Novel Simulation of Anaerobic Digestion Using Computational Fluid Dynamics

dc.contributor.advisorJames W. Leach, Committee Memberen_US
dc.contributor.advisorJiayang Cheng, Committee Memberen_US
dc.contributor.advisorHerbert M. Eckerlin, Committee Memberen_US
dc.contributor.advisorKevin M. Lyons, Committee Memberen_US
dc.contributor.advisorRichard R. Johnson, Committee Chairen_US
dc.contributor.authorFleming, Jason Grahamen_US
dc.date.accessioned2010-04-02T18:45:59Z
dc.date.available2010-04-02T18:45:59Z
dc.date.issued2002-11-13en_US
dc.degree.disciplineMechanical Engineeringen_US
dc.degree.leveldissertationen_US
dc.degree.namePhDen_US
dc.description.abstractIn an effort to optimize the economy and performance of covered anaerobic reactor systems, a comprehensive dynamic and mechanistic model was created to simulate the constituent processes of full-scale anaerobic digestion. These processes included the following: bulk fluid motion, sedimentation, bubble mixing, bubble entrainment, buoyant mixing, advection, biological reactions, internal heat transfer, and heat exchange with the environment. This model contrasted with conventional models that assumed uniform concentrations and temperature throughout the reacting medium. Novel numerical simulation techniques were developed to simulate the heat and mass transfer resulting from two phase gas-liquid flow and unsteady buoyancy driven flow. The complete model was implemented in a computer code called LagoonSim3D. Three years of performance data from a full-scale covered anaerobic digestion system in central North Carolina were used to quantify unknown parameters as well as validate the LagoonSim3D software. The LagoonSim3D software predicted the temperature of the covered lagoon within 5.7% and the dynamic monthly gas production within 11%. The external convective heat transfer coefficient was found to be a linear function of wind speed. The convective heat transfer coefficient of the gas gap between the cover and the slurry was found to be 10 W/m²K. The average particle settling velocity was found to be 0.02 cm/s. These previously unknown parameters were important for the design of future anaerobic digestion systems. The validated LagoonSim3D model was used to determine the effect of design changes on reactor performance. In part, it was found that the case study system had at least twice the optimal volume, and a nearly optimal depth. It was also found that the performance of the case study system could be improved by cutting the flush water volume in half. It was concluded that the LagoonSim3D software enabled a flexible and general evaluation of covered anaerobic lagoon designs that was not possible with previously available steady state and complete-mix models.en_US
dc.identifier.otheretd-10152002-220904en_US
dc.identifier.urihttp://www.lib.ncsu.edu/resolver/1840.16/4158
dc.rightsI hereby certify that, if appropriate, I have obtained and attached hereto a written permission statement from the owner(s) of each third party copyrighted matter to be included in my thesis, dissertation, or project report, allowing distribution as specified below. I certify that the version I submitted is the same as that approved by my advisory committee. I hereby grant to NC State University or its agents the non-exclusive license to archive and make accessible, under the conditions specified below, my thesis, dissertation, or project report in whole or in part in all forms of media, now or hereafter known. I retain all other ownership rights to the copyright of the thesis, dissertation or project report. I also retain the right to use in future works (such as articles or books) all or part of this thesis, dissertation, or project report.en_US
dc.subjectreactor engineeringen_US
dc.subjecttemperature effectsen_US
dc.subjectspatial effectsen_US
dc.subjectanaerobic digestionen_US
dc.subjectgreen poweren_US
dc.subjectbiomass energyen_US
dc.subjectcomputational fluid dynamicsen_US
dc.titleNovel Simulation of Anaerobic Digestion Using Computational Fluid Dynamicsen_US

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