• Proceedings of the KIEE Conference
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• 2011.07a
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• pp.1848-1849
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• 2011

Oxy-PC 발전시스템은 화석 연료를 연소하는 과정에서 발생하는 다량의 이산화탄소를 회수처리 하기위해 고려되고 있는 방법 중 하나이며, 신규 발전 시스템은 물론이며 기존 발전시스템에도 개조 과정을 거쳐 적용이 용이한 장점이 있다. 하지만 현재 국내에 해당 시스템의 적용 사례는 없을 뿐만 아니라 설계 기술의 확보도 부족한 실정이다. 따라서 순산소 연소 시 발생하는 복합적인 문제를 사전에 예측하고 시스템 구현 과정에서 발생되는 시행착오를 최소화하기 위해서는 순산소 연소 공정모델을 반영한 Dynamic Engineering Simulator 개발이 요구된다. 본 논문에서는 Oxy-PC 발전 시스템의 특징을 기존 공기 연소 발전 시스템과 비교하여 설명하고 Oxy-PC 발전 플랜트용 Dynamic Engineering Simulator 개발 절차에 대해 기술한다.

• Proceedings of the KSME Conference
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• 2000.04b
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• pp.871-878
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• 2000

Exergetic and thermoeconomic analysis were performed for a 500-MW combined cycle plant and a 137-MW steam power plant without decomposition of exergy stream of matter into thermal and mechanical exergies. The calculated costs of electricity are almost same within 0.5% as those obtained by the thermoeconomic method with decomposition of exergy into thermal and mechanical exergies of the combined cycle plant. However for the gas-turbine cogeneration plant having different kinds of products. the difference in the unit costs of products, obtained from the two methodologies is about 2%. Such outcome indicates that the level at which the cost balances are formulated does not affect the result of thermoeconomic analysis, that is somewhat contradictory to that concluded previously.

• Proceedings of the Membrane Society of Korea Conference
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• 1995.04a
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• pp.38-39
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• 1995

최근 자동차 대체 연료로 가솔린에 10% 무수에탄올이 혼합된 Gasohol 사용에 관한 관심이 고조되고 있으며, 이는 Gasohol이 자동차 배기 가스중의 일산화탄소 및 탄화수소 함유량을 감소시켜 대기 오염을 줄일 수 있기 때문이다. Gasohol에 사용되는 무수에탄올의 농도는 99.5% 이상이어야 하며, 이러한 고순도의 에탄올을 제조하기 위해서는 물과 에탄올의 공비 혼합물(95.6% 에탄올)로부터 공비증류, 분자체 흡착, 투과증발과 같은 분리 조작을 이용하여 물을 제거하는 공정이 필요하다. 현재 에탄올 탈수에는 공비증류가 많이 사용되고 있으나 공비증류는 에너지 사용량이 많을 뿐더러 유독한 Entrainer를 첨가하기 때문에 투과증발과 같은 저 에너지 소비형, 환경친화적인 공정으로의 전환이 이루어지고 있다. 에탄올 탈수용 투과증발 플랜트는 전세계 20여개가 가동되고 있으며, 상업화된 플랜트의 대부분은 독일의 Deutsche Carbone사가 제조한 PVA/PAN 투과증발 복합막을 사용하고 있다. 투과증발 시스템은 물에 대한 친화도가 높은 투과증발막 및 모듈, 기타 분리 구동력을 높여주기 위한 Heater, 진공펌프, 냉각기, 열 교환기 등의 주변 설비로 구성되며, 투과증발 시스템 개발을 위해서는 우수한 막/모듈 제조와 아울러 최적 공정 설계 기술 개발이 필수적이라 하겠다.

• Proceedings of the Korean Institute of Navigation and Port Research Conference
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• 2022.11a
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• pp.94-95
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• 2022

선박 운항 안전 확보를 위해 필요한 선박과 선박, 선박과 육상 및 기타 해양 안전 관련 주체와의 통신은 자율/무인 선박의 출현 및 유무인 선박이 혼재 운항하는 과도기적 상황에서 기존 VHF, AIS 등의 통신 기능을 능가하는 고용량, 고신뢰 선박 중심 직접통신 체계를 요구한다. IMO의 자율운항 선박 자율화 단계에 필요한 원격에서의 모니터링 및 제어 필요성(Ship to Shore), 나아가 완전한 자율운항을 위한 고용량의 선박중심통신(Ship to Ship) 및 해양 객체와의 통신(Ship to Shore, Air, People)이 구현되어야 유무인 선박의 혼재 운항 과도기를 거쳐 완전한 자율운항 시대로 나아갈 수 있다는 점에서 이를 포괄하는 S2X(Ship to Everything) 통신 기술의 개발 당위성을 찾을 수 있다. S2X 통신은 정보 교환 상대를 신뢰할 수 있고 이를 기반으로 선박의 안전 운항 관련 정보를 상호 교환하고 부가 서비스를 위한 고용량의 데이터를 자유롭게 교환할 수 있도록 하는 선박중심직접통신 기술이 될 것이다.

• 한국생물공학회:학술대회논문집
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• 2003.04a
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• pp.676-679
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• 2003

Long time over 6 month was required to form granuler sludge, which is critically necessary for UASB reactor. By feeding both high molecular cationic polymer and anionic silica sol to conventional digestion sludge, granular sludge was obtained within 5 minutes. Succession adaptation was performed for granular sludge for 30 days. $80{\sim}90%$ COD removal efficiency was shown with granular sludge, which was comparable with that of typical UASB granular sludge.

• Proceedings of the Korea Society for Energy Engineering kosee Conference
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• 2000.11a
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• pp.39-44
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• 2000

석탄가스화 복합발전(IGCC; Integrated Gasification Combined Cycle) 은 석탄을 연료로 사용하면서 NOx, SOx 등 오염물 발생량이 적고 가스터빈을 채용한 복합발전 방식으로 효율이 높은 청정에너지 발전방식이다. 특히 우리나라와 같이 전력생산 분야에서 석탄화력의 비중이 높은('99년 6월 현재 27.8%(한전통계자료)) 우리나라에서 급격히 강화되는 석탄화력발전소에 대한 오염물 배출량 제한에 대처하기 위해 기존 석탄화력의 대안으로써 석탄가스화 복합발전이 부각되고 있다. 본 연구에서 국내에 IGCC 상용설비 도입에 대비하여 참조플랜트로서 Texaco 가스화공정을 채용한 2 case의 IGCC 시스템 연구를 수행하였다.(중략)

• Journal of Technology Innovation
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• v.25 no.2
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• pp.89-125
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• 2017

Complex product systems (CoPs) is a engineering-intensive products with high-ended design technology, which are closely linked with national economic growth and development of social infrastructures. Accordingly, in order to understand the technological evolution of CoPs, it is necessary to identify the macro-environmental drivers surrounding the CoPs and their impact on the technological evolution of the CoPS. Therefore, we investigate the effect of policy, economic and social drivers on the technological evolution of CoPS by implementing the longitudinal case study on nuclear power plant during the periods between 1950 and 2010s. Based on the analysis of various sources of secondary data and primary data through interviews, we found that the technological evolution of nuclear power plant is progressed as "Phase 1: Application research for peaceful utilization of nuclear energy" between 1950s and 1960s, "Phase 2: The first renaissance of nuclear energy" during 1970s, "Phase 3: Enhancement of safety and the catch-up of latecomers in nuclear energy" between 1990s and 2000s, and "Phase 4: Top prioritization of safety and the development of next generation reactors for the second renaissance of nuclear energy" since 2010s. We also found that various kinds of policy, economic and social drivers, such as energy policy, investment in technology development, economic growth and energy demand, social acceptability and environmental concern, have affected the technology evolution of nuclear power plant at each phase. We emphasize the role of macroenvironmental drivers in the technological evolution of CoPS. We also suggest that countries that endeavor to develop CoPs need to utilize those drivers for enhancing competitiveness and sustaining leadership.

• Journal of Energy Engineering
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• v.27 no.2
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• pp.14-25
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• 2018

The combined cycle power plant has a cycle of operating the gas turbine with fuel, such as natural gas, and then producing steam using residual heat. The fuel gas is supplied to the gas turbine at a level of 4 to 5 MPa, $200^{\circ}C$ through a compressor and a heat exchanger. In this study, the risk assessment method considering the piping system stress was carried out for safe operation and soundness of the gas fuel supply piping system. The API 580/581 RBI code, which is well known for its risk assessment techniques, is limited to reflect the effect of piping stress on risk. Therefore, the systematic stress of the pipeline is analyzed by using the piping analysis. For the study, the piping system stress analysis was performed using design data of a gas fuel supply piping of a combined cycle power plant. The result of probability of failure evaluated by the API code is compared to the result of stress ratio by piping analysis.

• Journal of the Korea Academia-Industrial cooperation Society
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• v.18 no.4
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• pp.118-124
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• 2017

In this study, a numerical simulation was performed using commercial code Fluent(v.17.1). The underground Combined Cycle Power Plant (CCPP) was simplified to analyze the methane gas leakage with the crack size and position. In addition, extensive numerical simulations were carried out for different crack sizes from 10 mm to 20 mm. The crack position is the gas leakage, which is assumed to be near the pipe elbow and the gas turbine. A total of 4 cases were compared and analyzed. To analyze the gas leakage, the concept of the Lower Flammable Limit (LFL) was applied. The leakage distance was defined in the longitudinal direction, and the transverse direction was estimated and quantitatively analyzed. As a result, the leakage distance in the longitudinal direction varies by 52.3 % depending on the crack size at the same crack position. Moreover, the maximum difference was 34.8 % according to the crack position when the crack sizes are identical. As jet flow impacts on the obstacle and changes its direction, the recirculation flows are formed. These results are expected to provide useful data to optimize the location and number of gas detections in confined spaces, such as underground CCPP.

• Korean Chemical Engineering Research
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• v.61 no.3
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• pp.368-377
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• 2023

Natural Gas Combined Cycle(NGCC) recently receives lots of attention as an attractive form of power plants by virtue of its low carbon emission compared with coal-fired power plant. Nevertheless, it also needs carbon capture process since it is difficult to completely suppress carbon emission even for the NGCC. A simulation study has been performed to optimize operating condition of a carbon capture process using MEA considering low partial pressure of carbon dioxide in NGCC emission gas. For accurate optimization, overall process model including both NGCC and the carbon capture process has been built with a simulation software. Then, optimization in which various performance indices such as carbon dioxide absorption rate, solvent regeneration rate and power loss in the NGCC are simultaneously reflected has been done. Especially, it is noticeable that this study focuses on not only the amount of energy consumption but also the absorption and regeneration performance of carbon capture process. The best result considering all the performance indices has been achieved when the reboiler temperature is 120 ℃ and the reason has been analyzed.