• Journal of Advanced Marine Engineering and Technology
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• v.20 no.5
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• pp.76-81
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• 1996

In this paper, a calculation method for fin efficiency of continuous fin is introduced. The continuous fin of in-line and staggered arrangement was divided into many sectors and fin efficiencies of each sectors were calculated by assuming that each sectors be the circular fins. To get the converged fin efficiency which is averaged by the each areas, the number of sectors was increased. The results were compared with equivalnet method by varying the aspect ratios in both cases of in-line and staggered tube arrangement and showed some differences of fin efficiencies.

• Proceedings of the Korean Society for Agricultural Machinery Conference
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• 2002.02a
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• pp.133-138
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• 2002

온풍난방기 20대를 대상으로 온풍난방기의 베기가스중 탄산가스농도, 온풍온도차, 배기가스온도 및 열효율을 조사하여 사용연수별로 분석하였으며 주요 결과는 다음과 같다. 가. 사용연수별 온풍난방기 배기가스중 탄산가스농도와 온풍온도차는 사용연수에 따른 조사표본의 부족으로 큰 차이가 있었다고 하기는 어렵고 정확한 조사를 위해서는 보다 많은 대수가 필요할 것으로 판단된다. 나. 사용연수별 배기가스온도는 사용연한이 오래될수록 높아졌다고 판단된다. 이는 열교환기에서 흡입공기와 연소열이 열교환이 충분히 이루어지지 않았거나, 버너노즐의 노후화, 버너송풍기, 온풍난방기 송풍기의 노후화에 따른 결과라 여겨진다. 사용연수에 따른 배기가스온도는 회귀방정식 Y= 79.032Ln(X) + 116.66 ($R^2$= 0.6784)로 나타낼 수 있었다. 다. 사용연수별 온풍난방기의 열효율은 사용연한이 오래될수록 감소하는 경향을 보였으며 회귀방정식 Y = 95.167 X $^{-0.054}$ ($R^2$= 0.5696)로 나타낼 수 있었다.

• Transactions of the Korean hydrogen and new energy society
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• v.33 no.6
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• pp.838-844
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• 2022

In this paper, an experimental study was conducted on the energy efficiency ratio of performance for air source heat pump. The energy efficiency ratio presents the operating efficiency of heat pump performance. In order to improve reliability in the energy efficiency ratio test of air source heat pump, the measurement uncertainty of the instrument was estimated. Measurement uncertainty refers to the uncertainty of a measurement, estimates the range in which the expected value of the measurement can be within a certain confidence level, and suggests a range in which the measured representative value is incorrect. The measurement uncertainty for the energy efficiency ratio test of air source heat pump was calculated and the measured results were presented.

• Journal of the Korea Academia-Industrial cooperation Society
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• v.21 no.6
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• pp.403-410
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• 2020

This paper focuses on the design of a 12-kW small-scale supercritical CO₂ test loop. A theoretical study, stabilization, and optimization of carbon dioxide were carried out with the application of a solar heat source based on solar thermal data in Pohang. The thermodynamic cycle of the test facility is a Rankine cycle (transcritical cycle), which contains liquid, gas, and supercritical CO₂. The system is designed to achieve 6.98% efficiency at a maximum pressure of 12 MPa and a maximum temperature of 70℃. In addition, the optimum turbine inlet temperature and pressure were calculated to increase the cycle efficiency, and the application of an internal heat exchanger (IHX) was simulated. It was found that the maximum efficiency increases to 18.75%. The simulation confirmed that the efficiency of the cycle is 6.7% in May and 6.26% in June.

• Journal of the Korean Society of Propulsion Engineers
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• v.13 no.4
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• pp.45-54
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• 2009

An exergy analysis is carried out for the regenerative steam-injection gas turbine systems which has a potential of enhanced thermal efficiency and specific power. Using the analysis model in the view of the second law of thermodynamics, the effects of pressure ratio, steam injection ratio, ambient temperature and turbine inlet temperature are investigated on the performance of the system such as exergetic efficiency, heat recovery ratio of heat exchangers, exergy destruction, loss ratios, and on the optimal conditions for maximum exergy efficiency. The results of computation show that the regenerative steam-injection gas turbine system can make a notable enhancement of exergy efficiency and reduce irreversibilities of the system.

• Clean Technology
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• v.23 no.4
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• pp.441-447
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• 2017

The economic analysis for the power plant developed in the conceptual design phase is becoming more important and, research on process optimization for process development that meets the target economic is actively carried out. In the filed of power generation systems, economic assessment methods to predict the levelized cost of electricity (LCOE) has been widely applied for comparing economic effect quantitatively. In this paper, the platform that design criteria of key component required to optimize economic of power cycle can be calculated reversely was established roughly and design criteria of the key equipment (Compressor, turbine, heat exchanger) required to meet the target LCOE (the LCOE of supercritical steam Rankine cycle) was derived when the supercritical $CO_2$ power cycle is applied to the coal-fired power plant.

• Journal of the Korean Society of Propulsion Engineers
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• v.3 no.2
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• pp.48-55
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• 1999

Performance analysis of a 50KW turbo-generator gas turbine engine with a recuperator was studied. Recuperated cycle has been employed to meet maximum fuel economy and ultra low emissions especially for military and vehicular engines. From thermodynamic stand point, it is known that recuperative cycle can contribute most to enhance thermal cycle efficiency for the Pressure ratios under 10 and of comparatively low turbine inlet temperature. Efficiency of a simple cycle with a recuperator increases relatively about 30% than without one at effectiveness of 0.5. Pressure losses in the heat exchanger less than 5.2% is considered in the design process. A tubular type heat exchanger is selected for this particular engine because it can provide simple construction as well as structural sturdiness and excellent leak tightness.

• Proceedings of the Korean Society for Agricultural Machinery Conference
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• 2017.04a
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• pp.125-125
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• 2017

본 연구에서 원추형 태양열 집광기의 흡수관 표면의 흑색 도색 여부에 따른 효율분석을 수행하였다. 원추형 집광기 시스템은 열 손실 최소화 및 집광비가 우수한 $45^{\circ}$의 원추각을 갖는 원추형 집광기를 설계 및 제작하였다. 원추형 태양열 집광시스템은 열매체 축열을 위한 온도센서가 내장된 축열조와 태양에너지를 집열시키는 원추형 집광기, 유량측정을 위한 유량계, 열매체의 강제순환을 위한 펌프로 구성되어있다. 또한 지속적인 태양추적을 위해 2축 태양 추적 장치를 설치하였다. 흡수관은 원추형 집광기의 중심부에 설비되었으며, 열매체의 순환을 위해 이중 열교환기 구조로 제작되었다. 흡수관의 길이는 열 손실을 최소화하기 위하여 집광기의 높이와 동일하게 설계하였다. 원추형 집광시스템의 작동유체인 물은 펌프에 의해 흡수관과 축열조를 강제순환 하게되고, 용량이 70L인 축열조에 흡수관으로부터 흡수된 태양 복사열이 저장된다. 원추형 집광시스템의 성능실험은 청명한 날 유량 2L/min, 4L/min, 6L/min에 대해 수행되었으며, 집열효율을 계산하여 비교 및 분석하였다. 흑색으로 도색된 흡수기를 부착한 원추형 집광시스템의 집열효율은 82.25%로 나타났으며, 무 도색 흡수관을 갖는 원추형 집광시스템은 73.26%의 집열효율을 나타내었다. 따라서 본 연구를 통해 흡수관 표면의 흑색 도색이 원추형 집광시스템의 집열효율에 큰 영향을 미친다는 것을 알 수 있었다.

• Journal of Advanced Marine Engineering and Technology
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• v.40 no.3
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• pp.174-179
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• 2016

To protect the ocean environment, the use of liquefied natural gas (LNG) carriers, bunkering ships, and fueled ships is increasing. Recently, Korean shipbuilders have developed and supplied a partial reliquefaction facility for boil-off-gas (BOG). Despite reasonable insulation, heat leakage in vessel storage tanks causes LNG to be continuously evaporated as BOG. This research analyzed the maximum liquid yield rate for various partial reliquefaction systems (PRS) and considered related factors affecting yields. The results showed a liquid yield of 48.7% from an indirect PRS system (heat exchanges between cold flash gas and compressed natural gas), and 41% from a direct PRS system (BOG is mixed with flash gas and discharged from a liquid-vapor separator). The primary factor affecting liquid yield was heat exchanger effectiveness; the exchanger's efficiency and insulation characteristics directly affect the performance of BOG reliquefaction systems.

• 한국신재생에너지학회:학술대회논문집
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• 2010.06a
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• pp.246.1-246.1
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• 2010

본 연구는 바이오가스의 에너지효율성을 높이기 위한 연구로서 바이오가스 정제공정과 초저온액화공정을 통하여 액화바이오메탄을 생산하는 바이오가스 고질화기술개발 연구이다. 바이오가스 정제공정은 탈황, 제습, 흡착, 압축, $CO_2/CH_4$ 분리공정으로 구성하고, 초저온액화공정은 열교환기, $CO_2$ 제거설비, 질소냉매 공급공정으로 구성하여 혐기성소화조에서 발생하는 바이오가스($CH_4$ 농도: 60~65%, $H_2S$: 1,500~2,500ppm)를 $200Nm^3/hr$의 유량으로 인입시켜 액화바이오메탄을 생산하였다. 연구결과, 탈황공정에서는 가성소다 세정법을 이용하여 1,500~2,500ppm으로 인입되는 $H_2S$를 100ppm 이하로 제거한 후, 흡착법을 이용하여 $H_2S$를 완전히 제거하였다. 바이오가스에 포화된 수분은 냉각제습과 흡착제습공정을 통해 Dew point $-70{\sim}-90^{\circ}C$까지 제거하여 안정적으로 $CO_2/CH_4$ 분리공정에 인입시켰다. $CO_2/CH_4$ 분리공정은 흡착방식을 적용하여 $CH_4$ 순도가 95% 이상인 바이오메탄을 생산하였으며, 이때 메탄 회수율은 약 87%이였다. $CO_2$가 분리된 바이오메탄은 초저온액화공정을 이용하여 액화바이오메탄으로 전환시켰다. 이때 초저온액화공정은 Reverse Brayton cycle로 구성하였으며, 냉매로는 질소를 사용하였다. 액화바이오메탄의 생산은 바이오메탄을 등엔트로피과정인 단열팽창을 통하여 $-155{\sim}-159^{\circ}C$의 초저온으로 냉각되는 질소냉매와 열교환기에서 열교환시켜 이루어졌으며 그 생산량은 $3.46m^3$/day(1bar, $-161^{\circ}C$)이었다.