• 제목/요약/키워드: Aqueous system

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수계 세정시스템의 세정액/헹굼수의 모니터링 및 재활용 기술 분석 (Analysis of Monitoring and Recycling Technology Technologies of Cleaning Solution and Rinse Water in the Aqeous Cleaning System)

  • 한상원;이호열;배제흠;유종훈;박병덕;전성덕
    • 청정기술
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    • 제7권4호
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    • pp.225-242
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    • 2001
  • 산업체에서 부품을 가공하거나 완성품을 제조하는 과정에서 세정 공정은 필수적으로 사용하고 있고 현재 국내외 대부분의 제조업체에서는 오존파괴물질인 CFC-113이나 1,1,1-TCE 대신에 보다 환경친화적인 수계 세정제로의 대체가 진행중이다. 그러나 수계 세정시스템은 세정공정이나 헹굼공정에서 다량의 물을 사용하기 때문에 많은 폐수를 발생시키는 단점이 있다. 따라서 수계 세정시스템에서는 이러한 발생을 최소화하고 세정액과 헹굼수의 성능을 오랫동안 유지시키기 위한 모니터링 기술과 재활용 기술의 도입이 긴요하다. 본고에서는 수계 세정시스템에 사용하는 세정제와 주요 오염물질인 절삭유를 조사 분석하였고 산업현장에서 도입 가능한 수계 세정시스템의 모니터링 기술과 재활용 기술 등을 분석 평가하였다.

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공냉형 흡수식 냉방 시스템에서 LiBr 수용액의 과열도가 증기 흡수에 미치는 영향 (Effect of degree of superheat of LiBr aqueous solution on the vapor absorption process for an air-cooled absorption cooling system)

  • 김선창;오명도;이재헌
    • 설비공학논문집
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    • 제9권2호
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    • pp.122-133
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    • 1997
  • Numerical analysis using finite volume method has been carried out to examine the effect of degree of superheat of LiBr aqueous solution on heat and mass transfer occurred in absorption process. According to the result of this study, it was found that refrigerant vaper was generated at the entrance region of absorber when LiBr aqueous soltion was superheated. As the degree of superheat increases, heat transfer rate increases and vapor absorption rate decreases. The increase in averaged Nusselt and Sherwood numbers could be found as film Reynolds number increases. The larger the degree of superheat, the greater the averaged Nusselt and Sherwood numbers.

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$\alpha$-Amylase로 전분 가수분해를 위한 PEG/Dextran 수성 2상계 구성 (Formation of PEG/Dextran Aqueous Two-Phase System for Starch Hydrolysis Using $\alpha$-Amylase)

  • 박병춘;임동준
    • 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.

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전산모사를 활용한 Fe-Cr-Ni 전주용 수용액의 안정성 분석 (Computational Analysis of Aqueous Solution Stability for Electroformed Fe-Cr-Ni Thin Layer)

  • 전승환;한상선;김마로;최용;이상범
    • 한국표면공학회:학술대회논문집
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    • 한국표면공학회 2014년도 추계학술대회 논문집
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    • pp.214-214
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    • 2014
  • Computational analysis of aqueous solution stability of Fe-Cr-Ni system to find an electroplating condition of Fe-Cr-Ni layer. Aqueous sulfate solution with iron, chromium and nickel ions was selected by using a numerical S/W with which aqueous solution stability was analyzed. Several possible conditions to perform electro-forming of Fe-Cr-Ni were selected with thermo-dynamical data. The Fe-Cr-Ni system was electro-formed which composition and microstructure of the electroplated Fe-Cr-Ni significantly depended on the solution temperature and electro-potential. The final composition of Fe-3%Cr-48%Ni with less than $30{\mu}m$ thick was well electroplated.

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Diffusion Coefficients and Membrane Potential within Carrier Membrane by Reverse Transport System

  • Yang, Wong-Kang;Jeong, Sung-Hyun;Lee, Won-Chul
    • Korean Membrane Journal
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    • 제4권1호
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    • pp.36-40
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    • 2002
  • The diffusion coefficients of ions in the reverse transport system using the carrier mediated membrane were estimated from the diffusional membrane permeabilities and the ion activity in membrane system. In the aqueous alkali metal ions-membrane system diffusional flux of alkali metal ions driven by coupled proton was analyzed. The aqueous phase I contained NaOH solution and the aqueous phase II also contained NaCl and HCl mixed solution. The concentration of Na ions of both phases were $10^{0},\;10^{-1},\;10^{-2},\;5{\times}10^{-1}\;and\;5{\times}10^{-2}\;mol{\cdot}dm^{-3}$ and the concentration of HCI in aqueous phase II was always kept at $1{\times}10^{-1}\;mol{\cdot}dm^{-3}$. Moreover, the carrier concentration in liquid membrane was $10^{-2}\;mol{\cdot}dm^{-3}$. The results indicated that the diffusion coefficients depend strongly on the concentration of both phases electrolyte solution equilibriated with the membrane. The points were interpreted in terms of the energy barrier theory. Furthermore, eliminating the potential terms from the membrane equation was derived.

Partitioning of Recombinant Human Interleukin-2 in a Poly(ethylene glycol)-Dextran Aqueous Two-Phase System

  • Lee, In-Young;Lee, Sun-Bok
    • Journal of Microbiology and Biotechnology
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    • 제2권2호
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    • pp.135-140
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    • 1992
  • The partitioning of recombinant human interleukin-2(rhII-2) in PEG 8000-dextran 38800 aqueous two-phase system has been investigated using three different sources of rhIL-2. In the case of pure rhIL-2, the solubility in a PEG-dextran two-phase system was low and most of rhIL-2 was partitioned into the bottom phase. For the recovery of rhIL-2 from insoluble protein aggregates, the inclusion bodies of recombinant E. coli were solubilized by the treatment with sodium dodecyl sulfate (SDS). The addition of SDS significantly enhanced not only the solubility of rhIL-2 but also the partitioning of rhIL-2 to the top phase. When the ratio of SDS to rhIL-2 was 2.0, the partition coefficient(K) and the recovery yield(Y) at the top phase were 4.5 and 88%, respectively, at pH 6.8. In order to reduce the recovery steps further, SDS was directly added to the intact recombinant E. coli cells and then partitioned into the PEG/dextran aqueous two-phase system. The observed partition coefficient ($K{\cong{3.0$) and recovery yield ($Y{\geq}80%$ )of this method were comparable to the rhIL-2 recovery from insoluble protein aggregates. The results obtained in this work indicate that PEG-dextran two-phase partitioning might provide a simple way for the recovery and partial purification of recombinant proteins which are produced as inclusion bodies.

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Production of Cyclodextrin Homologues Using Aqueous Two-Phase System

  • Chang, Woo-Jin;Koo, Yoon-Mo;Park, Sung-Sik
    • Biotechnology and Bioprocess Engineering:BBE
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    • 제2권2호
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    • pp.97-100
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    • 1997
  • Cyclodxtrin homologues(CDs), produced by cyclodextrin glycosyltransferase(CGTase), were simultaneously partitioned in aqueous two-phase system(ATPS). Partition coefficients of CDs were measured in PEG/dextran systems. Phosphate, citrate, sulfate were tested as salt. ATPS of PEG/salt and PEG/dextran had the partition coefficients of the CDs, larger than unity. However, PEG/dextran system was observed better than PEG/salt as CGTase activity decreased sharply with salt concentration. Enzymatic rection occurred mainly in PEG-rich bottom phase because of the low partition coefficient of CGTase. The resulting CDs transferred to the PEG-rich top phase, obeying the diffusional partition. In the ATPS of 7% PEG(M.W.40, 000), 7mg/ml of CDs were obtained in top phase at 4.5 hours.

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Large-Scale Purification of Protease Produced by Bacillus sp. from Meju by Consecutive Polyethylene Glycol/Potassium Phosphate Buffer Aqueous Two-Phase System

  • Cho, Seong-Jun;Kim, Chan-Hwa;Yim, Moo-Hyun;Lee, Cherl-Ho
    • Journal of Microbiology and Biotechnology
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    • 제9권4호
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    • pp.498-503
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    • 1999
  • Protease produced from Bacillus sp. FSE-68 was isolated from Meju, a Korean fermented soybean starter, and was purified by a two-consecutive aqueous two-phase system. The change of partition coefficient (K) in the polyethylene glycol (PEG)/potassium phosphate buffer (PPB) aqueous two-phase system was measured at different pHs (6.0- 9.2), PPB concentrations (8-12%), and temperatures (4 and $20^{\circ}C$). As the PPB concentration in the aqueous two-phase system increased, the protease concentration in the top phase (PEG-rich phase) increased, thereby enhancing the partition coefficient. The minimum partition coefficient of the protease was achieved at pH 7.0, whereas that of the total protein was at pH 6.0. The biggest difference in partition coefficients of total protein and protease occurred at pH 6.0. It was interesting to note that the partition coefficient of protease decreased as the temperature increased. The optimum condition of the primary aqueous two-phase extraction of Bacillus sp. FSE-68 was pH 6.0, 14% (w/w) PPB, and 16% (w/w) PEG at $4^{\circ}C$, and the crude enzyme concentration in this system was 50% (w/w). The protease, which was concentrated in the top phase, was further mixed with 15% (w/w) PPB (pH 7.0) in the ratio of 1:1 at $20^{\circ}C$ to elute the bottom phase (PPB-rich phase). Using these steps, the purification fold achieved was 9.2 with a 44.7% yield.

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수용성 이상계에서의 젖산과 Lactobacillus helveticus세포의 분배특성 (Partitioning of Lactobacillus helveticus Cells and Lactic Acid in Aqueous PEI/HEC Two-Phase Systems.)

  • 안한군;권윤중
    • 한국미생물·생명공학회지
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    • 제26권1호
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    • pp.55-60
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    • 1998
  • 수용성 이상계에서 효율적인 추출발효를 수행하기 위해서는 생체촉매와 생성물이 서로 반대 상에 우세하게 분배되어아 한다. 일반적으로 분자량이 낮은 생성물은 양쪽상에 비슷하게 분배되므로, 상의 조성 등을 조절하여 한쪽상의 체적을 증가시켜 최대한으로 생성물을 추출하여야 한다. 본 연구에서는 PEI와 HEC으로 구성된 수용성 이상계에서 L. helveticus와 젖산의 분배에 미치는 다가 음이온의 농도, pH, 배지의 농도 및 생육배지 농도 등의 영향을 검토하였다. PEI의 상대 이온으로 작용하는 phosphate, sulfate 음이온수의 증가는 PEI 상의 체적을 감소시켜 하부상에 분배되는 세포의 양(Cb)을 감소시켰으며, sulfate 농도의 영향은 phosphate에 비해 적었다. 검토한 범위에서 대략 93%이상의 세포가 HEC-rich상부상에 분배되었다. 이상계에 생육배지 농도를 달리하여 첨가했을 때 배지 중에 존재하는 phosphate와 sulfate 농도에 따라 비슷한 경향을 나타냈지만 낮은 농도로 인하여 그 영향은 크지 않았다. Phosphate 농도에 따른 젖산분배를 검토한 결과 농도가 증가할수록 분배계수는 감소하였으며, 대략 85%가량의 젖산이 PEI의 하부상에 분배되었다. 이 결과로부터 수용성 이상계에서 전하를 띤 저 분자량의 생성물의 추출은 반대 전하를 띠는 폴리머를 하나의 상형성 풀리머로 사용함으로써 증진되었음을 알 수 있었다. 따라서 L. helveticus 세포는 95% 정도가 상부상에 분배되고 젖산은 85%정도가 하부상에 우세하게 분배되므로 PEI/HEC 이상계는 치즈유청으로 부터의 젖산의 추출발효에 가능성이 높은 시스템으로 응용될 수 있는 것으로 생각된다.

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수열합성법으로 합성된 나노 SmxCe1-xO2-2/x 분말의 수계 분산 (Dispersion of SmxCe1-xO2-2/x Nanoparticles which is Synthesized by Hydrothermal Process in Aqueous System)

  • 배동식;김은정;한경섭
    • 한국재료학회지
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    • 제15권2호
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    • pp.112-114
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    • 2005
  • Dispersion stability of the $Sm_xCe_{1-x}O_{2-2/x}$ nanoparticles, which was produced by hydrothermal process, was studied in aqueous suspension using ESA (Eletrokinetic Sonic Amplitude). The average particle size of the synthesized $Sm_xCe_{1-x}O_{2-2/x}$ at nanoparticles was about $5{\pm}2nm$. The dispersion and rheological behavior of the $Sm_xCe_{1-x}O_{2-2/x}$ nanoparticles aqueous suspension was investigated using $NH_4OH\;and\;HNO_3$ as a disperse agent. The colloidal stability of aqueous suspensions with $Sm_xCe_{1-x}O_{2-2/x}$ nanoparticles at different pH values has been investigated by means of zeta potential, average particle size, and the distribution of synthesized $Sm_xCe_{1-x}O_{2-2/x}$ nanoparticles. The isoelectric point of the $Sm_xCe_{1-x}O_{2-2/x}$ nanoparticles was at pH around 11 and the value of zeta potential was at its maximum near pH 6.5.