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dc.contributor.advisorLawler, Desmond F.
dc.contributor.advisorKinney, Kerry A.
dc.creatorGarcia, Hector A., 1975-
dc.date.accessioned2017-02-09T20:39:01Z
dc.date.accessioned2018-01-22T22:31:36Z
dc.date.available2017-02-09T20:39:01Z
dc.date.available2018-01-22T22:31:36Z
dc.date.issued2007-08
dc.identifierdoi:10.15781/T2N58CR23
dc.identifier.urihttp://hdl.handle.net/2152/45624
dc.description.abstractMembrane bioreactors (MBRs) combine the advantages of biological treatment and microfiltration processes. MBRs have been successfully tested for many purposes including municipal and industrial wastewater. Although numerous research efforts involving MBRs have been performed, most have been focused on the removal efficiency of the wastes being treated, rather than developing models that describe the biological and physical processes that occur in MBRs. The main objective of this research was to apply the standard biokinetic model used for conventional activated sludge to a MBR treating malonate, an organic acid contaminant found in industrial wastewater. Consequently, the biokinetic parameters synthesis yield coefficient (Y), endogenous decay coefficient (Kd), half velocity constant (Ks), and maximum specific substrate rate utilization (k) were determined. The experimental results were obtained in an 8.1 L laboratory-scale MBR fed with malonic acid, essential nutrients, and a buffer. The submerged polyethylene flat sheet microfiltration membrane (0.4 μm pore size) was obtained from Enviroquip, Inc, Austin, TX, and air was input continuously directly under the membrane to provide scouring. Monitoring included influent and effluent pH and malonic acid concentration, and the total suspended solid concentration in the reactor. The experimental values were fit to the standard biokinetic model for conventional activated sludge process to obtain values for the biokinetic parameters: Y = 0.297 g active biomass/g malonic acid, kd = 0.331 d⁻¹, Ks = 76.1 mg malonic acid / L, k = 16.8 g malonic acid / g active biomass -- d. The last step of the experimental program was to validate the model at conditions different from those used to calibrate the model parameters. The agreement between the model and experimental results suggests that the model (with its assumptions) is a reasonable description of the phenomena associated with a submerged MBR treating wastewater contaminated with malonic acid.en_US
dc.format.mediumelectronicen_US
dc.language.isoengen_US
dc.relation.ispartofUT Electronic Theses and Dissertationsen_US
dc.rightsCopyright © is held by the author. Presentation of this material on the Libraries' web site by University Libraries, The University of Texas at Austin was made possible under a limited license grant from the author who has retained all copyrights in the works.en_US
dc.subjectMembrane bioreactors (MBRs)en_US
dc.subjectWastewater treatmenten_US
dc.subjectMalonateen_US
dc.titleDegrading malonate waste in a membrane bioreactor : modeling and experimentsen_US
dc.typeThesisen_US
dc.description.departmentEnvironmental and Water Resources Engineeringen_US
dc.type.genreThesisen_US
dc.rights.restrictionRestricteden_US


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