In this paper we present an exponential stability result for a diffusion equation arising from dumbbell models for polymer flow. Using the methods of semigroup theory, we show that the semigroup U(t) associated with the diffusion equation is well defined and that all solutions converge exponentially to an equilibrium solution. Both finitely and infinitely extensible dumbbell models are considered. The main tool in establishing stability is the proof of compactness of the semigroup. / Ph. D.

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Simulation of viscoelastic fluid flows in complex geometry at high Weissenburg (Wi) number is still a challenging problem in computational rheology. In this thesis, parallel computing toolbox available in OpenFOAM has been analysed in details. The scalability of parallel viscoelastic flow solver has been critically evaluated under benchmark flow problems, including 2D and 3D 4:1 contraction flow, 2D flow past a cylinder with 50% blockage, using up to 4096 CPU cores and 55 million computational grids. Areas for further improvements in parallel computational rheology are discussed. A new monitoring and preserving molecular conformation method is proposed to overcome the unphysical artefact problem in simulation of the FENE-CD-JS model under benchmark flow problems. It greatly enhances the stability of parallel viscoelastic flow solver in simulation of high Wi number flows and, for the first time, successfully captures elastic turbulence in flow past a cylinder problem. A new constitutive model, named as FENE-CD2-JS model, is proposed to overcome the existing shortcomings of the original FENE dumbbell model. The model accounts for high order interactions between non-equilibrium polymer chain molecules and could reproduce the asymmetric oscillatory vortex dynamics in the 16:1 contraction flow geometry at high Wi number (up to 48) flow observed in the experiments. For the first time, the analysis of the spatial distribution of non-equilibrium polymer conformation, through the conformational tensor, in strong complex flow and the results of their power-law scaling are also presented.

The main focus of this work is on the non-Newtonian effects on the inertial instabilities in shear flows. Both inelastic (Carreau) and elastic models (Oldroyd-B and FENE-P) have been employed to examine the main features of the non-Newtonian fluids; shear-thinning, shear-thickening and elasticity. Several classical configurations have been considered; flow past a circular cylinder, in a lid-driven cavity and in a channel. We have used a wide range of tools for linear stability analysis, modal, non-modal, energy and sensitivity analysis, to determine the instability mechanisms of the non-Newtonian flows and compare them with those of the Newtonian flows. Direct numerical simulations have been also used to prove the results obtained by the linear stability analysis. Significant modifications/alterations in the instability of the different flows have been observed under the action of the non-Newtonian effects. In general, shear-thinning/shear-thickening effects destabilize/stabilize the flow around the cylinder and in a lid driven cavity. Viscoelastic effects both stabilize and destabilize the channel flow depending on the ratio between the viscoelastic and flow time scales. The instability mechanism is just slightly modified in the cylinder flow whereas new instability mechanisms arise in the lid-driven cavity flow. We observe that the non-Newtonian effect can alter the inertial flow at both baseflow and perturbation level (e.g. Carreau fluid past a cylinder or in a lid driven cavity) or it may just affect the perturbations (e.g. Oldroyd-B fluid in channel). In all the flow cases studied, the modifications in the instability dynamics are shown to be strongly connected to the contribution of the different terms in the perturbation kinetic energy budget. / <p>QC 20140113</p>

The flow of polymer solutions in the high Elasticity number, El, regime in complex geometries may lead to strong viscoelastic behaviour and eventually become unstable as the Weissenberg number, Wi, is increased beyond a critical level. So far, the success of numerical simulations in predicting the highly non-linear behaviour of polymer solutions in complex flows has been limited. In this thesis, selected constitutive models are evaluated under the high El flow regime in the cross-slot and contraction benchmark flows using a numerical technique based on the finite volume method. The numerical technique is implemented within the OpenFOAM framework and thoroughly validated in the benchmark flow. A modification to the FENE dumbbell model based on the non-affine deformation of polymer solutions is proposed, which enabled the prediction of some non-linear material functions and also enhanced numerical stability, allowing a higher Wi to be attained. Asymmetric flow instability in the cross-slot flow has been studied. Time-dependent stability diagrams were constructed based on Wi and the strain, ε, both of which govern the stretching of a polymer chain. In the contraction flow, elastic instability is simulated for the first time in this geometry. Substantial time-dependent asymmetric flow patterns were predicted as seen in experiments. The effect of the contraction ratio is investigated through a stability diagram. Three-dimensional finite element simulations were also carried out to study the effect of the aspect ratio in the contraction flow of a Phan-Thien-Tanner fluid. The simulations suggest that a lip vortex mechanism is a signature for the onset of strong viscoelastic behaviour.

[pt] Soluções poliméricas diluídas podem ser usadas na indústria de Óleo e Gás para injeção em reservatórios de petróleo como agentes de controle de mobilidade em técnicas de recuperação avançada de óleo, com o objetivo de aumentar o fator de recuperação do campo e postergar a indesejada alta taxa de produção de água. No entanto, o fenômeno macroscópico esperado, aumento da eficiência de varrido, é influenciado diretamente por fatores microscópicos que ocorrem na escala de poro. Devido às suas grandes cadeias moleculares, ao avançar através do meio poroso, soluções poliméricas de alto peso molecular dificultam o avanço da água alterando a razão de mobilidades água/óleo. Porém, o estudo de escoamento de soluções poliméricas ainda é um desafio devido ao comportamento não Newtoniano da relação vazão x diferença de pressão e à sensibilidade a diversos fatores como: tipo de polímero utilizado, concentração, razão de viscosidades, temperatura, salinidade e taxa de cisalhamento. O presente trabalho analisa a implementação de dois modelos constitutivos, Oldroyd-B e FENE-CR, aplicados ao método de solução de elementos finitos, EF, utilizando a formulação dos resíduos ponderados de Galerkin para modelar o escoamento de soluções poliméricas diluídas através de capilares com constrição e entender os fenômenos viscosos e elásticos envolvidos. Os resultados obtidos fornecem uma descrição mais detalhada da aplicação dos modelos testados e do escoamento de soluções poliméricas diluídas em gargantas de poros. / [en] Diluted polymeric solutions can be used in Oil & Gas industry for reservoir injection as mobility control agents in enhanced oil recovery technics, which goal is to increase the oil field recovery factor and postpone the high water production rates. However, the macroscopic expected phenomena, increase of the areal sweep, is directly influenced by microscopic factors that occurs at the pore scale. Due to their huge molecular chains, by advancing through the porous media, high molecular weight polymer solutions hinder the water flow changing the water/oil mobility ratio. Nevertheless, the comprehension of polymeric solutions flow is still a great challenge due to the Non-Newtonian behavior of the flow rate x pressure gradient relation and the sensibility to several variables such as: type of polymer used, concentration, viscosity ratio, temperature, salinity and shear rate. The present work analyzes the implementation of two constitutive models, Oldroyd-B and FENE-CR, coupled with the Finite Element method using the Galerkin weighted residual formulation to model the flow of diluted polymeric solutions through constricted capillaries and understand the viscous and elastic phenomena involved. The obtained results provide a more detailed portrait of the constitutive models and the flow of diluted polymeric solutions through pore throats.