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Gas and pervaporation separations using styrenic polymer membranes
dc.creator | Chen, Wen-Janq | |
dc.date.accessioned | 2020-09-07T17:20:41Z | |
dc.date.available | 2020-09-07T17:20:41Z | |
dc.date.issued | 1995 | |
dc.identifier.uri | https://hdl.handle.net/1969.1/DISSERTATIONS-1561425 | |
dc.description | Vita. | en |
dc.description.abstract | Poly(DVB/EVB) and sulfonated polystyrenes were investigated for possible use in gas separations. Defect-free ultrathin film composite membranes were synthesized using an electrochemical method using DVB/EVB as the monomer. Ultrathin poly(DVB/EVB) films ([ ca. 2.0 gm thickness) showed identical gas-transport selectivity to those obtained for bulk poly(DVB/EVB) membranes. The effect of various experimental parameters (including monomer concentration, supporting electrolyte concentration, and voltage scan rate) on the thickness of the polymer film were investigated. Gas-transport properties of sulfonated polystyrenes were investigated. The polymers were sulfonated to various sulfonation levels. Permeability coefficients were obtained using the single gas permeation measurement. The time-lag method was applied to obtain the diffusion coefficient. The correlation of the gas-transport properties with the chemical properties of the polymers is discussed. The results suggest that highly-sulfonated Mg2+-forin polystyrene is a promising material for the 02/N2 separation. Water-transport properties were investigated using PSS/AI203 composite membranes. A dew-point device was used to measure the water penneate rate. A mathematical model (used in a previous investigation of water transport in the sulfonated perfluorocarbon polymer Nafion TM) was used to analyze the water transport data for the PSS/AI203 film. In the ethanol/water separation, the results showed that the PSS/ A1203 composite membranes can break up the azeotrope of the ethanol/ water mixtures by pervaporation. Water is the preferred permeate. The highest separation factor (400) was obtained for the 10.5 mole% PSSNa/AI203 composite at the azeotropic feed composition. Ethanol weight fraction in the permeate is always less than 6 wtO/o for this composite membrane and all feed compositions. In the MTBE/MeOH separation, the results showed that the PSS/A1203 composite membranes possess high MEOH transport selectivity, relative to MTBE. MEOH concentrations in the permeate were always greater than 99.5 wtO/o for all membranes and all feed solution compositions studied. Extremely high separation factors (25,000 to 35,000) were observed for the PSS-Mg/AI203 composite membrane of 27.5 mole% sulfonate. | en |
dc.format.extent | xvii, 179 leaves | en |
dc.format.medium | electronic | en |
dc.format.mimetype | application/pdf | |
dc.language.iso | eng | |
dc.rights | This thesis was part of a retrospective digitization project authorized by the Texas A&M University Libraries. Copyright remains vested with the author(s). It is the user's responsibility to secure permission from the copyright holder(s) for re-use of the work beyond the provision of Fair Use. | en |
dc.rights.uri | http://rightsstatements.org/vocab/InC/1.0/ | |
dc.subject | Major chemistry | en |
dc.subject.classification | 1995 Dissertation C4495 | |
dc.title | Gas and pervaporation separations using styrenic polymer membranes | en |
dc.type | Thesis | en |
thesis.degree.grantor | Texas A&M University | en |
thesis.degree.name | Doctor of Philosophy | en |
thesis.degree.name | Ph. D | en |
dc.type.genre | dissertations | en |
dc.type.material | text | en |
dc.format.digitalOrigin | reformatted digital | en |
dc.publisher.digital | Texas A&M University. Libraries | |
dc.identifier.oclc | 35072081 |
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