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dc.contributor.advisorGarcia, Albert
dc.creatorYantarasri, Thongchai
dc.date.accessioned2020-08-21T22:10:14Z
dc.date.available2020-08-21T22:10:14Z
dc.date.issued1989
dc.identifier.urihttps://hdl.handle.net/1969.1/DISSERTATIONS-1117173
dc.descriptionTypescript (photocopy).en
dc.description.abstractA rap id rate nitrification filter, called a retained biomass disk (RBD). has been used to examine the response of Nitrosomonas spp. to different levels of nitrite (14- 196 mg-N/L) an d the response of Nitrobacter spp. to different levels of of nitrate (11- 250 mg-N/L). Fresh water at 28.4°C and pH 8.5 was used for the experimental trials. The substrate oxidation rates of both bacteria were measured for various combinations of substrate and end -product concentrations. For both bacteria spp. the responses of the filter to substrate and end-product concentrations were found to be best explained by a mixed Monod inhibition model. The maximum specific oxidation rate of Nitrosomonas was determined to be about double that of Nitrobacter. This large difference in growth response reveals the fact that in a nitrification filter the nitrite generation rate by Nitrosomonas can be twice the nitrite consumption rate by Nitrobacter when ammonia loading suddenly Increases. Thus, a nitrite pulse in reactor effluent is inevitable. By knowing the kinetic parameters for Nitrosomonas. Nitrobacter and anticipated ammonia loading schedules, management strategy can be devised to avoid nitrite peaks. Further, the oxidation rates of both bacteria were found to be linearly related to free-energy changes (AG) for the respective oxidation reactions with correlation coefficients of 0.841 and 0.934. It is shown that the inhibition model that accounts for both substrate and product concentrations can be replaced by a simpler model based on the availability of free-energy. At the same ratio of ammonia /nitrite and nitrite /nitrate over the range of 0.001 to 0.1. ammonia conversion rate was about double the nitrite conversion rate. Management strategies can be devised to maximize the nitrite removal rate. Further, by knowing the thermodynamic models' parameters and cell population, the filter's performance can be maximized during peak periods while minimizing high nitrite pulsesen
dc.format.extentxiv, 154 leavesen
dc.format.mediumelectronicen
dc.format.mimetypeapplication/pdf
dc.language.isoeng
dc.rightsThis thesis was part of a retrospective digitization project authorized by the Texas A&M University Libraries. Copyright remains vested with the author(s). It is the user's responsibility to secure permission from the copyright holder(s) for re-use of the work beyond the provision of Fair Use.en
dc.rights.urihttp://rightsstatements.org/vocab/InC/1.0/
dc.subjectAgricultural Engineeringen
dc.subject.classification1989 Dissertation Y24
dc.subject.lcshNitrificationen
dc.subject.lcshModelsen
dc.subject.lcshResearchen
dc.subject.lcshNitrification inhibitorsen
dc.subject.lcshNitrifying bacteriaen
dc.subject.lcshLinear free energy relationshipen
dc.titleThe effect of available free-energy on nitrification kineticsen
dc.typeThesisen
thesis.degree.grantorTexas A&M Universityen
thesis.degree.nameDoctor of Philosophyen
thesis.degree.namePh. Den
dc.type.genredissertationsen
dc.type.materialtexten
dc.format.digitalOriginreformatted digitalen
dc.publisher.digitalTexas A&M University. Libraries
dc.identifier.oclc22996827


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