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Auteur Jürgen Miethlinger
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Institute of Polymer Extrusion Compouding - Johannes Kepler University - Linz - Austria
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Analyzing the influence of surface renewal on diffusive mass transport in vented single-screw extruders / Christian Marschik in INTERNATIONAL POLYMER PROCESSING, Vol. XXXII, N° 3 (07/2017)
[article]
Titre : Analyzing the influence of surface renewal on diffusive mass transport in vented single-screw extruders Type de document : texte imprimé Auteurs : Christian Marschik, Auteur ; B. Löw-Baselli, Auteur ; Jürgen Miethlinger, Auteur Année de publication : 2017 Article en page(s) : p. 387-393 Note générale : Bibliogr. Langues : Anglais (eng) Catégories : Extrudeuse monovis
Matières plastiques -- Extrusion
Modèles numériques
RhéologieIndex. décimale : 668.4 Plastiques, vinyles Résumé : We present a semi-numerical modeling approach to analyzing the role of surface renewal during bubble-free devolatilization in vented single-screw extruders. To demonstrate the significance of surface renewal in the mass transport of volatiles, we derived approximate analytical solutions for the two-dimensional circulatory flow in a partially filled screw channel, placing special emphasis on the melt pool that forms in front of the active flight. By applying the resulting velocity field to the governing conservation equation for the volatile concentration in the polymeric phase, the convective influence of the polymer flow on mass transport is taken into account. The resulting convection-diffusion equation, which is solved numerically using the finite-volume method, provides both qualitative and quantitative insights into how volatile depletion in the melt pool is related to the flow field developed. Thus, we clearly demonstrate that surface renewal improves mass transport efficiency considerably, even at very low screw speeds. Note de contenu : DEVOLATILIZATION IN VENTED SINGLE-SCREW EXTRUDERS : Mass transport in partially filled screw channels - Modeling diffusive mass transport in the melt pool
- MODELING FRAMEWORK : Modeling the flow in the melt pool - Modeling diffusive mass transport in moving fluids
- RESULTS AND DISCUSSION : Circulatory flow in the melt pool - Influence of surface renewal on diffusive mass transport - Influence of test parametersDOI : 10.3139/217.3373 En ligne : https://drive.google.com/file/d/1r3j9c2fG8H0VagHWgCOr3jqZyDxlzMFY/view?usp=drive [...] Format de la ressource électronique : Permalink : https://e-campus.itech.fr/pmb/opac_css/index.php?lvl=notice_display&id=28840
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Code-barres Cote Support Localisation Section Disponibilité 19064 - Périodique Bibliothèque principale Documentaires Disponible Application of the network simulation method to flat dies with inverted prelands / Thomas Köpplmayr in INTERNATIONAL POLYMER PROCESSING, Vol. XXVIII, N° 3 (07/2013)
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Titre : Application of the network simulation method to flat dies with inverted prelands Type de document : texte imprimé Auteurs : Thomas Köpplmayr, Auteur ; Jürgen Miethlinger, Auteur Année de publication : 2013 Article en page(s) : p. 322-330 Note générale : Bibliogr. Langues : Anglais (eng) Catégories : Algèbre
Analyse mathématique
Ecoulement tridimensionnel
Ecoulement visqueux
Etat fondu (matériaux)
Fluide de CarreauLe fluide de carreau est un type de fluide newtonien généralisé où la viscosité, dépend du taux de cisaillement.
Fluides, Mécanique des
Polymères
Simulation, Méthode deIndex. décimale : 668.4 Plastiques, vinyles Résumé : We present a systematic approach based on Kirchhoff’s laws that uses tensor algebra and analytical formulae obtained from constitutive equations for the analysis of flow resistance networks. The flow of a Carreau fluid in a flat die with inverted preland is analyzed in terms of mass flow, velocity, and residence time distributions. Viscous heating is taken into account by using an analytical model which depends on the Cameron number of the flow at different positions. Further, we report the results of a three-dimensional simulation, using the commercially available ANSYS Polyflow software, which are in good agreement with our numerical study. Note de contenu : - MODELING FRAMEWORK : Implementation of carreau model - Network analysis - Numerical determination of flow coefficients - Viscous dissipation
- SIMULATIONDOI : 10.3139/217.2758 En ligne : https://drive.google.com/file/d/1EabP6OgqMVCfCO3seu19wDS6XUf2gwnt/view?usp=drive [...] Format de la ressource électronique : Permalink : https://e-campus.itech.fr/pmb/opac_css/index.php?lvl=notice_display&id=19022
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Code-barres Cote Support Localisation Section Disponibilité 15238 - Périodique Bibliothèque principale Documentaires Disponible Balanced mixing screw for single-screw extruder / Christian Marschik in KUNSTSTOFFE INTERNATIONAL, Vol. 108, N° 6 (06-07/2018)
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Titre : Balanced mixing screw for single-screw extruder : Design of mixing elements for demanding extrusion processes Type de document : texte imprimé Auteurs : Christian Marschik, Auteur ; Otto Skrabala, Auteur ; Jürgen Miethlinger Année de publication : 2018 Article en page(s) : p. 46-49 Langues : Anglais (eng) Catégories : Malaxeurs et mélangeurs
Matières plastiques -- Extrusion -- Appareils et matériels
Vis d'extrusion simpleIndex. décimale : 668.4 Plastiques, vinyles Résumé : The homogenization of the melt – for example when coloring plastic – is a fundamental prerequisite for good end product quality in extrusion. Homogeneity is determined to a large extent by the mixing section. However, a supposedly intensive mixer is not always the best choice. Note de contenu : - Variety of geometries
- Result 1 - Velocity field
- Result 2 - Pressure consumption
- Result 3 - Dissipation
- Result 4 - Distributive mixing
- Result 5 - Stretching
- Conclusion : Basis for new geometries
- Table : lnvestigated single-screw mixer geometries : the number of flights and blocks was varied; the identical single screw no. 3 and 5 serves as the reference geometry
- Fig. 1 : Investigated block-head mixers : the nominal dia-meter of the block-head mixers is 60 mm. Reference geometries 3 and 5 are identical
- Fig. 2 : Velocity field of high-molecular HDPE pipe grades : a) in the axial direction, b) in the cross-section of one block, and c) in the cross-section in between two blocks
- Fig. 3 : Pressure loss: influence of the number of flights per block (a) and blocks (b)
- Fig. 4 : Dissipation: influence of the number of flights per block (a) and blocks (b)
- Fig. 5 : Particle distribution for geometry 1: a) at the start and b) at the end of the block-head mixer
- Fig. 6 : Particle distribution at the end of the block-head mixer: a) for geometry 1 and b) geometry 8
- Fig. 7 : Particle surface stretching at the end of the block-head mixers: influence of the number of flights per block and blocksEn ligne : https://drive.google.com/file/d/1iyPeNsI01amr1CobMm3433IKSohAmXst/view?usp=drive [...] Format de la ressource électronique : Permalink : https://e-campus.itech.fr/pmb/opac_css/index.php?lvl=notice_display&id=31030
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Code-barres Cote Support Localisation Section Disponibilité 20081 - Périodique Bibliothèque principale Documentaires Disponible Control strategies for reactive extrusion of polypropylene by peroxide degradation - A brief review and an experimental study / S. Wolf in INTERNATIONAL POLYMER PROCESSING, Vol. 36, N° 5 (2021)
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Titre : Control strategies for reactive extrusion of polypropylene by peroxide degradation - A brief review and an experimental study Type de document : texte imprimé Auteurs : S. Wolf, Auteur ; Jürgen Miethlinger, Auteur Année de publication : 2021 Article en page(s) : p. 472-498 Note générale : Bibliogr. Langues : Anglais (eng) Catégories : Capteurs (technologie)
Contrôle technique
Essais (technologie)
Extrudeuse bi-vis
Extrusion réactive
Formulation (Génie chimique)
Peroxydes
PolypropylèneIndex. décimale : 668.4 Plastiques, vinyles Résumé : Industry 4.0 and digitalization are widely argued for the future success of numerous industrial solutions. Big data management might lead to the assumption that every issue can be solved numerically without any physical background. To some extent, this strategy will help within the plastics industry in general and in the extrusion technology in particular. However, a deep process knowledge together with process-relevant sensors, as well as the right process arrangements within the processing chain combined with smart data mining methods will be still the key success of industry 4.0. This presentation illustrates, based on a brief review on existing control strategies (Part 1), including sensory and predictive control models for reactive extrusion applied at a real-life on-site best practice project (Part 2), possibilities in combination of process tasks with digitalization approaches for PP-Polymer production. Specifically, rheological research conducted with a novel, patented multi-point rheometer (part 3), will provide a deeper insight into dynamic processes such as reactive extrusion. With those results and derivations thereof, improvements in predictive process control in addition to artificial control systems are made and might even lead to further interesting opportunities. Note de contenu : - BRIEF REVIEW ON CONTROL STRATEGIES FOR REACTIVE EXTRUSION (Part 1) : Control strategies : extrusion control - Soft sensors - Reactive extrusion in general - Reactive extrusion process control of peroxide modified pp
- PRACTICAL IMPLEMENTATION OF REACTIVE EXTRUSION CONTROL (PART 2) : Background and problem definition - Theses/proposal for solution - Proof of concept on twin-screw extruder - Smart process engineering and control - Results/validation of the implementation on world-scale production site/adjustable melt quality based on in-line-viscosity measurements
- VALIDATION/PROOF OF HYSTERESIS BEHAVIOR WITH SMART SENSORS (PART 3) : Setup and principal test procedure for lab-scale trials - Extensional rheometer/smart process quality device - Results/effect of peroxide during ramp-up and ramp-down (220 °c) - Results/effect of peroxide during ramp-up and ramp-down (temperature variation) - Discussion
- Table 1 : Literature review based on Garge et al. (2010) of “modelling of reactive extrusion" and “process control of reactive extrusion
- Table 2 : Characteristics of polymer grades (unstabilized powder samples from reactor) for peroxide trials and relevant Russian standards (RussianGOST, 2019)
- Table 3 : Standard process parameters for the trials
- Table 4 : Formulations for evaluating the ramp-up and ramp-down behavior of PP polymer melts; given quantities are weight percent (wt%) of polymer, masterbatch or premix, whereas the active concentration of peroxide is 10%DOI : https://doi.org/10.1515/ipp-2020-4088 En ligne : https://drive.google.com/file/d/1wDJx2TwgcvJxRJJfcOLY5DGzuum0nuva/view?usp=shari [...] Format de la ressource électronique : Permalink : https://e-campus.itech.fr/pmb/opac_css/index.php?lvl=notice_display&id=36516
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Code-barres Cote Support Localisation Section Disponibilité 23735 - Périodique Bibliothèque principale Documentaires Disponible Flow behavior of a polypropylene melt in capillary dies read more / L.-S. Pan in INTERNATIONAL POLYMER PROCESSING, Vol. XXXIII, N° 5 (11/2018)
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Titre : Flow behavior of a polypropylene melt in capillary dies read more Type de document : texte imprimé Auteurs : L.-S. Pan, Auteur ; H.-J. Luger, Auteur ; Jürgen Miethlinger, Auteur ; W. Friesenbichler, Auteur Année de publication : 2018 Article en page(s) : p. 642-651 Note générale : Bibliogr. Langues : Anglais (eng) Catégories : Etat fondu (matériaux)
Modèles mathématiques
Polypropylène
RhéologieIndex. décimale : 668.4 Plastiques, vinyles Résumé : Using capillary dies having different diameters, D, and length-to-diameter L/D ratios, a full rheological characterization has been carried out for a polypropylene melt, and the experimental data have been fitted both with a viscous model (Cross) and a viscoelastic one (the Kaye – Bernstein, Kearsley, Zapas/Papanastasiou, Scriven, Macosko or K-BKZ/PSM model). Particular emphasis has been given on the pressure-dependence of viscosity. It was found that only the viscoelastic simulations were capable of reproducing the experimental data well, while any viscous modeling always underestimates the pressures, especially at the higher apparent shear rates and L/D ratios. Note de contenu : - EXPERIMENTAL : Materials and rheological methods
- MATHEMATICAL MODELING : Governing equations - Non-isothermal modeling - pressure dependent modeling
- METHOD OF SOLUTION
- RESULTS AND DISCUSSION : Rheological characterization - Capillary dies simulationsDOI : 10.3139/217.3581 En ligne : https://www.degruyter.com/document/doi/10.3139/217.3581/pdf Format de la ressource électronique : Permalink : https://e-campus.itech.fr/pmb/opac_css/index.php?lvl=notice_display&id=31403
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Code-barres Cote Support Localisation Section Disponibilité 20352 - Périodique Bibliothèque principale Documentaires Disponible A gas-sensor-based measurement setup for inline quality and process control in polymer extrusion / Michael Aigner in INTERNATIONAL POLYMER PROCESSING, Vol. XXIX, N° 4 (08/2014)
PermalinkA generalized 2D output model of polymer melt flow in single-screw extrusion / S. Pachner in INTERNATIONAL POLYMER PROCESSING, Vol. XXXII, N° 2 (05/2017)
PermalinkKeeping track of elongation / Sven Wolf in KUNSTSTOFFE INTERNATIONAL, Vol. 108, N° 1-2 (01-02/2018)
PermalinkModeling and estimation of the pressure and temperature dependent bulk density of polymers / Christian Kneidinger in INTERNATIONAL POLYMER PROCESSING, Vol. XXXV, N° 1 (03/2020)
PermalinkModelling the solids feed section in rooved-feed extruders / Jürgen Miethlinger in KUNSTSTOFFE PLAST EUROPE, Vol. 93, N° 4/2003 (04/2003)
PermalinkProcessing of metallic pigments in a co-rotating twin-screw extruder studied by means of dielectric analysis and terahertz spectroscopy / Alexander Lepschi in INTERNATIONAL POLYMER PROCESSING, Vol. XXXI, N° 4 (08/2016)
PermalinkVerifying the melting behavior in single-screw plasticization units using a novel simulation model and experimental method / M. Aigner in INTERNATIONAL POLYMER PROCESSING, Vol. XXIX, N° 5 (11/2014)
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