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dc.contributor.advisorAnnamalai, Kalyan
dc.creatorSpear, Aubrey Alvin
dc.date.accessioned2019-02-25T22:05:31Z
dc.date.available2019-02-25T22:05:31Z
dc.date.created2015-08
dc.date.issued2015-08-05
dc.date.submittedAugust 2015
dc.identifier.urihttps://hdl.handle.net/1969.1/174811
dc.description.abstractGovernment regulations on emission standards and constantly fluctuating fuel availability and prices have led to the need of more readily usable and available models for power generating combustors. A common, versatile, power generating combustor is the circulating fluidized bed (CFB) boiler. Waste tire is viewed as a potential fuel in a CFB boiler. Extensive literature review is used to create a model of a CFB boiler. The model is programmed using Microsoft Excel software. The program consists of four major tabs being the ‘Input’, ‘Bed’, ‘Riser’, and ‘Output’ tabs. The ‘Input’ tab consists of appropriate and minimal input parameters to allow for enough variability while not over burdening the user with acquiring large amounts of data. The ‘Bed’ tab describes the instantaneous chemical reactions assumed to take place in the dense bed region of the combustor. The ‘Riser’ tab tracks the time dependent chemical kinetics through a predetermined number of time steps divided evenly throughout the lean riser region of the combustor. The ‘Output’ tab calculates the concentration at the exit of the combustor riser for ten different species important to both combustion and government regulations being CO, H2O, O2, N2, NH3, HCN, SO2, CO2, H2, and NO. With 5,000 chemical kinetics calculation rows, the computation time for varying an input is approximately ten seconds. The model has been validated against an anonymous industrial CFB boiler firing lignite coal fuel resulting in emission concentrations being 22% different or less between the model predictions and the actual emissions when kinetics are slightly modified. The model was also validated against a Babcock and Wilcox pilot/laboratory scale bubbling fluidized bed (BFB) boiler firing subbituminous coal fuel resulting in emission concentrations being 10% different at most between the model predictions and the actual emissions without kinetics modification except for the O2 concentration being off by about 74% due to differences with CFB. The anonymous CFB boiler had fuel switched to waste tire fuel, and 24 inputs were varied as part of a parametric analysis of the fuel to discover emission trends.en
dc.format.mimetypeapplication/pdf
dc.language.isoen
dc.subjectCirculatingen
dc.subjectFluidizeden
dc.subjectBeden
dc.subjectBoileren
dc.subjectModelen
dc.subjectEmissionen
dc.subjectFuelen
dc.subjectTireen
dc.subjectLigniteen
dc.subjectCoalen
dc.subjectCombustionen
dc.subjectPoweren
dc.subjectGenerateen
dc.subjectCombustoren
dc.subjectWasteen
dc.subjectRiseren
dc.subjectChemicalen
dc.subjectKineticsen
dc.subjectReactionen
dc.subjectConcentrationen
dc.subjectParametricen
dc.subjectAnalysisen
dc.subjectComputeren
dc.subjectExcelen
dc.subjectPyrolysisen
dc.subjectDevolatilizationen
dc.subjectTwo-phaseen
dc.subjectLimestoneen
dc.subjectCalcinationen
dc.subjectSulfationen
dc.subjectVolatileen
dc.subjectAshen
dc.subjectResidenceen
dc.subjectBurnen
dc.subjectParticleen
dc.subjectTerminalen
dc.subjectVelocityen
dc.subjectDiffusionen
dc.subjectNitrogenen
dc.subjectCarbonen
dc.subjectHydrogenen
dc.subjectOxygenen
dc.subjectSulfuren
dc.subjectRecirculationen
dc.subjectValidationen
dc.titleCirculating Fluidized Bed Boiler Model for Predicting Emission Levels of Tire Fuel using Base Case of Lignite Fuelen
dc.typeThesisen
thesis.degree.departmentMechanical Engineeringen
thesis.degree.disciplineMechanical Engineeringen
thesis.degree.grantorTexas A & M Universityen
thesis.degree.nameMaster of Scienceen
thesis.degree.levelMastersen
dc.contributor.committeeMemberPetersen, Eric L
dc.contributor.committeeMemberHassan, Yassin A
dc.type.materialtexten
dc.date.updated2019-02-25T22:05:31Z
local.etdauthor.orcid0000-0002-8468-3763


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