In this research thermal properties enhancement of phase change material (PCM) using boron nitride nanomaterials such as nanoparticles and nanotubes is studied through experimental measurements, finite element method (FEM) through COMSOL 5.3 package and molecular dynamics simulations via equilibrium molecular dynamics simulation (EMD) with the Materials and Process Simulations (MAPS 4.3). This study includes two sections: thermal properties enhancement of inorganic salt hydrate (CaCl2∙6H2O) as the phase change material by mixing boron nitride nanoparticles (BNNPs), and thermal properties enhancement of organic phase change material (paraffin wax) as the phase change material via encapsulation into boron nitride nanotubes (BNNTs). The results of the proposed research will contribute to enhance the thermal transport properties of inorganic and organic phase change material applying nanotechnology for increasing energy efficiency of systems including electronic devices, vehicles in cold areas to overcome the cold start problem, thermal interface materials for efficient heat conduction and spacecraft in planetary missions for efficient thermal managements.

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Petrobras / Petróleos parafínicos são complexas misturas de hidrocarbonetos saturados, aromáticos, naftênicos e, em menor quantidade, de componentes que apresentam heteroátomos como resinas e asfaltenos. Em baixas temperaturas, a solubilidade das parafinas em solução diminui e ocorre a precipitação de hidrocarbonetos no petróleo. Devido à cristalização nota-se não apenas o aumento considerável da viscosidade dos petróleos em baixas temperaturas, mas também a deposição de parafina nas paredes internas da tubulação e a gelificação do petróleo nos oleodutos em eventuais paradas da produção. Os trabalhos disponíveis na literatura mostram que os históricos térmico e de cisalhamento influenciam o comportamento mecânico de petróleos parafínicos em baixas temperaturas. No presente trabalho são apresentados resultados da influência da temperatura inicial de resfriamento na temperatura de cristalização, na temperatura de gelificação e na tensão crítica necessária para reiniciar o escoamento de petróleos parafínicos. A temperatura em que o material é submetido antes do resfriamento influencia nas propriedades reológicas do petróleo. A partir da revisão de conceitos de cristalização define-se que para a precipitação do primeiro cristal é necessário a ocorrência de super-resfriamento na solução. Em outras palavras, não é possível que ocorra a cristalização da parafina exatamente na temperatura de equilíbrio sólido-líquido, Teq,SL. É proposta uma metodologia experimental para determinar a temperatura de saturação de óleos parafínicos. A partir de resultados reométricos pode-se notar que a magnitude do superresfriamento influencia a taxa de nucleação e o tamanho final dos cristais precipitados. O tamanho da região metaestável é influenciado pela taxa de resfriamento e pela temperatura inicial do teste. A partir de microscopia de campo claro observa-se que quanto maior o superresfriamento maior o número de cristais formados. Pode-se adiantar que a morfologia e o tamanho dos cristais formados influenciam o comportamento reológico do óleo parafínico em baixas temperaturas. / Waxy crude oil is a complex mixture of hydrocarbons consisting of paraffins, aromatics, naphthenes, asphaltenes and resins. At low temperatures the solubility of high molecular weight components in the oil is decreased and especially the n-paraffins tend to precipitate as crystal structures. These crystals provide a non-Newtonian behavior to the fluid, tend to deposit in the inner surface of pipelines and are responsible for the gelation of the oil when the flow is interrupted. In such cases, the pressure needed to restart the oil flow in subsea pipelines can be much larger than the usual steady-state pressure as the temperature in such environment can be as low as 4 °C. The literature has shown that not only the temperature itself but also the fluid shear and thermal histories have significant influence on the yield stress of waxy crude oils. The current work shows the effect of the initial cooling temperature on the waxy crude oil viscosity, gelation temperature and critical stress. It is showed that the initial cooling temperature affects the mechanical behavior of crude oils at low temperature. It is presented that crystallization is the process where an ordered solid structure is formed from a disordered phase. This process involves two main stages, namely nucleation and crystals growth. As paraffins nucleation is a stochastic process, a supercooling is needed to the onset of this phenomenon. In other words precipitation of crystals could not take place at the solidliquid equilibrium thermodynamic temperature, Teq,SL. Therefore, during the cooling, it is required that the fluid reaches a certain temperature, below the Teq,SL, to initiate the nucleation process. This work proposes an experimental procedure to determine consistently the highest solid-liquid thermodynamic equilibrium temperature. By means of rheometric tests, it is showed that the supercooling affects the nucleation rate and the crystals morphology, and also it is influenced by the cooling rate and the initial cooling temperature. One can conclude that the higher the supercooling the higher the number of crystals and, as consequence, the lower the crystals length. Finally, the crystals morphology and the length affect the mechanical properties of the waxy oil.

Petrobras / Petróleos parafínicos são complexas misturas de hidrocarbonetos saturados, aromáticos, naftênicos e, em menor quantidade, de componentes que apresentam heteroátomos como resinas e asfaltenos. Em baixas temperaturas, a solubilidade das parafinas em solução diminui e ocorre a precipitação de hidrocarbonetos no petróleo. Devido à cristalização nota-se não apenas o aumento considerável da viscosidade dos petróleos em baixas temperaturas, mas também a deposição de parafina nas paredes internas da tubulação e a gelificação do petróleo nos oleodutos em eventuais paradas da produção. Os trabalhos disponíveis na literatura mostram que os históricos térmico e de cisalhamento influenciam o comportamento mecânico de petróleos parafínicos em baixas temperaturas. No presente trabalho são apresentados resultados da influência da temperatura inicial de resfriamento na temperatura de cristalização, na temperatura de gelificação e na tensão crítica necessária para reiniciar o escoamento de petróleos parafínicos. A temperatura em que o material é submetido antes do resfriamento influencia nas propriedades reológicas do petróleo. A partir da revisão de conceitos de cristalização define-se que para a precipitação do primeiro cristal é necessário a ocorrência de super-resfriamento na solução. Em outras palavras, não é possível que ocorra a cristalização da parafina exatamente na temperatura de equilíbrio sólido-líquido, Teq,SL. É proposta uma metodologia experimental para determinar a temperatura de saturação de óleos parafínicos. A partir de resultados reométricos pode-se notar que a magnitude do superresfriamento influencia a taxa de nucleação e o tamanho final dos cristais precipitados. O tamanho da região metaestável é influenciado pela taxa de resfriamento e pela temperatura inicial do teste. A partir de microscopia de campo claro observa-se que quanto maior o superresfriamento maior o número de cristais formados. Pode-se adiantar que a morfologia e o tamanho dos cristais formados influenciam o comportamento reológico do óleo parafínico em baixas temperaturas. / Waxy crude oil is a complex mixture of hydrocarbons consisting of paraffins, aromatics, naphthenes, asphaltenes and resins. At low temperatures the solubility of high molecular weight components in the oil is decreased and especially the n-paraffins tend to precipitate as crystal structures. These crystals provide a non-Newtonian behavior to the fluid, tend to deposit in the inner surface of pipelines and are responsible for the gelation of the oil when the flow is interrupted. In such cases, the pressure needed to restart the oil flow in subsea pipelines can be much larger than the usual steady-state pressure as the temperature in such environment can be as low as 4 °C. The literature has shown that not only the temperature itself but also the fluid shear and thermal histories have significant influence on the yield stress of waxy crude oils. The current work shows the effect of the initial cooling temperature on the waxy crude oil viscosity, gelation temperature and critical stress. It is showed that the initial cooling temperature affects the mechanical behavior of crude oils at low temperature. It is presented that crystallization is the process where an ordered solid structure is formed from a disordered phase. This process involves two main stages, namely nucleation and crystals growth. As paraffins nucleation is a stochastic process, a supercooling is needed to the onset of this phenomenon. In other words precipitation of crystals could not take place at the solidliquid equilibrium thermodynamic temperature, Teq,SL. Therefore, during the cooling, it is required that the fluid reaches a certain temperature, below the Teq,SL, to initiate the nucleation process. This work proposes an experimental procedure to determine consistently the highest solid-liquid thermodynamic equilibrium temperature. By means of rheometric tests, it is showed that the supercooling affects the nucleation rate and the crystals morphology, and also it is influenced by the cooling rate and the initial cooling temperature. One can conclude that the higher the supercooling the higher the number of crystals and, as consequence, the lower the crystals length. Finally, the crystals morphology and the length affect the mechanical properties of the waxy oil.

Orientadora: Profa. Dra. Ivanise Gaubeur / Tese (doutorado) - Universidade Federal do ABC, Programa de Pós-Graduação em Ciência e Tecnologia/Química, Santo André, 2018. / Dois novos procedimentos de extração que utilizam materiais extratores não-convencionais são apresentados nesta tese. A utilização de cera de parafina derretida como um extrator químico permitiu agregar as principais vantagens da extração em fase líquida (homogeneidade do extrato, curto tempo de extração e simplicidade de operação) na extração em fase sólida, delineando um procedimento inovador. O papel matte foi outro material estudado nesse trabalho e mostrou-se interessante como extrator químico, especialmente pelo baixo custo dessa fase sólida. Como prova de conceito, o íon metálico cobre (II) em solução aquosa foi utilizado para o desenvolvimento da metodologia. O extrato resultante de ambos os procedimentos de extração foi analisado diretamente por Espectrometria de Emissão Óptica com Plasma Induzido por LASER (LIBS). Os fatores que afetam a reação de complexação, a extração e a detecção do analito na fase sólida foram otimizados num estudo univariado. Nas melhores condições encontradas, foram construídas curvas de calibração numa faixa linear de 0,50 até 10,00 mg L-1 e alcançados limites inferiores de detecção de 0,12 mg L-1 e 0,08 mg L-1 de cobre (II) em solução aquosa, para os procedimentos com cera de parafina e com o papel matte, respectivamente. A precisão de ambos os métodos propostos mostrou-se inferior a 5% e a exatidão foi avaliada por: (i) análise de material de referência certificado de soro sanguíneo humano; (ii) ensaios de adição e recuperação do analito em amostras líquidas de composição química distintas (água mineral, água do mar, água de torneira, cachaça, refrigerante e urina humana) e (iii) comparação dos resultados obtidos com os fornecidos pelo método de Espectrometria de Absorção Atômica com Forno de Grafite. Ambos os procedimentos se destacaram pela: (i) elevada eficiência no processo de extração (>94%); (ii) facilidade de execução; (iii) baixo custo e inocuidade dos extratores; (iv) microhomogeneidade das fases sólidas obtidas; (v) possibilidade de préconcentração de íons metálicos e (vi) superação das dificuldades intrínsecas na análise de líquido por LIBS. / Two new extraction procedures that use non-conventional extractant materials are described in this thesis. The use of melted paraffin wax as a chemical extractant allowed to aggregate the main advantages of the liquid phase extraction (homogeneity of the extract, short extraction time and simplicity of operation) in solid phase extraction, delineating an innovative procedure. The matte paper was another material studied in this work and was interesting as a chemical extractant, especially for the low cost of this solid phase. As proof of concept, the copper (II) ion in aqueous solution was applied for the development of the methodology. The extract obtained from both extraction procedures was analyzed directly by LASER-Induced Breakdown Spectroscopy (LIBS). The parameters that affecting the complexation reaction, extraction and analyte detection in the solid phase were optimized in a univariate approach. Under the best conditions, calibration curves were constructed in a linear range of 0.50 to 10.00 mg L-1 and lower detection limits of 0.12 mg L-1 and 0.08 mg L-1 of copper (II) in aqueous solution were obtained, for the procedures with paraffin wax and matte paper, respectively. The precision of both methods was less than 5% and accuracy was assessed by: (i) analysis of certified reference material of human blood serum; (ii) spike and recovery analyte in liquid samples of different chemical compositions (seawater, tap water, mineral water, cachaça, soft drink and human urine) and (iii) comparison of the results obtained with those provided by the Graphite Furnace Atomic Absorption Spectrometry. Both procedures were highlighted by: (i) high efficiency in the extraction process (> 94%); (ii) ease of execution; (iii) low cost and safety of extractants; (iv) microhomogeneity of the solid phases obtained; (v) the ability of preconcentration metal ions and (vi) overcoming the intrinsic drawbacks in liquid analysis by LIBS.

Ph. D. (Department of Chemical Engineering, Faculty of Engineering and Technology), Vaal University of Technology. / Investment casting process is the most suitable technique for producing high quality castings which are dimensionally accurate with excellent surface finish and complex in nature. Recently with the ever-changing manufacturing landscape, the process has been increasingly used to produce components for the medical, aerospace and sports industry. The present study looked at three investigative scenarios in the development of a pattern material for investment casting process: (i) the development of wax/ethyl vinyl acetate (EVA) and wax/linear low-density polyethylene (LLDPE) blends as the carrier vehicle materials for the development of pattern material for investment casting; (ii) the development of wax/EVA/polymethyl methacrylate (PMMA) based investment casting pattern and lastly (iii) the development of wax/LLDPE/PMMA based investment casting pattern material. The first part of the studies elucidates the effects in terms of the thermal, mechanical, surface and rheological properties when paraffin wax in blended with poly EVA and LLDPE. The developments involved the extrusion of seven formulations for EVA and also LLDPE using a twin-screw extrusion compounder. The paraffin wax weight percent investigated ranged from 33% to 87% thus encompassing both low and high wax loading ratios. The thermal properties of the developed binary blends were characterized via thermogravimetric analysis (TGA) and differential scanning calorimetry (DSC). The mechanical properties were characterized using three-point bending test. The thermo-mechanical and rheological properties were determined using thermomechanical analysis (TMA) and a rheometer respectively. A scanning electron microscope (SEM) was used to study the surface texture of the extruded blends. The thermal properties indicated that the thermal stability of paraffin wax is improved when it is blended with both EVA and LLDPE. DSC curves showed two endothermic melting peaks and two exothermic crystallisation peaks. In the case of wax/EVA blends, there was no distinct peak showing the independent melting of neat wax and EVA. The peak at a temperature of 50 – 72 °C corresponds to the melting of the wax/EVA blend. In the case of wax/LLDPE blends, the peak at 50 -66 °C corresponds to the melting of wax whereas the large peak at 112 - 125°C corresponds to the melting of the LLDPE. Wax/EVA and wax/LLDPE had improved mechanical properties as compared to that of neat wax. The rheological properties of both the EVA based and LLDPE based blends indicated that the viscosity of the blends increased as compared to that of neat wax. SEM confirmed that EVA alters the wax crystal habit at higher concentrations. In the case of wax/LLDPE blends, at 20-30 % wax content, a heterogeneous surface was observed, indicating the immiscibility of the paraffin wax within the LLDPE matrix. At a high wax content, there was agglomeration of wax. LLDPE allows amorphous structure of wax to disperse easily between the chains. The second part of the studies focussed on the wax/EVA filled with poly (methyl methacrylate) (PMMA) microbeads. TGA behaviour on the pyrolysis of wax/EVA/PMMA showed that the compounds volatilise readily with virtually no residue remaining above 500 °C. The DSC curves indicated that, the incorporation of PMMA reduced the crystallinity of wax/EVA blend. A distinct endothermic peak and another small peak was observed in all the formulations. The mechanical properties of wax/EVA/PMMA improved significantly. The methylene group present in both wax and EVA combined to form a blend with enhanced mechanical properties whereas the PMMA microbeads improved the needle penetration hardness. The melt viscosity of wax/EVA/PMMA increased as the EVA and/or the PMMA content is increased. The rheological experimental data fitted with the data predicted using the modified Krieger and Dougherty expression. The maximum attainable volume fraction of suspended PMMA particles was at max = 0.81. The SEM micrograph of wax/EVA/PMMA revealed a near perfect spherical nature for the filler particles in the wax/EVA polymer matrix. It further shows that the PMMA microbeads were weakly bonded and well distributed in the wax/EVA matrix. The third part of the studies focussed on the wax/LLDPE filled with Poly (methyl methacrylate) (PMMA) microbeads. The incorporation of LLDPE and PMMA into paraffin wax had a strong influence on the thermal properties, tensile properties, flow properties and its morphology. The TGA analysis showed that there was a slight observable decrease in the melting onset temperatures when the wax content was increased. From the DSC curves, the corresponding values of onset temperatures observed are between melting and crystallization temperature of neat paraffin wax and neat LLDPE. The short chains of the paraffin wax and the fragments formed by scission of wax chain have sufficient energy to escape from the matrix at lower temperatures. The slight decrease in peak temperatures associated with melting and crystallization could be attributed to the decrease in the average lamellar thickness of the blends. The tensile properties by three-point bending tests indicated an increase in the stress with an increase in the LLDPE content. This can be attributed to the formation of paraffin wax crystals in the amorphous phase of the blend which may influence the chain mobility. Since the paraffin wax used for this study had a low viscosity as compared to LLDPE, both LLDPE or PMMA had an influence on the viscosities of the blends. The data obtained from the experiments fitted with the data predicted obtained from the modified Krieger and Dougherty expression. The maximum attainable volume fraction of suspended PMMA particles was at max = 0.74. Similar observation with that of wax/EVA/PMMA was made in terms of the morphology of the wax/LLDPE/PMMA blends. The excellent thermal stabilities, the superior mechanical strength of wax/EVA/PMMA and wax/LLDPE/PMMA and the flow properties with relatively high EVA and also with high PMMA loadings, open new opportunities for EVA and LLDPE based pattern material for in investment casting process. It is worth pursuing further comprehensive studies since it offers a strong potential for realizing further technological improvement in the field of investment casting and rapid prototyping technologies.

From the Proceedings of the 1974 Meetings of the Arizona Section - American Water Resources Assn. and the Hydrology Section - Arizona Academy of Science - April 19-20, 1974, Flagstaff, Arizona / Reported are laboratory evaluations to screen water-repellent materials and treatments before testing them in the field. Water repellency tests were conducted on paraffin wax, a wax emulsion and silicon, lard, and a liquid dust suppressant. Six water repellency tests showed that the high rates of paraffin wax and all rates of the dust suppressant produced highly water-repellent soil surfaces. The six water repellency tests were: (1) the aqueous-alcohol drop test for determination of the 90 degree surface tension for a porous solid, (2) the water drop penetration time test, (3) the relative height of a large sessile water drop resting on the smoothed, treated soil surface, (4) and (5) the presence and persistence of air bubbles trapped between the soil-water interface, and test (6) was made to note whether the large sessile water drop from test (3) would infiltrate the soil or evaporate. Tests (3), (4), and (5) proved the most useful of the six methods for measuring water repellency. Soil type had no significant influence on degree of water repellency as measured in the laboratory by these six tests.