• Title/Summary/Keyword: BOG

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

  • Seo, Ju-Wan;Yoo, Seung-Yeol;Lee, Jae-Chul;Kim, Young-Hun;Lee, Soon-Sup
    • Journal of the Korean Society of Marine Environment & Safety
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    • v.26 no.6
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    • pp.732-741
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    • 2020
  • Environmental regulations have recently been strengthened. Consequently, floating LNG(Liquefied Natural Gas) power plants are being developed, which are new power generation plants that generate electricity by utilizing LNG. A floating LNG power plant generates BOG(Boil-Off Gas) during its operation, and the system design of such a plant should be capable of removing or re-liquefying BOG. However, the design of an offshore plant differs according to the marine requirements. Hence, a process simulation model of the BOG re-liquefaction system is needed, which can be continuously modified to avoid designing the floating LNG power plant through trial and error. In this paper, to develop a model appropriate for the floating LNG power plant, a commercial process simulation program was employed. Depending on the presence of refrigerants, various BOG re-liquefaction systems were modeled for comparing and analyzing the re-liquefaction rates and liquid points of BOG. Consequently, the BOG re-liquefaction system model incorporating nitrogen refrigerants is proposed as the re-liquefaction system model for the floating LNG power plant.

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

  • Choi, Sung-Eun;Chin, Young-Wook
    • Proceedings of the Safety Management and Science Conference
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    • 2008.11a
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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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The BOG Handling System for LNG Carrier (LNG운반선의 BOG 처리설비)

  • Kim, M.E.;Kim, Y.T.
    • 유체기계공업학회:학술대회논문집
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    • 2005.12a
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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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Case Study on Optimization of Send-out Operation in Liquefied Natural Gas Receiving Terminal (LNG 터미널 송출 운전 최적화 사례 연구)

  • Park, Chansaem;Han, Chonghun
    • Korean Chemical Engineering Research
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    • v.53 no.2
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    • pp.150-155
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    • 2015
  • Recently, LNG receiving terminals have been widely constructed and expanded for an increase in LNG demand. Selection of the storage tank for send-out and estimation of send-out flow rate have significant influence to process operation and economics. In this study, a send-out flow rate of each storage tank is optimized in order to minimize the total BOG generation rate. Considering a size and characteristic of each storage tanks, BOG flow rates are estimated using a dynamic simulation with varying liquid levels in the tanks. The regression model is developed fitting BOG flow rates and tank liquid levels, which are boil off rate model to predict BOG flow rates with particular level data. The objective function and constraints including required total send-out flow rate and level limit in the tanks are formulated to optimize a send-out flow rate of each tank. This method for optimization of send-out operation is applied to the Incheon LNG receiving terminal considering two scenarios for various liquid levels and maximum and minimum required send-out flow rates. For maximum required send-out flow rate, this method achieves BOG reduction of 9% comparing with assumed conventional operation.

Study on the Comparison of New and Used Reliquefaction System of Boil-Off-Gas by LNG Cold Energy (냉열을 이용한 LNG 증발기체 BOG 재액화 신공정과 기존공정에 관한 비교연구)

  • Lee, Dong-Hyuck;Jang, Chang-Bong;Jung, Sang-Yong;Kim, Jung-Hwan;Lee, Heon-Seok;Kim, Bum-Su;Ko, Jae-Wook
    • Journal of the Korean Institute of Gas
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    • v.14 no.1
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    • pp.42-46
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    • 2010
  • BOG(Boil Off Gas) is formed about 0.05 vol%/day from LNG(Liquefied Natural Gas) tanks of LNG receiving terminal. To recycle the BOG using direct contacting, Previously the quantities of LNG and BOG is mixed at the ratio of 11:1 by mass. However simple this process uses, there is the difficulty of processing operation resulted from decrease of using LNG in summer. To complement these shortcomings, Advantages of the process are investigated by comparison of cost and analysis of the indirect contact method using LNG cold energy. It was studied that principles and types of development using LNG cold energy which is abandoned in the carburettor and found how to contact each to find the appropriate cold energy development process. Therefore, in this research, the indirect contact method will be investigated the feasibility of a comparative analysis by using HYSYS.

Characteristics of boil-off-gas partial re-liquefaction systems in LNG ships (LNG선박용 BOG 부분재액화 시스템 특성 연구)

  • Yun, Sang-Kook
    • 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.

Pharmacognostical Study on the To Bog Ryung (토복령의 생약학적 연구)

  • Park, Jong-Hee;Kim, Jeong-Myo;Do, Weon-Im
    • Korean Journal of Pharmacognosy
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    • v.33 no.3 s.130
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    • pp.169-172
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    • 2002
  • Chinese crude drug 'To Bog Ryung' has been to cure chronic aperient, syphilis cough and diabetes. The botanical origin of the crude drug has never been studied pharmacognostically. To clarify the botanical origin of To Bog Ryung, the morphological and anatomical characteristics of the rhizomes of Smilax species growing in Korea, i.e. S. china, S. riparia var. ussuriensis, S. nipponica, S. sieboldii were compared. As a result, it was determined that To Bog Ryung was the rhizome of Smilax china and Smilax sieboldii.

LNG운반선의 증발기체 재액화 장치의 사이클 해석

  • Jin, Yeong-Uk
    • Proceedings of the Safety Management and Science Conference
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    • 2012.04a
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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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Performance Simulation of BOG Reliquefaction System for Dual Fuel Engine of LNG Carrier (LNG 선박 Dual Fuel 엔진용 BOG 재액화 시스템의 성능 시뮬레이션)

  • Lee, Sang-Hoon;Shin, You-Hwan;Lee, Yoon-Pyo;Yoo, Ho-Seon
    • Proceedings of the SAREK Conference
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    • 2008.06a
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    • pp.148-153
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    • 2008
  • As the oil price is dramatically jumping up, the consumption of LNG is rapidly expanding and the size of LNG carriers becomes bigger. For LNG ships, the application of DF (Dual-Fuel) engines gradually increases because of high efficiency, which alternatively use diesel or BOG (Boil-Off Gas) from cargo tank as a fuel. The surplus BOG from LNG cargo tank should be exhausted by GCU or liquefied through the BOG reliquefaction system and returned back. This study focused into its operational characteristics through the process simulation using HYSYS and discussed details on the influence of the variations of some operational parameters such as a distribution ratio by the change of fuel mass flow into the DF engine.

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