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Mathematical Modelling of Granulation Processes

Patrick Rynhart

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06 March 2009
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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.

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RRP: $109.21
$88.00
Ships in 3-5 business days
Hurry up! Current stock:

Mathematical Modelling of Granulation Processes

RRP: $109.21
$88.00

Description

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.

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