• 대한기계학회논문집B
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• 제23권7호
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• pp.928-936
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• 1999

The electronic refrigerating kimchi jar operates with a low noise because it contains no compressor but it consumes more energy than that of an refrigerator with compressor. In this paper, the heat flow characteristics and cooling performance of an electronic refrigerating kimchi jar are studied by means of experiments. When the storage temperature is kept in a range of $-5.7^{\circ}C$ to $4.1^{\circ}C$. in the case of three ambient temperatures; $12.7^{\circ}C$, $22.3^{\circ}C$ and $32.2^{\circ}C$, the cooling performance of $20{\ell}$ kimchi jar is investigated. The experiments show that the temperature difference that exists between kimchi jar and its ambient provides a measure of the coefficient of performance of kimchi jar. It is also found that ratio of net pumping heat to the heat pumping rate of thermoelectric module is independent of the temperature difference.

• 한국기계기술학회지
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• 제13권4호
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• pp.71-76
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• 2011

Earth to air heat exchangers made by iron, aluminium, copper and poly-ethylene pipe for single greenhouse heating were experimented and blowers. Earth to air heat exchanger was installed by pipelines in earth tube at 70cm depths and air blower was the heating capacity 3kW/h, As the result, Temperature difference due to temperature history of the inlet and outlet air on the various type in earth tube in greenhouse showed that air temperature at the various type in earth tube, comparison tube were make no difference respectively. Under the experimental condition, heat fluxes and heating load were showed 6,800Kcal/h, 19,699kcal/h generally yield of Lactuca Sativa cultured during days of sowing 90day in greenhouse using copper pipe was 170% incleased.

• Nuclear Engineering and Technology
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• 제54권3호
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• pp.1085-1097
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• 2022

A printed circuit steam generator (PCSG) is being considered as the component for pressurized water reactor (PWR) type small modular reactor (SMR) that can further reduce the physical size of the system. Since a steam generator in many PWR-type SMR generates superheated steam, it is expected that dryout front oscillation can potentially cause thermal fatigue failure due to cyclic thermal stresses induced by the transition in boiling regimes between convective evaporation and film boiling. To investigate the fatigue issue of a PCSG, a reference PCSG is designed in this study first using an in-house PCSG design tool. For the stress analysis, a finite element method analysis model is developed to obtain the temperature and stress fields of the designed PCSG. Fatigue estimation is performed based on ASME Boiler and pressure vessel code to identify the major parameters influencing the fatigue life time originating from the dryout front oscillation. As a result of this study, the limit on the temperature difference between the hot side and cold side fluids is obtained. Moreover, it is found that the heat transfer coefficient of convective evaporation and film boiling regimes play an essential role in the fatigue life cycle as well as the temperature difference.

• 생물환경조절학회지
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• 제21권2호
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• pp.79-87
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• 2012

본 연구는 온실의 난방 에너지 절감을 목적으로 온실 내부에 알루미늄 온수배관을 설치하여 난방효과에 대한 기초자료를 구축하고자 수행되었다. 그 연구결과를 요약하면 다음과 같다. 전체 실험을 포함하여 온실내의 높이별 온도편차는 4.0~$7.0^{\circ}C$ 정도의 범위로서 그 차이가 크게 나타났다. 팬코일유니트(FCU)를 작동시킨 경우가 작동시키지 않은 경우에 비해 유출입수의 온도차가 $3.3^{\circ}C$ 정도 크고, 소비전력량은 36.2~40.1%정도 증가하였으며, 시간당 방열량은 44.6~52.0% 정도 증가하는 것으로 나타났다. 실험기간동안 순환유량은 0.48~$0.49L{\cdot}s^{-1}$ 정도의 범위에 있었고, 평균유속은 1.53~$1.56m{\cdot}s^{-1}$ 정도였다. 유출입수의 평균 온도차는 6.24~$11.50^{\circ}C$이었다. 최저 외기온 -14.0~$-0.6^{\circ}C$ 범위에서 설정온도별 방열량은 135,930~307,150kcal 정도의 범위로서 시간당 9,610~$19,630kcal{\cdot}h^{-1}$ 정도의 범위에 있었다. 이것은 최대난방부하의 약 23~53% 정도의 난방에너지를 공급할 수 있을 것으로 나타났다. 전체 방열량과 소비전력량은 각각 2,548,306kcal 및 3,075.7kWh이다. 화석연료인 경유로 난방할 경우, 소요되는 경유의 총 소비량은 281.6L 정도이고 비용은 321,000won인 것으로 나타났다. 농가용 전력요금을 적용하면 전력사용에 대한 총비용은 110,730won 정도로서 경유 소비 비용의 33.5% 정도로 나타났다. 실험구의 온도가 대조구보다 약 8.3~$14.6^{\circ}C$ 정도 높게 나타났다.

• 청정기술
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• 제21권3호
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• pp.200-206
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• 2015

산화세륨의 첨가가 수성가스전이반응 효율에 미치는 영향을 조사하기 위해서, Cu-ZnO-CeO₂촉매를 공침법을 사용하여 제조하였다. 일련의 Cu-ZnO-CeO₂ 촉매는 Cu 함량(50 wt%)을을 고정시키고 산화세륨(CeO₂ 기준으로, 0, 5, 10, 20, 30, 40 wt%)의 함량을 조절하면서 제조되었고 이를 이용하여 GHSV 95,541 h^-1의 기체 유량범위, 200~400 ℃의 온도범위에서 수성가스전이반응 촉매활성이 측정되었다. 또한, BET, SEM, XRD, H₂-TPR, XPS 분석을 통하여 촉매특성이 분석되었다. CeO₂가 첨가된 촉매는 구리 분산도와 결합에너지 같은 촉매특성의 다양한 변화를 나타내었다. 10wt%의 CeO₂가 최적의 첨가량으로 판단되며 이때 촉매는 가장 낮은 온도에서 환원이 일어났으며 반응에서 가장 높은 촉매 활성을 보였다. 또한 CeO₂가 첨가된 촉매는 CeO₂가 첨가되지 않는 촉매와 비교하여 높은 온도영역에서 활성이 향상되었다. 따라서, 최적 조성의 CeO₂첨가는 높은 구리 분산도, 낮은 결합에너지, 구리 금속의 응집 방지를 유도하여 높은 촉매활성을 유도하였다.

• 한국태양에너지학회 논문집
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• 제27권3호
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• pp.155-160
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• 2007

This study shows the results on thermal performance test with domestic solar collector for low-temperature applications using KS, then reveals the efficiency difference between KS and EN standard. Using the test results, this study Presents the status of thermal performance with domestic solar collector including flat-plate, single evacuated, and double evacuated (with mirror or U-tube) solar collector.

• 설비공학논문집
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• 제7권2호
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• pp.234-248
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• 1995

A super-heat pump system composed of a suction line heat exchanger, low and high stage economizers, and a screw compressor is simulated to examine the energy performance and design options. CFC12, HCFC22, HFC134a, HCFC22/HCFC142b, HFC32/HFC134a, and HFC125/HFC134a are used as working fluids for comparison. The results indicate that the proposed system charged with appropriate mixtures is up to 33.4% more energy efficient than the normal system with CFC12. The performance of the super-heat pump system charged with mixtures was influenced by such factors as the temperature matching, heat source temperature difference, low stage economizer, and high stage economizer. The fluids with a larger liquid specific heat such as HFC134a would have more benefits when a suction line heat exchanger is installed. 40%HCFC22/60%HCFC142b mixture seems to be a good candidate to replace CFC12. On the other hand, 25%HFC32/75% HFC134a would be a good long term candidate to replace HCFC22.

• 한국환경과학회지
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• 제23권9호
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• pp.1551-1562
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• 2014

To clarify the characteristics of TKE (Turbulence Kinetic Energy) variation for offshore wind power development, several numerical experiments using WRF were carried out in three different coastal area of the Korean Peninsula. Buoyancy, mechanical and shear production term of the TKE budget are fundamental elements in the production or dissipation of turbulence. Turbulent kinetic energy of the south coast region was higher than in other sea areas due to the higher sea surface temperature and strong wind speed. In south coast region, strong wind passing through the Korea Strait is caused by channelling effect of the terrain of the Geoje Island. Although wind speed is weak in east coast, because of large difference in wind speed between the upper and lower layer, the development of mechanical turbulence tend to be predominant. Since lower sea surface temperature and smaller wind shear were detected in west coastal region, the possibility of turbulence production not so great in comparison with other regions. The understanding of the characteristics of turbulence in three different coastal region can be reduced the uncertainty of offshore wind construction.

• 에너지공학
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• 제25권4호
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• pp.30-36
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• 2016

전동스쿠터용 배터리팩은 상온보다 고온일수록 내부저항이 감소하여 충전효율은 상승하나 배터리 안전성 문제로 인하여 냉각시스템을 필요로 한다. 본 연구의 목적은 냉각용 공기 흡입과 배출 방법과 시기를 다르게 하여 냉각 효율성을 분석하는 것이다. 배터리팩 내부에서 각각의 배터리 사이에 큰 온도편차가 존재하는 경우 배터리의 성능과 효율이 저감된다. 따라서, 배터리팩 냉각성능을 입-출구 냉각팬의 작동 방법 및 시기 변화에 의해 배터리의 성능과 효율을 개선시키도록 한다. 연구에 사용된 수치해석 상용코드는 17.0버젼의 ANSYS CFX이다.

• 한국수소및신에너지학회논문집
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• 제21권1호
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• pp.72-79
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• 2010

This paper is studying the selective separation of methane and carbon dioxide which are the main ingredients of biogas. Adsorption performance of molecular sieve 13x for carbon dioxide seems to be reasonable. In this experiments carbon dioxide contains about 3~5 ppm of methane and it is impossible to obtain high purity carbon dioxide. Applying the low temperature technique, it is possible to separate methane and carbon dioxide from bio gas. PRO II simulation shows results a small change of liquefaction temperatures and no difference with the used thermodynamic models. Applying low temperature technique, It is possible to separate carbon dioxide and methane from biogas.