• KSBB Journal
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• 제6권4호
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• pp.337-344
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• 1991

The liquid-liquid extraction of lipase A from Candide cylindracea and lipase B from porcine pancrease was carried out using reversed micellar organic solvents. Effects of various factors such as ionic strength, pH, and species and concentration of surfactant, on lipase solubilization were studied. A cationic surfactant cetyl-trimethyl ammonium bromide (CTAB) in isooctane/nhexanol(1:1) was found to be an effective solvent and its optimum concentration was 50 mM. KCl among various salts tested was the most effective and the efficiency of solubilization of lipase increased with decreasing the ionic strength of salts. The maximum activity and solubiliz ation of protein were obtained at pH 8. The stripping efficiency has a maximum value at pH 4 and increases with KCl concentration in the range of 0.2∼1.0 M. After the solubilization and stripping, the overall recovery efficiency of mass and specific activity of lipases was 62% and 66%, respectively.

• 방사성폐기물학회지
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• 제6권3호
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• pp.163-170
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• 2008

30 % TBP/NDD-2 M $HNO_3$ (0.005 M $K_2Cr_2O_7$ 함유) 계에 의해 산화 추출된 Np의 유기상을 대상으로 n-butyraldehyde (NBA)에 의한 Np의 환원 역추출을 고찰하였다. Np의 역추출은 NBA의 농도 증가에 따라, 역추출 수용상 내 질산농도 감소에 따라, 그리고 반응 온도 감소에 따라 증가하였으며, 이때 겉보기 환원 역추출 속도식은 $-d[Np]_{Org.}/dt$ =1,524 exp(-2,906/T) $[NBA]^{0.91}\;[H^+]^{-0.92}[Np]_{Org.}$. 이었다. 1.04M NBA 및 2M $HNO_3$에서 Np 및 U의 역추출률은 각각 70.1 % 및 7.1 % 이며 이때 분리계수(($=D_U/D_{Np}$)는 30.4 정도로, TBP-$HNO_3$ 계에 의해 공추출된 Np과 U은 NBA에 의해 효과적으로 상호 분리할 수 있음을 알 수 있었다.

• 대한치과의사협회지
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• 제57권6호
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• pp.326-332
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• 2019

Extraction treatment has been used for a long time to treat crowding or lip protrusion patients and still extraction decision is the most difficult and important decision during diagnosis and treatment planning. If the amount of crowidng is severe, premolar extraction is often considered. Because of their location, premolar extractions would seem to allow for the most straightforward relief of crowding and the improvement of soft tissue profile. But patients and their parents often prefer nonextraction approach if possible and such a preference gives us serious question about the boundary of nonextraction treatment. Because Orthodontic Mini-Implant (OMI) become popular these days, distalization of posterior teeth can be obtained easily without patient's compliance. For this reason, many orthodontists are trying to treat crowding patient with nonextraction than before. But sometime, unexpected side effects are observed including unesthetic profile, impaction of second molar and long treatment time. All the tools for space gaining - extraction, arch expansion, molar distalization and interproximal enamel reduction - have their limitations and indications. Possible side effects and limitations should be carefully considered during the treatment planning. Although Korean patients usually require extraction more often than US or European patients, more knowledge about the tools for space gaining would help us to decrease the rate of extraction and the problems during treatment of crowding patients.

• 자원리싸이클링
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• 제1권1호
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• pp.58-68
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• 1992

아연을 함유하고 있는 산업폐기물로부터 첨단산업의 소재원료인 미립의 고순도 ZnO 분말을 아연제련의 용매추출 공정에서 직접 합성할 수 있는 방법을 개발하고자 하였다. 아연 함량이 55%인 선재산업의 폐기물을 황산으로 침출하여 아연을 추출하였다. 함아연 용액에서 철분을 침전시켜 제거한 후 D2EHPA를 추출제로 사용하는 용매추출에 의해 아연이온을 유기상으로 추출하여 정제한 뒤 oxalic acid와 같은 침전제를 사용하여 유기상의 아연 이온을 precipitation stripping 법으로 탈거, 침전시켜 $ZnC_2O_4$ 분말을 합성하였으며 이를 해소하여 99.9% 이상의 ZnO 분말을 제조하였다. 황산농도, 침출시간, 황액농도가 아연의 침출율에 미치는 영향과 용매추출시 용액의 산도에 따른 아연과 불순물의 추출거동을 조사하여 최적정제조건을 얻었다. 또한 oxalic acid의 농도, 온도, 계면활성제의첨가, 침전시간 등이 생성된 $ZnC_2O_4$ 분말의 형상과 입자크기 및 분포에 미치는 영향에 대해 조사하였다.

• Membrane and Water Treatment
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• 제4권1호
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• pp.11-25
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• 2013

Emulsion liquid membrane (ELM) process suffers from emulsion instability problem. So far, emulsion produced by mechanical methods such as stirrer and homogenizer has big size and high emulsion breakage. This paper discussed the application of emulsion produced by sonicator to extract cadmium in a batch ELM system. The emulsions consist of N,N-Dioctyl-1-octanamine (trioctylamine/TOA), nitrogen trihydride (ammonia/NH4OH), sorbitan monooleate (Span 80), and kerosene as carrier, stripping solution, emulsifying agent, and organic diluent, respectively. Effects of comprehensive parameters on extraction efficiency of Cd(II) such as emulsification time, extraction time, stirring speed, surfactant concentration, initial feed phase concentration, carrier concentration, volume ratio of the emulsion to feed phase, and pH of initial feed phase were evaluated. The results showed that extraction efficiencies of Cd(II) greater than 98% could be obtained under the following conditions: 15 minutes of emulsification time, 4 wt.% of Span 80 concentration, 4 wt.% of TOA concentration, 15 minutes of extraction time, 250 rpm of stirring speed, 100 ppm of initial feed concentration, volume ratio of emulsion to feed phase of 1:5, and initial feed pH of 1.53.

• 한국환경과학회지
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• 제9권6호
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• pp.517-522
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• 2000

Separation of strontium ion from synthetic seawater in the contained liquid membrane permeator with two micro-porous films was performed. The permeator consisted of a liquid membrane and two cells for aqueous solutions. The liquid membrane consisted of $D_2EHPA(di-2-ethylhexy1-phosphoric acid)$ and DCH18C6 (dicyclohexano-18-crown-6),diluted to 30 vol% with kerosine and was trapped between two micro-porous hydrophilic films. This liquid membrane separated two aqueous solutions, one of which was synthetic seawater and the other of which was the stripping solutions consisting of 1mol/L $H_2SO_4$ solution. The effects of various operating parameters on the extraction rate and equilibrium extraction ratio of strontium ion from synthetic seawater were experimentally examined. The addition of DCH18C6 to the $D_2EHPA$ solution caused synergy effect on the extraction of strontium ion. The permeator extracted strontium ion from synthetic seawater effectively with high membrane life time.

• 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.

• Membrane and Water Treatment
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• 제13권4호
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• pp.201-208
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• 2022

Emulsion Liquid Membrane (ELM) is a prominent technique for the separation of heavy metal ions from wastewater due to the fast extraction and is a single-stage operation of stripping-extraction. The selection of the components (Surfactant and Carrier) of ELM is a very significant step for its preparation. In the ELM technique, the primary water- in-oil (W/O) emulsion is emulsified in water to produce water-in-oil-in-water (W/O/W) emulsion. The water in oil emulsion was prepared by mixing the membrane phase and internal phase. To prepare the membrane phase, the extractant D2EHPA (di-2-ethylhexylphosphoric acid) was used as a mobile carrier, Span-80 as a surfactant, and Paraffin as a diluent. Moreover, the internal (receiving) phase was prepared by dissolving sulphuric acid in water. Di-(2- ethylhexyl) phosphoric acid such as surfactant concentration, carrier concentration, sulphuric acid concentration in the receiving (internal) phase, agitation time (emulsion phase and feed phase), the volume ratio of the membrane phase to the receiving phase, the volume ratio of the external feed phase to the primary water-in-oil emulsion and pH of feed were studied on the percentage extraction of metal ions at 20℃. The results show that it is possible to remove 78% for As(V), 98% for Cd(II), and 99% for Pb(II). Emulsion Liquid Membrane (ELM) is a well-known technique for separating heavy metal ions from wastewater due to the fast extraction and is a single-stage operation of stripping-extraction. The selection of ELM components (Surfactant and Carrier) is a very significant step in its preparation. In the ELM technique, the primary water-in-oil (W/O) emulsion is emulsified to produce water-in-oil-in-water (W/O/W) emulsion. The water in the oil emulsion was prepared by mixing the membrane and internal phases. The extractant D2EHPA (di-2-ethylhexylphosphoric acid) was used as a mobile carrier, Span-80 as a surfactant, and Paraffin as a diluent. Moreover, the internal (receiving) phase was prepared by dissolving sulphuric acid in water. Di-(2-ethylhexyl) phosphoric acid such as surfactant concentration, carrier concentration, sulphuric acid concentration in the receiving (internal) phase, agitation time (emulsion phase and feed phase), the volume ratio of the membrane phase to the receiving phase, the volume ratio of the external feed phase to the primary water-in-oil emulsion and pH of feed were studied on the percentage extraction of metal ions at 20℃. The results show that it is possible to remove 78% for As(V), 98% for Cd(II), and 99% for Pb(II).

• 청정기술
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• 제13권4호
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• pp.274-280
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• 2007

본 연구에서는 염화 제2철 수용액의 재생 공정에 주로 쓰이고 있는 철환원법을 대체하기 위한 방법으로, 액-액 용매 추출법을 사용하여 수용액 내에 잔존해 있는 중금속인 Fe와 Ni을 분리 회수하는 공정을 개발하였다. Lab 실험을 통해 우선 염화 제2철 수용액으로부터 선택적으로 염화 제2철만을 추출할 수 있는 용매조건을 개발하였고, 그 결과를 사용하여 액-액 추출공정의 상업화 추진을 위한 pilot 공정 및 장치를 개발하였다. 또한 pilot test를 통하여 추출단과 역추출단의 단수를 결정할 수 있었고, 양산 공정에 적용할 수 있는 공정 데이터를 확보하였다.

• KSBB Journal
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• 제8권1호
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• pp.83-88
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• 1993

연속추출시 그 상의 분리가 용이한 spray column 에서 역미셀을 이용한 추출에 영향을 미치는 pH, 접촉횟수, 유속, 수용상과 유기상의 비 등 추출에 영향을 미치는 여러 인자들을 조사해 보았다. 그 결과 lipase는 등전점보다 낮은 3.6-4.5 사이에서 추출이 잘되었으며 역추출시에는 그와 반대로 등전점보다 높은 pH인 8.0-9.0에서 잘 추출되었다. 수용상과 유기상 사이의 접촉횟수가 증가함에 따라 추출량이 증가되었으며 추출시 계면활성제의 손실 때문에 유기상의 계속적인 공급이 필요하다. 유속의 효과는 접촉면적과 유기상 사이의 물의 함량의 반대효과로 0 0.068ml/sec과 0.101ml/sec사이에서 최적의 값을 갖는다. 수용상과 유기상간의 비에 따른 추출량은 예측했던데로 수용상의 양이 많을수록 그 추출량이 급격히 증가하는 경 향을 보였다. 각각에서 활성도는 추출전에 비해 70%의 회수율을 보였다.