• Solar Energy
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• v.17 no.2
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• pp.75-89
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• 1997

In this paper, the operating thermal characterictics of liquid-ice was expeimentally investigated in an adiabatic and a non-adiabatic direct contact liquid-ice heat exchanger. Experiments were carried out varing inlet temperature, Ice Packing Factor, and the flow rate of heat transfer fluid. The higher inlet temperature and the more much inlet flow rate, thermal stratification in liquid-ice heat exchanger was established faster. In the case of adiabatic ice storage tank, temperature distribution was a little higher at all conditions than that of non-adiabatic one. The ratio of latent energy to total discharge energy($E_{\lambda}/E_[tot}$) was about 80%, and the discharge of latent heat energy was appeared rapidly as inlet temperature and flow rate were higher.

• Solar Energy
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• v.16 no.2
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• pp.65-77
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• 1996

The operating thermal chracteristics of direct contact liquid-ice heat exchanger was experimentally investigated. In this paper, The effects of Ice Packing Factor(IPF), the inlet temperature and the flow rate of Heat Transfer Fluid(HTF) were stuided in the liquid-ice heat exchanger. Thermal stratification in liquid-ice heat exchanger was established clearly and faster at the higher inlet temperature and flow rate of HTF. At the end of melting of the lower flow rate is cleared the thermal stratification in liquid-ice heat exchanger. The temperature stratification is long with higher value of IPF of liquid-ice heat exchanger. The mean temperature of liquid-ice storage was changed rapidly with increasing flow rate and inlet temperature of HTF. The gradiant of ratio of total energy to latent energy was found higher with increasing inlet temperature and flow rate.

• Journal of Advanced Marine Engineering and Technology
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• v.30 no.3
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• pp.382-388
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• 2006

This study experimented to understand the effect of transporting ice slurry through in pipe with valve. And at this experiment it used ethylene glycol-water solution and a concentration is 30wt%. The experimental apparatus was constructed of ice slurry generation tank, turbo flow meter, manometers for differential pressure measuring, PIV system for flow pattern measuring. illumination and along a horizontal circular tube with valve as test section. The experiments were carried out under various conditions, with velocity of fluid at the entry ranging from 0.5 to 1.5 m/s and concentration of IPF is 30%. Also valve open rate is 50%, 75%, 100%.

• 한국가시화정보학회:학술대회논문집
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• 2004.11a
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• pp.98-101
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• 2004

Experimental studies were reported on the characteristics of flows in a circular pipe in which ice slurry is flowing. This was mainly due to deficiency of conventional measurement techniques. In this report, the flow characteristics are quantitatively investigated by the use of PIV technique concerning the Ice Packing Factor(IPF) and the power changes of pump motor. It was experimentally verified that the power loss does not increase any more at a certain IPF value.

• Journal of Advanced Marine Engineering and Technology
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• v.29 no.2
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• pp.177-184
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• 2005

Experimental studies on the characteristics of ice slurry flows in a circular pipe is rare due to the deficiency of conventional measurement techniques. In this report the flow characteristics are quantitatively investigated by the use of PIV technique concerning the Ice Packing Factor(IPF) and the power changes of pump motor It was experimentally verified that the power loss does not increase any more at a certain IPF value.

• 한국신재생에너지학회:학술대회논문집
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• 2009.06a
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• pp.699-702
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• 2009

가스하이드레이트(Gas Hydrate)는 특정한 온도와 압력조건하에서 물분자로 이루어진 공동 내로 메탄, 에탄, 프로판 등의 가스가 들어가 물분자와 상호 물리적 결합으로 형성된 외관상 얼음과 비슷한 고체 포유물로 자연상태에 존재하는 하이드레이트의 주 성분이 메탄(Methane)인 경우가 대부분인 까닭에 메탄 하이드레이트라고도 불린다. 표준상태에서 $1m^3$의 메탄하이드레이트는 $172m^3$의 메탄가스와 $0.8m^3$의 물로 분해된다. 그러나 메탄 하이드레이트를 인공적으로 만들경우 물과 가스의 반응율이 낮아 하이드레이트 생성시간이 상당히 길고 가스 용해율도 낮다. 따라서 하이드레이트를 빨리 만들며 가스충진율도 증가시킬 수 있는 방법으로 가스 흡착성이 있는 탄소나노튜브(Carbon Nano Tube)를 기계적 분산방법인 초음파 분산(Dispersion)과 화학적 개질에 의한 분산방법인 산화처리분산을 사용하여 탄소나노튜브와 산화탄화나노튜브를 순수한물에 분산하여 나노유체를 만들고, 나노유체와 메탄가스를 반응시켜 메탄하이드레이트를 생성시키는 실험을 수행하였다. 나노유체와 순수한물의 상평형(Phase Equilibrium)은 비슷하였으며, 탄소나노튜브를 0.0005Vol%를 분산한 나노유체와 순수한물의 메탄가스 소모량의 비교한결과 나노유체의 가스소모량의 순수한물보다 ${\Delta}T_{sub}$=0.5K에서는 2배 ${\Delta}T_{sub}$=9.7K에서는 1.6배 증가하였다. 또한 산화나노유체와 나노유체의 메탄 가스소모량은 산화나노유체가 0.01 ~ 0.02mol정도 높았으나 그 효과가 미미하였고, 교반기를 사용하여 RPM300으로 교반시켰을 경우 역시 메탄 가스소모량은 큰 차이가 없었으나 산화나노유체의 경우 메탄 가스소모량이 나노유체보다 급격히 증가함을 확인하였다.