• 설비공학논문집
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• 제29권8호
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• pp.408-418
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• 2017

Supercritical carbon dioxide ($sCO_2$) power system is emerging technology because of its high cycle efficiency and compactness. Meanwhile, PCHE (Printed Circuit Heat Exchanger) is gaining attention in $sCO_2$ power system technology because PCHE with high pressure-resistance and larger heat transfer surface per unit volume is fundamentally needed. Thermo-fluidic characteristics of $sCO_2$ in the micro channel of PCHE should be investigated. In this study, heat transfer characteristics of $sCO_2$ of various inlet conditions and cross-sectional shapes of single micro channel were investigated experimentally. Experiment was conducted at supercritical state of higher than critical temperature and pressure. Test sections were made of copper and hydraulic diameter was 1 mm. Convective heat transfer coefficients were measured according to each interval of the channel and pressure drop was also measured. Convective heat transfer coefficients from experimental data were compared with existing correlation. In this study, using measured data, a new empirical correlation to predict near critical region heat transfer coefficient is developed and suggested. Test results of single channel will be used for design of PCHE.

• 한국마린엔지니어링학회:학술대회논문집
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• 한국마린엔지니어링학회 2005년도 전기학술대회논문집
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• pp.216-221
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• 2005

The heat transfer coefficient and pressure drop during gas cooling process of carbon dioxide in a helically coiled tube were investigated experimentally. The experiments were conducted without oil in the refrigerant loop. The main components of the refrigerant loop are a receiver, a variable speed pump, a mass flowmeter, a pre-heater, a gas cooler(test section) and an isothermal tank. The test section is a double pipe type heat exchanger with refrigerant flowing in the inner tube and water flowing in the annulus. It was made of a copper tube with the inner diameter of 4.85 [mm], the outer diameter of 6.35 [mm] and length of 10000 [mm]. The refrigerant mass fluxes were 200${\sim}$600 [kg/$m^2$s] and the average pressure varied from 7.5 [MPa] to 10.0 [MPa]. The main results were summarized as follows: The heat transfer coefficient of supercritical $CO_2$ increases, as the cooling pressure of gas cooler decreases. And the heat transfer coefficient increases with the increase of the refrigerant mass flux. The pressure drop decreases in increase of the gas cooler pressure and increases with increase the refrigerant mass flux.

• 대한설비공학회:학술대회논문집
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• 대한설비공학회 2007년도 동계학술발표대회 논문집
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• pp.241-246
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• 2007

The present paper dealt with an experimental study of boiling heat transfer characteristics of $CO_2$. Heat transfer coefficients of the refrigerant flow inside horizontal smooth microchannel were obtained with inner tube diameter of 0.3mm and length of 300mm. The direct electric heating method was applied for supplying the heat uniformly to the refrigerant. The experiments were conducted with $CO_2$ purity of 99.99%, at saturation temperature of $10^{\circ}C$, mass flux ranges of $300{\sim}900\;kg/m^2s$, and heat flux ranges of $15{\sim}45\;kW/m^2$. While heat transfer coefficient increased with the increase of heat flux in the low quality region, the heat transfer coefficient decreased with the increase of quality in the high quality region. The heat transfer coefficients were compared with seven existing correlations with the Gungor-Winterton's(1986) correlation gave the best prediction. A new corelation to predict the two-phase flow heat transfer coefficient was developed based on the Chen(1966) correlation. The new correlation predicted the experimental data well with a mean deviation of 9.69% and average deviation of -3.03%.

• 설비공학논문집
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• 제20권8호
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• pp.517-525
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• 2008

In order to study the heat transfer and pressure drop of an internal heat exchanger for $CO_2$ heat pump under cooling condition, the experiment and numerical analysis were performed. Four kinds of internal heat exchangers with a coaxial tube type and a micro-channel tube type were used. The experimental apparatus consisted of a test section, a power supply, a heater, a chiller, a mass flow meter, a pump and a measurement system. The section-by-section method and Hardy-Cross method were used for the numerical analysis. The effects of the internal heat exchanger refrigerant flow rate, the length of the internal heat exchanger, the operating condition of the gas-cooler, the evaporator and the type of the internal heat exchangers were investigated. With increasing of the flow rate, the heat transfer rate increased about 25%. The heat transfer rate of the micro-channel tube type was higher about 100% than that of the coaxial tube type. With increasing of the length of the internal heat exchanger, the heat transfer rate increased about $20{\sim}50%$. The pressure drop of the low-side tube was larger compared with that of the high-side tube.

• 설비공학논문집
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• 제19권9호
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• pp.615-621
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• 2007

Experimental study on the heat transfer characteristics of $CO_2$ in a horizontal smooth tube was carried out to investigate the heat transfer coefficient and pressure drop during evaporation of $CO_2$. The experiment apparatus consisted of a test section, a DC power supply, a heater, a chiller, a mass flow meter, a pump and a measurement system. Experiment was conducted for various mass fluxes ($200{\sim}1200kg/m^2s$), heat flukes ($10{\sim}100kW/m^2$) and saturation temperatures (-5, 0, $5^{\circ}C$). With increasing the heat flux, the evaporation heat transfer coefficient increased. But the variation of the heat transfer coefficient on the increase of the mass flux was not large. And the significantly drops of the heat transfer coefficient was observed at any heat flux and mass flux because of the change of the flow pattern in the tube. With increasing the saturation temperature, the heat transfer coefficient increased due to the promotion of a nucleate boiling. The measured pressure drop during evaporation increased with increasing the mass flux and decreasing the saturation temperature.

• 대한설비공학회:학술대회논문집
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• 대한설비공학회 2005년도 동계학술발표대회 논문집
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• pp.353-358
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• 2005

The heat transfer and pressure drop of supercritical $CO_2$ cooled in a helically coiled tube was investigated experimentally. The experiments were conducted without oil in the refrigerant loop. The experimental apparatus of the refrigerant loop consist of receiver, a variable speed pump, a mass flowmeter, a pre-heater, a gas cooler(test section) and an isothermal tank. The test section is a helically coiled tube in tube counter flow heat exchanger with $CO_2$ flowed inside the inner tube and coolant( water) flowed along the outside annular passage, It was made of it copper tube with the inner diameter of 4.55[mm]. the outer diameter of 6.35 [mm] and length of 10000 [mm]. The refrigerant mass fluxes were $200^{\sim}600$ [kg/m2s] and the inlet pressure of gas cooler varied from 7.5 [MPa] to 10.0 [MPa]. The main results are summarized as follows : The heat transfer coefficient of supercritical $CO_2$ increases, as the cooling pressure of gas cooler decreases. And the heat transfer coefficient increases with the increase of the refrigerant mass flux. The pressure drop decreases in increase of the gas cooler pressure and increases with increase the refrigerant mass flux.

• 한국식품저장유통학회지
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• 제11권2호
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• pp.195-200
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• 2004

Sous vide 방법에 의하여 가공된 시금치 식자재 제품에 대해서 포장단위 및 저온살균 조건이 살균치와 제품에 미치는 영향을 분석하였다. 포장단위로 500g, 1kg 및 2kg에 대하여 차단성 플라스틱 포장필름에 데친 시금치를 진공포장하고 저온 살균한 후에 3$^{\circ}C$의 물에서 급냉 하는 조건에 대하여 공정조건의 영향을 검토하였다. 우선 각 포장단위 제품의 열침투 특성을 측정하고, 이를 이용하여 제품의 중심부를 가열단계에서 L. monocytogenes 의 6D 사멸조건으로 살균하는 살균시간을 계산하였다. 8$0^{\circ}C$, 9$0^{\circ}C$, 97$^{\circ}C$에서의 가열살균조건에 얻어질 수 있는 시금치의 품질로서 ascorbic acid와 chlorophyll의 보존정도를 예측 평가하였고, 아울러 실제 공정 조건에서 이들 성분의 보존 및 색택, texture, drip을 측정하였다. 예측에서는 제품의 열전달 특성과 이들 영양성분 파괴의 kinetics를 결합하여 제품에서 얻어지는 평균 영양성분의 함량을 얻었다. 포장단위가 클수록 긴 살균소요시간으로 인하여 중심부에서는 높은 살균치와 낮은 ascorbic acid와 chlorophyll의 보존을 얻는 것으로 예측되었고 실험적으로도 확인되었다. 낮은 살균온도에서 상대적으로 긴 살균시간으로 인하여 중심부의 낮은 살균치와 낮은 ascorbic acid 함량을 유지시키지만 chlorophyll 보존에서는 살균온도의 영향은 미미한 것으로 예측되었다. 실제적 제품의 살균 실험에서는 ascorbic acid와 chlorophyll의 보존에서 소포장과 고온의 단시간 살균이 양호하였다. 그리고 texture와 색택의 보존, drip의 양을 모두 고려한 경우에도 소포장 시금치를 고온에서 단시간의 조건으로 살균하는 것이 바람직한 것으로 나타났다./TEX>g)가 19.0로 감잎에 비해 높았다.systems including hardware and software and guarantee the service continuity of he systems.어지지 않았을 것이다.질 분해물이 비교적 강한 쓴맛을 나타내었다. 분해물의 단맛은 시료별로 큰 차이가 나타나지 않았으나 Bacillu megarerium Bl6과 Aspergillus oryzae M4를 조합하였을 때 상대적으로 단맛의 정도가 높게 나타났다. 따라서 이와 같은 효소특성을 이용하여 대두단백질을 가수분해를 하였을 때 다양한 단백질 분해물의 제조에 이용이 가능할 것으로 사료된다.EX> 조건에서 저장한 시료의 경우 성숙이 억제되었으며, 저장 품질 분석실험결과 저장품질이 우수한 것으로 나타났다. 관능검사에서 대조구에 비해 낮은 점수를 받았으나, 이는 시료의 성숙도가 다른데 기인하는 것으로 분석되었다. 이상의 모든결과를 분석해 볼 때 환경기체조절저장은 방울토마토의 성숙 억제 및 저장품질유지에 효과가 있는 것으로 나타났다. 환경기체조성은 일반토마토의 저장조건보다 이산화탄소농도가 다소 높은 산소농도 3%~5% 이산화탄소 농도 5~8%에서 저장하는 것이 효과적일 것으로 판단되었다.철쭉군목으로 대표되나 군단이 하의 군목들은 다소 차이를 보이는 것으로 나타났다. 중간상인이론의 수정이 필요하다고 본다.가\ulcorner 본 논문에서는 표면적 형태에도 불구하고 [-wh]의미의 겹의문사는 병렬적 관계의 합성어가 아니라 내부구조를 지니지 않은 단순한 단어(minimal $X^{0}$ elements)로 가정한다. 즉, [+wh] 의미의 겹의문사는 동일한 구성요 소를 지닌 병렬적 합성어([$[W1]_{XO-}$ $[W1]_{XO}$ ]$_{XO}$)로 그리고 [-wh] 의미의 겹의문사는 중복된 발은을 지닌 한 단어로