• 태양에너지
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• 제8권2호
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• pp.46-56
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• 1988

This investigation concerns thermal stratification of the water due to the temperature difference (${\Delta}T=T_{\infty}-T_i$) between the mean temperature of the water in the test tank (1m wide, 1m high, 2.1m long) and the temperature of the inflow water into the tank; flow rate of circulating water and height of the sink diffuser in the test tank. The additional objectives was to observe a stratification phenomena near an interface by measuring the velosities and the temperature difference and investigate an availabilities of the better effective hot water through establishing thermocline near an interface around the bottom of the tank. Following results were obtained through the experiments. 1. When the flow rate was constant and the temperature difference (${\Delta}T=T_{\infty}-T_i$) between the mean temperature of the flow in the test tank and the temperature of the inflow water increased by 5.6, 9.5, 13.5($^{\circ}C$), obtained the better effective advantage of hot water and the stress near an interface increased gradually. 2. When the ${\Delta}T=T_{\infty}-T_i$ was constant and flow rate increased by 4.0, 4.8, 6.4, 8.0 (LPM), obtained the better effective advent age of hot water and the mean stress near an interface increased gradually. 3. When the height of the sink diffuser was 25cm from tank bottom in comparison with 50cm, obtained the better effective advantage of hot water and the mean stress near an interface increased.

• 대한설비공학회:학술대회논문집
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• 대한설비공학회 2007년도 동계학술발표대회 논문집
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• pp.447-452
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• 2007

Greenhouses should be heated during nights and cold days in order to fit growth conditions in greenhouses. Ground source heat pump(GSHP) or geothermal heat pump system(GHPs) is recognized to be outstanding heating and cooling system. Horizontal GSHP system is typically less expensive than vertical GSHP system but requires wide ground area to bury ground heat exchanger(GHE). In this study, a horizontal GSHP system with thermal storage tank was installed in greenhouse and investigated as performance characteristics. In the daytime, heating load of greenhouse is very small or needless because solar radiation increases inner air temperature. The results of study showed that the heating coefficient of performance of the heat pump ($COP_h$) was 2.9 and the overall heating coefficient of performance of the system($COP_{sys}$) was 2.4. Heating energy cost was saved 76% using the horizontal GSHP system with thermal storage tank.

• 한국태양에너지학회 논문집
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• 제31권5호
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• pp.41-46
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• 2011

In the present work, a new freeze protection method has been proposed for a natural circulation system of solar water heater. Though electrothermal wire is popularly used for the purpose, there are freezing troubles by wire cut-off and excessive electric power consumption. In the experimental device, hot water in a storage tank was circulated by a small pump and used to heat the outdoor pipes if the cold water pipe surface temperature falls lower than a set point. As a result, It was observed that there was no hot water waste while the solar water heating system operated without freeze and burst.

• 한국가스학회지
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• 제19권3호
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• pp.32-37
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• 2015

LNG는 극저온액체로 저장탱크의 열유입으로 인하여 지속적으로 BOG가 발생하고 있으며, 이의 효과적인 방법의 재액화가 요구되고 있다. 이 BOG의 재액화에는 공급되는 저압 펌프 후의 LNG의 냉열을 이용하는 데, 현재의 공정은 BOG 단위 발생량에 대하여 10배 이상의 LNG 흐름이 요구되고 있다. 본 연구에서는 NGL분리액화와 2차 고압펌프 후의 LNG 냉열을 이용하는 공정을 새롭게 고안하였으며, 이를 분석한 결과 LNG 소요유량이 3~4배에 불과한 매우 효과적인 재액화 시스템이 되었다. 본 고안에 의하면 하절기에도 원활한 BOG 재액화가 가능하므로, LNG기지의 안전성 향상과 공급 의 효율을 높일 수 있는 매우 효과적인 공정으로 분석되었다.

• 한국원자력학회:학술대회논문집
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• 한국원자력학회 1996년도 추계학술발표회논문집(1)
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• pp.328-333
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• 1996

Boric acid concentrations of the refueling water storage tank (RWST) and the accumulators for Ulchin 1&2 (UCN 1&2) are increased to meet the post loss of coolant accident (post-LOCA) shutdown requirement for the extended fuel cycles from 12 months to 18 months. To maintain long term cooling (LTC) capability following a LOCA, the switchover tine is examined using BORON code to prevent the boron precipitation in the reactor core with the increased boron concentrations. The analysis results show that, at 8 hours after the initiation of LOCA. the emergency core noting system (ECCS) should be manually realigned to the simultaneous recirculation mode from the cold leg recirculation mode.

• 한국태양에너지학회 논문집
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• 제25권2호
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• pp.63-69
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• 2005

This study is the survey of a transition procedure of building services systems(heat source, HVAC, water supply) through the survey of existing office buildings, building design documents. The preference & major consideration of system selection is the engineer's opinions. The results of this survey can be used in selection of building services system design. In this survey, "Hot & cold water generator system" and "single duct CAV+FCU system", "Elevated water tank system" are selected. The most important consideration in system selection is the energy saving in heat source system, and comfort in HVAC system, and water pressure in water supply system. They prefer "steam boiler+absorption chiller system" for heat source system, "steam boiler+ice thermal storage system", "hot & cold water generator system", "district heating+absorption chiller system" : "single duct CAV+FCU system" and "single duct VAV+convector system" for HVAC system: and "booster pump system" for water supply system.

• Korean Chemical Engineering Research
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• 제59권3호
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• pp.345-358
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• 2021

본 연구에서는 액화천연가스(LNG; liquefied natural gas) 재기화 과정에서 버려지는 냉열을 회수하는 방법으로 액화 공기를 생산하는 공정을 개발하였다. 액화 공기는 LNG 수출국으로 운송하여 천연가스 액화를 위한 냉매를 부분적으로 대체하는 용도로 활용될 수 있다. 이를 위하여, 액화 공기는 LNG 운반선에 저장 가능한 압력을 만족하여야 한다. 따라서, 가장 널리 사용되는 멤브레인 탱크로 액화 공기를 운송하기 위해 약 1.3 bar에서 공기가 액체 상태로 존재할 수 있도록 설계하였다. 제안한 공정에서, 공기는 LNG와의 열교환 이후 추가적인 질소 냉매 사이클과의 열교환을 통해 과냉된다. LNG 운반선의 최대 용량만큼 액화 공기를 생산할 때 운송비용 측면에서 가장 경제적일 수 있으며, 천연가스 액화공정에서 활용할 수 있는 냉열이 많아지게 된다. 이를 비교하기 위하여, 동일한 1 kg/s의 LNG 공급 조건 하에서 기존 공정을 이용한 Base case와 제안공정 내 유입 공기 유량을 각각 0.50 kg/s, 0.75 kg/s, 1.00 kg/s으로 하는 Case1, Case2, Case3를 구성하고 열역학적 및 경제적 측면에서 분석하였다. 액화 공기 생산량이 많을수록 1kg의 생산량 당 더 많은 에너지가 요구되는 경향을 보였으며 Case3는 Base case 대비 0.18 kWh 높게 나타났다. 그 결과 Case3의 액화 공기 1 kg 당 생산 비용이 $0.0172 더 높게 나타났다. 그러나 액화 공기의 생산량이 증가함에 따라 1 kg 당 운송 비용이 $0.0395 감소하여 전체 비용 측면에서 Case3는 Base case에 비해 1 kg 당 $0.0223 적은 비용으로 액화 공기를 생산 및 운송할 수 있음을 확인하였다.