dc.creatorSalazar Esquivel, Randall
dc.creatorCasanova Treto, Pedro
dc.creatorSolís Ramírez, Kattia
dc.date.accessioned2022-11-29T18:49:05Z
dc.date.accessioned2023-03-13T12:51:41Z
dc.date.available2022-11-29T18:49:05Z
dc.date.available2023-03-13T12:51:41Z
dc.date.created2022-11-29T18:49:05Z
dc.date.issued2018
dc.identifierhttps://www.iosrjournals.org/iosr-jce/pages/20(2)Version-2.html
dc.identifier2278-0661
dc.identifierhttps://hdl.handle.net/10669/87818
dc.identifier10.9790/0661-2002021626
dc.identifier.urihttps://repositorioslatinoamericanos.uchile.cl/handle/2250/6119035
dc.description.abstractA numerical modeling was performed that simulates the thermal and fluid-dynamic behavior and generation of chemical species from the biomass gasification process in a downdraft reactor using computational fluid dynamics (CFD). The simulation process was assumed as a stationary state, energy models, turbulence, transport of species and multiphase were established to adequately represent the equations that govern the transfer of mass, momentum and energy in the thermo-chemical degradation process of biomass. Variations in the airflow rate entered into the reactor were established in order to determine the optimum point of operation of the reactor. It was determined that using a flow rate of 400 l/min of air, the best results in terms of the quality of syngas produced are obtained, establishing this condition as the optimum operating point of the reactor.
dc.languageeng
dc.sourceJournal of Computer Engineering (IOSR-JCE), 20(2), p. 16-26
dc.subjectBIOMASS
dc.subjectCFD
dc.subjectdowndraft gasifier
dc.subjectsyngas
dc.subjectENERGY CONSUMPTION
dc.subjectFLUID DYNAMICS
dc.titleAnalysis of a downdraft gasifier for energy use of biomass waste applying computational fluid dynamics
dc.typeartículo científico


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