Viscoelastic behaviour of polystyrene/supercritical CO2 mixtures used for foaming applications

dc.contributor.advisorBonilla Rios, Jaimeen_US
dc.contributor.authorIbarra Garza, César Miguelen_US
dc.contributor.committeememberTreviño Quintanilla, Cecilia Danielaen_US
dc.contributor.committeememberCortés Rodríguez, Leonardo Federicoen_US
dc.contributor.committeememberBarrera, Enriqueen_US
dc.date.accessioned2018-05-18T17:36:08Z
dc.date.available2018-05-18T17:36:08Z
dc.date.issued2017-05-12
dc.description.abstractA study of polystyrene resins containing supercritical CO2 was made to understand their viscoelastic behavior for foaming applications. Three resins of polystyrene with different molecular weight distribution (MWD) were tested at three temperatures (170, 185 and 200ºC) and two pressures (6.89 MPa and 13.78 MPa) using CO2 as diluent. A testing methodology was developed to provide accuracy and repeatability. It reduced standard deviations by at least 52% for high pressure oscillatory rheology tests. Methodology included data correction using Sanchez-Lacombe EOS to describe the mixing phenomenon and polymer swelling. Effects of temperature, pressure and CO2 concentration were evaluated and isolated according to a time-temperature-pressure-concentration superposition. Another approach was accomplished using a high pressure rheology model developed by Total Petrochemicals & Refining USA, Inc. to identify differences in viscoelastic behavior of polystyrene resins. Overall, the model accurately described the shear-thinning behavior of PS and PS+CO2 systems. Finally, elongational viscosities were estimated to speculate about the polymer’s foaming behavior at different operating conditions. The analysis showed that apparently there were no significant differences between resins’ viscosities at high pressures. However, results were expected to differentiate according to resins’ MWD; the higher the molecular weight, the higher the elongational viscosity. Therefore, it is concluded that obtained rheological data is not suitable for this model and additional data adjustment is mandatory for this particular analysis.
dc.identifier.urihttp://hdl.handle.net/11285/629702
dc.language.isoengen_US
dc.rightsRestricted Accessen_US
dc.rights.urihttp://creativecommons.org/licenses/by-nc-nd/4.0/*
dc.subject.disciplineCiencias / Sciencesen_US
dc.subject.keywordPolymeren_US
dc.subject.keywordPolystyreneen_US
dc.subject.keywordSupercritical CO2en_US
dc.subject.keywordEngineeringen_US
dc.titleViscoelastic behaviour of polystyrene/supercritical CO2 mixtures used for foaming applicationsen_US
dc.typeTesis de maestría
html.description.abstract<html> <head> <title></title> </head> <body> <p>A study of polystyrene resins containing supercritical CO2 was made to understand their viscoelastic behavior for foaming applications. Three resins of polystyrene with different molecular weight distribution (MWD) were tested at three temperatures (170, 185 and 200&#186;C) and two pressures (6.89 MPa and 13.78 MPa) using CO2 as diluent. A testing methodology was developed to provide accuracy and repeatability. It reduced standard deviations by at least 52% for high pressure oscillatory rheology tests. Methodology included data correction using Sanchez-Lacombe EOS to describe the mixing phenomenon and polymer swelling. Effects of temperature, pressure and CO2 concentration were evaluated and isolated according to a time-temperature-pressure-concentration superposition. Another approach was accomplished using a high pressure rheology model developed by Total Petrochemicals &#38; Refining USA, Inc. to identify differences in viscoelastic behavior of polystyrene resins. Overall, the model accurately described the shear-thinning behavior of PS and PS+CO2 systems. Finally, elongational viscosities were estimated to speculate about the polymer&#8217;s foaming behavior at different operating conditions. The analysis showed that apparently there were no significant differences between resins&#8217; viscosities at high pressures. However, results were expected to differentiate according to resins&#8217; MWD; the higher the molecular weight, the higher the elongational viscosity. Therefore, it is concluded that obtained rheological data is not suitable for this model and additional data adjustment is mandatory for this particular analysis.</p> </body> </html>en_US
refterms.dateFOA2018-05-18T17:36:08Z
thesis.degree.disciplineEscuela de Ingeniería y Cienciasen_US
thesis.degree.grantorInstituto Tecnológico y de Estudios Superiores de Monterreyes
thesis.degree.levelMaestro en Ciencias en Sistemas de Manufacturaen_US
thesis.degree.nameMaestría en Ciencias con Especialidad en Sistemas de Manufacturaen_US
thesis.degree.programCampus Monterreyen_US

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