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dc.contributor.authorAida Izwana, Md Bakhri-
dc.date.accessioned2021-03-08T03:20:30Z-
dc.date.available2021-03-08T03:20:30Z-
dc.date.issued2016-
dc.identifier.urihttp://dspace.unimap.edu.my:80/xmlui/handle/123456789/70300-
dc.descriptionAccess is limited to UniMAP community.en_US
dc.description.abstractThe PRICO process is a single mixed-refrigerant process used for small-scale LNG plants, including offshore terminals. The working fluid (refrigerant) is a mixture of methane, ethane, butane and nitrogen. The behavior of the mixture in processes such as cooling, heating, compression, evaporation and condensation depends on its composition and on the part of the chemical constituents of the mixture that are in the gas and liquid phases. The state-of-the art for the evaluation and optimization of the PRICO process is discussed. The perspectives from the thermodynamic and economic points of view are discussed. Based on the estimated fixed-capital investment and the assumptions for the economic, financial, operating, and market input variables, the total revenue requirement (TRR) is calculated. The non-uniform annual monetary values associated with the investment (carrying charges, CC), operation & maintenance (OMC), and fuel costs (FC) of the system being analyzed are levelized, that is they are converted into an equivalent series of constant payments (annuities). This report technically presents the calculation and results of TRR.en_US
dc.language.isoenen_US
dc.publisherUniversiti Malaysia Perlis (UniMAP)en_US
dc.subjectPRICO processen_US
dc.subjectNatural gasen_US
dc.subjectLiquefaction processen_US
dc.subjectLiquefactionen_US
dc.titleEconomic analysis on PRICO process for liquefaction of natural gasen_US
dc.typeLearning Objecten_US
dc.contributor.advisorMohd Nazri, Omar-
Appears in Collections:School of Manufacturing Engineering (FYP)

Files in This Item:
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Abstract,Acknowledgement.pdf317.62 kBAdobe PDFView/Open
Introduction.pdf442.97 kBAdobe PDFView/Open
Literature review.pdf369.48 kBAdobe PDFView/Open
Methodology.pdf417.68 kBAdobe PDFView/Open
Results and discussion.pdf688.88 kBAdobe PDFView/Open
Conclusion.pdf224.95 kBAdobe PDFView/Open
Reference and appendix.pdf307.25 kBAdobe PDFView/Open


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