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dc.contributor.authorMartinez-Castilla, Guillermo
dc.contributor.authorMocholí Montañés, Rubén
dc.contributor.authorPallarès, David
dc.contributor.authorJohnsson, Filip
dc.date.accessioned2023-05-08T12:09:33Z
dc.date.available2023-05-08T12:09:33Z
dc.date.created2022-11-06T18:29:52Z
dc.date.issued2022
dc.identifier.citationApplied Thermal Engineering. 2022, 219 B 119591-?.en_US
dc.identifier.issn1359-4311
dc.identifier.urihttps://hdl.handle.net/11250/3067075
dc.description.abstractAs the share of variable renewable electricity increases, thermal power plants will have to adapt their operational protocols in order to remain economically competitive while also providing grid-balancing services required to deal with the inherent fluctuations of variable renewable electricity. This work presents a dynamic model of fluidized bed combustion plants for combined heat and power production. The novelty of the work lays in that (i) it provides an analysis of the transient performance of biomass-based fluidized bed combustion plants for combined heat and power production, (ii) the dynamic model includes a description of both the gas and water-steam sides and (iii) the model is validated against operational data acquired from a commercial-scale plant. The validated model is here applied to analyze the inherent dynamics of the investigated plant and to evaluate the performance of the plant when operated under different control and operational strategies, using a relative gain analysis and a variable ramping rate test. The results of the simulations reveal that the inherent dynamics of the process have stabilization times in the range of 5–25 min for all the step changes investigated, with variables connected to district heating production being the slowest. In contrast, variables connected to the live steam are the fastest, with stabilization times of magnitude similar to those of the in-furnace variables (i.e., around 10 min). Thus, it is concluded that the proper description of the dynamics in fluidized bed combustion plants for combined heat and power production requires modeling of both the gas and water sides (which is rare in previous literature). Regarding the assessment of control strategies, the boiler-following and hybrid control (combined fixed live steam and sliding pressure) strategies are found to be able to provide load changes as fast as −5%-unit/s, albeit while causing operational issues such as large pressure overshoots. The relative gain analysis outcomes show that these control structures do not have a steady-state gain on the power produced, and therefore it is the dynamic effect of the steam throttling that triggers the rapid power response. This study also includes the assessment of a turbine bypass strategy, the results of which show that it enables fast load-changing capabilities at constant combustion load, as well as decoupling power and heat production at the expense of thermodynamic losses.en_US
dc.language.isoengen_US
dc.publisherElsevieren_US
dc.rightsNavngivelse 4.0 Internasjonal*
dc.rights.urihttp://creativecommons.org/licenses/by/4.0/deed.no*
dc.titleDynamics and control of large-scale fluidized bed plants for renewable heat and power generationen_US
dc.title.alternativeDynamics and control of large-scale fluidized bed plants for renewable heat and power generationen_US
dc.typePeer revieweden_US
dc.typeJournal articleen_US
dc.description.versionpublishedVersionen_US
dc.rights.holderThe Authorsen_US
dc.source.volume219 Ben_US
dc.source.journalApplied Thermal Engineeringen_US
dc.identifier.doi10.1016/j.applthermaleng.2022.119591
dc.identifier.cristin2069627
dc.source.articlenumber119591en_US
cristin.ispublishedtrue
cristin.fulltextoriginal
cristin.qualitycode1


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