• 해양환경안전학회지
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• 제15권3호
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• pp.269-274
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• 2009

LNGC(Liquefied Natural Gas Carrier)의 역사는 1959년 $5,000m^3$ 급 LNG선 "Methane Pioneer"호를 시작으로 1969년에는 $71,500m^3$ 급, 1973년에는 Moss Type의 최초 LNG운반선 "Norman Lady($87,600m^3$)호, 1980년대 $125,000m^3$ 급을 시작으로 1990년대를 거처 $135,000m^3$ 급, 2007년 $210,000m^3$급 그리고 2008년에는 $266,000m^3$ 급의 초대형 액화천연가스 운반선이 출현하였다. 또한 2006년 11월에는 기존 내 외연 기관이 아닌 발전기 기동으로 Propeller를 움직이는 DFDE(Duel Fuel Diesel Electric)엔진, 육상의 Storage Tank를 생략한 기화설비를 갖춘 LNG-RV(Re-gasification Vessel)와 주 기관은 Slow Diesel을 택하고, 운항 중 발생하는 BOG(Boil Off Gas)를 재액화시키는 설비를 갖춘 DRL(Diesel Re-Liquefaction)선박 및 해상 LNG 생산 저장시설인 LNG-FPSO(Floating Production and Storage Offshore), 그리 고 해상 LNG 인수기지 역할을 하는 LNG-FSRU(Floating Store and Re-gasification Unit) 등이 개발되었다. 이 논문에서는 LNG Project, 전 세계 에너지 시장과 LNGC의 발전 추세에 대하여 다루었다.

• Journal of Advanced Marine Engineering and Technology
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• 제36권5호
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• pp.574-579
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• 2012

본 논문에서는 $CO_2-C_2H_6-N_2$와 $CO_2-N_2$를 각각 적용한 캐스케이드 액화사이클을 새롭게 제안하고, HYSYS를 이용하여 이에 대한 성능 및 엑서지를 분석한 후, 이 사이클이 LNG-FPSO선에 적용가능여부를 확인하였다. 그 분석 결과로부터, 효율적인 측면에서는 $CO_2-C_2H_6-N_2$ 액화사이클이 우수하였고, 엑서지 손실측면에서는 장치 수가 적은 $CO_2-N_2$ 액화사이클이 오히려 높게 나왔다. 그리고 $CO_2-N_2$ 냉매용액화사이클은 기존의 $C_3H_8-C_2H_4-C_1H_4$ 보다 낮은 효율과 높은 압축일량을 보였다. 하지만, $N_2$ 사이클의 효율이 더 개선된다면 액화사이클의 구조가 간단하기 때문에 LNG-FPSO용 액화사이클로서 적합할 것으로 생각된다.

• Ocean Systems Engineering
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• 제2권1호
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• pp.49-68
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• 2012

In this paper, an offshore process front end engineering design (FEED) method is systematically introduced and reviewed to enable efficient offshore oil and gas production plant engineering. An integrated process engineering environment is also presented for the topside systems of a liquefied natural gas floating production, storage, and offloading (LNG FPSO) unit, based on the concepts and procedures for the process FEED of general offshore production plants. Various activities of the general process FEED scheme are first summarized, and then the offshore process FEED method, which is applicable to all types of offshore oil and gas production plants, is presented. The integrated process engineering environment is presented according to the aforementioned FEED method. Finally, the offshore process FEED method is applied to the topside systems of an LNG FPSO in order to verify the validity and applicability of the FEED method.

• 한국정밀공학회지
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• 제29권12호
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• pp.1331-1339
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• 2012

Safety valve used in LNG/LNG-FPSO ships is a high value valve, and it plays an important role in maintaining a fixed level of pressure by emitting LNG gas out of pipes in LNG piping system under the cryogenic and high-pressure condition when the pressure of the system connected with the LNG storage tank and pipes reaches over the set pressure. The structural stability is required for the inner pressure and thermal load because of the cryogenic and high-pressure condition, and a reliability of the safety valve is necessary for impact and deformation by opening the valve. But, the safety valve, which plays a key role for a safety of the transport and storage system, is depended on imports for over 90%, and in domestic production, the design of the valve is performed on the basis of experiences of the works without quantitative analysis for the inner operation characteristics and structural stability of the valve. In this study, impact velocity is calculated by theoretical analysis for obtaining the structural stability of the guide according to the impact load by opening the valve. The shape of the guide and the diaphragm for satisfying the structural stability are suggested and verified by using a thermal-structural analysis.

• 한국CDE학회지
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• 제22권1호
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• pp.63-69
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• 2016

• 대한조선학회논문집
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• 제47권5호
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• pp.733-742
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• 2010

In this study, optimization was performed to improve the conventional liquefaction process of offshore plants, such as a LNG-FPSO(Liquefied Natural Gas-Floating, Production, Storage, and Offloading unit) by maximizing the energy efficiency of the process. The major equipments of the liquefaction process are compressors, expanders, and heat exchangers. These are connected by stream which has some thermodynamic properties, such as the temperature, pressure, enthalpy or specific volume, and entropy. For this, a process design problem for the liquefaction process of offshore plants was mathematically formulated as an optimization problem. The minimization of the total energy requirement of the liquefaction process was used as an objective function. Governing equations and other equations derived from thermodynamic laws acted as constraints. To solve this problem, the sequential quadratic programming(SQP) method was used. To evaluate the proposed method in this study, it was applied to the natural gas liquefaction process of the LNG-FPSO. The result showed that the proposed method could present the improved liquefaction process minimizing the total energy requirement as compared to conventional process.

• 한국CDE학회논문집
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• 제21권2호
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• pp.111-121
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• 2016

The plant equipment usually has a long life cycle. During its O&M (Operation & Maintenance) phase, since the occurrence of an accident of offshore plant equipment causes catastrophic damage, it is necessary to make more efforts for managing critical offshore equipment. Nowadays due to the emerging ICTs (Information Communication Technologies) and sensor technologies, it is possible to gather the health status data of important offshore equipment and their environment data, which leads to much concern on CBM (Condition-Based Maintenance). In this study, we will propose an approach to estimate the remaining lifetime of an offshore plant equipment (pump tower) based on gathered ocean environment data.

• International Journal of Naval Architecture and Ocean Engineering
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• 제8권6호
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• pp.537-553
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• 2016

This paper addresses the safety of two-row tank design by performing the extensive sloshing model tests. Owing to the uncertainties entangled with the scale law transforming the measured impact pressure up to the full scale one, so called comparative approach was taken to derive the design sloshing load. The target design vessel was chosen as 230 K LNG-FPSO with tow-row tank arrangement and the reference vessel as 138 K conventional LNG carrier, which has past track record without any significant failure due to sloshing loads. Starting with the site-specific metocean data, ship motion analysis was carried out with 3D diffraction-radiation program, then the obtained ship motion data was used as 6DOF tank excitation for subsequent sloshing model test and analysis. The statistical analysis was carried out with obtained peak data and the long-term sloshing load was determined out of it. It was concluded that the normalized sloshing impact pressure on 230 K LNG-FPSO with two-row tank arrangement is higher than that of convectional LNG carrier, hence requires the use of reinforced cargo containment system for the sake of failure-free operation without filling limitation.

• 대한조선학회지
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• 제47권4호
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• pp.23-27
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• 2010

• 대한조선학회지
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• 제50권4호
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• pp.19-23
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• 2013