This thesis studies wet granulation on three different levels. First, micro-level investigations of liquid bridges between two and three particles are performed. For the two-particle case, the fluid profile of static (stationary) and dynamic (moving) liquid bridges are investigated. Static liquid bridges between three equally sized primary particles are then studied; the symmetry of the problem is used to obtain a numerical solution to the Young-Laplace equation. Secondly, a model to estimate the stickiness (fractional wet surface area) of agglomerates is proposed. The model includes parameters to control the inter-particle separation distance and the fluid saturation state. Computational geometry is used to obtain results which relate the number of particles and the volume of binder fluid to the stickiness of the agglomerates. Finally, a population balance model for wet granulation is developed by extending an earlier model to incorporate the effects of binder fluid. The model is solved numerically for a range of coalescence kernels and results are presented which show the effect of binder volume and the drying rate.
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This thesis studies wet granulation on three different levels. First, micro-level investigations of liquid bridges between two and three particles are performed. For the two-particle case, the fluid profile of static (stationary) and dynamic (moving) liquid bridges are investigated. Static liquid bridges between three equally sized primary particles are then studied; the symmetry of the problem is used to obtain a numerical solution to the Young-Laplace equation. Secondly, a model to estimate the stickiness (fractional wet surface area) of agglomerates is proposed. The model includes parameters to control the inter-particle separation distance and the fluid saturation state. Computational geometry is used to obtain results which relate the number of particles and the volume of binder fluid to the stickiness of the agglomerates. Finally, a population balance model for wet granulation is developed by extending an earlier model to incorporate the effects of binder fluid. The model is solved numerically for a range of coalescence kernels and results are presented which show the effect of binder volume and the drying rate.
Patrick completed BSc(Hons) and PhD degrees in Mathematical Physics at Massey University, New Zealand and later worked as a Postdoctoral Fellow in the Institute of Fundamental Sciences, Massey University. Patrick has a range of technical expertise in the areas of parallel/high performance computing and scientific software.
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Kartoniert / Broschiert. Condición: New. Dieser Artikel ist ein Print on Demand Artikel und wird nach Ihrer Bestellung fuer Sie gedruckt. Autor/Autorin: Rynhart PatrickPatrick completed BSc(Hons) and PhD degrees in MathematicalnPhysics at Massey University, New Zealand and later worked as anPostdoctoral Fellow in the Institute of Fundamental Sciences,nMassey University. Patrick has a. Nº de ref. del artículo: 4949928
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Taschenbuch. Condición: Neu. Mathematical Modelling of Granulation Processes | Patrick Rynhart | Taschenbuch | Einband - flex.(Paperback) | Englisch | 2009 | VDM Verlag Dr. Müller | EAN 9783639019773 | Verantwortliche Person für die EU: OmniScriptum GmbH & Co. KG, Bahnhofstr. 28, 66111 Saarbrücken, info[at]akademikerverlag[dot]de | Anbieter: preigu. Nº de ref. del artículo: 101646789
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Taschenbuch. Condición: Neu. nach der Bestellung gedruckt Neuware - Printed after ordering - This thesis studies wet granulation on threedifferent levels. First, micro-level investigationsof liquid bridges between two and three particles areperformed. For the two-particle case, the fluidprofile of static (stationary) and dynamic (moving)liquid bridges are investigated. Static liquidbridges between three equally sized primary particlesare then studied; the symmetry of the problem is usedto obtain a numerical solution to the Young-Laplaceequation. Secondly, a model to estimate thestickiness (fractional wet surface area) ofagglomerates is proposed. The model includesparameters to control the inter-particle separationdistance and the fluid saturation state.Computational geometry is used to obtain resultswhich relate the number of particles and the volumeof binder fluid to the stickiness of theagglomerates. Finally, a population balance model forwet granulation is developed by extending an earliermodel to incorporate the effects of binder fluid. Themodel is solved numerically for a range ofcoalescence kernels and results are presented whichshow the effect of binder volume and the drying rate. Nº de ref. del artículo: 9783639019773
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