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Plant Wide Exergy Analysis of Petroleum Refinery

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dc.contributor.author Adil, Sana
dc.date.accessioned 2023-07-20T04:54:38Z
dc.date.available 2023-07-20T04:54:38Z
dc.date.issued 2022
dc.identifier.other 00000318535
dc.identifier.uri http://10.250.8.41:8080/xmlui/handle/123456789/34862
dc.description.abstract In this work, plantwide exergy analysis of a petroleum refinery was conducted. An Aspen HYSYS® model of a petroleum refinery was used for collection of information to perform the exergy analysis. The plant wide model consisted of alkylation unit, reformer, naphtha hydrotreater, catalytic cracker, diesel hydrotreater, isomerization unit, hydrocracker, and kerosene hydrotreater. Seventeen (17) independent input streams and twenty-eight (28) output streams of the plant were considered for the analysis. The physical and chemical exergies of the streams were summed for assessing the overall exergy efficiency, exergy destruction, and improvement potentials of the plant. Exergy efficiency of the plant was 91.38% with exergy destruction of 704054.64 kW and exergetic improvement potential of 60707.50 kW. The current study gives an insight into the plant-wide transformation from physical exergies of the process streams and utilities into the chemical exergies of the fuels (product) produced in the refineries. en_US
dc.description.sponsorship Supervisor Name: Dr. Iftikhar Ahmad en_US
dc.publisher School of Chemical and Material Engineering (SCME), NUST en_US
dc.subject Exergy analysis, Aspen HYSYS, Petroleum Refinery, Exergy Dstruction, Process Irreversibility, Exergy efficiency. en_US
dc.title Plant Wide Exergy Analysis of Petroleum Refinery en_US
dc.type Thesis en_US


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