• 한국태양에너지학회 논문집
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• 제24권1호
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• pp.47-52
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• 2004

An experimental investigation was performed to compare ice making characteristics of ice storage system with smooth and spiral tube. During the freezing processes in the shell and tube type ice storage tank with smooth tube, heat resistance of the ice layer caused a decrease in freezing rate. Also, the phenomena of bridging made the increasing rate of ice making less. In order to improve the ice making rate, spiral tube(pitch=6mm) was used in the present study. The ice making rate and the decreasing of bridging for the spiral tube were higher than those for the smooth tube.

• Nuclear Engineering and Technology
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• 제55권10호
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• pp.3581-3590
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• 2023

High-temperature design evaluations were conducted on Type 316L stainless steel piping for a 700 ℃ large-capacity thermal energy storage verification test loop (TESET) under construction at KAERI. The hot leg piping with sodium coolant at 700 ℃ connects the main components of the loop heater, hot storage tank, and air-to-sodium heat exchanger. Currently, the design rules of ASME B31.1 and RCC-MRx provide design procedures for high-temperature piping in the creep range for Type 316L stainless steel. However, the design material properties around 700 ℃ are not available in those rules. Therefore, a number of material tests, including creep tests at various temperatures, were conducted to determine the insufficient material properties and relevant design coefficients so that high-temperature design on the 700 ℃ piping may be possible. It was shown that Type 316L stainless steel can be used in a 700 ℃ high-temperature piping system of Generation IV reactor systems or a renewable energy systems, such as thermal energy storage systems, for a limited operation time.

• 한국콘크리트학회:학술대회논문집
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• 한국콘크리트학회 2008년도 춘계 학술발표회 제20권1호
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• pp.637-640
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• 2008

1998년 인천 LNG 인수기지에 국내 최초로 14만kl의 지하식 저장탱크가 건설되는 것을 시작으로 20만kl의 지하식 저장탱크가 연이어 건설되었다. 또한, 평택 및 통영 LNG 인수기지에 14만kl 및 20만kl의 지상식 저장탱크가 건설되고 있다. 저장탱크의 용량 및 방식에 따라 저장탱크의 설계단면이 변화하였으며, 콘크리트에 요구되는 특성 또한 변화하였다. 특히, 수화열에 의한 온도균열 발생 확률이 높은 Bottom 및 하부벽체는 4종 저열포틀랜드시멘트가 적용되고 있다. 20만kl 용량인 지상탱크 평택 16호기 상부벽체에 대한 동절기 온도균열제어를 위해 양생방법, 타설간격조절 및 배합변경에 따른 수화열 해석을 실시하였다. 기존 1종+FA25%인 배합을 적용시 목표균열지수를 만족하기 위해서는 보온양생 및 타설간격 증가 등 시공적 대책이 필요하며, 배합을 4종+FA15%로 변경시에는 추가적인 시공대책 없이 온도균열 제어가 가능한 것으로 나타났다.

• 수산해양기술연구
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• 제60권2호
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• pp.194-206
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• 2024

This study focuses on analyzing the energy-saving effects of the recirculation aquaculture system using seawater source heat pumps and solar power generation. Based on the thermal load analysis conducted using the transient system simulation tool, the annual energy consumption of the recirculation aquaculture system was analyzed and the energy-saving effects of utilizing the photovoltaic system was evaluated. When analyzing the heat load, the sea areas where the fish farms are located, the type of breeding tank, and the circulation rate of breeding water were taken into consideration. In addition, a method for determining the appropriate capacity for each operation time was examined when applying the energy storage system instead of the existing diesel generator as an emergency power, which is required to maintain the water temperature of breeding water during power outage. The results suggest that, among the four seas considered, Jeju should be estimated to achieve the highest energy-saving performance using the solar power generation, with approximately 45% energy savings.

• 한국가스학회지
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• 제24권4호
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• pp.18-24
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• 2020

본 연구의 목적은 화재사고가 발생한 건물에 인접한 LPG 탱크용 방화벽의 적용성을 검증하는 것이다. 제안된 방화벽 재료는 (1) 두께 10 mm 목재합판, (2) 내화도료를 도포한 목재합판, (3) 두께 75 mm Expanded Polystyrene, (4) 두께 75 mm 유리섬유 충진 샌드위치 판넬, (5) 두께 75 mm Autoclave Lightweight Concrete이다. 화원은 1 m 정사각형으로 120-140 g/s의 LPG를 균일하게 분사하여 방화벽과 후단의 탱크를 가열한다. 적용성은 시험 후 방화벽의 구조적 건전성 확인, 방화벽 양면 및 탱크표면 온도, 탱크 인근 복사열을 분석하여 판단한다. 그 결과, ALC 방화벽이 유일하게 구조 건전성을 유지하였고 저장탱크 온도를 가작 적게 상승시켜 폭발 방지 적용성을 확인하였다. 본 실험결과를 활용하여 방화벽의 성능평가 기준 마련에 필요한 핵심인자를 도출하였다.

• Agricultural and Biosystems Engineering
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• 제6권1호
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• pp.22-26
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• 2005

A wind-heat generation system was developed and the system consisted of an electric motor, a heat generation drum, a heat exchanger, two circulation pumps and a water storage tank. The heat generation drum is an essential element determining performance of the system. Frictional heat was generated by rotation of a rotor in the drum filled with a working fluid, and the heat stored in the fluid was used to increase water temperature through the heat exchanger. Effects of some factors such as rotor shape, kind and amount of working fluid, rotor rpm and water flow rate in the heat exchanger, affecting the system performance were investigated. Amounts of heat generated were varied, ranging from 126,000 to 32,760 kJ/hr, depending on combination of the factors. Statistical analysis using GLM procedure revealed that the most influential factor to decide the system performance was amount of the fluid in the drum. Experiments showed that the faster the speed of the rotor, the greater heat was obtained. The greatest efficiency of the heat generation system, electric power consumption rate vs gained heat amount of water, was about 70%. Though the heat amount was not enough for plant bed heating of a 0.1-ha greenhouse, the system would be promising if some supplementary heat source such as air- water heat pump is added.

• 한국태양에너지학회 논문집
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• 제35권5호
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• pp.21-29
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• 2015

In this study, the performance of hybrid solar air-water heater when the heated air was used as inlet air was investigated during air and liquid were heated simultaneously. Temperature difference between inlet air and ambient was set as $0^{\circ}C$, $13^{\circ}C$ and $22^{\circ}C$ and it was maintained during the daily operation. As a result, thermal efficiency of liquid heating was increased when the inlet air temperature was increased and heat gain of the water in heat storage tank was also increased with increment of temperature difference between inlet air and ambient temperature. On the contrary to this, the decrement of air heating efficiency and total efficiency of collector was confirmed with increment of inlet air temperature and it is considered that heat gain of liquid side is lower than heat loss of air side that occurring by using heated air as inlet air of collector. So, from these results, maximum temperature that the liquid in heat storage tank can reach was expected to increase if the return air or any heated air was used as inlet air. But air and total efficiency of hybrid solar air-water is decreased, so using outdoor air as inlet air is considered as better way on perspective of using of solar thermal energy by hybrid solar collector. However, it is hard to conclude that using outdoor air is better than heated air on the perspective of energy saving of building because the performance of heat storage performance was increased even air and total thermal efficiency was decreased, so the necessity of more profound consideration about these result in further research was confirmed for putting the hybrid solar air-water heater to practical use.

• 태양에너지
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• 제7권2호
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• pp.22-29
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• 1987

This paper dealed with thickness variation of bottom heat sotrage zone due to salinity and flow rate of extration hot brine in small test solar pond (0.5m wide, 0.5m high, 1.0m long). Testing apparatus and situation were follows: 7.1 cm of height of suction diffuser and 1.8cm of height of discharge diffuser above the test pond respectively, 0.3cm of slot size of suction diffuser, 1.0cm of slot size of discharge diffuser, 47cm of length of the slot; heating of hot water ($75^{\circ}C$) through separated hot water tank, discharge of the brine into storage zone through discharge diffuser, the extration of the brine through suction diffuser, circulation of the extracted brine through a heat exchanger (cooler). Following results were obtained through the experiments. 1. In small test solar pond, the typical three zone which showed up in real solar pond were established. 2. Richardson Number was used more effectively to confirm hydrodynamic stability of the stratified flow. 3. The thickness of non convective layer had a great effect on the heat storage of the bottom convective layer, then the temperature of bottom convective layer had a relation to that of upper convective layer. 4. Optimum operating condition in the test pond was on 10%-15% of salt concentration and $0.05m^3/hr$ of flow rate of extraction hot brine. 5. Following thickness of 3 zones were available to obtain under optimum operation condition: o bottom storage zone: $30%{\pm}10%$ of total pond depth o non-convective zone: $40%{\pm}10%$ of total pond depth o Upper surface zone: $20%{\pm}10%$ of total pond depth.

• 한국산학기술학회논문지
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• 제22권4호
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• pp.56-66
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• 2021

본 연구에서는 가축분뇨 처리시설의 호기성 액비화 과정에서 발생하는 열을 회수하기 위한 폐열회수 시스템을 고안하여 시스템을 구성하는 요소 장치의 성능을 분석하였다. 또한, 회수된 열의 활용 가능성을 확인하였다. 실험 설정을 위해 가축분뇨 처리시설의 액비 발효조에서 발생하는 발효열을 확인하였다. 호기성 액비화를 위한 발효조의 온도가 균일성을 나타낸 특성과 34.5 ~ 43.9 ℃의 범위에서 운영되는 점을 고려하여 실험 온도 수준을 35, 40, 45 ℃로 설정하였다. PE 및 STS 파이프로 구성된 복합열교환기는 53.5, 65.6, 74.4 MJ/h 열에너지를 회수하고, 5 RT 용량의 히트펌프는 95.6, 96.1, 98.9 MJ/h 열에너지를 축열 하였으며, 이때 히트펌프의 난방성능계수는 4.53, 4.62, 4.65이었다. 발효조의 온도를 45 ℃로 가정한 열교환기의 최대 온수 생산능력을 급탕량 산정 방법으로 비교했을 때 56 360 kcal/day의 에너지 공급량을 확인하였다. 축열조와 연계된 FCU의 온풍 난방능력은 20.8 MJ/h, 에너지 이용효율은 96.1 %였다. FCU의 온풍으로 퇴비를 건조하였을 때 초기함수율 50.5 %에서 건조 후 함수율 45.8 %로 4.7 % 감소함을 확인할 수 있었다.

• 대한안전경영과학회지
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• 제20권3호
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• pp.27-36
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• 2018

The steel pipe manufacturing industry deals with facilities and materials. Especially thermal facilities are close to vapor cloud explosion (VCE) and may cause secondary damage to facilities because they deal with corrosive substances such as hydrofluoric acid, sulfuric acid and acid, fire, explosion, leakage etc. It is in danger. In this study, hazard identification method was conducted using HAZOP techniques and quantitative risk analysis was conducted using e-CA, a program that supports accident impact analysis. Equipment in the influence range of ERPG - 3 was determined to be a facility requiring replacement. It was decided that neutralization is necessary using slaked lime. Based on the cost of loss, We presented the proper replacement which is the timing of the dangerous facility. As a result, It was ideal to replace the facilities with 20 years of heat treatment facilities, one year of hydrofluoric acid storage tank, 20 years of sulfuric acid storage tank, and 5 years of hydrochloric acid storage tank.