Orientador: Marco-Aurelio De Paoli / Dissertação (mestrado) - Universidade Estadual de Campinas, Instituto de Quimica / Made available in DSpace on 2018-08-13T13:43:01Z (GMT). No. of bitstreams: 1 Romao_Wanderson_M.pdf: 3473303 bytes, checksum: 3ef4c09640bf5042dfcbfd4c110e4244 (MD5) Previous issue date: 2009 / Resumo: Atualmente, o Brasil apresenta um dos maiores índices mundiais de reciclagem mecânica do poli (tereftalato de etileno), PET. O sucesso desse termoplástico na indústria de reciclagem deve-se à sua ampla diversidade de aplicações. As embalagens recicladas grau alimentício podem ser misturadas com a resina virgem e reprocessadas. Três metodologias foram estudadas para detectar a presença do PET pós-consumo graugarrafa (PETpc-btg) em PET virgem grau-garrafa (PETv-btg): calorimetria exploratória diferencial (DSC), espectrometria de massas (MALDI-TOF MS) e Fluorescência de raios-X (XRF). Amostras de PETv-btg de três fabricantes foram analisadas: Braskem, Rhodia e Eastman. Amostras de PETpc-btg submetidas ao processo super-clean® também foram analisadas. Elas apresentam a mesma [h] do PETv-btg e foram fornecidas pela empresa Bahia PET. Amostras de PETv-btg Braskem e PETpc-btg foram misturadas e processadas em nosso laboratório em diversas proporções através de um misturador interno acoplado ao reômetro de torque. Os resultados de DSC mostram que a Tm, Tc, DCp e a cinética de cristalização são as principais propriedades térmicas que servem para diferenciar entre PETv-btg e PETpc-btg. Utilizando a técnica de MALDI-TOF MS aliado ao PCA (Análise Componentes Principais), foi possível distinguir as amostras em vários grupos. Esses grupos eram separados em função de alterações químicas como: variações na viscosidade intrínseca ([h] 0,80 e [h] = 0,65-60); submetidas e não submetidas a algum processo industrial; wt % de PETpc-btg em PETv-btg Braskem; e variação no processo de síntese do polímero (fabricante). A partir desses resultados foi possível construir um modelo de calibração, onde ele consegue distinguir entre uma amostra de PETv-btg e uma amostra de PETpc-btg. As medidas de XRF mostraram que alguns fabricantes utilizam mais de um catalisador para o processo de síntese do PETv-btg. A Braskem utiliza manganês e antimônio. Portanto, o modelo de previsão funciona para prever a wt % PETpc nas misturas que foram utilizadas na construção dele, como é o caso das resinas de PETv-btg Braskem e PETpc-btg. Observamos também, através das medidas de XRF, que o teor de Ferro presente no PET aumenta em função do processo de reciclagem. Esta variável poderá ser utilizada para a construção de um modelo quimiométrico abrangendo uma maior quantidade de variáveis / Abstract: Recently, Brazil recorded mechanical recycling of the poly (ethylene terepththalate), PET, the highest in the world, corresponding to about 53 wt %. This success in the recycling industry is due to the wide range of its applications, from textiles to packaging for the food industry. The recycled food-grade packaging could be mixed with virgin resin and reprocessing. Three methodologies were used to detect the presence of the bottle-grade post-consumption PET (PETpc-btg) in the bottle-grade virgin PET (PETv-btg): differential scanning calorimetry (DSC), x-ray fluorescence and matrix assisted laser desorption ionisation time-of-flight mass spectrometry (MALDI-TOF MS). PETv-btg samples were supplied by the manufacturers (Braskem, Rhodia and Eastman). Samples from a superclean ® process (Bahia PET Reciclagem) were also analysed. All samples had the same intrinsic viscosity values, [h]. Braskem PETv-btg and PETpc-btg samples were blended and processed in different proportions in our laboratory using a HAAKE mixer system. DSC results show that cristallization kinetics, heat capacity (DCp), melting and crystallization temperature are the principal thermal properties that can be used to distinguish between PETv-btg and PETpc-btg. MALDI-TOF MS results together with PCA (principal component analysis) was used to classify the samples into several groups: intrinsic viscosity changes ([h] 0,80 e [h] = 0,65-60); processed and not submitted to some industrial process; wt % PETpc-btg in the PETv-btg Braskem; synthesis process change (manufacturer). From these results, it was possible to creat a calibration model, that differentiated between PETv-btg and PETpc-btg resins. However, we were not able to forecast the percentage of PETpc-btg in the PETv-btg. A model can be made from processed samples where its Mw could be corrected for solid state polymerization or the super-clean® process. XRF results show that some manufacturers use one or more catalysts for PETv-btg synthesis. The Braskem resin is made using manganese and antimony catalysts. Therefore, the prediction model is valid only when the origin of the studied mixture is known, such as PETv-btg/PETpc-btg processed blends. For other resins, the prediction model does not work. The Braskem resin had characteristics distintct from the others. We observed also that the Fe concentration in PET increase in as a function of the recycling process. Therefore, this variable could be used, in the future work, to create chemometric models incluing a higher number of variables / Mestrado / Físico-Química / Mestre em Química

Novel poly(ethylene isophthalate) (PEI) and poly(ethylene terephthalate) (PET) polymers containing terminal units derived from sodio 3-sulfobenzoic acid (SSBA) were synthesized using catalyzed melt polymerization techniques. Various concentrations of the ionic end group, SSBA, were successfully incorporated in a telechelic fashion. For comparison, polyesters containing telechelic alkyl groups with controllable molecular weights were also synthesized. Furthermore, ionic copolymers of dimethyl isophthalate and trans-cyclohexane dicarboxylate, dimethyl isophthalate and dimethyl terephthalate were synthesized to study the influences of polarity and rigidity of the polymer chain backbone on material properties. Novel branched polyester ionomers using trimellitic anhydride were also prepared. In addition to modifying the polymer compositions, PET ionomers were blended with zinc stearate to investigate the effect of plasticizer on the melt processibilty of the ionomers. FTIR spectroscopy, which was used to quantify the sulfonate end groups for all of the ionomers, indicated an absorbance peak for the S-O stretching mode between 600-700 cm⁻¹. ¹H NMR spectroscopy was used to confirm the structure of the ionic and non-ionic polyesters, as well as to verify the presence of the terminal groups. By systematically varying the chemical structure of these ionomer model systems (i.e., altering the contents of ionic functional groups), detailed characterizations were carried out, wherein the ionic interactions/aggregations in the ionomers were found to play an important role in the resulting material properties. Differential scanning calorimetry (DSC) and thermogravimetric analysis (TGA) measurements were performed to study the effects of ionic groups and oligomer composition on the thermal properties of the polyesters. The glass transition temperatures of the ionomers revealed that the ionic interaction helped to maintain the structural integrity of the polymer chains, thus limiting their mobility. The dilute solution viscosity behavior of the ionomers exhibited upward curvature, which is a key characteristic of an ionomer. In PEI ionomers, the ionic aggregates formed at lower temperatures (<150 °C), while at higher temperatures (>150 °C), the ionic aggregations dissociated and behaved similarly to oligomers with lower molecular weights. Dodecanol was used as an effective end-capper to control the molecular weight of the non-ionic polyesters. In addition to telechelic ionic PEI and PET homopolymers, copolymers of poly(ethylene isophthalate-co-trans-1,4-cyclohexane dicarboxylate) (PEI-co-trans-CHDC) and poly(ethylene isophthalate-co-terephthalate) (PEIT) telechelic ionomers were also synthesized and characterized. Introducing trans-1,4-cyclohexane dicarboxylate into PEI ionomers decreased the polarity and packing regularity of the polymer chains. Also, the kinked-structure of dimethyl isophthalate reduced the regularity of the polymer chains in PET ionomers, thus reducing their propensity for rapid crystallization. Crystallization kinetics were studied for both ionic and alkyl telechelic polyesters, and resulting data revealed that the nature of the endgroup had a dramatic effect on crystallization from the melt state. The catalyst residue in the polymers also affected the crystallization rate for both ionic and non-ionic polyesters. With regard to the ionomers, antimony catalyst interacted with ionic aggregates, further increasing the crystallization rate. Branched PEI and PET ionomers showed an increase in melt strength. After blending with zinc stearate, the melt viscosity of the PET ionomers dropped dramatically. / Master of Science

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The dissertation describes and assembles the building blocks for sound and accurate models for solid-state polymerization process systems of condensation polymers, particularly poly(ethylene terephthalate) and nylon-6. The work centers on an approach for modeling commercial-scale, as opposed to laboratory-scale, systems. The focus is not solely on coupled polymerization and diffusion, but extends to crystallization, physical properties, and phase equilibrium, which all enhance the robustness of the complete model. There are three applications demonstrating the utility of the model for a variety of real, industrial plant operations. One of the validated simulation models is for commercial production of three different grades of solid-state PET. There are also validated simulation models for the industrial leaching and solid-state polymerization of nylon-6 covering a range of operating conditions. The results of these studies justify our mixing-cell modeling approach as well as the inclusion of all relevant fundamental concepts. The first several chapters discuss in detail the engineering fundamentals that we must consider for modeling these polymerization process systems. These include physical properties, phase equilibrium, crystallization, diffusion, polymerization, and additional modeling considerations. The last two chapters cover the modeling applications. / Ph. D.

Supercritical carbon dioxide (scCO2) was used as a processing aid to improve the level of exfoliation achievable in a PET-layered silicate nanocomposite produced from melt compounding. Layered silicate and scCO2 were allowed to mix for a period of time before being released into the second stage of a single screw extruder. The rapid expansion forced silicate particles into a modified hopper containing neat PET pellets. The mixture of layered silicate and PET was immediately melt mixed in a single screw extruder, cooled in a water bath and pelletized. Two sets of samples each containing layered silicate with different surface chemistries were produced with this method at 1, 3 and 5 wt% silicate. For comparison, samples of the same weight fraction and type of silicate were produced from a traditional melt compounding method. Wide angle x-ray diffraction (WAXD), mechanical testing and rheological analysis were used in order to characterize the silicate morphology, the composite mechanical properties and the relative amount of degradation between the various samples. Results show that scCO2 processed samples contain a higher degree of layered silicate exfoliation than samples produced with traditional melt compounding. Mechanical property improvements are shown to be dependent on the type of silicate surface modification employed. Finally, degradation of the PET matrix appears to be far less extensive in the scCO2 processed samples as shown from rheological data. / Master of Science

The increasing use of polymeric materials in food packaging applications is due to many factors; however, most are related to cost. While poly(ethylene terephthalate) (PET) is currently the industry standard for soft-drink bottles, more stringent requirements on the barrier properties to oxygen are needed for PET to expand further into more demanding markets (i.e., juice, etc). The current work examines the fundamental oxygen and carbon dioxide permeation and sorption properties of amorphous, caffeine antiplasticized PET and amorphous poly(ethylene furanoate) (PEF), which is a new biologically sourced polyester that exhibits significantly enhanced performance compared to petroleum-sourced PET. The fundamental transport data reported herein at 35°C illustrate that amorphous PEF exhibits significant reductions in permeability for oxygen (11X), carbon dioxide (19X), and water (2X) compared to amorphous PET. Such impressive barrier enhancements are unexpected since PEF exhibits a higher free volume compared to PET. Further investigation into the fundamental chain motional processes which contribute to penetrant diffusion, as probed via dynamic mechanical and solid-state NMR methods, reveals that the polymer ring-flipping motions in PEF are largely suppressed compared to those for PET. Such behavior allows for rationalization of the reduced transport properties compared to PET. Additional characterization techniques (i.e., thermal, mechanical, density, etc.) are used to develop a more complete understanding of PEF and caffeine antiplasticized PET, with the ultimate goal of relating these properties to penetrant transport.