dc.contributor.author | Valencia Ochoa, Guillermo | |
dc.contributor.other | Acevedo Peñaloza, Carlos | |
dc.contributor.other | Piero Rojas, Jhan | |
dc.date.accessioned | 2023-01-17T16:16:47Z | |
dc.date.available | 2023-01-17T16:16:47Z | |
dc.date.issued | 2019-10-25 | |
dc.date.submitted | 2019-09-05 | |
dc.identifier.uri | https://hdl.handle.net/20.500.12834/1163 | |
dc.description.abstract | This paper presents a thermo-economic analysis of a simple organic Rankine cycle (SORC)
as a waste heat recovery (WHR) systems of a 2 MW stationary gas engine evaluating different
working fluids. Initially, a systematic methodology was implemented to select three organic fluids
according to environmental and safety criteria, as well as critical system operational conditions.
Then, thermodynamic, exergy, and exergo-economic models of the system were developed under
certain defined considerations, and a set of parametric studies are presented considering key variables
of the system such as pump efficiency, turbine efficiency, pinch point condenser, and evaporator.
The results show the influence of these variables on the combined power of the system (gas engine
plus ORC), ORC exergetic efficiency, specific fuel consumption (∆BSFC), and exergo indicators such
as the payback period (PBP), levelized cost of energy (LCOE), and the specific investment cost (SIC).
The results revealed that heat transfer equipment had the highest exergy destruction cost rates
representing 81.25% of the total system cost. On the other hand, sensitivity analyses showed that
acetone presented better energetic and exergetic performance when the efficiency of the turbine,
evaporator, and condenser pinch point was increased. However, toluene was the fluid with the best
results when pump efficiency was increased. In terms of the cost of exergy destroyed by equipment,
the results revealed that acetone was the working fluid that positively impacted cost reduction when
pump efficiency was improved; and toluene, when turbine efficiency was increased. Finally, the
evaporator and condenser pinch point increased all the economic indicators of the system. In this
sense, the working fluid with the best performance in economic terms was acetone, when the efficiency
of the turbine, pinch condenser, and pinch evaporator was enhanced. | spa |
dc.format.mimetype | application/pdf | spa |
dc.language.iso | eng | spa |
dc.rights.uri | http://creativecommons.org/licenses/by-nc/4.0/ | * |
dc.title | Thermoeconomic modelling and parametric study of a simple orc for the recovery ofwaste heat in a 2 MW gas engine under differentworking fluids | spa |
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datacite.rights | http://purl.org/coar/access_right/c_abf2 | spa |
oaire.resourcetype | http://purl.org/coar/resource_type/c_6501 | spa |
oaire.version | http://purl.org/coar/version/c_970fb48d4fbd8a85 | spa |
dc.audience | Público general | spa |
dc.identifier.doi | 10.3390/app9214526 | |
dc.identifier.instname | Universidad del Atlántico | spa |
dc.identifier.reponame | Repositorio Universidad del Atlántico | spa |
dc.rights.cc | Attribution-NonCommercial 4.0 International | * |
dc.subject.keywords | energy analysis | spa |
dc.subject.keywords | exergy analysis | spa |
dc.subject.keywords | organic Rankine cycle | spa |
dc.subject.keywords | waste heat recovery | spa |
dc.subject.keywords | natural gas engine | spa |
dc.type.driver | info:eu-repo/semantics/article | spa |
dc.type.hasVersion | info:eu-repo/semantics/publishedVersion | spa |
dc.type.spa | Artículo | spa |
dc.publisher.place | Barranquilla | spa |
dc.rights.accessRights | info:eu-repo/semantics/openAccess | spa |
dc.publisher.discipline | Ingeniería Mecánica | spa |
dc.publisher.sede | Sede Norte | spa |