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dc.contributor.advisorCharles L. Cooney.en_US
dc.contributor.authorMa, Junfen, 1972-en_US
dc.contributor.otherMassachusetts Institute of Technology. Dept. of Chemical Engineering.en_US
dc.date.accessioned2005-05-19T15:38:35Z
dc.date.available2005-05-19T15:38:35Z
dc.date.copyright2003en_US
dc.date.issued2003en_US
dc.identifier.urihttp://hdl.handle.net/1721.1/17010
dc.descriptionThesis (Ph. D.)--Massachusetts Institute of Technology, Dept. of Chemical Engineering, 2003.en_US
dc.descriptionIncludes bibliographical references (p. 173-180).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.description.abstractOne strategy to reduce costs in manufacturing a biochemical product is simplification of downstream processing. Biochemical product recovery often starts from fermentation broth or cell culture. In conventional downstream processing, the initial steps are clarification, concentration, and purification. Simplification of downstream processing may be achieved by reducing the number of unit operations. Integrative technologies seek to combine steps into a new single unit operation, thereby tightening the whole process. Vortex flow occurs in the annular gap between an inner rotating solid cylinder and an outer stationary cylindrical shell. Above a critical rotation rate, circular Couette flow bifurcates to a series of counter-rotating toroidal vortices. By suspending adsorbent resin in the vortices, a novel unit operation, vortex flow adsorption (VFA), is created. In VFA, the rotation of the inner cylinder facilitates the fluidization of the adsorbent resin. In addition, VFA has high fluid voidage so that it can be used to recover biochemical products directly from fermentation broths or cell homogenates without removing cells or cell debris first. VFA was characterized through two experimental approaches, tracer residence time distribution (RTD) study and breakthrough capacity measurements, and two modeling approaches, a one-dimensional dispersion convective model and a two-region vortex flow model. It was concluded that the axial dispersion in the vortex flow system is distinct in different vortex flow regimes.en_US
dc.description.abstract(cont.) The effect of the operating variables, including the rotation rate of the inner cylinder, the axial loading flowrate, and the adsorbent volume fraction, on the performance of VFA was explored. In this research, recombinant human (cl-antitrypsin ([alpha]l-AT) was expressed in Escherichia coli as a C-terminal fusion to a modified intein containing a chitin-binding domain. The VFA results indicated that VFA not only captures the fusion protein from crude cell extract containing cell debris but also purifies ocl-AT. Therefore, vortex flow adsorption is an integrative technology to combine the primary clarification, concentration, and purification steps to simplify conventional downstream processing.en_US
dc.description.statementofresponsibilityby Junfen Ma.en_US
dc.format.extent180 p.en_US
dc.format.extent984486 bytes
dc.format.extent970872 bytes
dc.format.mimetypeapplication/pdf
dc.format.mimetypeapplication/pdf
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/1721.1/7582
dc.subjectChemical Engineering.en_US
dc.titleCharacterization and application of vortex flow adsorption for simplification of biochemical product downstream processingen_US
dc.title.alternativeCharacterization and application of VFA for simplification of biochemical product downstream processingen_US
dc.typeThesisen_US
dc.description.degreePh.D.en_US
dc.contributor.departmentMassachusetts Institute of Technology. Department of Chemical Engineering
dc.identifier.oclc54454366en_US


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