토양오염 공정시험방법상의 용출법, 0.1N 유지용출법, Tessir et al.(1979)의 연속추출방법을 적용하여 중금속을 추출하고 그 결과를 비교하였다. 공정시험방법상의 용출법 사용시 산에 대한 완충능력이 있는 시료는 용출액의 pH 1(0.1N HCl)이 유지되지 못했고 용출액의 pH가 최고 8.0까지 증가하였다. 또한, 토양오염 공정시험방법상의 용출법 사용시 중금속 추출량(HPE)/0.1 N 유지용출법 사용시 중금속 추출량(HPEM) 값의 평균치와 범위는 Cd의 경우 0.479와 0.145~0.929, Zn의 경우 0.534와 0.078~0.928, Mn의 경우 0.432와 0.041~0.992, Cu의 경우 0,359와 0.011~0.874, Cr의 경우 0.150과 0.018~0.530, Pb의 경우 0.219와 0.003~0.853, 그리고 Fe의 경우 0.088과 1.73${\times}$$10^{-5}$~0.303이다. 이는 두 전처리 방법에 의해 추출된 중금속량의 차이가 Fe>Cr>Pb>Cu〉Mn>Cd>Zn 순임을 지시한다. HPE, HPEM과 연속추출법 비교시 Zn, Cd, Mn의 경우 추출량은 대체적으로 연속추출 3단계까지의 합$\geq$0.1N 유지용출법>연속추출 2단계까지의 합$\geq$용출법 순이었으며, Cr과 Fe의 경우 연속추출 3단계까지 합》0.1N 유지용출법>용출법 순이었으며 연속추출 2단계 까지 합은 Cr의 경우 0.1N 유지용출법의 추출량보다 낮았고 용출법의 추출량보다 높았다. Cu의 경우 연속추출 4단계까지의 합$\geq$0.1N 유지용출법>3단계까지의 합 용출법으로 나타났다. 0.1N유지위해 첨가된 염산의 양이 증가할수록, 즉 시료내의 산에 대한 완충능력이 증가할수록 HPE/HPEM 값이 감소하며, 완충능력이 큰 시료의 경우 모든 원소에서 HPE/HPEM이 0.2보다 낮다. 완충능력이 낮은 시료의 경우 Zn, Cd, Mn, Cu는 연속추출 1,2단계의 합과 연속추출 3단계의 중금속 추출함량간의 차이가 적고, 다른 원소에 비해서 상대적인 유동도가 높기 때문에 HPE/HPEM이 대채적으로 0.2보다 높으며 0.6이상의 값을 갖는 시료가 많다. 그러나, Fe, Cr의 경우는 상대적으로 Zn, Cd, Mn, Cu에 비해 유동도가 낮고, 연속추출 3단계의 함량이 1+2단계의 함량과 차이가 커 완충능력이 낮은 시료의 HPE/HPEM값도 전반적으로 0.2보다 낮다. 이러한 연구결과는 국내 토양오염 공정시험방법상의 전처리 방법인 용출법이 장래에 장기적으로 산성비와 같은 환경피해에 노출되어 토양의 완충능력이 감소하거나 상실될 수 있는 지역의 오염평가에 적합치 않을 가능성을 제시한다.

• 펄프종이기술
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• 제43권1호
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• pp.83-91
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• 2011

Hemicelluloses are useful materials for papermaking and other biotechnological applications. To recover and further utilize the hemicelluloses, this study carried out the pre-extraction of the hemicelluloses from Korean mixed hardwoods chips using hot water and sodium hydroxide solution at various temperature and time conditions. Through the hot water pre-extraction, the wood components of 22% was extracted and the 35% of the hemicelluloses which were contained in the original wood chips were dissolved into the pre-extractives. The yield of the pre-extractives was more significantly influenced by the pre-extraction temperature than the time. The pre-extractives with the yield of 30% could be obtained by alkali pre-extraction and alkali concentration was the most important factor. It had lower hemicellulose content but high molecular weight, compared with the hot water pre-extractives.

• 한국염색가공학회지
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• 제9권3호
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• pp.10-17
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• 1997

The study was performed to obtain the optimum extraction conditions for crocin from gardenia fructus. Generally crocin is unstable on heat, light, acid and base solution. The extraction efficiency of crocin from gardenia depended upon the extraction time, extraction temperature, pH in the extraction bath and the optimum conditions of crocin extraction were determined as 60 minutes of extraction time, 4$0^{\circ}C$ of extraction temperature, pH 7 of extraction bath. The molar extinction coefficient of crocin was 12,515 and the color yield of purified crocin was about six times higher than that of non-purified crocin. The heat-stability at extraction temperature and lightstability in irradiation with xenon lamp for one hour of the purified crocin were higher than those of non-purified crocin. Intensity of &{\lambda}_{max}&of crocin was decreased by irradiation for one hour but UV-Vis. spectra of crocin was not changed. The colors of purified and non-purified crocin dissolved wit methanol was evaluated by means of CIE L* a* b* system.

• 자원리싸이클링
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• 제25권2호
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• pp.33-41
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• 2016

망간단괴 매트상 모의 침출용액에서 구리 용매추출과 수산화 침전법에 의해 구리와 철이 제거 된 용액(Co 1.91 g/L, Ni 14.65 g/L)으로부터 용매추출-전해채취 연속공정을 통해 코발트를 분리, 회수를 위한 규모확대 실험(망간단괴 기준 380 kg/day)을 수행하였다. 용매추출의 경우 추출제로는 NaOH로 45% 비누화 된 0.22 M Cyanex 272, 세정용액은 코발트 2 g/L(pH : 3.0), 탈거용액은 코발트 전해폐액(Co 36.0 g/L, $Na_2SO_4\;70g/L$, pH : 1.5)을 사용하였으며, 탈거된 유기상은 산과 증류수의 세척 공정을 통해 재사용하였다. 추출단, 세정단 그리고 탈거단의 O/A 비는 각각 1/1.5, 10/1 그리고 1.5/1 이었으며, 산세척과 수세척단의 O/A 비는 각각 1/1, 6/1이었다. 용매추출공정의 코발트의 추출율과 탈거율은 각각 99.8%와 99.88%이었으며 탈거액의 코발트와 니켈의 농도는 각각 40.27 g/L, 4 ppm이었다. 전해액의 pH 조절을 위해 전해폐액 순환 방식을 도입한 전해채취공정은 $0.563A/dm^2$의 전류밀도에서 67.0%의 전류효율을 나타내었으며, 99.963% 순도의 금속 코발트를 얻었다.

• Journal of the Korean Wood Science and Technology
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• 제12권4호
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• pp.19-30
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• 1984

This experiment was carried out to investigate the effects of autohydrolysis and extraction conditions on the separation of the chemical substances, the extractability of lignin by dioxane, and the yield of reducing sugars from cellulosic substrates by using a commercial cellulase derived from Trichoderma viride. Air-dried wood meals through 0.42mm (40 mesh) screen and retained on 0.25 mm (60 mesh) of Populus alba-glandulosa and Pinus koraiensis were autohydrolyzed with water at $180^{\circ}C$ for 30 and/or 60 minutes in a 6 liter stainless-steel digester with or without 2% 2-naphthol. The hydrothermally-treated wood meals were extracted the lignin with 100%, 90%, 75% and 50% dioxane solutions at $70^{\circ}C$ for 4 hours, respectively. The results obtained were as follows; 1) After autohydrolysis of Populus alba-glandulosa, the yield of wood meals decreased with lengthening the auto hydrolysis time from 30 minutes to 60 minutes and with 2% 2-naphthol addition. In case of Pinus koraiensis, the yield was not affected by 2%, 2-naphthol addition at the autohydrolysis in the digester. 2) After autohydrolysis and lignin extraction of Populus alba-glandulosa, the yield of wood meals decreased with lengthening the autohydrolysis time from 30 minutes to 60 minutes and with 2% 2-naphthol addition. Extraction of 50% dioxane solution was the best solvent for the yield among the solutions of 100%, 90%. 75% and 50% dioxane. In case of Pinus koraiensis, the yield was not affected by 2% 2-naphthol addition and the solution of 90% dioxane was the poorest solvent for the yield. 3) After autohydrolysis and lignin extraction of Populus alba-glandulosa, the Klason lignin content in cellulosic substrates for enzymatic hydrolysis decreased with lengthening the autohydrolysis time from 30 minutes to 60 minutes and with 2% 2-naphthol addition. Klason lignin content was the lowest after extraction by 90% or 75% dioxane solution. The content was also affected by interaction of the three factors-autohydrolysis time, 2% 2-naphthol addition and concentration of dioxane. In case of Pinus koraiensis, the Klason lignin content increased with 2% 2-naphthol addition but was not affected by the concentration of dioxane solution. 4) After autohydrolysis and lignin extraction of Populus alba-glandulosa, the extractable Klason lignin content by extraction increased with lengthening the auto hydrolysis time from 30 minutes to 60 minutes and with 2% 2-naphthol addition. The extractable lignin content was the highest after extraction by 90% or 75% dioxane solution. In case of Pinus koraiensis, the extractable lignin content increased with 2% 2-naphthol addition. Extractions by 100%, 90% and 50% dioxane solutions were more effective for the extraction of Klason lignin than by 75% dioxane solution. 5) After autohydrolysis and lignin extraction of Populus alba-glandulosa, the yield of reducing sugars increased with lengthening the autohydrolysis time from 30 minutes to 60 minutes but was not affected by 2% 2-naphthol addition and the concentration of dioxane. The yield of reducing sugars after enzymatic hydrolysis was slightly higher by extractions with 90%, 75% and 50% dioxane solutions than with 100% dioxane. In case of Pinus koraiensis, the yield of reducing sugars was not affected by 2% 2-naphthol addition but affected by the concentration of dioxane. The yield of reducing sugars was the highest in cellulosic substrates extracted by 100% dioxane solution.

• Bulletin of the Korean Chemical Society
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• 제27권10호
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• pp.1557-1561
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• 2006

The use of chemically modified silica-salen$(NEt_2)_2$ was studied for the separation and concentration of the metal ions from an aqueous solution by a solid phase extraction. After the salen(NEt2)2 was synthesized, it was chemically bonded to silica gel by a diazonium coupling reaction. The adsorption capacities and binding constants were obtained with respect to Cu(II), Mn(II), Pb(II) and Zn(II) by a graphical method. Some experimental conditions were optimized for the determination of the trace elements. After the silica-salen(NEt2)2 was pulverized in a sample solution of which the pH was adjusted, the solution was stirred to pre-concentrate the metal ions. The metal ions adsorbed were desorbed with nitric acid solution. And the concentrated analytes were determined by a flame AAS. The method proposed here was so rarely influenced by a sample matrix that the procedure was applied to 3 types of water samples. The reproducible results of less than 10% RSD were obtained at the concentration level of ca. 100 ng/mL and the recoveries of 95-109% were obtained in the spiked samples in which given amounts of analytes were added.

• 대한화학회지
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• 제31권4호
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• pp.315-321
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• 1987

우라늄 추출을 위한 리간드를 페닐알라닌과 3-oxoglutaric acid로 부터 합성하였다. 여러가지 pH, 리간드와 우라늄의 여러 농도비에서 리간드를 녹인 이염화메탄 용액을 사용하여 우라늄 추출 실험을 한 결과, pH 8에서 최대의 추출효율이 나타났으며, 리간드와 우라늄의 농도비가 커질수록 추출율이 증가하였고, 농도비가 4이상에서 완전추출이 되었다. 또한 다른 양이온들과의 경쟁반응에서 리간드가 우라늄에 대해 높은 선택성을 나타내는 것이 확인 되었으며, 추출된 우라늄이 1M 염산용액에 정량적으로 회수되었고 리간드도 재사용 할 수 있었다. 그리고 우라닐 이온과 리간드의 안정도 상수를 측정 하였으며, 총괄 생성상수 값들은 다음과 같다. ${\beta}_1=1.20{\times}10^5\;,\;{\beta}_2=1.01{\times}10^8$.