• 제목/요약/키워드: two-liquid phase system

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식기세척기 내부 유동 분포 분석을 위한 유동가시화 기법 개발 (Development of Flow Visualization Technique for Analysis of Flow Distribution inside Dishwasher)

  • 김아란;함정윤;조진호;조위삼;고한서
    • 한국가시화정보학회지
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    • 제11권2호
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    • pp.12-17
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    • 2013
  • A flow visualization technique was developed to analyze flow distribution inside a dishwasher in this study. Then, a new design plan was proposed to improve the efficiency of the dishwasher by the analyzed results and it was confirmed experimentally by the developed technique. Gas flow fields inside a drying duct of a tub for a drying process was investigated by a developed PIV (Particle Image Velocimetry) and a CFD (Computational Fluid Dynamics) method. Also, the flow visualization technique was developed for the liquid flow field of a rotor-arm system to propose the improved design idea. Also, interactions between liquid and gas were observed around the rotor-arm system. The two-phase flow was modified to the liquid flow field because laser sheets are refracted when pass through the two-phase flow. Thus, the flow visualization techniques was developed in this study to measure the instantaneous flow velocities in the liquid quantitatively.

다중 층 화장료에서 수성 이상계의 응용 (Applying Aqueous Two Phase Systems to Multi-layer Cosmetics)

  • 홍준기;유재원;유장영;남승옥;이상길;표형배
    • 대한화장품학회지
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    • 제39권2호
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    • pp.83-88
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    • 2013
  • 수성 이상계는 물에 친수 성분만을 용해시킨 후 용해 물질들 사이에 유발되는 단순한 물리적 불친화성에 의해 액상 다중 층으로 분리되기 때문에 생체적합성에 대한 장점을 가지고 있다. 본 연구에서는 물에 친수 성분만을 용해시킨 후 두 층으로 분리되는 수성 이상계 상분리 원리를 수성 다중 층 액상 화장료에 응용하여 수성 다중 층 화장료에 적용이 가능한 대표적인 두 종의 수성 이상계를 선정하였으며, 이들에 대해 바이노달 곡선과 임계점 및 농도 대응선 그리고 새로운 개념의 상분리 부피 및 상분리 시간 대응곡선을 포함하는 상도를 실험을 통해 작성하였으며, 상 도표로부터 액상 다중 층으로 분리되는 최적의 조건을 관찰할 수 있었다.

사성분계 시스템의 액액상분리에 관한 연구 (폴리술폰/폴리에테르술폰/NMP/물) (Liquid-Liquid Phase Separation in a Quaternary System of PolysuIfone/Polyethersulfone/N-Methyl-2-pyrrolidone/water)

  • 백기전;김제영;이환광;김성철
    • 한국막학회:학술대회논문집
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    • 한국막학회 1998년도 춘계 총회 및 학술발표회
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    • pp.22-24
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    • 1998
  • 1. INTRODUCTION : The phase inversion method is widely used to prepare a variety of polymeric membranes ranging from micro-filtration to gas separation. The final morphology obtained by immersion precipitation strongly reflects the thermodynamics and kinetics of the system involved. The equilibrium thermodynamics of the ternary system of polymer/solvent/ nonsolvent is still very important to understand and predict membrane structure. Polysulfone (PSf) and polyethersulfone (PES) are important polymers as membrane materials due to the chemical resistance, mechanical strength, thermal stability and transport properies. There are several reports on the experimental phase diagrams in ternary mixtures of PSf/solvent/nonsolvent, and PES/solvent/nonsolvent. It would be interesting to investigate the solution thermodynamics containing these two polymers since PES is slightly less hyclrophobic than PSf.

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Counter-Current Air-Water Flow in Narrow Rectangular Channels With Offset Strip Fins

  • Kim, Byong-Joo;Sohn, Byung-Hu;Koo, Kee-Kahb
    • Journal of Mechanical Science and Technology
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    • 제17권3호
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    • pp.429-439
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    • 2003
  • Counter-current two-phase flows of air- water in narrow rectangular channels with offset strip fins have been experimentally investigated in a 760 mm long and 100 mm wide test section with 3.0 and 5.0 mm gap widths. The two-phase flow regime, channel-average void fractions and two-phase pressure gradients were studied. Flow regime transition occurred at lower superficial velocities of air than in the channels without fins. In the bubbly and slug flow regimes, elongated bubbles rose along the subchannel formed by fins without lateral movement. The critical void fraction for the bubbly-to-slug transition was about 0.14 for the 3 mm gap channel and 0.2 for the 5 mm gap channel. respectively. Channel-average void fractions in the channels with fins were almost the same as those in the channels without fins. Void fractions increased as the gap width increased, especially at high superficial velocity of air. The presence of fins enhanced the two-phase distribution parameter significantly in the slug flow, where the effect of gap width was almost negligible. Superficial velocity of air dominated the two-phase pressure gradients. Liquid superficial velocity and channel gap width has only a minor effect on the pressure gradients.

Microstructural Behavior of Alumina Aggregate Compacts Prepared by Transient Liquid Phase Sintering

  • Lee, Seung-Jae;Kim, Hai-Doo;Lee, Deuk-Yong;Kim, Dae-Joon
    • The Korean Journal of Ceramics
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    • 제6권1호
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    • pp.78-82
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    • 2000
  • Although alumina aggregates have been used as refractory aggregates due to the improved mechanical properties of refractories as a result of the low contraction of alumina aggregates, the aggregates have a difficulty in fabrication due to its low sinterability. Two types of alumina aggregates and a fused alumina aggregate containing transient liquid forming additives are prepared to investigate the sintering characteristics of aggregates. $Al_2O_3$rich composition in the $Al_2O_3$-MgO-$SiO_2$(-$TiO_2$) system is chosen for the transient liquid phase sintering and the final recrystallized bonding phase between grains inside the fused alumina aggregates is found to be a needle-like mullite phase. The flexural strength of alumina bars, reaction-bonded using the paste having a composition of $Al_2O_3$-MgO-$SiO_2$-$TiO_2$, is about 78 MPa, which is one half value of that of pure alumina.

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Two-Phase Flow through a T-Junction

  • Tae Sang-Jin;Cho Keum-Nam
    • International Journal of Air-Conditioning and Refrigeration
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    • 제14권1호
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    • pp.28-39
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    • 2006
  • Two-phase flow through a T-junction has been studied by numerous researchers so far. The dividing characteristics of the gas and liquid phases at the T-junction are very complicated due to a lot of related variables. The prediction models have been suggested by using experimental data for a specific condition or working fluid. But, they showed the application limitation for the most of the other conditions or fluids. Since most of them are applicable for their own experimental range, the generalized model for the wide range of conditions and fluids is needed. Even though it's not available now, some of the models developed for air-water flow at a T-junction might be applicable for the part of refrigerants with some modifications. Especially, for the two-phase flow of refrigerants at the T-junction, very few studies have been performed. Further experimental study is required to be performed for the wide range of test conditions and fluids to predict properly the two-phase flow distribution and phase separation through the T-junction.

중성자 래디오그래피를 이용한 액체금속 유동장 측정 (Measurement of Liquid-Metal Flow with a Dynamic Neutron Radiography)

  • 차재은;사이토
    • 한국가시화정보학회지
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    • 제9권4호
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    • pp.63-68
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    • 2011
  • The flow-field of a liquid-metal system is very important for the safety analysis and the design of the steam generator of liquid-metal fast breeder reactor. Dynamic neutron radiography (DNR) is suitable for a visualization and measurement of a liquid metal flow and a two-phase flow in a metallic duct. However, the three dimensional DNR techniques is not enough to obtain the velocity information in the wide channel up to now. In this research, a high speed DNR technique was applied to visualize the heavy liquid-metal flow field in the narrow channel with the HANARO-beam facility. The images were taken with a high frame-rate neutron radiography at 250 fps and analyzed with a Particle Image Velocimetry(PIV) method. The images were compared with the results of the commercial CFX code to study the feasibility of DNR technique for the measuring the heavy liquid-metal flow field. The PIV images could discern the turbulent vortex flow in the two-dimensional narrow channel.

교반조에서 비혼화성 액상(n-헥산/물)계의 액-액분산 (Liquid-Liquid Dispersion of an Immiscible Liquid Phase (n-Hexane/Water) System in a Stirred Tank)

  • 김태옥;김동욱;전종한
    • 공업화학
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    • 제4권3호
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    • pp.537-543
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    • 1993
  • N-헥산과 증류수로 이루어진 비혼화성 액상계에서 교반에 의한 액-액분산을 해석하였다. 교반기는 blade형태가 flat, 60mesh와 40mesh의 금망, 그리고 60mesh금망의 외부에 금속띠를 두른 4가지의 6-bladed turbine 교반기를 사용하였다. 실험결과, 동일한 교반속도에서 유기상의 분산정도와 교반기의 소요동력은 blade형태가 flat>solid edged>60mesh>40mesh의 순서이었으며 유기상의 부피비가 증가할수록 완전분산에 필요한 최소교반속도가 증가되었다. 또한 분산상의 액적의 평균직경은 교반속도의 증가에 따라 감소하였으며 동일한 교반속도에서는 Solid edged$d_{32}$)은 다음과 같이 유기상의 부피비(${\phi}$)와 Weber number($N_{We}$)의 함수로 나타낼 수 있었다.$d_{32}/D=a(1+b{\phi})N_{We}{^{-0.6}}$.

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Analysis of the Esterification Process for Poly(ethylene terephthalate)

  • Ahn, Young-Cheol;Park, Soo-Myung
    • Macromolecular Research
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    • 제11권6호
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    • pp.399-409
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    • 2003
  • The first esterification reactor in the continuous polymerization of poly(ethylene terephthalate) has been analyzed by solving the material balances for the two-phase system with respect to the solubility of terephthalic acid. The Newton-Raphson method was used to solve the material balance equations instead of the Simplex method that is frequently used for finding a minimum point of a residual rather than a solution of an equation. A solution for the material balance equations, with the constraint of non-zero liquid phase fraction, could not be obtained with the solubility data of Yamada et al., but could be obtained with solubilities over a minimum value that is larger than their data. Thus, the solubility data of Yamada et al. are considered to be too small. On the other hand, the solubility data of Baranova and Kremer are so large that they gave a solution with the liquid phase only. Based on our results, several typical solubility curves satisfying the constraint of a non-zero liquid phase fraction are suggested in this study; we studied the reaction characteristics of the system using these curves. A higher temperature and a lower pressure are preferred for reducing the content of diethylene glycol.

Isobutyl-Acetate와 Isobutyl-Alcohol 이성분계의 압력변환증류 공정 최적화 연구 (Optimization Study for Pressure Swing Distillation Process for the Mixture of Isobutyl-Acetate and Isobutyl-Alcohol System)

  • 조성진;신재선;최석훈;이의수;박상진
    • Korean Chemical Engineering Research
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    • 제52권3호
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    • pp.307-313
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    • 2014
  • 본 연구에서는 Isobutyl Acetate와 Isobutyl Alcohol의 공비혼합물을 압력변환증류공정(PSD; Pressure Swing Distillation Process)을 이용하여 99.9 mol% 이상의 Isobutyl Acetate를 분리하는 공정모사를 수행하였다. 압력변환증류공정은 공비혼합물의 상대휘발도와 공비조성이 압력의 변화에 따라 차이가 나는 특성을 이용한 공정이다. 액상에서는 Non-Random Two Liquid (NRTL) model을 그리고 기상에서는 Peng-Robinson equation을 이용하였다. 최적화 방법으로 환류비와 주입단 위치를 변수로 두고 총 재비기 소요 열량을 최소화시키는 목적으로 최적화를 수행하였다. 압력변환 증류공정은 두 개의 증류탑을 필요로 함에 따라 고압 증류탑과 저압 증류탑의 배열에 따른 최적화 조건 또한 비교를 수행하였다.