• 제목/요약/키워드: BOG liquefaction

검색결과 20건 처리시간 0.031초

NGL 분리식 BOG 재액화 공정 고안 및 해석 (Process Design and Analysis of BOG Re-liquefaction System with Pre-liquefaction of NGL)

  • 윤상국
    • 한국가스학회지
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    • 제19권3호
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    • pp.32-37
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    • 2015
  • LNG는 극저온액체로 저장탱크의 열유입으로 인하여 지속적으로 BOG가 발생하고 있으며, 이의 효과적인 방법의 재액화가 요구되고 있다. 이 BOG의 재액화에는 공급되는 저압 펌프 후의 LNG의 냉열을 이용하는 데, 현재의 공정은 BOG 단위 발생량에 대하여 10배 이상의 LNG 흐름이 요구되고 있다. 본 연구에서는 NGL분리액화와 2차 고압펌프 후의 LNG 냉열을 이용하는 공정을 새롭게 고안하였으며, 이를 분석한 결과 LNG 소요유량이 3~4배에 불과한 매우 효과적인 재액화 시스템이 되었다. 본 고안에 의하면 하절기에도 원활한 BOG 재액화가 가능하므로, LNG기지의 안전성 향상과 공급 의 효율을 높일 수 있는 매우 효과적인 공정으로 분석되었다.

역 브레이튼 냉동사이클을 이용한 LNG 운반선의 증발기체 재액화 시스템에 관한 연구 (A Study on the BOG Re-liquefaction System based on the Reverse Brayton Refrigeration Cycle for LNG Carriers)

  • 진영욱
    • 대한안전경영과학회지
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    • 제9권4호
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    • pp.149-154
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    • 2007
  • The LNG carriers have been propelled by steam turbines and the LNG boil-off(BOG) has been used as fuel or vented. However, as the alternative propulsion systems such as diesel engines are being equipped on the LNG carriers for better fuel efficiency, a need for the LNG BOG re-liquefaction system that liquefies the BOG and sends the liquid BOG back to the LNG cargo has arisen in recent years. This study investigates the design of the BOG re-liquefaction system based on the reverse Brayton refrigeration cycle. The thermodynamic and heat exchanger analysis are carried out and the limitations to the system performance are discussed.

상용 공정시뮬레이션 프로그램을 이용한 부유식 LNG 발전설비의 BOG 회수시스템 공정모사 (Process Simulation of the BOG Re-Liquefaction system for a Floating LNG Power Plant using Commercial Process Simulation Program)

  • 서주완;유승열;이재철;김영훈;이순섭
    • 해양환경안전학회지
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    • 제26권6호
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    • pp.732-741
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    • 2020
  • 최근 환경규제가 강화됨에 따라 액화천연가스(Liquefied Natural Gas)를 이용하여 전력을 생산해내는 신규발전설비인 부유식 LNG 발전설비(floating LNG power plant)가 개발되고 있다. 부유식 LNG 발전설비는 운용 시 증발가스가 발생하고 이를 제거하거나 회수할 수 있는 시스템의 설계가 필요하다. 그러나 해양플랜트는 해상요건에 따라 설계가 상이하고, 부유식 LNG 발전설비의 설계 전 시행착오를 줄이기 위해 지속적으로 수정이 가능한 BOG 회수시스템 공정모사 모델이 필요하다. 따라서 본 연구에서는 상용공정시뮬레이션 프로그램을 통해 부유식 LNG 발전설비에 적합한 모델을 모델링하고자 냉매사용 유무에 따라 서로 다른 BOG(Boil-Off Gas) 회수시스템을 모델링하여 BOG의 회수율과 액화점을 비교 및 분석하였으며, 그 결과 질소냉매를 사용한 BOG 회수시스템 모델을 부유식 LNG 발전설비용 BOG 회수시스템 모델로 제안하고자 한다.

LNG 운반선을 위한 BOG 재액화시스템 최적 설계 (Optimal Process Design of Onboard BOG Re-liquefaction System for LNG Carrier)

  • 황철민;임영섭
    • 한국해양공학회지
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    • 제32권5호
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    • pp.372-379
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    • 2018
  • High-pressure gas injection engines (HPGI) took center stage in LNG carrier propulsion systems after their advent. The HPGI engine system can be easily modified to include a re-liquefaction system by adding several devices, which can significantly increase the economic feasibility of the total system. This paper suggests the optimal operating conditions and capacity for a re-liquefaction system for an LNG carrier, which can minimize increases in the total annualized cost. The installation of a re-liquefaction system can save 0.23 million USD per year when the cost of LNG is 5 USD/Mscf. A sensitivity analysis with different LNG costs showed that the re-liquefaction system is profitable when the LNG cost is higher than 3.5 USD/Mscf.

역대향류 열교환기의 열 핀치(thermal pinch)에 관한 연구 (A Study on the thermal pinch problem in the counterflow heat exchanger)

  • 최성은;진영욱
    • 대한안전경영과학회:학술대회논문집
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    • 대한안전경영과학회 2008년도 추계학술대회
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    • pp.659-667
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    • 2008
  • The LNG carriers have been propelled by steam turbines and the LNG boil-off(BOG) has been used as fuel or vented. However, as the alternative propulsion systems such as diesel engines are being equipped on the LNG carriers for better fuel efficiency, a need for the LNG BOG re-liquefaction system that liquefies the BOG and sends the liquid BOG back to the LNG cargo has arisen in recent years. This study investigates the design of the BOG re-liquefaction system based on the reverse Brayton refrigeration cycle. The thermodynamic and heat exchanger analysis are carried out and the limitations to the system performance are discussed.

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Design of BOG re-liquefaction system of 20,000 m3 liquid hydrogen carrier

  • Byeongchang Byeon;Hwalong You;Dongmin Kim;Keun Tae Lee;Mo Se Kim;Gi Dock Kim;Jung Hun Kim;Sang Yoon Lee;Deuk Yong Koh
    • 한국초전도ㆍ저온공학회논문지
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    • 제25권3호
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    • pp.49-55
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    • 2023
  • This paper presents the design of a re-liquefaction system as a BOG (boil-off gas) handling process in liquid hydrogen transport vessels. The total capacity of the re-liquefaction system was assumed to be 3 ton/day, with a BOR (boil-off rate) of 0.2 %/day inside the cargo. The re-liquefaction cycle was devised using the He-Brayton Cycle, incorporating considerations of BOG capacity and operational stability. The primary components of the system, such as compressors, expanders, and heat exchangers, were selected to meet domestically available specifications. Case studies were conducted based on the specifications of the components to determine the optimal design parameters for the re-liquefaction system. This encompassed variables such as helium mass flow rate, the number of compressors, compressor inlet pressure and compression ratio, as well as the quantity and composition of expanders. Additionally, an analysis of exergy destruction and exergy efficiency was carried out for the components within the system. Remarkably, while previous design studies of BOG re-liquefaction systems for liquid hydrogen vessels were confined to theoretical and analytical realms, this research distinguishes itself by accounting for practical implementation through equipment and system design.

천연가스 운반선의 재액화 장치가 운항비용에 미치는 영향에 관한 연구: 연료비용 및 증발 가스 연소비용 관점에서 (Effect of Re-liquefaction System on Operating Expenditure of LNGC in Terms of Fuel Oil Consumption Cost and BOG Combustion Cost)

  • 유영준;이준채
    • 대한조선학회논문집
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    • 제57권3호
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    • pp.152-159
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    • 2020
  • Ship owners had pursued higher benefits by demanding the new design and construction of ships with higher operational efficiency. There was a necessity for shipyards to suggest a more economical design and advanced operation concept in order to meet the demands. Especially, since BOG combustion and activation of the re-liquefaction unit had to be taken into account in ship design in addition to fuel oil and gas consumption, the evaluation of the operating efficiency considering the technological trends was necessary. In this paper, it was aimed to study the design philosophy and operation strategy by considering the effect of fuel oil and gas consumption, BOG combustion, and activation of the re-liquefaction unit on the operating cost for laden voyage according to ship speed, BOR, and activation of the re-liquefaction unit. For this purpose, the costs were acquired by conducting the sailing simulation of an LNGC based on a mathematical model including the maneuvering equations of motion. The design philosophy and operation strategy was reviewed in terms of the operating cost.

LNG냉열이용 BOG 재액화긍정 해석연구 (New reliquefaction system of Boil-Off-Gas by LNG cold energy)

  • 윤상국;최형식
    • Journal of Advanced Marine Engineering and Technology
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    • 제26권2호
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    • pp.256-263
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    • 2002
  • The Boil-Off-Gases(BOG) in the LNG production terminal are continuously generated during the unloading, storage and supply processes by the heat penetration. In order to use these gases as useful fuel, the reliquefaction process should be installed to put the reliquefied BOG in the main LNG supply line before the secondary pump in terminal. The current reliquefaction method of BOG in LNG terminal is the direct contact one between LNG and BOG in the absorption column. But the system has severe disadvantage, which is the 10 times of LNG circulation needed for unit mass of BOG reliquefaction. It causes, therefore, high power consumption of LNG circulation pump and excessive city-gas supply, even if short demand of NG is needed in the summer time. In this paper, the new reliquefaction system of BOG by using LNG cold energy with indirect contact in precooler was suggested and analysed. The result showed new indirect contact method of BOG reliquefaction system between LNG cold energy and BOG is much more effective than the current direct contact one because of only about 1.3 times of LNG circulation needed and higher energy saving by pump power reduction.

LNG운반선의 증발기체 재액화 장치의 사이클 해석

  • 진영욱
    • 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.

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LNG운반선의 BOG 처리설비 (The BOG Handling System for LNG Carrier)

  • 김만응;김유택
    • 유체기계공업학회:학술대회논문집
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    • 유체기계공업학회 2005년도 연구개발 발표회 논문집
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    • pp.557-561
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    • 2005
  • In recent years, the LNGC fleet is expanded unprecedentedly. Ship's owners and shipbuilders are focusing on the idea how they choose the BOG handling system in economical, environmental and safety angles. This paper introduces general information for that and gives technical matters briefly.

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