Identificador persistente para citar o vincular este elemento: http://hdl.handle.net/10553/75303
Campo DC Valoridioma
dc.contributor.authorTinoco Caicedo, Diana Lucíaen_US
dc.contributor.authorLozano-Medina, Alexisen_US
dc.contributor.authorBlanco-Marigorta, Ana M.en_US
dc.date.accessioned2020-11-10T08:36:27Z-
dc.date.available2020-11-10T08:36:27Z-
dc.date.issued2020en_US
dc.identifier.issn1996-1073en_US
dc.identifier.otherScopus-
dc.identifier.urihttp://hdl.handle.net/10553/75303-
dc.description.abstractInstant coffee is produced worldwide by spray drying coffee extract on an industrial scale. This production process is energy intensive, 70% of the operational costs are due to energy requirements. This study aims to identify the potential for energy and cost improvements by performing a conventional and advanced exergy and exergoeconomic analysis to an industrial-scale spray drying process for the production of instant coffee, using actual operational data. The study analyzed the steam generation unit, the air and coffee extract preheater, the drying section, and the final post treatment process. The performance parameters such as exergetic efficiency, exergoeconomic factor, and avoidable investment cost rate for each individual component were determined. The overall energy and exergy efficiencies of the spray drying system are 67.6% and 30.6%, respectively. The highest rate of exergy destruction is located in the boiler, which amounts to 543 kW. However, the advanced exergoeconomic analysis shows that the highest exergy destruction cost rates are located in the spray dryer and the air heat exchanger (106.9 $/h and 60.5 $/h, respectively), of which 47.7% and 3.8%, respectively, are avoidable. Accordingly, any process improvement should focus on the exergoeconomic optimization of the spray dryer.en_US
dc.languageengen_US
dc.relation.ispartofEnergies (Basel)en_US
dc.sourceEnergies (Basel) [EISSN 1996-1073], v. 13 (21), 5622, (Octubre 2020)en_US
dc.subject331005 Ingeniería de procesosen_US
dc.subject.otherAdvanced Exergoeconomic Analysisen_US
dc.subject.otherExergy Destruction Cost Rateen_US
dc.subject.otherSpray Dryeren_US
dc.titleConventional and advanced exergy and exergoeconomic analysis of a spray drying system: a case study of an instant coffee factory in ecuadoren_US
dc.typeinfo:eu-repo/semantics/Articleen_US
dc.typeArticleen_US
dc.identifier.doi10.3390/en13215622en_US
dc.identifier.scopus85094834055-
dc.contributor.authorscopusid57219702004-
dc.contributor.authorscopusid56688593700-
dc.contributor.authorscopusid25652860100-
dc.identifier.eissn1996-1073-
dc.identifier.issue21-
dc.relation.volume13en_US
dc.investigacionIngeniería y Arquitecturaen_US
dc.type2Artículoen_US
dc.description.notasThis article belongs to the Special Issue Enhancement of Industrial Energy Efficiency and Sustainabilityen_US
dc.utils.revisionen_US
dc.date.coverdateOctubre 2020en_US
dc.identifier.ulpgcen_US
dc.contributor.buulpgcBU-INGen_US
dc.description.sjr0,598
dc.description.jcr3,004
dc.description.sjrqQ2
dc.description.jcrqQ3
dc.description.scieSCIE
item.grantfulltextopen-
item.fulltextCon texto completo-
crisitem.author.deptGIR Group for the Research on Renewable Energy Systems-
crisitem.author.deptDepartamento de Ingeniería Civil-
crisitem.author.deptGIR Group for the Research on Renewable Energy Systems-
crisitem.author.deptDepartamento de Ingeniería de Procesos-
crisitem.author.orcid0000-0001-8583-9398-
crisitem.author.orcid0000-0001-8478-3011-
crisitem.author.orcid0000-0003-4635-7235-
crisitem.author.parentorgDepartamento de Ingeniería Mecánica-
crisitem.author.parentorgDepartamento de Ingeniería Mecánica-
crisitem.author.fullNameTinoco Caicedo, Diana Lucía-
crisitem.author.fullNameLozano Medina, Alexis-
crisitem.author.fullNameBlanco Marigorta, Ana María-
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