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A new model for the drying of droplets containing suspended solids

A new model for the drying of droplets containing suspended solids. C.S. Handscomb, M. Kraft and A.E. Bayly Wednesday 19 th September, 2007. outline. Motivation Industrial Application The Drying Process Model Description Results for a Sodium Sulphate Droplet. motivation - spray drying.

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A new model for the drying of droplets containing suspended solids

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  1. A new model for the drying of droplets containing suspended solids C.S. Handscomb, M. Kraft and A.E. Bayly Wednesday 19th September, 2007

  2. outline • Motivation • Industrial Application • The Drying Process • Model Description • Results for a Sodium Sulphate Droplet

  3. motivation - spray drying • An important technology in industry • Used to produce, for example: • Pharmaceuticals • Food stuffs (e.g. milk powder and coffee) • Detergents • Unique drying technology combining moisture removal and particle formation

  4. motivation – spray drying Consider droplet drying in a spray dryer Droplets dry by atomisation and contact with hot drying air Consider a single droplet Droplets contain suspended solids Continuous phase may be either single- or multi-component

  5. particle morphologies Solid Particle Collapse ‘Puffed’ Particle Re-inflation ‘Dry Shell’ High temperature ‘Wet Shell’ A. Cheyne, D. Wilson and D. Bridgwater, Spray Dried Detergent Particles, unpublished, 2003 A. Cheyne, D. Wilson and D. Bridgwater, Spray Dried Detergent Particle, unpublished, 2003 Internal Bubble Nucleation Crust Formation Saturated Surface Drying Initial Droplet Blistered (Burst) Particle Shrivelled Particle Inflated, Hollow Particle

  6. particle morphologies No particle formation Solid Particle Collapse Low solids concentration <1%w/w ‘Puffed’ Particle Re-inflation ‘Dry Shell’ High temperature A. Lee and C.Law. ‘Gasification and shell characteristics in slurry droplet burning’ Combust. Flame,85(1): 77-93, 1991 ‘Wet Shell’ Internal Bubble Nucleation Crust Formation Saturated Surface Drying Initial Droplet Tsapis et al. ‘Onset of buckling in Drying Droplets of Colloidal Suspensions’ Phys. Rev. Let. 94(1), 2005 Blistered (Burst) Particle Shrivelled Particle Inflated, Hollow Particle

  7. Demonstrates the core features of the new model particle morphologies • Focus on drying prior to shell formation in this paper Solid Particle Collapse ‘Puffed’ Particle Re-inflation ‘Dry Shell’ High temperature ‘Wet Shell’ Internal Bubble Nucleation Crust Formation Saturated Surface Drying Initial Droplet Blistered (Burst) Particle Shrivelled Particle Inflated, Hollow Particle

  8. new drying model • Assumptions in the present model: • Three component system: • A – solvent; • B – solute; • D – solid • Spherical particles, 1D model • Small Biot number  uniform particle temperature • Allow for a single centrally located bubble Assumed ideal binary solution

  9. discrete phase • Population balance for solids • Spherical symmetry  reduce to 1-D • One internal and one external coordinate external coordinate internal coordinate diffusion term advection term • Solve for the moments of this equation

  10. discrete phase • Principle variable of interest is solids volume fraction • Related to the moments of the population balance equation by: • Integer moments of the internal coordinate

  11. discrete phase • Stokes-Einstein equation for solids diffusion coefficient • Moment evolution equation • Equation system is unclosed with size dependent diffusion coefficient Particle nucleation rate per unit volume

  12. discrete phase • Moment hierarchy closed by linear extrapolation on a log-scale • 4 PDEs required to describe the discrete phase

  13. continuous phase Volume Averages Superficial Intrinsic Total • Volume averaged equations for the continuous phase • Assume Fickian diffusion is primary transport mechanism evolution diffusion crystallization advection

  14. continuous phase • Advection velocity arises due to density difference between the solute and solvent

  15. continuous phase • Effective diffusion coefficient is a strong function of local solids fraction and solute mass fraction • Diffusion coefficient must be obtained from experiments

  16. continuous phase • Continuous phase equation coupled to the population balance through the last term • 1 PDE required to describe the continuous phase • 5 coupled PDEs in total

  17. continuous phase

  18. Consider only low temperature drying Initially ideal shrinkage Droplet radius decreases as particles are free to move At some point, shell formation occurs boundary conditions

  19. Zero solute mass flux following receding interface External solute boundary condition boundary conditions

  20. Droplet shrinkage rate boundary conditions Solvent mass flux to the bulk calculated using standard correlations based on a partial pressure driving force

  21. Population balance boundary condition… …which gives BCs for the moments Solids remain wetted and are drawn inwards by capillary forces between particles boundary conditions ;

  22. numerical implementation • Apply coordinate transformation to all equations • Time derivatives are transformed according to A virtual flux is introduced into all evolution equations

  23. sodium sulphate droplet • Simulate the drying of a droplet of sodium sulphate solution • Initial conditions: • Solute content: 14 wt% (near saturated) • Droplet temperature: 20 C • Solids volume fraction: 1.1 x 10-12

  24. sodium sulphate droplet • Crystallisation kinetics D. Rosenblatt, S. Marks and R. Pigford ‘Kinetics of phase transitions in the system sodium sulfate-water’ Ind Eng Chem23(2): 143-147, 1984 • Nucleation kinetics (heterogeneous) J. Dirksen and T. Ring. ‘Fundamentals of crystallization: Kinetic effect on particle size distributions and morphology. Chem Eng Sci,46(10): 2389-2427, 1991

  25. sodium sulphate droplet Experimental data taken from: S. Nesic and J. Vodnik. ‘Kinetics of droplet evaporation’ Chem Eng Sci,46(2): 527-537, 1991

  26. sodium sulphate droplet • Radial solute profiles Profiles plotted at 5s intervals Saturated solute mass fraction = 0.34

  27. sodium sulphate droplet • Integrated moments

  28. sodium sulphate droplet • Spatially resolved particle number density Profiles plotted at 5s intervals

  29. sodium sulphate droplet • Spatially resolved solids volume fraction Profiles plotted at 1s intervals

  30. conclusions • Spray dying to form particles is an important and complex industrial process • Outlined droplet drying model incorporating a population balance to describe the solid phase • New model capable of enhanced morphological prediction

  31. acknowledgements

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