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dc.contributor.advisorAhmed F. Ghoniem.en_US
dc.contributor.authorHunt, Anton (Anton Stuart)en_US
dc.contributor.otherMassachusetts Institute of Technology. Department of Mechanical Engineering.en_US
dc.date.accessioned2015-12-03T18:46:27Z
dc.date.available2015-12-03T18:46:27Z
dc.date.copyright2015en_US
dc.date.issued2015en_US
dc.identifier.urihttp://hdl.handle.net/1721.1/100059
dc.descriptionThesis: Ph. D., Massachusetts Institute of Technology, Department of Mechanical Engineering, 2015.en_US
dc.descriptionThis electronic version was submitted by the student author. The certified thesis is available in the Institute Archives and Special Collections.en_US
dc.descriptionCataloged from student-submitted PDF version of thesis.en_US
dc.descriptionIncludes bibliographical references.en_US
dc.description.abstractIon transport membranes (ITMs) are dense ceramic membranes which have the potential for 100% selective separation of oxygen from air. ITMs operate at extreme temperatures (>800°C), necessary for the mobility of lattice oxygen ions: this can result in significant experimental challenges. Specifically, the local gas compositions at both the high oxygen (air) and low oxygen (sweep) surfaces influence the oxygen flux: these experimental measurements have not been available until now. A novel ITM research reactor has thus been developed which can directly sample gases at the membrane surface at high temperature flux conditions. This ITM reactor has been scaled up to allow for gas-probing instruments to be used without overly disrupting the experimental flowfield. The ITM stoichiometry investigated in this study is La₀.₉9Ca₀.₁1FeO3-[delta] (LCF), and has been chosen for its chemical stability attributes and consequent applicability to industry. Two modes of operation have been investigated using the LCF ITM in the reactor: inert (using CO₂ sweep gas to carry away an oxygen-enriched stream) and reactive (using CO₂:CH₄ sweep gas resulting in fuel reactions with the permeating oxygen). There is a huge advantage to running ITMs reactive: the oxygen flux can be enhanced by an order of magnitude or more, whilst useful fuel synthesis reactions can be actively enhanced by the catalytic ITM surface. This study therefore utilizes the local measurement capabilities of the novel ITM reactor to develop a physical understanding through oxygen flux models for both modes of operation: inert and reactive. Both flux models enable the prediction of the oxygen lux with the operating conditions necessary as input parameters. They are therefore useful tools for future optimization of ITM reactor designs. Further insight using the flux models is also provided. The inert flux model is used to determine the surface oxygen vacancy concentration which drives the oxygen flux. The reactive flux model is used in preliminary numerical simulations of ITM reactors to produce flux performance maps based on the input operating conditions.en_US
dc.description.statementofresponsibilityby Anton Hunt.en_US
dc.format.extent237 pagesen_US
dc.language.isoengen_US
dc.publisherMassachusetts Institute of Technologyen_US
dc.rightsM.I.T. theses are protected by copyright. They may be viewed from this source for any purpose, but reproduction or distribution in any format is prohibited without written permission. See provided URL for inquiries about permission.en_US
dc.rights.urihttp://dspace.mit.edu/handle/1721.1/7582en_US
dc.subjectMechanical Engineering.en_US
dc.titleExperimental investigations of oxygen-separating ion transport membranes for clean fuel synthesisen_US
dc.typeThesisen_US
dc.description.degreePh. D.en_US
dc.contributor.departmentMassachusetts Institute of Technology. Department of Mechanical Engineering
dc.identifier.oclc929653178en_US


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