DC Field | Value | Language |
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dc.contributor.author | Nam, K | - |
dc.contributor.author | Chang, D | - |
dc.contributor.author | Chang, K | - |
dc.contributor.author | Rhee, T | - |
dc.contributor.author | Lee, IB | - |
dc.date.accessioned | 2016-03-31T09:40:29Z | - |
dc.date.available | 2016-03-31T09:40:29Z | - |
dc.date.created | 2011-05-16 | - |
dc.date.issued | 2011-03 | - |
dc.identifier.issn | 0360-5442 | - |
dc.identifier.other | 2011-OAK-0000023539 | - |
dc.identifier.uri | https://oasis.postech.ac.kr/handle/2014.oak/17465 | - |
dc.description.abstract | This study proposed a new LCC (life cycle cost) methodology with the risk expenditure taken into account for comparative evaluation of offshore process options at their conceptual design stage. The risk expenditure consisted of the failure risk expenditure and the accident risk expenditure. The former accounted for the production loss and the maintenance expense due to equipment failures while the latter reflected the asset damage and the fatality worth caused by disastrous accidents such as fire and explosion. It was demonstrated that the new LCC methodology was capable of playing the role of a process selection basis in choosing the best of the liquefaction process options including the power generation systems for a floating LNG (Liquefied natural gas) production facility. Without the risk expenditure, a simple economic comparison apparently favored the mixed refrigerant cycle which had the better efficiency. The new methodology with the risk expenditure, however, indicated that the nitrogen expansion cycle driven by steam turbines should be the optimum choice, mainly due to its better availability and safety. (C) 2011 Elsevier Ltd. All rights reserved. | - |
dc.description.statementofresponsibility | X | - |
dc.language | English | - |
dc.publisher | PERGAMON-ELSEVIER SCIENCE LTD | - |
dc.relation.isPartOf | ENERGY | - |
dc.subject | Life cycle cost | - |
dc.subject | Risk expenditure | - |
dc.subject | Production availability | - |
dc.subject | Risk assessment | - |
dc.subject | LNG FPS | - |
dc.subject | SAFETY | - |
dc.title | Methodology of life cycle cost with risk expenditure for offshore process at conceptual design stage | - |
dc.type | Article | - |
dc.contributor.college | 화학공학과 | - |
dc.identifier.doi | 10.1016/J.ENERGY.2011.01.005 | - |
dc.author.google | Nam, K | - |
dc.author.google | Chang, D | - |
dc.author.google | Chang, K | - |
dc.author.google | Rhee, T | - |
dc.author.google | Lee, IB | - |
dc.relation.volume | 36 | - |
dc.relation.issue | 3 | - |
dc.relation.startpage | 1554 | - |
dc.relation.lastpage | 1563 | - |
dc.contributor.id | 10104673 | - |
dc.relation.journal | ENERGY | - |
dc.relation.index | SCI급, SCOPUS 등재논문 | - |
dc.relation.sci | SCI | - |
dc.collections.name | Journal Papers | - |
dc.type.rims | ART | - |
dc.identifier.bibliographicCitation | ENERGY, v.36, no.3, pp.1554 - 1563 | - |
dc.identifier.wosid | 000289337600020 | - |
dc.date.tcdate | 2019-01-01 | - |
dc.citation.endPage | 1563 | - |
dc.citation.number | 3 | - |
dc.citation.startPage | 1554 | - |
dc.citation.title | ENERGY | - |
dc.citation.volume | 36 | - |
dc.contributor.affiliatedAuthor | Lee, IB | - |
dc.identifier.scopusid | 2-s2.0-79952139726 | - |
dc.description.journalClass | 1 | - |
dc.description.journalClass | 1 | - |
dc.description.wostc | 9 | - |
dc.description.scptc | 13 | * |
dc.date.scptcdate | 2018-05-121 | * |
dc.type.docType | Article | - |
dc.subject.keywordAuthor | Life cycle cost | - |
dc.subject.keywordAuthor | Risk expenditure | - |
dc.subject.keywordAuthor | Production availability | - |
dc.subject.keywordAuthor | Risk assessment | - |
dc.subject.keywordAuthor | LNG FPS | - |
dc.relation.journalWebOfScienceCategory | Thermodynamics | - |
dc.relation.journalWebOfScienceCategory | Energy & Fuels | - |
dc.description.journalRegisteredClass | scie | - |
dc.description.journalRegisteredClass | scopus | - |
dc.relation.journalResearchArea | Thermodynamics | - |
dc.relation.journalResearchArea | Energy & Fuels | - |
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