Abstract:Filament stretching rheometry is a prominent experimental method to determine rheological properties in extensional flow whereby the separating plates determine the extension rate. In literature, several correction factors that can compensate for the errors introduced by the shear contribution near the plates have been introduced and validated in the linear viscoelastic regime. In this work, a systematic analysis is conducted to determine if a material-independent correction factor can be found for non-linear … Show more
“…Using a full slip boundary condition, the flow type is predominantly extension along the complete lateral surface of the fiber, similar to the simulation results without the fiber inclusion. , Only at the tip of the fiber a slight appearance of shear flow is present. The size of the shear area remains constant throughout the elongation of the filament.…”
Section: Resultssupporting
confidence: 79%
“…The material, rheological, and experimental parameters used for the simulation are given in Table . Here, the viscosity is obtained by taking the shear viscosity at an effective shear rate of 3ε̇ for the iPP 1 material used in the work of Roozemond et al at a temperature of 160 °C . The obtained value is then shifted to a temperature of 133 °C using the Arrhenius equation …”
Section: Numerical Modelingmentioning
confidence: 99%
“…The work of van Berlo et al , is followed for applying the mesh movement and remeshing and projection procedure in the numerical simulation. − Here, a detailed explanation of the finite element model can be found. Analogously, the controller of the radius, which is added to ensure the radius decreases exponentially such that the strain rate is constant, is adopted from the work of Román Marín et al The domain Ω is discretized using triangular, isoparametric, P 2 –P 1 (Taylor-Hood) elements for the interpolation of the velocity and pressure.…”
Morphology development at the fiber/matrix interphase in fiber-reinforced isotactic polypropylene composites is a widely studied topic. While the application of shear flow may strongly enhance the nucleation density around the fiber, little is known about the influence of fibers on the crystallization of polypropylene subjected to an extensional flow. In this work, the flow around a single glass fiber upon uniaxial elongation of the melt is examined using X-ray scattering and diffraction techniques and compared to the response measured for the neat matrix. A comparison between a neat and compatibilized matrix is made given the strong influence of the addition of an adhesion modifier on the bulk crystallization kinetics of polypropylene. The flow is applied using an in-house-built filament stretching extensional rheometer, which, due to its midfilament control scheme, allows for in situ X-ray experiments. Combined small-angle X-ray scattering/wide-angle X-ray diffraction patterns are acquired during the flow and subsequent crystallization step. Postcrystallization area scans of the filament show that the introduction of a single glass fiber gives rise to the development of β-phase crystals, particularly in the area around the fiber ends, and in contrast to what is observed for the matrix materials alone, where solely α-phase is found. Surprisingly enough, the addition of a single fiber (0.00045 vol %) alters the crystallizing polymorph in almost the entire filament. However, the addition of the adhesion modifier hinders the formation of β-phase crystals around the fiber due to an acceleration of the bulk crystallization kinetics. Finite element simulations provide insight into the flow field around the fiber during stretching and demonstrate that the flow is no longer uniaxial extension, but dominated by shear, even though the volumetric amount of fiber as compared to the matrix is negligible. These findings explain the experimental observation of substantial β-phase formation after the introduction of a single fiber, while this is not observed in the matrix material. Worth noting, the formation of β-phase polypropylene depends not only on the presence and the strength of the flow but predominantly on the type of flow, i.e., shear as opposed to elongation.
“…Using a full slip boundary condition, the flow type is predominantly extension along the complete lateral surface of the fiber, similar to the simulation results without the fiber inclusion. , Only at the tip of the fiber a slight appearance of shear flow is present. The size of the shear area remains constant throughout the elongation of the filament.…”
Section: Resultssupporting
confidence: 79%
“…The material, rheological, and experimental parameters used for the simulation are given in Table . Here, the viscosity is obtained by taking the shear viscosity at an effective shear rate of 3ε̇ for the iPP 1 material used in the work of Roozemond et al at a temperature of 160 °C . The obtained value is then shifted to a temperature of 133 °C using the Arrhenius equation …”
Section: Numerical Modelingmentioning
confidence: 99%
“…The work of van Berlo et al , is followed for applying the mesh movement and remeshing and projection procedure in the numerical simulation. − Here, a detailed explanation of the finite element model can be found. Analogously, the controller of the radius, which is added to ensure the radius decreases exponentially such that the strain rate is constant, is adopted from the work of Román Marín et al The domain Ω is discretized using triangular, isoparametric, P 2 –P 1 (Taylor-Hood) elements for the interpolation of the velocity and pressure.…”
Morphology development at the fiber/matrix interphase in fiber-reinforced isotactic polypropylene composites is a widely studied topic. While the application of shear flow may strongly enhance the nucleation density around the fiber, little is known about the influence of fibers on the crystallization of polypropylene subjected to an extensional flow. In this work, the flow around a single glass fiber upon uniaxial elongation of the melt is examined using X-ray scattering and diffraction techniques and compared to the response measured for the neat matrix. A comparison between a neat and compatibilized matrix is made given the strong influence of the addition of an adhesion modifier on the bulk crystallization kinetics of polypropylene. The flow is applied using an in-house-built filament stretching extensional rheometer, which, due to its midfilament control scheme, allows for in situ X-ray experiments. Combined small-angle X-ray scattering/wide-angle X-ray diffraction patterns are acquired during the flow and subsequent crystallization step. Postcrystallization area scans of the filament show that the introduction of a single glass fiber gives rise to the development of β-phase crystals, particularly in the area around the fiber ends, and in contrast to what is observed for the matrix materials alone, where solely α-phase is found. Surprisingly enough, the addition of a single fiber (0.00045 vol %) alters the crystallizing polymorph in almost the entire filament. However, the addition of the adhesion modifier hinders the formation of β-phase crystals around the fiber due to an acceleration of the bulk crystallization kinetics. Finite element simulations provide insight into the flow field around the fiber during stretching and demonstrate that the flow is no longer uniaxial extension, but dominated by shear, even though the volumetric amount of fiber as compared to the matrix is negligible. These findings explain the experimental observation of substantial β-phase formation after the introduction of a single fiber, while this is not observed in the matrix material. Worth noting, the formation of β-phase polypropylene depends not only on the presence and the strength of the flow but predominantly on the type of flow, i.e., shear as opposed to elongation.
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