• Title/Summary/Keyword: Thermal Storage Heat-flux meter

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금속스크랩이 혼합된 상변화물질의 유효열전도율 (Effective thermal conductivity of the phase change material with metal scrap)

  • 김시범;노승탁
    • 대한기계학회논문집
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    • 제10권6호
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    • pp.923-928
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    • 1986
  • 본 논문에서는 열전도율이 큰 금속의 스크랩과 파라핀을 혼합한 축열 매질에 있어서 스크랩의 체적 혼합율에 따르는 열전도율의 변화를 모델링과 실험으로 구해서 축열 계산에 필요한 열전도율 자료를 제시하고자 한다.

Measurement Methods of Latent Heat for PCM with Low Melting Temperature in Closed Tube

  • Hong Hiki;Kang Chaedong;Peck Jong Hyeon
    • International Journal of Air-Conditioning and Refrigeration
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    • 제12권4호
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    • pp.206-213
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    • 2004
  • Cycle test for developed phase change material (PCM) is necessary in order to assess the variation of latent heat, which decreases with time by deterioration. T-history method and measurement using heat-flux meter are appropriate for the cycle test in a tube filled with PCM because they do not need an extraction of sample in measuring heat of fusion. In the present study, these methods were applied to a PCM having a melting point below a room temperature, different to the past studies for PCMs melting above a room temperature. As a result of experiment using pure water as specimen, we can obtained rea-sonable values for heat of fusion.

VMD 모듈의 열성능 특성 연구 (A Study on the Thermal Characteristics of Vacuum Membrane Distillation Module)

  • 주홍진;양용우;곽희열
    • 한국태양에너지학회 논문집
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    • 제34권5호
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    • pp.23-31
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    • 2014
  • This study was accomplished to get the foundation design data of VMD(Vacuum Membrane Distillation) system for Solar Thermal VMD plant. VMD experiment was designed to evaluate thermal performance of VMD using PVDF(polyvinylidene fluoride) hollow fiber hydrophobic membranes. The total membrane surface area in a VMD module is $5.3m^2$. Experimental equipments to evaluate VMD system consists of various parts such as VMD module, heat exchanger, heater, storage tank, pump, flow meter, micro filter. The experimental conditions to evaluate VMD module were salt concentration, temperature, flow rate of feed sea water. Salt concentration of feed water were used by aqueous NaCl solutions of 25g/l, 35g/l and 45g/l concentration. As a result, increase in permeate flux of VMD module is due to the increasing feed water temperature and feed water flow rate. Also, decrease in permeate flux of VMD module is due to increasing salinity of feed water. VMD module required about 590 kWh/day of heating energy to produce $1m^3/day$ of fresh water.