• Proceedings of KOSOMES biannual meeting
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• 2009.06a
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• pp.87-88
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• 2009

In evaporating distillation plant velocity characteristic of fluid to flow in a evaporator have great influence on flash phenomenon. In This experimental study about impinging water jet region having the inflow of wall jet flow and effect of baffle height to flow velocity in after baffle region, making a application by PIV.

• Journal of the KSME
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• v.33 no.11
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• pp.966-972
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• 1993

모세관(capillary tube)은 일정면적식 팽창기구의 대표적인 것으로서 사용역사가 길고, 신뢰성이 높고, 가격이 저럼하므로 냉동공조시스템의 냉매제어장치로 매우 많이 사용되고 있다. 이것은 냉동시스템의 응축기와 증발기 사이에서 유입하는 고압의 액상냉매를 증발기에서 증발하기 쉬운 증발압력까지 압력을 강하시키는 감압팽창작용과 증발기의 증발 용량에 적당한 냉매 질량유량을 공급하는 역할 (이 작용은 냉동시스템의 용량과 작동범위를 결정하는데 매우 중요하다.)을 한다. 이 글에서는 모세관의 형상, 재질 및 그장 . 단점과 작동원리, 내부 유동현상 등 일반적인 사항에 관하여 기술한다.

• Transactions of the Korean Society of Mechanical Engineers
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• v.14 no.3
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• pp.702-715
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• 1990

This paper describes behaviors of two-phase open channel flow inside the flash chamber of a horizontal Multi-Stage-Flash evaporator numerically along with the experimental observations. Bubble trajectories and the velocity and temperature distributions of the liquid phase were predicted by using the particle-source-in-cell(PSI-Cell) method with the appropriate bubble motion/growth equations. Size and number of bubble nuclei embedded in the incoming liquid(brine) were taken into account as important parameters in addition to the conventional ones such as the velocity, degree of inlet superheat, inlet opening height, and the liquid level. Bubble motions, which are unsteady, appeared to be mostly determined by the buoyancy and the drag forces. The calculations, though a number of simplifying assumptions were made, reasonably simulated the hydrodynamic behaviors of the two-phase horizontal stream observed in the experiments. The simulated temperature distributions also agreed fairly well with the other's measurements. Non-equilibrium allownaces, evaluated from the simulated temperature distributions, were within the range of those obtained from the existing correlations, and reduced with the increases of the number and size of incoming bubble nuclei due to vigorous flashing.

• Journal of the Korea Academia-Industrial cooperation Society
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• v.13 no.4
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• pp.1466-1473
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• 2012

Soft icecream is made by scraping an ice formed on the inside of the cylindrical evaporator, where R-404A is evaporating in the annulus. The heat transfer characteristics of the refrigerant evaporation and those during icecream formation were experimentally investigated. Results show that the refrigerant-side heat transfer coefficients are highly dependent on the location in the evaporator due to the complex annulus configuration. The heat transfer coefficient at the inlet is generally lower than those of other locations. The average heat transfer coefficient increases as heat flux increases or saturation temperature decreases. A correlation is developed to predict the refrigerant-side heat transfer coefficient. The icecream-side heat transfer coefficient oscillates continuously due to the periodic removal of ice formed on the surface. The average heat transfer coefficient during icecream formation is approximately 280 W/$m^2K$, and that during single-phase cooling increased from 150 W/$m^2K$ to 250 W/$m^2K$.

• Proceedings of the Korean Vacuum Society Conference
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• 2010.08a
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• pp.11-11
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• 2010

고도의 진공 환경을 요구하는 반도체 생산 라인에 적용되는 고진공 펌프는 주로 복합 분자펌프와 크라이오 펌프가 사용되고 있다. 이 중 크라이오 펌프는 극저온으로 냉각되는 냉각판에 기체 분자를 응축 또는 흡착시켜 기체를 제거하는 방식으로 복합 분자 펌프로 무게가 가볍고 증발 온도가 낮은 네온, 수소, 헬륨 기체 제거에 장점이 있다. 본 연구에서는 현재 상용화된 크라이오 펌프에 적용되는 GM 극저온 냉동기를 대체하기 위한 2단 GM형 맥동관 냉동기를 개발하여 기초 성능 시험을 수행하였다. 1단과 2단 모두 U-자형 형상으로 제작되었으며, 압력과 질량 유동 사이의 위상 조절을 위하여 오리피스 밸브와 이중 유입 밸브를 사용하였다. 개발된 맥동관 냉동기의 냉각 성능 목표는 1단(80 K)과 2단(20 K)에서 각각 45 W와 5 W이다. 기초 시험에서는 위상 조절용 밸브들의 개도와 작동 조건에 대한 냉각 특성과 부하 특성 시험을 수행하였다. 특히, 본 연구에서는 로터리 밸브 및 위상 조절 기구의 배치로 인해 고온부 형상이 복잡한 맥동관 냉동기를 크라이오 펌프로의 적용 편의성을 위하여 고온부 외형 구조를 단순화하였으며, 개발된 맥동관 냉동기와 기존에 크라이오 펌프에 적용되는 GM 극저온 냉동기를 비교, 고찰하였다.

• Microbiology and Biotechnology Letters
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• v.20 no.4
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• pp.451-458
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• 1992

Pervaporation which is capable of removing ethanol selectively was adopted to reduce the ethanol inhibition and in situ recovery of ethanol in ethanol fermentation, The composite membrane made of silicone and polysulfone was used to separate the ethanol selectively. The ethanol selectivity of the membrane was about 4 and the total flux was 300 g/m2 h at 301:: and 10 mmHg for 25 g/l of feed concentration. Saccharomyces cerevisiae entrapped within Ca-alginate gels was employed for ethanol fermentations in a fluidized-bed bioreactor. The pervaporation membrane unit and fluidized-bed bioreactor were combined into one system. The proposed model equations for the combined system showed good accordances with the experimental results. It was found from the simulation results that the ethanol concentration in the broth for the combined system was lower than that for the continuous fermentation system without a membrane unit. Ethanol productivity can be thus increased by employing the combined system.