• Title/Summary/Keyword: 헬륨 기포

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Numerical Study on Compressible Multiphase Flow Using Diffuse Interface Method (Diffuse Interface Method를 이용한 압축성 다상 유동에 관한 수치적 연구)

  • Yoo, Young-Lin;Sung, Hong-Gye
    • Journal of Aerospace System Engineering
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    • v.12 no.2
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    • pp.15-22
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    • 2018
  • A compressible multiphase flow was investigated using a DIM consisting of seven equations, including the fifth-order MLP and a modified HLLC Riemann solver to achieve a precise interface structure of liquid and gas. The numerical methods were verified by comparing the flow structures of the high-pressure water and low-pressure air in the shock tube. A 2D air-helium shock-bubble interaction at the incident shock wave condition (Mach number 1.22) was numerically solved and verified using the experimental results.

Experimental Performance Study of the Bubble Pump for the Diffusion Absorption Refrigerating System (확산형 흡수식 냉동시스템의 기포펌프 성능실험)

  • 이재효;정의갑;윤재호;정의갑
    • Korean Journal of Air-Conditioning and Refrigeration Engineering
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    • v.16 no.3
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    • pp.287-292
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    • 2004
  • An experimental investigation was carried out to study the performance of a bubble pump for the diffusion absorption refrigerating system. Ammonia was used as the refrigerant and the helium was charged in order to balance the pressure between the low and high pressure side. As experimental variables, the concentration of ammonia charged into system, heat input, and the pressure of helium were selected. Experimental results show that the generation rate of ammonia vapor and the circulation rate of diluted ammonia solution were increased as the heat input increases, but the ratio of the solution to vapor flow rate was decreased. The generation rate of refrigerant vapor and the circulation rate of diluted ammonia solution increased as the system pressure decreased. Finally under the condition of 25 bars, the concentration of rich ammonia solution was not affected by the generation rate of ammonia vapor and the circulation of diluted ammonia solution.

Power Savings of a Refrigerator with 3D-PTV Measurements (3D-PTV에 의한 냉장고 소비전력 저감)

  • Hwang Tae-Gyu;Doh Deog-Hee;Park Seong-Ryong;Bang Yoon-Seok;Yang Min-Cheol;Jang Gyu-Seob;Kim Suk-Roh;Lee Yeon-Won
    • Korean Journal of Air-Conditioning and Refrigeration Engineering
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    • v.17 no.12
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    • pp.1145-1153
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    • 2005
  • 3D-PTV measurement has been carried out for the inner flows of a refrigerator. To visualize the air flows three-dimensionally, a helium bubble generator has been used for the 3D-PTV measurements. Three-dimensional flow field of the refrigerator's compartments have been reconstructed by the results obtained by the 3D-PTV Measurements on the electric power-consumption was also carried out in order to evaluate the improvements of the flow characteristics. It was verified that $3\%$ of power consumption was saved by improving the flow passages and characteristics.

Optimum Size Combination of Heat Exchangers in a Small Gifford-Mchon/ Joule-Thomson Refrigerator (소형 Gifford-McMahon/Joule-Thomson 냉동기에서 열교환기의 최적 조합)

  • 김영률;이상용;장호명
    • Transactions of the Korean Society of Mechanical Engineers
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    • v.16 no.11
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    • pp.2196-2202
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    • 1992
  • The optimum size combination of heat exchangers in a Joule-Thomson(J-T) circuit for small cryogenic systems has been sought analytically, when the circuit is combined with a two-stage Gifford-McMahon(GM) cooler. Full thermodynamic cycle analysis was carried out to predict the performance of the combined refrigeration system. Relevant convective heat transfer coefficients, the computerized properties of helium, and the refrigeration capacity curve of a typical GM cooler have been used in the analysis. The result showed that, by changing the configuration(heat exchanger area ratio) of the system, the performance of the commonly-used GM/J-T refrigerators could be optimized. For the maximum refrigeration performance, the optimum mass flow rate of the refrigerant and the relative size between the heat exchangers have been obtained, when the cooling load was 0.1W at 3.995K with the total heat exchanger area being given.