• 한국미생물·생명공학회지
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• 제20권2호
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• pp.190-195
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• 1992

Polythylene glycol/dextran 수성 2단계에서 polyethylene glycol의분자량과 농도가 증가할수록 체적비는 증가하고 분배계수는 감소하였다. 또한 dextran의 분자량이 증가할 수록 체적비는 감소하고 분배계수는 증가하였다. 한편 dextran의 농도가 증가할수록 체적비와 분배계수는 감소하였다.

• KSBB Journal
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• 제8권2호
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• pp.178-184
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• 1993

Extractive fermentations with the extract of Jerusalem artichoke in an aqueous-two-phase-system of polyethyleneglycol(PEG) and dextran(Dx) were investigated to obtain the effects of composition of PEG and Dx on both fermentation ,characteristics and partition ratio of alcohol. The specific growth rate of K. Fraglis CBS 1555 increased with a decrease of concentration of PEG and Dx. It augmented along with concentration of initial sugar up to 80g/l but decreased thereafter. The specific production rate of alcohol showed a rising tendency up to 100g/lof initial sugar, whereafter represented a decreasing trend. The partition ratio of alcohol between two phases augmented according to decrease of Dx comic. and increase of PEG cone. regardless of initial sugar concentrations. The ratio, however, decreased with Increment of initial sugar concentration at constant composition of PEG and Dx. The partition coefficient of alcohol had an ascending effect to the increase of PEG cone, but it had little effect on the changes of concentrations of Dx and initial sugar. The present study suggests that the optimum composition of PEG and Dx in the aqueous-two-phase-system by extractive fermentation were around 6.5%(w/v) of PEG and 3%(w/v) of Dx in considerations of emulsion state, sedimentation and separation of two phases, alcohol partition ratio, and specific growth rate.

• 대한의용생체공학회:의공학회지
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• 제28권2호
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• pp.244-249
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• 2007

Fluidic conditions for the separation of phases were surveyed in a microfluidic aqueous two-phase extraction system. The infusion ratio between polyethylene glycol (PEG) and dextran solution defines the concentrations of each polymer in micro-channel, which determine the phase-separation. The appropriate ratio between PEG (M.W. 8000, 10%, w/v) and dextran T500 (M.W. 500000, 5%, w/v) in order to perform the separation of phases of both polymers was observed as changing the mixed ratio of both polymers. Based on the fluidic conditions, stable two-phase solutions were obtained within 4% to 8% and 3% to 1% of PEG and dextran, respectively. In addition, the characteristics of the two-phase were discussed. The separation technique studied in the paper can be applied for the implementation of a lab-on-a chip which can detect various biological entities such cells, bacterium, and virus in an integrated manner using built in a biosensor inside the chip.

• 한국환경과학회지
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• 제9권2호
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• pp.159-164
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• 2000

For the purpose of development of a liquid membrane permeator which separates metal ions from aqueous solutions continuously and effectively, a continuous membrane permeator with the membrane solution trapped between extraction and stripping phases by two micro-porous hydrophilic films was manufactured. Experimental researches on the separation of zinc ion from aqueous solutions were performed in the liquid membrane permeator with 30 vol % D2EHPA solution in kerosine as liquid membrane. As results, the liquid membrane permeator separates zinc ion from aqueous solutions continuously and effectively in the wide range of operating conditions. A simple mass transfer rate model using equilibrium constant of the extraction reaction for the system used were proposed, and the model was compared with experimental results of separation of zinc ion in the permeator. And the effects of operating factors, such as space time, pH of extraction solution, extraction temperature, on the separation rate of zinc ion in the permeator were experimentally examined.

• Nuclear Engineering and Technology
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• 제27권2호
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• pp.216-225
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• 1995

TBP 유기상으로 부터 질산용액으로 U(VI)의 물질 이동과 그 질산용액에서 U(VI)의 U(IV)으로 전해 환원과정을 갖는 두 상으로 구성된 계에서 U(IV)을 전해적인 방법으로 생산하기 위해 필요한 기본설계 자료로서의 운전조건 및 전극면적 계산을 위한 계의 수치해석이 수행되었다. 효과적인 U(IV)의 생산수율을 위해서는 적절한 물질전달 면적을 유지시키는 것이 전극면적을 증가시키는 것보다 중요하였으며, 전극면적과 운전시 간은 최종 수용액의 U(IV) 조성에 큰 영향을 주는 것을 알 수 있었다 또한 여러 계의 조건에서 최종 용액의 U(IV) 생산 조건을 만족시키기 위한 최적 전극면적이 계산되었다. 수용상의 최적 질산 농도는 U(IV) 생산만을 위해서는 약 0.37M이나, 용액중의 U(IV)의 가수분해를 방지하기 위해 최소한 0.5M을 유지해야 함을 알 수 있었다.

• 청정기술
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• 제20권4호
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• pp.349-353
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• 2014

숙신산은 의약품, 식품 첨가물, 청정용매와 같은 종래의 응용 이외에도 생분해성 고분자의 중요한 전구물질로 주목 받고 있다. 그러나 최근 화석 연료의 높은 가격과 화석 원료 유래 제품의 전주기에 걸친 온실가스 배출로 인해 재생 가능한 바이오매스에 의한 숙신산의 생물학적 생산에 대한 관심이 높아지고 있다. 본 연구에서는 숙신산의 선택적인 추출과 농축을 동시에 수행할 수 있는 공정으로서 이미다졸계 이온성 액체/$K_2HPO_4$에 의한 수상이성분계를 적용하였다. 실험 결과 숙신산에 존재하는 $K_2HPO_4$ 수용액에 적정량의 이미다졸계 이온성 액체가 첨가됨에 따라 안정한 수상이성분계가 형성됨을 확인할 수 있었으며 수상이성분계 형성 능력은 [HMIm][Br]${\fallingdotseq}$[OMIm][Br]>[BMIm][Br]>[EMImBr]의 순서로 나타났다. 숙신산의 최대 추출 효율은 약 90%였으며 이온성 액체에서 양이온 사슬길이가 증가할수록 상부상으로 동반 추출되는 물의 양이 줄어들어 숙신산의 선택적 농축효과가 크게 나타났다. 따라서 본 연구에서 사용된 이미다졸계 이온성 액체와 $K_2HPO_4$으로 구성된 수상이성분계는 숙신산의 선택적 추출과 농축에 효과적임을 알 수 있었다.

• Macromolecular Research
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• 제9권1호
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• pp.51-65
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• 2001

Two-stage emulsion polymerizations of hydrophobic monomers on hydrophilic seed polymer particles were carried out to make core-shell composite particles. It was found that the loci of polymerization in the second stage were the surface layer of the hydrophilic seed latex particles, and that it has resulted in the formation of either eccentric core-shell particles with the core exposed to the aqueous phase or aggregated nonspherical composite particles with the shell attached on the seed surface as many small separated particles. The driving force of these phenomena is related to the gain in free energy of the system in going from the hydrophobic polymer-water interface to hydrophilic polymer-water interface. Thermodynamic analysis of the present polymerization system, which was based on spreading coefficients, supported the likely occurrence of such nonspherical particles due to the combined effects of interfacial free energies and phase separation between the two polymer phases. A hypothetical pathway was proposed to prepare hydrophilic core-hydrophobic shell composite latex particles, which is based on the concept of opposing driving and resistance forces for the phase migration. It was found that the viscosity of the monomer-swollen polymer phase played important role in the formation of particle morphology.

• Korean Chemical Engineering Research
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• 제54권1호
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• pp.52-56
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• 2016

본 연구에서는 숙신산 추출을 위한 효과적인 분리공정으로서 피페리딘계 이온성 액체/$K_2HPO_4$에 의한 수상이성분계를 적용하여 수상이성분계 형성 특성 및 추출특성을 고찰하였다. 실험 결과 $K_2HPO_4$ 수용액에 적정량의 피페리딘계 이온성 액체를 첨가함에 따라 안정한 수상이성분계가 형성됨을 확인할 수 있었으며 이성분계 형성능력은 이온성 액체 내 양이온의 알킬 사슬길이에 따라 증가하였다. $K_2HPO_4$ 수용액을 기준으로 피페리딘계 이온성 액체의 수상이성분계 형성 능력은 이미다졸계나 피롤리딘계에 비해 우수하였다. 피페리딘계 이온성 액체를 이용한 수상이성분계 추출에 있어 숙신산 추출 효율은 75~95%의 범위를 가지며 이 값들은 이미다졸계나 피롤리딘계와 큰 차이가 없었다. 그러므로 피페리딘계 이온성 액체를 이용한 수상이성분계를 숙신산 추출에 적용할 경우 이미다졸계 및 피롤리딘계에 비해 적은 양의 이온성 액체를 사용하여 높은 추출효율을 얻을 수 있음을 확인할 수 있었다.

• 한국지하수토양환경학회:학술대회논문집
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• 한국지하수토양환경학회 2001년도 추계학술발표회
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• pp.115-119
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• 2001

Contaminant retardation factor is derived from the colloidal and contaminant transport equations for a four-phase porous medium: an aqueous phase, two mobile colloidal phases, and a solid matrix. It is assumed that the contaminant sorption to solid matrix and colloidal particles and the colloidal deposition on solid matrix follow the linear isotherms. The behavior of the contaminant retardation factor in response to the change of model parameters is examined employing the experimental data of Magee et al. (1991) and Jenkins and Lion (1993). In the four-phase system, the contaminant retardation factor is determined by both the contaminant association with solid matrix and colloidal particles and the colloidal deposition on solid matrix. The contaminant mobility is enhanced when the affinity of contaminants to mobile colloids increases. In addition, as the affinity of colloids to solid matrix decreases, the contaminant mobility increases.

• 한국막학회:학술대회논문집
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• 한국막학회 1998년도 추계 총회 및 학술발표회
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• pp.15-18
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• 1998

Membrane reactors are systems which combine a chemical reactor with a membrane separation process allowing to carry out simultaneously conversion and product separation. The catalyst can be immobilized on the membrane or simply compartmentalized in a reaction space by the membrane. Membrane reactors are today investigated to produce optically pure isomers and/or resolve racemic mixture of enantiomers. The interest towards these systems is due to the increasing demand of enantiomerically pure compounds to be used in the pharmaceutical, food, and agrochemical industries. In fact, enantiomers can have different biological activities, which often influence the efficacy or toxicity of the compound. On the basis of current literature there are basically two schemes on the use of membrane technology to produce enantiomers. In one case, the membrane itseft is intrinsically enantioselective: the membrane is the chiral system which selectively separates the wanted isomer on the basis of its conformation. In the other, a kinetic resolution using an enantiospecific biocatalyst is combined with a membrane separation process; the membrane separates the product from the substrate on the basis of their relative chemical properties (i.e. solubility). This kind of configuration is widely used to carry out kinetic resolutions of low water soluble substrams in biphasic membrane reactors [Giomo, 1995, 1997; Lopez, 1997]. These are systems where enzyme-loaded membranes promote reactions between two separate phases thanks to the properties of enzymes, such as lipases, to catalyse reactions at the org ic/aqueous interface; the two phases are maintained in contact and separated at the membrane level by operating at appropriate transmembrane pressure. A schematic representation of biphasic membrane reactor is shown in figure 1, while an example of enantiospecific reaction and product separation carried out with these systems is reported in figure 2.