• 대한금속재료학회지
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• 제48권2호
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• pp.148-153
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• 2010

The effects of Cu(II) and Al(III) on the extraction and separation of Pt(IV) and Pd(II) have been investigated in a mixed chloride solution using Alamine336 as the extractant. In the HCl concentration range of 1 to 5 M, more than 99% of Pt and Pd could be extracted by Alamine336 from all of the mixed chloride solutions investigated in this study. Lower HCl concentration led to a higher separation factor between Pd and Pt when Alamine336 concentration was constant. Extraction percentage of Cu increased with the increase of HCl concentration, while that of Al was nearly constant at 33% in our experimental range. The optimum conditions to extract Pt and Pd from Cu or Al and the separation factor under these conditions were obtained.

• Food Science and Biotechnology
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• 제15권2호
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• pp.189-195
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• 2006

A study was conducted to develop optimal conditions for a large-scale, sequential separation method for value-added components from egg yolk. Starting with liquid egg yolk, immunoglobulin Y (IgY), phospholipids, and neutral lipids were extracted sequentially using water, ethanol, and n-hexane. The remainder was yolk proteins. Adjusting the pH of diluted egg yolk to pH 5.0-5.2 decreased phospholipids content in the supernatant after centrifugation, which was very important for preventing clogging problem of ultrafiltration filters during the subsequent concentration step for IgY separation. Extraction of precipitants after centrifugation with four volumes of 100% ethanol once removed most of the phospholipids and the purity of phospholipids was more than 85% (wt.) after drying. The subsequent extraction of precipitant from ethanol extraction with four volumes of hexane 3 times removed neutral lipids almost completely and resulted in a high protein product with minimal lipids. The sequential separation method is considered to be advantageous for large-scale separations of many valuable components from egg yolk.

• 자원리싸이클링
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• 제14권2호
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• pp.33-42
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• 2005

Nd와 Sm이 혼합된 염산용액에서 PC88A에 의한 두 금속의 분리에 대한 실험을 수행하였다. 또한 PC88A의 비누화가 두 금속의 추출 및 분리에 미치는 영향을 조사하였다. 본 연구에서 수행한 실험조건에서 Sm의 분배계수가 Nd의 분배계수보다 크며, 분리인자는 수상의 pH에 따라 증가하였다. 비누화 PC88A로 추출하는 경우 PC88A로 추출하는 경우에 비해 분배계수와 분리인자 모두 증가하였다. PC88A와 비누화 PC88A에 의한 추출시 초기추출조건으로부터 Nd와 Sm의 분배계수와 분리인자를 예측할 수 잇는 모델을 개발하였다. 본 연구에서 개발된 모델을 초기추출조건에 적용하여 예측한 Nd와 Sm의 분배계수는 실험으로 측정한 값과 서로 잘 일치하였다.

• 한국식품위생안전성학회지
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• 제15권3호
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• pp.235-240
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• 2000

식품의 항균물질 분리에 있어 여러 가지 방법이 있지만 오차와 손실이 많아 실용화 하기에는 많은 문제점이 있다. 현재 일반적인 분리법으로 유기용매분획법, 크로마토그래피 등이 있으나, 많은 시간과 노력을 필요로 하며 시료에 따라 항균활성이 소실되는 경우가 많다. 본 연구는 전편의 '부추의 미생물학적 항균활성 특성과 가공식품에의 응용'에 이어 부추의 항균활성 물질을 효과적으로 분리하기 위한 방법을 정립하고 항균활성 물질을 확인하였다. 부추의 항균활성 물질 분리를 위하여 ultrafiltration, liquid-liquid extraction, TLC, HPLC 순으로 정제하였다. Ultrafiltration 결과 항균물질은 분자량 5,000 dalton 이하의 저분자 물질이었고, TLC로 분리된 8개의 spot중 대조군에 비하여 높은 항균활성을 나타내는 1개의 spot을 추출하여, HPLC로 유효 peak 2개를 얻었고 각 peak성분을 GC/MS로 확인한 결과 cis-propenyl methyl disulfide, 5-methyl methylthiosulphonate, dimethyl disulfide등의 황화합물로 구성된 복합물질로 확인되었다.

• 한국지구물리탐사학회:학술대회논문집
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• 한국지구물리탐사학회 2003년도 Proceedings of the international symposium on the fusion technology
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• pp.618-623
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• 2003

Solvent extraction experiments for separation of impurities from Ni-rich solution were carried out for manufacturing of high purity Ni compounds from acid leaching solution of spent Ni-Cd secondary battery. Artificial and leaching solutions were used as aqueous phases and PC88A saponified by sodium in kerosene were used as organic phase. The extraction order is Zn>Mn>Co>Ni and extraction percentage of metal ions was increased with increase of the concentration of extractant, initial pH of aqueous phase and ratio of O/A. The separation of cobalt, zinc and manganese from nickel was effectively accomplished at the condition of extraction stage=l, O/A=1 and initial pH 5.0 with 1.0 $mol/dm^3$ PC88A saponified to $50\%$ with NaOH.

• 자원리싸이클링
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• 제22권5호
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• pp.29-34
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• 2013

TEHA와TEHA 및TBP와 LIX63과의 혼합용매를 사용하여 염산용액으로부터 백금과 로듐을 분리하기 위한 용맥추출실험을 수행하였다. 염산농도 1-9 M 범위에서 추출제의 농도에 따른 두 금속의 추출거동과 분리 가능성을 조사하였다. 혼합용액에서 백금과 로듐의 농도는 각각 $1{\times}10^{-3}M$과 $2{\times}10^{-4}M$로 조절하였다. TEHA와 혼합추출제에 의한 추출시 로듐의 추출율은 추출조건에 의존하나, 백금은 염산농도와 무관하게 모두 추출되었다. 혼합용액에서 염산농도가 낮을 경우 로듐이 추출되지 않아 백금과 로듐의 분리가 가능하였다. LIX63을 첨가한 TEHA는 로듐의 추출율을 향상시켰으나, TBP를 첨가한 TEHA는 두 금속의 추출에 거의 영향을 미치지 않았다.

• Nuclear Engineering and Technology
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• 제31권5호
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• pp.498-505
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• 1999

Trivalent actinide-lanthanide group separation is difficult to perform on an industrial scale, because of the many drawbacks of the available chemical process. In this paper, picolinamide(C$_{8}$H$_{17}$) is synthesized and characterized, and extraction yields of Am-241, Eu-152 and Nd are determined in batch extraction experiments. In particular, the influence of the solvent is described. The extraction yields of Am-241, Eu-152 and Nd depended on the LiNO$_3$ concentration, the picolinamide(C$_{8}$H$_{17}$) concentration and the acidity. A favorable picolinamide(C$_{8}$H$_{17}$) concentration was found to be about 2M. The appropriate nitric acid concentration and LiNO$_3$ concentration were confirmed to be about 0.125M and 3M, respectively. The separation factor of Am and Eu was about 9.9 at optimum conditions. The picolinamide(C$_{8}$H$_{17}$) is a very promising extractant for the actinide(III)-lanthanides(III) separation.aration.aration.

• 대한전자공학회:학술대회논문집
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• 대한전자공학회 2001년도 The 6th International Symposium of East Asian Resources Recycling Technology
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• pp.259-263
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• 2001

There are several steps such as slicing, lapping, chemical etching and mechanical polishing in the silicon wafer production process. The chemical etching step is necessary to remove damaged layer caused In the slicing and lapping steps. The typical etching liquor is the acid mixture comprising nitric acid, acetic acid and hydrofluoric acid. At present, the waste acid is treated by a neutralization method with a high alkali cost and balky solid residue. A solvent extraction method is applicable to separate and recover each acid. Acetic acid is first separated from the waste liquor using 2-ethlyhexyl alcohols as an extractant. Then, nitric acid is recovered using TBP(Tri-butyl phosphate) as an extractant. Finally hydrofluoric acid is separated with the TBP solvent extraction. The expected recovered acids in this process are 2㏖/l acetic acid, 6㏖/1 nitric acid and 6㏖/l hydrofluoric acid. The yields of this process are almost 100% for acetic acid and nitric acid. On the other hand, it is important to recover and reuse the metal values contained in various industrial wastes in a viewpoint of environmental preservation. Most of industrial products are made through the processes to separate impurities in raw materials, solid and liquid wastes being necessarily discharged as industrial wastes. Chemical methods such as solvent extraction, ion exchange and membrane, and physical methods such as heavy media separation, magnetic separation and electrostatic separation are considered as the methods for separation and recovery of the metal values from the wastes. Some examples of the application of solvent extraction to the treatment of wastes such as Ni-Co alloy scrap, Sm-Co alloy scrap, fly ash and flue dust, and liquid wastes such as plating solution, the rinse solution, etching solution and pickling solution are introduced.

• 한국식품영양학회지
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• 제10권4호
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• pp.503-508
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• 1997

L. edodes의 배양액 및 균사체로부터 항암작용이 있는 단백 다당류의 추출 및 정제방법에 관한 실험을 실시하였다. 단백다당류 추출에서 비이온성 계명 활성제인 2% Triton X-100 용액으로 추출할 경우 상온에서 추출하여도 통상의 10$0^{\circ}C$ 열수 추출을 통해 얻을 수 있는 것보다 수율이 높았다. 그러나 계명활성제 용액에 4N NaCl을 첨가하여 추출하면 ethanol 침전과정에서 단백다당류의 침전물을 얻을 수 없었다. 열수 추출에 있어서 추출 온도는 10$0^{\circ}C$가 효과적이고 추출 시간은 4시간 정도면 충분하였다. 열수 추출 결과 ethanol 침전 및 동결건조를 통하여 얻어진 조단백 다당류의 정제 실험에서는 alumina를 충전제로 하는 gel filtration보다 sephadex에 의한 gel filtration 또는 DEAE-cellulose, DEAE-sephadex를 이용한 ion exchange chromatography가 보다 효과적이다.

• 방사선산업학회지
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• 제5권2호
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• pp.101-106
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• 2011

The separation of germanium and gallium ion with metal oxide was introduced into the development of $^{68}Ge/^{68}Ga$ generator. Germanium and gallium within mixed solution were respectively separated by using a liquid-liquid extraction and a column chromatographic method. The separation of Ge within high concentrated hydrochloric and sulfuric acid was conducted by the extraction to $CCl_4$ and the back-extraction to 0.05 M HCl. An optimum condition of the extraction by $CCl_4$ was in 5~7 M HCl and efficiency was around 80%. The gallium was selectively separated by using $Al_2O_3$ among metal oxides as sorbents from the mixed solution in 0.04~0.10 M HCl condition.