• 에너지공학
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• 제18권3호
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• pp.191-202
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• 2009

2005년 2월 교토의정서가 효력을 발휘하게 됨에 따라 우리나라는 세계 10위의 이산화탄소 배출국으로서 2013년 이후에는 감축의무를 지어야 할 실정이다. 특히 온실가스 배출량의 약 30%가 발전부문에 의한 것이므로 전환부문의 에너지 소비 저감은 매우 중요하다. 이에 정부는 온실가스 감축환경에 대응하기 위하여 "제1차 국가에너지기본계획"을 발표하여 원전설비를 2030년까지 최대 41%까지 확대하고, 신재생에너지보급률 또한 11%로 높이겠다는 목표를 내세웠다. 이에 근거하여 원자력과 신재생에너지발전설비를 확대하였을 경우 온실가스 저감 잠재량과 그 유효성을 LEAP(Long-range Energy Alternative Planing system)을 이용하여 정량적으로 분석하였다. 분석결과 2030년 기준으로 총 $CO_2$ 발생 저감률은 28.8% 였다. 또한 BAU 시나리오 발전량을 토대로 하였을 때 유연탄발전 $0.85\;kgCO_2/kWh$, LNG발전 $0.51\;kgCO_2/kWh$의 단위 발전량당 온실가스 배출량을 보였다. 따라서 기존설비를 대체할 시, 유연탄발전을 대체할 경우에 온실가스 저감 효과가 크다는 결론을 보였다.

• 국제학술발표논문집
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• The 3th International Conference on Construction Engineering and Project Management
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• pp.375-380
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• 2009

Gas & Oil plant construction projects are increasing recently all over oil-producing countries. An EPC (Engineering, Procurement and Construction) company, which participates in the plant projects, should possess pertinent engineering licenses and EPC management skills to create high added-value. Nonetheless, there exist various risks involved in the EPC life cycle process due to such characteristics of construction projects as long duration of construction time and complicated processes along with the procured goods or services subjected to various logistics. The objective of this paper is to analyze the overall EPC life cycle for proper process and to examine various information and document. Additionally, the principal data for the analysis of the EPC process are derived from personal interviews with experts and specialty contractors of the plant projects. The results of this study would be widely used as a guide for efficient and effective management of overseas gas plant projects.

• 전력전자학회논문지
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• 제13권5호
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• pp.344-351
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• 2008

본 논문의 배경은 제주지역의 안정적 전력공급을 위하여 최적의 전력공급체계를 분석한 논문이다. 본 논문에서 검토한 내용은 제주도 전력공급 현황파악 및 문제점 분석, 전력계통 운영측면에서 최적의 전력설비건설 타당성 검토 그리고 경제성 및 신뢰도 검토이다. 결론적으로 2011년에 HVDC 연계 선을 제주에 건설하는 경우에 경제성 평가(30년간 2011년 현가합 비교)를 한 경우 HVDC 연계선 추가건설이 기력(중유)발전이나 LNG 발전 보다 경제적임을 보여주고 있다. 그리고 신뢰도 측면에서도 좋은 역할을 할 것으로 기대되어진다.

• 한국산업융합학회 논문집
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• 제26권6_3호
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• pp.1305-1314
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• 2023

The global ship repair and modification market is expected to grow up to approximately $ 30 billion by 2025. Korea's shipbuilding industry is leading the world grounded on its international competitiveness in design and production technology. The reality, however, is that the ship repair and modification industry is centered on Gyeongnam, and there are only two to three ship repair workplaces that can repair large ships. Therefore, domestic ship repair companies target small and medium-sized ships mainly. This is because there are few workplaces equipped with a large dock in which large ships like LNG ships can be inspected regularly or repaired, complaints are severe for environmental problems, and related environmental regulations are so strict that it is very hard to obtain government approval for the extension of ship repair and modification workplaces or the opening of new shipbuilding sites. Besides, on account of the workers' high wages, few experts related, and higher ship repair price compared to that of Southeast Asia, most of the volume of repairing large ships including domestic LNG ships is being lost to Southeast Asian or Chinese markets. In this study, the work process and pre-work preparation process for ship hull (winch, windlass, hatch cover, ramp door, cargo gear, anchor chain) repair were analyzed and presented to foster domestic ship repair experts and revitalize related industries.

• 한국조명전기설비학회:학술대회논문집
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• 한국조명전기설비학회 2007년도 추계학술대회 논문집
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• pp.341-344
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• 2007

교토의정서(Kyoto Protocol)는 1997년 일본 교토에서 채택되어 2005년 2월에 공식 발효되었다. 우리나라는 현재 온실가스 감축의무 부담이 없지만 2013년부터 감축의무가 거의 확실시되고 있는 상황이다 국내 온실가스 배출량의 25%를 차지하는 발전산업은 화석연료를 사용하고 있어 전력생산에 따른 $CO_2$ 배출량의 계산은 매우 중요한 일이 되었다. 본 논문은 - D발전소의 성능시험에 대하여 기술하고, - 성능시험 결과 얻어진 D발전소 성능시험 Data a, b, c 특성계수를 이용, LNG와 중유 연소시 각각 연료소모량에 대한 $CO_2$ 대기 배출량을 계산 비교하였으며, - 화학적인 방법에 의한 $CO_2$ 대기 배출량 산정방법을 간략히 언급하였다.

• 동력기계공학회지
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• 제20권1호
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• pp.5-10
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• 2016

Swing check valve is opened when the flow direction is forward, when the flow is reversed, the valve is automatically closed by back pressure. In this study, the internal flow field analysis of the valve was conducted by Fluent. The working fluid used in the study, using liquefied methane $-165^{\circ}C$ (CH4) and velocity field, pressure field, pressure drop coefficient were simulated by varying separately the opening divergence into four intervals from 0 to 100%. The approximate research result are as follow : When the opening divergence is smaller, it appears high pressure on the upstream side, this value is relaxed when the opening divergence is large. Flow rate coefficient of the valve shows a larger value as the degree of opening becomes larger, confirming that the check valve used in the study is in the effective flow rate counting range.

• 한국마린엔지니어링학회:학술대회논문집
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• 한국마린엔지니어링학회 2005년도 후기학술대회논문집
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• pp.210-211
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• 2005

Desuperheater is a passive device to control the temperature of steam in various plants. However, in spite of its simple structure, the accurate prediction of a desuperheater is very difficult because there are many designed factors for the design of a desuperheater. In this study, the theory of heat transfer phenomena in a desuperheater was developed and the various design factors are evaluated. As a results, we confirmed that the droplet size of 30 - 200 is best effective for the performance of a desuperheater.

• 대한안전경영과학회:학술대회논문집
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• 대한안전경영과학회 2012년 춘계학술대회
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• pp.221-232
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• 2012

Cycle analysis has been performed to find out the optimum design point of the BOG re-liquefaction plant. The cycle state, defined by three cycle variables, was mainly described by the three cold temperatures of the three-pass heat exchanger, on which the constraints by the heat exchanger are imposed. The cycle states which are confined within a domain limited by the temperature constraints were the primary issue of this study. The BOG mass within the domain was analyzed first and then the cycle performance was related to the BOG mass afterwards, which enabled us to explain the observed behavior of the cycle performance under the temperature constraints by the heat exchanger. A good cycle performance could be ensured if the two cold Nitrogen temperatures of the three temperatures were placed close together near $-140^{\circ}C$ while the BOG temperature is kept far above enough, but not too far, from $-140^{\circ}C$ such that it does not interfere in their optimum temperature range.

• 한국초전도ㆍ저온공학회논문지
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• 제8권4호
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• pp.34-38
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• 2006

Cycle analysis was performed in order to find the optimum design point of the LNG Boil-off gas re-liquefaction system. Thermodynamic analysis revealed the system could be defined by three state variables. Thus the system performance could be described by the three cold endpoint temperatures of the three-pass heat exchanger. This enabled us to investigate the cycle performance in terms of the heat exchanger parameters. To get access to the cycle states of higher system performances, larger heat exchangers were found necessary. Also the thermal pinch in cryogenic heat exchangers was found to act as a limiting factor to the system performance.

• 대한기계학회:학술대회논문집
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• 대한기계학회 2007년도 춘계학술대회B
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• pp.2321-2326
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• 2007

To return LNG to a gaseous state, it is fed into a regasification plant. For inland area, where pipelines do not exist or difficult to construct, the LNG is delivered to the inland-receiving terminal available at that area, regasified and delivered to consumers. At inland-receiving terminal, air-heating vaporizer type is usually used. To contribute in developing an efficient air-heating vaporizer, experiment on finned type air-heating vaporizer using 8 fins, 50 mm fin length (8fin50le) and 4 fins, 75 mm fin length (4fin75le) were conducted. The experiments were conducted by varying the ambient condition and the length of the vaporizer. The ambient air was controlled so that it has the same condition with air condition in every season available. $LN_2$ is used to substitute LNG because of safety reason. The results show that characteristics of the finned type 4fin75le vaporizer are comparable to finned type 8fin50le vaporizer at all season.