Please use this identifier to cite or link to this item: https://hdl.handle.net/10216/105943
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dc.creatorA. N. Vilarinho
dc.creatorJ. B. L. M. Campos
dc.creatorC. Pinho
dc.date.accessioned2019-11-01T00:11:58Z-
dc.date.available2019-11-01T00:11:58Z-
dc.date.issued2016
dc.identifier.othersigarra:202586
dc.identifier.urihttps://hdl.handle.net/10216/105943-
dc.description.abstractEnergy and exergy balances were evaluated for the units that constitute the Aromatics plant of a refinery in Portugal (FAR): pre-distillation (Un-0100), Arosolvan (Un-0200), Parex (Un-0300), Isomar (Un-0400) and production of solvents (Un-0500).The FAR had an overall energy yield of 0.81% and an exergetic efficiency of 65.9%. The equipment with higher energy losses, were the condensers, representing 25.9% of the energy losses, followed by air coolers, with 15.4% of the energy losses. The furnaces were in third place with 14.7% of the energy losses. Most of the energy lost in FAR was due to the cooling process. The irreversibilities observed in the condensers and air coolers were equivalent to 1.61% and 0.86% of the total plant irreversibility. Furnaces represent 14.7% of energy losses, but stand out above the irreversibilities analysis with 14.5% of the total. This equipment presents a high potential of energetic and exergetic performance improving, with natural positive impact on energetic and exergetic performance in the FAR.The unaccounted thermal losses represented 32.9% which is mainly justified by the unknown mass flow rate of the gaseous effluent burned in the flare.
dc.language.isoeng
dc.rightsrestrictedAccess
dc.titleEnergy and exergy analysis of an aromatics plant
dc.typeArtigo em Revista Científica Internacional
dc.contributor.uportoFaculdade de Engenharia
dc.identifier.doi10.1016/j.csite.2016.06.003
dc.identifier.authenticusP-00K-JJP
Appears in Collections:FEUP - Artigo em Revista Científica Internacional

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