Please use this identifier to cite or link to this item: https://doi.org/10.3390/en14123478
Title: Study on boil-off gas (Bog) minimization and recovery strategies from actual baseload lng export terminal: Towards sustainable lng chains
Authors: Bouabidi, Zineb
Almomani, Fares
Al-musleh, Easa, I
Katebah, Mary A.
Hussein, Mohamed M.
Shazed, Abdur Rahman
Karimi, Iftekhar A. 
Alfadala, Hassan
Keywords: BOG recovery
Boil-off-gas
C3MR process
Exporting terminal
Flare minimization
Fuel balance
Liquefied natural gas
Steady-state simulation
Issue Date: 11-Jun-2021
Publisher: MDPI AG
Citation: Bouabidi, Zineb, Almomani, Fares, Al-musleh, Easa, I, Katebah, Mary A., Hussein, Mohamed M., Shazed, Abdur Rahman, Karimi, Iftekhar A., Alfadala, Hassan (2021-06-11). Study on boil-off gas (Bog) minimization and recovery strategies from actual baseload lng export terminal: Towards sustainable lng chains. Energies 14 (12) : 3478. ScholarBank@NUS Repository. https://doi.org/10.3390/en14123478
Rights: Attribution 4.0 International
Abstract: Boil-off Gas (BOG) generated at the liquefied natural gas (LNG) export terminal causes negative economic and environmental impacts. Thus, the objective of this study is to develop and evaluate various handling schemes to minimize and/or recover the generated BOG from an actual baseload LNG export terminal with a capacity of 554 million standard cubic feet per day (MMSCFD) of natural gas feed. The following three main scenarios were assessed: JBOG re-liquefaction, LNG sub-cooling, and lean fuel gas (LFG) reflux. For the LNG subcooling, two sub-cases were considered; standalone subcooling before LNG storage and subcooling in the prevailing liquefaction cycle. Steadystate models for these scenarios were simulated using Aspen Plus® based on a shortcut approach to quickly evaluate the proposed scenarios and determine the promising options that should be considered for further rigorous analysis. Results indicated that the flow of attainable excess LNG is 0.07, 0.03, and 0.022 million metric tons per annum (MTA) for the standalone LNG sub-cooling, LNG sub-cooling in the main cryogenic heat exchanger (MCHE), and both LFG-refluxing and jetty boil-off gas (JBOG) liquefaction, respectively. This in turn results in a profit of 24.58, 12.24, 8.14, and 7.63 million $/year for the LNG price of 7$ per Metric Million British Thermal Unit (MMBtu) of LNG. © 2021 by the authors. Licensee MDPI, Basel, Switzerland.
Source Title: Energies
URI: https://scholarbank.nus.edu.sg/handle/10635/233174
ISSN: 1996-1073
DOI: 10.3390/en14123478
Rights: Attribution 4.0 International
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