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dc.identifier.urihttp://hdl.handle.net/1951/55639
dc.identifier.urihttp://hdl.handle.net/11401/72684
dc.description.sponsorshipThis work is sponsored by the Stony Brook University Graduate School in compliance with the requirements for completion of degree.en_US
dc.formatMonograph
dc.format.mediumElectronic Resourceen_US
dc.language.isoen_US
dc.publisherThe Graduate School, Stony Brook University: Stony Brook, NY.
dc.typeThesis
dcterms.abstractIn this thesis, we experimentally studied the mass transfer during CO<sub>2</sub> absorption into water, ethanol, methanol and silicone oil under slug flow in microchannels. We showed that the initial bubble size is determined by the liquid fraction and channel geometry, while the CO<sub>2</sub> diffusion rate is determined by the gas pressure and liquid properties, such as the Henry's constant and the diffusion coefficient. The reduction of the gas void fraction&#913;<sub>G</sub> along the flow direction and the transformation of segmented flows into dilute bubbly flows was observed and predicted. In high viscosity liquids, we showed the liquid film thickness is related to the capillary number and the gas pressure. We also constructed experimental setup for investigating CO<sub>2</sub> cavitation in microchannels. A linear time dependence of bubble growth from depressurization is observed. In addition, we proposed the fabrication procedure of co-flowing capillary tip and listed its current limitations.
dcterms.available2012-05-15T18:07:05Z
dcterms.available2015-04-24T14:53:13Z
dcterms.contributorKrainer, Adrian R.en_US
dcterms.contributorJon Longtinen_US
dcterms.contributorJohn Kincaid.en_US
dcterms.creatorSun, Ruopeng
dcterms.dateAccepted2012-05-15T18:07:05Z
dcterms.dateAccepted2015-04-24T14:53:13Z
dcterms.dateSubmitted2012-05-15T18:07:05Z
dcterms.dateSubmitted2015-04-24T14:53:13Z
dcterms.descriptionDepartment of Mechanical Engineeringen_US
dcterms.formatApplication/PDFen_US
dcterms.formatMonograph
dcterms.identifierhttp://hdl.handle.net/1951/55639
dcterms.identifierSun_grad.sunysb_0771M_10346.pdfen_US
dcterms.identifierhttp://hdl.handle.net/11401/72684
dcterms.issued2010-12-01
dcterms.languageen_US
dcterms.provenanceMade available in DSpace on 2012-05-15T18:07:05Z (GMT). No. of bitstreams: 1 Sun_grad.sunysb_0771M_10346.pdf: 2140477 bytes, checksum: 2c5fa76d96568a25e2695875ba051b87 (MD5) Previous issue date: 1en
dcterms.provenanceMade available in DSpace on 2015-04-24T14:53:13Z (GMT). No. of bitstreams: 3 Sun_grad.sunysb_0771M_10346.pdf.jpg: 1894 bytes, checksum: a6009c46e6ec8251b348085684cba80d (MD5) Sun_grad.sunysb_0771M_10346.pdf.txt: 60990 bytes, checksum: e736887ebcdb34272f2da04ceb53fccf (MD5) Sun_grad.sunysb_0771M_10346.pdf: 2140477 bytes, checksum: 2c5fa76d96568a25e2695875ba051b87 (MD5) Previous issue date: 1en
dcterms.publisherThe Graduate School, Stony Brook University: Stony Brook, NY.
dcterms.subjectCarbon Dioxide, Microfluidics, Multiphase flow
dcterms.subjectMechanical Engineering
dcterms.titleCarbon Dioxide Multiphase Flows in Microfluidic Devices
dcterms.typeThesis


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