Non-Newtonian Fluid Flow Model For Ceramic Tape Casting
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The fluid mechanics associated with the flow of a ceramic slurry during the tape casting process is analyzed in this paper. The rheology of the slurry is described in generalized terms using the Ostw One of the parameters that influences the final tape thickness is the side flow factor (α) which is mostly measured at the end of the process by a volumetric comparison of the tape which flowed outside the casting width to the tape within the casting width. This phenomenon has not been predicted theoretically yet in the literature. Abstract The main goal of this work is to study the multiple material flows in side-by-side (SBS) tape casting and analyze the influence of the different material properties, i.e. the density and the viscosity, on the interface between the fluids, since this is highly important for the efficiency of a graded configuration of the magnetocaloric materials. The Newtonian flow
Power law fluids and Bingham plastics flow models for ceramic tape
One of the most challenging parts of modelling the flow of the ceramic slurry in the tape casting process is to conduct the modelling with the proper constitutive equation which governs the material’s rheological behaviour. In general, this rheological behaviour can be classified by five different material types as shown in Fig. 1. For Newtonian fluids, the shear stress t has a linear In this paper, the migration of secondary particles in a non-Newtonian ceramic slurry in the tape casting process is investigated with the purpose of understanding the particle distribution It is crucial that the green tape thickness is controlled precisely and consistently. The fluid mechanics associated with the flow of a ceramic slurry during the tape casting process is analyzed.
It is crucial that the green tape thickness is controlled precisely and consistently. The fluid mechanics associated with the flow of a ceramic slurry during the tape casting process is analyzed. The flow of the slurry onto the casting surface can be modeled as a two-dimensional fluid flow through a parallel channel. A translucent Newtonian model fluid which, in the relevant processing window, at higher shear rates, exhibits a rheological behavior similar to that of a typical ceramic slurry, was chosen to Jabbari M, Spangenberg J, Hattel JH (2016) Particle migration using local variation of the viscosity (LVOV) model in flow of a non-Newtonian fluid for ceramic tape casting.
Bingham plastic fluid flow model in tape casting of ceramics using two doctor blades – analytical approach Masoud JabbariJ. Hattel Engineering, Materials Science 2014 Particle migration using local variation of the viscosity (LVOV) model in flow of a non-Newtonian fluid for ceramic tape casting In this paper, the migration of secondary particles in a non-Newtonian ceramic slurry inthe tape casting process is investigated with the purpose of understanding the particle distribution patterns along the casting direction. The Ostwald-de Flow of particles inside a non-Newtonian ceramic slurry during tape casting is mainly dictated by two competing forces: (1) hydrostatic forces due to fluid column in the reservoir and gravity, and (2) viscous forces as a results of moving substrate (v casting).
An evaluation of interface capturing methods in a VOF based model for multiphase flow of a non-Newtonian ceramic in tape casting, Applied Mathematical Modelling, 38(13), 2014, 3222-3232. Tape casting has been used to produce thin layers of ceramics that can be used as single layers or can be stacked and laminated into multilayered structures. Today, tape casting is the basic fabrication process that provides multilayered capacitors and multilayered ceramic packages. In tape casting the rheological behaviour of the slurry as well as the material flow during casting
Power Law Fluids and Bingham Plastics Flow Models for Ceramic Tape Casting
内容提示: Materials Science and Engineering A280 (2000) 282–288Non-Newtonian fluid flow model for ceramic tape castingAlfred I.Y. Tok, Freddy Y.C. Boey *, Y.C. LamSchool of Mechanical and Production Engineering, Nanyang Technological Uni?ersity, Nanyang A?enue, Singapore 639798, SingaporeReceived 13 September 1998; received in revised form 27 September The fluid flow model was first developed for a single fluid in the tape casting process and validated both from a mathematical view point [8] but also from a process technology view point [9].
One of the parameters that influences the final tape thickness is the side flow factor (α) which is mostly measured at the end of the process by a volumetric comparison of the tape which flowed outside the casting width to the tape within the casting width. This phenomenon has not been predicted theoretically yet in the literature.
The ceramic slurry in the tape casting process is normally categorised as a non-Newtonian fluid with relatively high viscosity. A summary of works published regarding the rheological classification of non-Newtonian fluids and the existence of analytical/numerical models with focus on tape casting has been reviewed previously by Journal of Materials Processing Technology 120 (2002) 215±225 Power law ¯uids and Bingham plastics ¯ow models for ceramic tape casting Sunil C. Joshi*, Y.C. Lam, F.Y.C. Boey, A.I.Y. Tok School of Mechanical and Production Engineering, Nanyang Technological University, Nanyang Avenue, Singapore 639798, Singapore Received 1 June 2001 Abstract A generalized pressure
Download scientific diagram | Rheological classification of fluids. from publication: Numerical Modeling of the Flow of a Power Law Ceramic Slurry in the Tape Casting Process | Multilayer ceramics
The fluid mechanics associated with the flow of a ceramic slurry during the tape casting process is analyzed in this paper. The rheology of the slurry is described in generalized terms using the In this paper, the migration of secondary particles in a non-Newtonian ceramic slurry inthe tape casting process is investigated with the purpose of understanding the particle distribution patterns along the casting direction. The Ostwald-de Waele power law model for the non-Newtonian flow behaviour is assumed in the simulation of the ceramic slurry flow.A local variation of the
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Jabbari et al. [7] evaluated different interface methods when simulating a multiphase flow of non-Newtonian ceramic slurries in tape casting. They state that any one of three equations – Bingham, Herschel–Bulkley or Ostwald-de-Waele power law constitutive equations – could be used to model non-Newtonian fluids (like ceramic slurries).
Bingham plastic fluid flow model in tape casting of ceramics using two doctor blades – analytical approach M. JabbariJ. Hattel Materials Science 2014 In this paper, the migration of secondary particles in a non-Newtonian ceramic slurry in the tape casting process is investigated with the purpose of understanding the particle distribution patterns along the casting direction. The Ostwald-de Waele power law model for the non-Newtonian flow behaviour is assumed in the simulation of the ceramic slurry flow. A local
Various constitutive models have been proposed to quantify a wide range of non-Newtonian fluids, but there is lack of a systematic classification and evaluation of these competing models, such as the quantitative comparison between the classical integer-order constitutive models and the newly proposed fractional derivative equations for non-Newtonian fluids. This In this paper, the migration of secondary particles in a non-Newtonian ceramic slurry in the tape casting process is investigated with the purpose of understanding the particle distribution University of Leeds – Cited by 1,784 – CFD/Complex Flow – Porous Media – Ceramic Manufacturing – Additive Manufacturing – Battery Manufacturing
Generalized Fluid Flow Model for Ceramic Tape Casting. Journal of the American Ceramic Society 1995, 78 (9) , 2497-2503. https://doi.org/10.1111/j.1151-2916.1995.tb08691.x Bingham plastic fluid flow model in tape casting of ceramics using two doctor blades – analytical approach M. Jabbari, J. Hattel Materials Science 2014
The details of fluid flow in tape casting of a Newtonian slurry with a parallel blade are analyzed in terms of the relative magnitudes of the driving forces (wall shear and pressure gradient) and th Hydrodynamics viscous flow – Newtonian fluids boundary layer non-Newtonian fluids particle dynamics – fluidized beds turbulence and mixing – jets, wakes flow over aerofoils – cascades propellers, fans, windmills appendix.
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