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dc.contributor.advisorFikile R. Brushett.en_US
dc.contributor.authorBarton, John Leonard.en_US
dc.contributor.otherMassachusetts Institute of Technology. Department of Chemical Engineering.en_US
dc.date.accessioned2019-07-22T19:37:22Z
dc.date.available2019-07-22T19:37:22Z
dc.date.copyright2019en_US
dc.date.issued2019en_US
dc.identifier.urihttps://hdl.handle.net/1721.1/121901
dc.descriptionThesis: Ph. D., Massachusetts Institute of Technology, Department of Chemical Engineering, 2019en_US
dc.descriptionCataloged from PDF version of thesis.en_US
dc.descriptionIncludes bibliographical references (pages 113-134).en_US
dc.description.abstractThe focus of this thesis is the development and assessment of techniques for the analysis of electrochemical and transport processes in redox flow batteries (RFBs) at moderate to high active species concentrations under direct current conditions. RFBs hold promise as an energy-intensive storage technology suitable for supporting the integration of intermittent renewable energy sources into the grid, but further improvements in technical performance and reductions in system cost are needed for broad deployment. At their core, all thesis projects are aimed at enabling the development of system descriptors that correlate material properties (e.g., viscosity, conductivity), cell geometry (e.g., flow field design), and operating parameters (e.g., flow rate, current density) to system performance metrics, such as cycle efficiencies and area-specific resistance.en_US
dc.description.abstractMore specifically, the investigation is divided into three primary projects: the development and assessment of a research-scale flow cell; measurements of mass-transfer coefficients; and integration of a polarization model into a standalone application useful for assessing system performance. The differential flow cell is engineered leveraging validation material from industrial collaborators. Not only is the performance is consistent with that of a ten-fold larger cell, but its smaller modular design enables rapid assessment of new chemistries and cell components with minimal materials requirements. Mass-transfer coefficients are then measured using this cell with a well-behaved redox active electrolyte (RAE), in which glucose is added in various amounts to modify the system viscosity with minimal changes to other properties.en_US
dc.description.abstractThe results or methodology developed could be extended other similar RAE systems either as preliminary estimates of mass-transfer performance or as a protocol for carefully evaluating the impact of new system parameters on mass-transfer. Finally, results of this mass-transfer analysis are incorporated into a simple flexible stack model, which can be used to estimate system performance as a function of key materials properties with limited empiricism.en_US
dc.description.statementofresponsibilityby John Leonard Barton.en_US
dc.format.extent228 pagesen_US
dc.language.isoengen_US
dc.publisherMassachusetts Institute of Technologyen_US
dc.rightsMIT theses are protected by copyright. They may be viewed, downloaded, or printed from this source but further reproduction or distribution in any format is prohibited without written permission.en_US
dc.rights.urihttp://dspace.mit.edu/handle/1721.1/7582en_US
dc.subjectChemical Engineering.en_US
dc.titleMethod development for the analysis of electrochemical and transport processes in redox flow batteries at practical operating conditionsen_US
dc.typeThesisen_US
dc.description.degreePh. D.en_US
dc.contributor.departmentMassachusetts Institute of Technology. Department of Chemical Engineeringen_US
dc.identifier.oclc1103317625en_US
dc.description.collectionPh.D. Massachusetts Institute of Technology, Department of Chemical Engineeringen_US
dspace.imported2019-07-22T19:37:17Zen_US
mit.thesis.degreeDoctoralen_US
mit.thesis.departmentChemEngen_US


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