{"@context":"http://iiif.io/api/presentation/2/context.json","@id":"https://repo.library.stonybrook.edu/cantaloupe/iiif/2/manifest.json","@type":"sc:Manifest","label":"Carbon Dioxide Multiphase Flows in Microfluidic Devices","metadata":[{"label":"dc.description.sponsorship","value":"This work is sponsored by the Stony Brook University Graduate School in compliance with the requirements for completion of degree."},{"label":"dc.format","value":"Monograph"},{"label":"dc.format.medium","value":"Electronic Resource"},{"label":"dc.identifier.uri","value":"http://hdl.handle.net/1951/55639"},{"label":"dc.language.iso","value":"en_US"},{"label":"dc.publisher","value":"The Graduate School, Stony Brook University: Stony Brook, NY."},{"label":"dcterms.abstract","value":"In 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."},{"label":"dcterms.available","value":"2015-04-24T14:53:13Z"},{"label":"dcterms.contributor","value":"Krainer, Adrian R."},{"label":"dcterms.creator","value":"Sun, Ruopeng"},{"label":"dcterms.dateAccepted","value":"2015-04-24T14:53:13Z"},{"label":"dcterms.dateSubmitted","value":"2015-04-24T14:53:13Z"},{"label":"dcterms.description","value":"Department of Mechanical Engineering"},{"label":"dcterms.format","value":"Application/PDF"},{"label":"dcterms.identifier","value":"http://hdl.handle.net/1951/55639"},{"label":"dcterms.issued","value":"2010-12-01"},{"label":"dcterms.language","value":"en_US"},{"label":"dcterms.provenance","value":"Made available in DSpace on 2012-05-15T18:07:05Z (GMT). No. of bitstreams: 1\nSun_grad.sunysb_0771M_10346.pdf: 2140477 bytes, checksum: 2c5fa76d96568a25e2695875ba051b87 (MD5)\n  Previous issue date:    1"},{"label":"dcterms.publisher","value":"The Graduate School, Stony Brook University: Stony Brook, NY."},{"label":"dcterms.subject","value":"Carbon Dioxide, Microfluidics, Multiphase flow"},{"label":"dcterms.title","value":"Carbon Dioxide Multiphase Flows in Microfluidic Devices"},{"label":"dcterms.type","value":"Thesis"},{"label":"dc.type","value":"Thesis"}],"description":"This manifest was generated dynamically","viewingDirection":"left-to-right","sequences":[{"@type":"sc:Sequence","canvases":[{"@id":"https://repo.library.stonybrook.edu/cantaloupe/iiif/2/canvas/page-1.json","@type":"sc:Canvas","label":"Page 1","height":1650,"width":1275,"images":[{"@type":"oa:Annotation","motivation":"sc:painting","resource":{"@id":"https://repo.library.stonybrook.edu/cantaloupe/iiif/2/10%2F97%2F73%2F109773677311141646968828696518224593153/full/full/0/default.jpg","@type":"dctypes:Image","format":"image/jpeg","height":1650,"width":1275,"service":{"@context":"http://iiif.io/api/image/2/context.json","@id":"https://repo.library.stonybrook.edu/cantaloupe/iiif/2/10%2F97%2F73%2F109773677311141646968828696518224593153","profile":"http://iiif.io/api/image/2/level2.json"}},"on":"https://repo.library.stonybrook.edu/cantaloupe/iiif/2/canvas/page-1.json"}]}]}]}