Optimization of the design, operating conditions, and coupling configuration of combined cycle power plants and CO2 capture processes by minimizing the mitigation cost

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dc.contributorComputer Optimization of Chemical Engineering Processes and Technologies (CONCEPT)es_ES
dc.contributor.authorMores, Patricia Liliana-
dc.contributor.authorManassaldi, Juan I.-
dc.contributor.authorScenna, Nicolás José-
dc.contributor.authorCaballero, José A.-
dc.contributor.authorMussati, Miguel Ceferino-
dc.contributor.authorMussati, Sergio Fabián-
dc.contributor.otherUniversidad de Alicante. Departamento de Ingeniería Químicaes_ES
dc.date.accessioned2017-10-06T10:04:21Z-
dc.date.available2017-10-06T10:04:21Z-
dc.date.issued2018-01-01-
dc.identifier.citationChemical Engineering Journal. 2018, 331: 870-894. doi:10.1016/j.cej.2017.08.111es_ES
dc.identifier.issn1385-8947 (Print)-
dc.identifier.issn1873-3212 (Online)-
dc.identifier.urihttp://hdl.handle.net/10045/69957-
dc.description.abstractThis paper deals with the optimization of the coupling between a natural gas combined cycle (NGCC) plant and a post-combustion CO2 capture process by minimizing the mitigation cost – defined as the ratio between the cost of electric power generation and the amount of CO2 emitted per unit of total net electric power generated – while satisfying the design specifications: electric power generation capacity and CO2 capture level. Three candidate coupling configurations, which differ in the place where the steam is extracted from, are optimized using detailed and rigorous models for both the NGCC and the CO2 capture plants. By comparing the mitigation cost of each configuration, the optimal integration configuration and the corresponding optimal sizes and operating conditions of all process units (steam turbines, gas turbines, heat recovery steam generators HRSGs, absorption and regeneration columns, reboilers and condensers, and pumps) are provided. In the computed optimal solution, the steam required by the CO2 capture plant is extracted from both the steam turbine and the HRSG (evaporator operating at low pressure), and the mitigation cost is 90.88 $/t CO2. The optimal solution is compared with suboptimal solutions corresponding to the other two candidate coupling schemes. These solutions are compared in detail regarding capital investment and operating costs, HRSG configuration, process unit sizes, and operating conditions.es_ES
dc.description.sponsorshipThe financial support from the Consejo Nacional de Investigaciones Científicas y Técnicas (CONICET) and the Facultad Regional Rosario of the Universidad Tecnológica Nacional from Argentina are gratefully acknowledged.es_ES
dc.languageenges_ES
dc.publisherElsevieres_ES
dc.rights© 2017 Elsevier B.V.es_ES
dc.subjectNatural gas combined cycle NGCCes_ES
dc.subjectPost-combustion CO2 capturees_ES
dc.subjectMitigation costes_ES
dc.subjectOptimal coupling schemeses_ES
dc.subjectNLP modeles_ES
dc.subjectGAMSes_ES
dc.subject.otherIngeniería Químicaes_ES
dc.titleOptimization of the design, operating conditions, and coupling configuration of combined cycle power plants and CO2 capture processes by minimizing the mitigation costes_ES
dc.typeinfo:eu-repo/semantics/articlees_ES
dc.peerreviewedsies_ES
dc.identifier.doi10.1016/j.cej.2017.08.111-
dc.relation.publisherversionhttp://dx.doi.org/10.1016/j.cej.2017.08.111es_ES
dc.rights.accessRightsinfo:eu-repo/semantics/embargoedAccesses_ES
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