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dc.contributor.advisorJ. Christopher Love.en_US
dc.contributor.authorMascarenhas, Craig Anthonyen_US
dc.contributor.otherMassachusetts Institute of Technology. Department of Mechanical Engineering.en_US
dc.date.accessioned2017-12-05T19:16:43Z
dc.date.available2017-12-05T19:16:43Z
dc.date.copyright2017en_US
dc.date.issued2017en_US
dc.identifier.urihttp://hdl.handle.net/1721.1/112524
dc.descriptionThesis: S.M., Massachusetts Institute of Technology, Department of Mechanical Engineering, 2017.en_US
dc.descriptionPage 206 blank. Cataloged from PDF version of thesis.en_US
dc.descriptionIncludes bibliographical references (pages 196-205).en_US
dc.description.abstractBiologic drug manufacturing is traditionally conducted in large-scale, industrial bioreactors. The emergence of interest in disposable, bench-top bioreactors as a viable alternative is due to potential advantages such as lower contamination risk, time and cost savings, and ease of handling. The challenges associated with disposable, bench-top bioreactors include poor mixing, limited oxygen transfer, and a scarcity of non-invasive sensors for process control. This thesis investigates multiple aspects of a disposable, perfusion-capable bioreactor, in order to facilitate an optimal design. In order to determine an impeller configuration that improves the mixing and mass transfer characteristics of a i-liter bioreactor, Computational Fluid Dynamics (CFD) was used. The potential benefits of switching to a dual-Marine impeller system was revealed, which was then validated during fermentation experiments. Further predictions of a merging flow pattern in the i-liter vessel was consistent with the literature based on the impeller spacing. A scaled-up 5-liter vessel was designed with Rushton impellers spaced so as to create a parallel flow pattern, which was later successfully predicted in the CFD simulations. Flow patterns were analyzed at various locations in both vessels to aid future design iterations. Monitoring of process parameters, including liquid level, is important for automated control in bioreactors. Three novel, non-invasive, optical liquid level sensing methods were conceptualized, prototyped, and successfully tested. These solutions relied on self-developed image processing algorithms. Additionally, a magnetic liquid level sensor was also developed and tested that relied on a magnetic float and a series of reed switches. In order to increase the perfusion membrane surface area and reduce complexity, the switch to a hollow-fiber harvest probe was examined. CFD studies guided design iterations by modeling the flow around the probe, giving insight into the stagnation properties and shear forces acting on the fibers. Additionally, experimental testing of the new harvest probe revealed its successful functionality and viability in the bioreactor.en_US
dc.description.statementofresponsibilityby Craig Anthony Mascarenhas.en_US
dc.format.extent206 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.subjectMechanical Engineering.en_US
dc.titleDesign and development of components of a modular bioreactoren_US
dc.typeThesisen_US
dc.description.degreeS.M.en_US
dc.contributor.departmentMassachusetts Institute of Technology. Department of Mechanical Engineering
dc.identifier.oclc1012939123en_US


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