Coupled Temperature-Displacement Modelling of Injection Stretch Blow Moulding of PET bottles using Buckley Model

This study presents a fully coupled temperature–displacement finite element modelling of the injection stretch-blow moulding (ISBM) process of polyethylene terephthalate (PET) bottles using ABAQUS with a view to optimising the process conditions. A physically-based material model (Buckley model) was used to predict the mechanical behaviour of PET at temperatures slightly above its glass transition temperature. A model incorporating heat transfer between the stretch rod, the preform and the mould was built using axisymmetric solid elements. Extensive finite element analyses were carried out to predict the deformation, the distribution and history of strain and temperature during ISBM of a 20 g–330 ml bottle, which was made in an in situ test on a Sidel SB06 machine. Comparisons of numerical results with the measurements demonstrate that the model can satisfactorily model the sidewall thickness and material distributions. It is also shown that significant non-linear differentials exist in temperature and strain in both bottle thickness and length directions during the process. This justifies the employment of a volume approach to accurately predict the final mechanical properties of the bottles governed by the orientation and crystallinity which are highly temperature and strain dependent.

Anomalous flow behaviour of bauxite tailings

This paper deals with the anomalous flow behaviour observed in two bauxite tailings pumping systems, with 450 mm and 680 mm outer diameter. In order to enlarge the pipeline lengths in the field, tests were carried out in a laboratory test-loop in order to try to understand the anomalous (intermittent) flow behaviour and to solve the problem. Based on data obtained from these laboratory tests and using a generalized REYNOLDS number it was possible to obtain results that fit the MOODY ROUSE diagram.

Layered silicate nanocomposites based on various high-functionality epoxy resins. Part II: The influence of an organoclay on the rheological behavior of epoxy prepolymers

The effect of an organically surface modified layered silicate on the viscosity of various epoxy resins of different structures and different functionalities was investigated. Steady and dynamic shear viscosities of the epoxy resins containing 0-10 wt% of the organoclay were determined using parallel plate rheology. Viscosity results were compared with those achieved through addition of a commonly used micron-sized CaCO3 filler. It was found that changes in viscosities due to the different fillers were of the same order, since the layered silicate was only dispersed on a micron-sized scale in the monomer (prior to reaction), as indicated by X-ray diffraction measurements. Flow activation energies at a low frequency were determined and did not show any significant changes due to the addition of organoclay or CaCO3. Comparison between dynamic and steady shear experiments showed good agreement for low layered silicate concentrations below 7.5 wt%, i.e. the Cox-Merz rule can be applied. Deviations from the Cox-Merz rule appeared at and above 10 wt%, although such deviations were only slightly above experimental error. Most resin organoclay blends were well predicted by the Power Law model, only concentrations of 10 wt% and above requiring the Herschel-Buckley (yield stress) model to achieve better fits. Wide-angle X-ray measurements have shown that the epoxy resin swells the layered silicate with an increase in the interlayer distance of approximately 15 Angstrom, and that the rheology behavior is due to the lateral, micron-size of these swollen tactoids.

Modelling of poly(ethylene terephthalate) in injection stretch-blow moulding

Simulations of the injection stretch-blow moulding process have been developed for the manufacture of poly(ethylene terephthalate) bottles using the commercial finite element package ABAQUS/standard. Initially a simulation of the manufacture of a 330 mL bottle was developed with three different material models (hyperelastic, creep, and a non-linear viscoelastic model (Buckley model)) to ascertain their suitability for modelling poly(ethylene terephthalate). The Buckley model was found to give results for the sidewall thickness that matched best with those measured from bottles off the production line. Following the investigation of the material models, the Buckley model was chosen to conduct a three-dimensional simulation of the manufacture of a 2 L bottle. It was found that the model was also capable of predicting the wall thickness distribution accurately for this bottle. In the development of the three-dimensional simulation a novel approach, which uses an axisymmetric model until the material reaches the petaloid base, was developed. This resulted in substantial savings in computing time. © 2000 IoM Communication Ltd.

Influence des caractéristiques rhéologiques des bétons autoplaçants sur leur durabilité

Résumé : De même degré d’importance que les paramètres de formulation, les conditions de consolidation sont des facteurs déterminants pour la durabilité des bétons conventionnels vibrés. Dans le cas des bétons autoplaçants (BAP), grâce à leur grande fluidité, la mise en place dans les coffrages a lieu par écoulement libre sous l’effet de leur poids propre. Leur consolidation se fait sans vibration grâce à leurs caractéristiques rhéologiques. Il est donc légitime de penser que les caractéristiques rhéologiques des BAP peuvent avoir une influence importante sur les propriétés qui déterminent la durabilité. Cette thèse étudie les liens possibles entre les caractéristiques rhéologiques des BAP et leur durabilité vis-à-vis du transport des agents agressifs. Dix-sept formulations de BAP couvrant une large gamme de caractéristiques rhéologiques et se différenciant uniquement par leur dosage en adjuvants ont été étudiées à cet effet. Trois modèles rhéologiques classiques ont été mis en œuvre pour la détermination des paramètres rhéologiques des bétons étudiés. L’essai de sorptivité et dans une moindre mesure l’essai de carbonatation accélérée ont été utilisés comme indicateur de durabilité vis-à-vis du transport des agressifs. La durabilité de la couche superficielle au contact respectivement avec le coffrage en bois et en PVC a été étudiée et les résultats ont été comparés à la durabilité du béton à cœur. Cette étude a été faite en tenant compte des échanges hydriques et de l’arrangement granulaire au droit du coffrage. D’autre part, l’étude de la durabilité de la couche superficielle dans des conditions de mise en place proches du chantier a été faite sur 6 poutres partiellement armées longues de 2 m ainsi que sur 3 bétons semi-autoplaçants légèrement vibrés. Les résultats montrent qu’il existe une corrélation forte entre la viscosité plastique du modèle Bingham modifié ou le coefficient de consistance du modèle Herschel-Bulkley et la sorptivité. Très probablement, la viscosité agit sur le volume relatif des pores capillaires de gros diamètres. L’étude spécifique de la couche superficielle a montré que sa sorptivité dépend du type de coffrage utilisé à cause des éventuels échanges hydriques opérés entre le béton et la surface du coffrage. De plus, l’arrangement granulaire au droit du coffrage est également influencé. Ainsi, la sorptivité de la couche superficielle au contact du PVC est proche mais inférieure à celle du béton à cœur. La sorptivité de la couche superficielle au contact du bois est significativement inférieure à celle de la couche superficielle au contact du PVC tout en restant corrélé avec la viscosité plastique du modèle Bingham modifié ou le coefficient de consistance du modèle Herschel-Bulkley.

Avaliação e modelagem reológica de fluido de perfuração base água

The determination of the rheology of drilling fluids is of fundamental importance to select the best composition and the best treatment to be applied in these fluids. This work presents a study of the rheological behavior of some addictives used as viscosifiers in water-based drilling fluids. The evaluated addictives were: Carboxymethylcellulose (CMC), Xanthan gum (GX), and Bentonite. The main objective was to rheologically characterize suspensions composed by these addictives, by applying mathematical models for fluid flow behavior, in order to determine the best flow equation to represent the system, as well as the model parameters. The mathematical models applied in this research were: the Bingham Model, the Ostwald de Wale Model, and the Herschel-Bulkley Model. A previous study of hydration time for each used addictive was accomplished seeking to evaluate the effect of polymer and clay hydration on rheological behavior of the fluid. The rheological characterization was made through typical rheology experiments, using a coaxial cylinder viscosimeter, where the flow curves and the thixotropic magnitude of each fluid was obtained. For each used addictive the rheological behavior as a function of temperature was also evaluated as well as fluid stability as a function of the concentration and kind of addictive used. After analyses of results, mixtures of polymer and clay were made seeking to evaluate the rheological modifications provided by the polymer incorporation in the water + bentonite system. The obtained results showed that the Ostwald de Waale model provided the best fit for fluids prepared using CMC and for fluids with Xanthan gum and Bentonite the best fit was given by the Herschel-Bulkley one

Friction factors and rheological properties of orange juice

The rheological behavior of Brazilian orange juice with different water content (0.34-0.73 w/w) was studied at a wide range of temperatures (0.5-62 degrees C) using a concentric cylinder viscometer. The results indicated that the juices behave as pseudoplastic fluids with yield stress, being represented by the Herschel-Bulkley model. The rheological parameters were fitted as functions of both temperature and water content in the tested range. Based on dimensional analysis it was proposed a modified Reynolds number (Re-M), which includes the Herschel-Bulkley parameters. Experimental data of friction factors during heating and cooling processes of orange juice in laminar flow through circular tubes could be well correlated as a function of Re-M. (C) 1999 Elsevier B.V. Ltd. All rights reserved.

Rheological Analysis of Water Clay Compositions in Order to Investigate Mudflows Developing in Canals

Fundação de Amparo à Pesquisa do Estado de São Paulo (FAPESP)

Estudo da influência da granulometria no comportamento reológico de polpa de bauxita e no fator de atrito

O presente trabalho apresenta estudos de caracterização reológica e determinações de fatores de atrito em três polpas de bauxita, originárias da Mina de Miltônia, Paragominas – Pará, resultantes de condições operacionais com graus diferentes de moagem. Deste modo, a diferenciação básica entre as mesmas reside na distribuição granulométrica. O objetivo é fazer uma proposta de revisão da especificação granulométrica do produto (polpa de bauxita para o mineroduto), permitindo uma comparação com as polpas do projeto (planta piloto) e da operação atual (usina de beneficiamento) quanto a resposta a alterações, principalmente, da viscosidade e fatores de atrito. A polpa proposta incorpora um percentual maior de finos (< 10 microns) em relação as demais polpas. Os benefícios possibilitarão ganhos de recuperação com a incorporação desta parcela de finos, a qual atualmente é descartada para a bacia de rejeitos. O material foi caracterizado por análises granulométricas da série Tyler, físicas e físico-químicas, microscopia eletrônica de varredura (MEV) e espectrometria de raios-x dispersiva em energia (EDS). Utilizando-se de um viscosímetro de cilindros coaxiais, tipo Searle, abordo use os aspectos reológicos destas polpas, em função da sua distribuição granulométrica e da variação da concentração de sólidos. As propriedades reológicas avaliadas foram a viscosidade, a tensão de escoamento e também os comportamentos que mostram a dependência da viscosidade com o tempo de aplicação de uma taxa de cisalhamento constante, verificando-se por meio de curva de histerese, a existência ou não da tixotropia e da reopexia. Os resultados experimentais mostraram que para as polpas ensaiadas, a granulometria e a concentração de sólidos são parâmetros relevantes na determinação da viscosidade. Os testes com estas três polpas de bauxita, de granulometrias diferentes, foram realizados a concentrações pré-determinadas, de modo a determinar o modelo reológico cujos parâmetros apresentaram os melhores coeficientes de correlação (R²), sendo que os melhores ajustes encontrados foram segundo o modelo de Herschel-Bulkley. Os fatores de atrito foram obtidos por formulações que envolvem uma relação logarítmica, utilizando-se da Lei da Parede como método de obtenção das expressões aplicáveis a estes fluidos não- Newtonianos viscoplásticos, sendo comparados com os calculados pelas correlações de Dodge e Metzner e verificou-se que de uma maneira geral há a concordância entre o modelo estudado nas três polpas. A análise dos fatores de atrito na concentração de 50% de sólidos, concentração de bombeio por mineroduto, mostra que o comportamento das polpas estudadas é semelhante, com os melhores ajustes para a faixa de 10.000 a 100.000 Reynolds (faixa média de trabalho para o escoamento turbulento de polpas de minério, homogêneas e heterogêneas).

Rheological behavior of Brazilian Cherry (Eugenia uniflora L.) pulp at pasteurization temperatures

Neste trabalho, foi estudado o comportamento reológico da polpa de pitanga na faixa de temperatura de pasteurização de 83 a 97 °C. Os resultados indicaram que a polpa apresentou comportamento pseudoplástico e o modelo de Herschel-Bulkley foi considerado o mais adequado para representar o comportamento reológico do produto nas temperaturas estudadas. Os índices de comportamento de fluido (n) variaram na faixa de 0,448 a 0,627. O efeito da temperatura sobre a viscosidade aparente pôde ser descrito pela equação análoga à de Arrenhius, observando-se a diminuição da viscosidade aparente da polpa de pitanga com o aumento da temperatura.

Designing radical business model innovation : a case study

“The process of innovation is often seen as being very linear, with research results, new technologies or user insights being channelled, often prematurely, into specific products and process” (Kyffin and Gardien 2009). It is precisely this perception of innovation-as-linear-process which this paper seeks to challenge. While there are many current theories and much contemporary literature available which discuss the management and catalysts of innovation, what is missing are examples of how innovation occurs from the application of these theories and literature (Wrigley & Bucolo 2010). This paper addresses both this gap and perceptions of the viability of linear innovation by presenting a case study for the commercialisation of a core technology (a cleantech, semi-portable mass-energy generator posited as a direct competitor to conventional energy provision systems), within an 18-month timeframe by the use of the Design-Led Innovation approach: “a process of creating a sustainable competitive advantage by radically changing the customer value proposition” (Bucolo & Matthews 2011).