3 Dynamics of Spray Granulation in Continuously …
105
5. Peglow, M., Kumar, J., Heinrich, S., Warnecke, G., Tsotsas, E., Mörl, L., Wolf, B.: A generic
population balance model for simultaneous agglomeration and drying in fluidized beds. Chem.
Eng. Sci. 62(1–2), 513–532 (2007)
6. Seydel, P., Blömer, J., Bertling, J.: Modeling particle formation at spray drying using population
balances. Drying Technol. 24(2), 137–146 (2006)
7. Vreman, A., van Lare, C., Hounslow, M.: A basic population balance model for fluidized bed
spray granulation. Chem. Eng. Sci. 64, 4389–4398 (2009)
8. Maronga, S.J., Wnukowski, P.: Modelling of the three-domain fluidized-bed particulate coating
process. Chem. Eng. Sci. 52(17), 2915–2925 (1997)
9. Sherony, D.F.: A model of surface renewal with application to fluid bed coating of particles.
Chem. Eng. Sci. 36(5), 845–848 (1981)
10. Wnukowski, P., Setterwall, F.: The coating of particles in a fluidized bed (residence time
distribution in a system of two coupled perfect mixers). Chem. Eng. Sci. 44(3), 493–505
(1989)
11. Bück, A., Neugebauer, C., Meyer, K., Palis, S., Diez, E., Kienle, A., Heinrich, S., Tsotsas, E.:
Influence of operation parameters on process stability in continuous fluidized bed layering with
external classification. Powder Technol. 300, 37–45 (2016)
12. Dreyschultze, C., Neugebauer, C., Palis, S., Bück, A., Tsotsas, E., Heinrich, S., Kienle, A.:
Influence of zone formation on stability of continuous fluidized bed spray granulation with
external product classification. Particuology 23, 1–7 (2015)
13. Hampel, N., Bück, A., Peglow, M., Tsotsas, E.: Continuous pellet coating in a Wurster fluidized
bed process. Chem. Eng. Sci. 86, 87–98 (2013)
14. Neugebauer, C., Palis, S., Bück, A., Tsotsas, E., Heinrich, S., Kienle, A.: A dynamic two zone
model of continuous fluidized bed layering granulation with internal product classification.
Particuology 31, 8–14 (2017)
15. Mörl, L., Heinrich, S., Peglow, M.: Fluidized bed spray granulation. In: Granulation, Handbook
of Powder Technology (Chap. 2), vol. 11, pp 21–188. Elsevier, Amsterdam (2007)
16. Rieck, C., Hoffmann, T., Bück, A., Peglow, M., Tsotsas, E.: Influence of drying conditions on
layer porosity in fluidized bed spray granulation. Powder Technol. 272, 120–131 (2015)
17. Meyer, K., Bück, A., Tsotsas, E.: Determination of particle exchange rates at over-flow weirs
in horizontal fluidised beds by particle tracking velocimetry. Particuology 32, 1–9 (2017)
18. Boucher, D., Deng, Z., Leadbeater, T., Langlois, R., Renaud, M., Waters, K.: PEPT studies of
heavy particle flow within a spiral concentrator. Miner. Eng. 62, 120–128 (2014)
19. Nilsson, L., Wimmerstedt, R.: Residence time distribution and particle dispersion in a
longitudinal-flow fluidised bed. Chem. Eng. Sci. 43, 1153–1160 (1988)
20. Satija, S., Zucker, I.: Hydrodynamics of vibro-fluidized beds. Drying Technol. 4, 19–43 (1986)
21. de Velden, M.V., Baeyens, J., Seville, J., Fan, X.: The solids flow in the riser of a circulating
fluidised bed (CFB) viewed by positron emission particle tracking (PEPT). Powder Technol.
183, 290–296 (2008)
22. Börner, M., Peglow, M., Tsotsas, E.: Derivation of parameters for a two compartment population
balance model of Wurster fluidized bed granulation. Powder Technol. 238, 122–131 (2013)
23. Hagemeier, T., Börner, M., Bück, A., Tsotsas, E.: A comparative study on optical techniques
for the estimation of granular flow velocities. Chem. Eng. Sci. 131, 63–75 (2015a)
24. Hagemeier, T., Roloff, C., Bück, A., Tsotsas, E.: Estimation of particle dynamics in 2-D fluidized beds using particle tracking velocimetry. Particuology 22, 39–51 (2015b)
25. Bendicks, C., Tarlet, D., Roloff, C., Bordas, R., Wunderlich, B., Michaelis, B., Thevenin, D.:
Improved 3-D particle tracking velocimetry with colored particles. J. Sign. Inf. Process. 2,
59–71 (2011)
26. Capart, H., Young, D., Zech, Y.: Voronoi imaging methods for the measurement of granular
flows. Exp. Fluids 32, 121–135 (2002)
27. You, C., Zhao, H., Cai, Y., Qi, H., Xu, X.: Experimental investigation of interparticle collision
rate in particulate flow. Int. J. Multiph. Flow 30, 1121–1138 (2004)
28. Charlou, C., Sauceau, M., Milhe, M., Arlabosse, P.: Application of Markov chains to the
modeling of sludge flow in an agitated indirect continuous dryer. In: Proceedings of European
Symposium on Drying (EuroDrying 2013), Paris (2013)
105
5. Peglow, M., Kumar, J., Heinrich, S., Warnecke, G., Tsotsas, E., Mörl, L., Wolf, B.: A generic
population balance model for simultaneous agglomeration and drying in fluidized beds. Chem.
Eng. Sci. 62(1–2), 513–532 (2007)
6. Seydel, P., Blömer, J., Bertling, J.: Modeling particle formation at spray drying using population
balances. Drying Technol. 24(2), 137–146 (2006)
7. Vreman, A., van Lare, C., Hounslow, M.: A basic population balance model for fluidized bed
spray granulation. Chem. Eng. Sci. 64, 4389–4398 (2009)
8. Maronga, S.J., Wnukowski, P.: Modelling of the three-domain fluidized-bed particulate coating
process. Chem. Eng. Sci. 52(17), 2915–2925 (1997)
9. Sherony, D.F.: A model of surface renewal with application to fluid bed coating of particles.
Chem. Eng. Sci. 36(5), 845–848 (1981)
10. Wnukowski, P., Setterwall, F.: The coating of particles in a fluidized bed (residence time
distribution in a system of two coupled perfect mixers). Chem. Eng. Sci. 44(3), 493–505
(1989)
11. Bück, A., Neugebauer, C., Meyer, K., Palis, S., Diez, E., Kienle, A., Heinrich, S., Tsotsas, E.:
Influence of operation parameters on process stability in continuous fluidized bed layering with
external classification. Powder Technol. 300, 37–45 (2016)
12. Dreyschultze, C., Neugebauer, C., Palis, S., Bück, A., Tsotsas, E., Heinrich, S., Kienle, A.:
Influence of zone formation on stability of continuous fluidized bed spray granulation with
external product classification. Particuology 23, 1–7 (2015)
13. Hampel, N., Bück, A., Peglow, M., Tsotsas, E.: Continuous pellet coating in a Wurster fluidized
bed process. Chem. Eng. Sci. 86, 87–98 (2013)
14. Neugebauer, C., Palis, S., Bück, A., Tsotsas, E., Heinrich, S., Kienle, A.: A dynamic two zone
model of continuous fluidized bed layering granulation with internal product classification.
Particuology 31, 8–14 (2017)
15. Mörl, L., Heinrich, S., Peglow, M.: Fluidized bed spray granulation. In: Granulation, Handbook
of Powder Technology (Chap. 2), vol. 11, pp 21–188. Elsevier, Amsterdam (2007)
16. Rieck, C., Hoffmann, T., Bück, A., Peglow, M., Tsotsas, E.: Influence of drying conditions on
layer porosity in fluidized bed spray granulation. Powder Technol. 272, 120–131 (2015)
17. Meyer, K., Bück, A., Tsotsas, E.: Determination of particle exchange rates at over-flow weirs
in horizontal fluidised beds by particle tracking velocimetry. Particuology 32, 1–9 (2017)
18. Boucher, D., Deng, Z., Leadbeater, T., Langlois, R., Renaud, M., Waters, K.: PEPT studies of
heavy particle flow within a spiral concentrator. Miner. Eng. 62, 120–128 (2014)
19. Nilsson, L., Wimmerstedt, R.: Residence time distribution and particle dispersion in a
longitudinal-flow fluidised bed. Chem. Eng. Sci. 43, 1153–1160 (1988)
20. Satija, S., Zucker, I.: Hydrodynamics of vibro-fluidized beds. Drying Technol. 4, 19–43 (1986)
21. de Velden, M.V., Baeyens, J., Seville, J., Fan, X.: The solids flow in the riser of a circulating
fluidised bed (CFB) viewed by positron emission particle tracking (PEPT). Powder Technol.
183, 290–296 (2008)
22. Börner, M., Peglow, M., Tsotsas, E.: Derivation of parameters for a two compartment population
balance model of Wurster fluidized bed granulation. Powder Technol. 238, 122–131 (2013)
23. Hagemeier, T., Börner, M., Bück, A., Tsotsas, E.: A comparative study on optical techniques
for the estimation of granular flow velocities. Chem. Eng. Sci. 131, 63–75 (2015a)
24. Hagemeier, T., Roloff, C., Bück, A., Tsotsas, E.: Estimation of particle dynamics in 2-D fluidized beds using particle tracking velocimetry. Particuology 22, 39–51 (2015b)
25. Bendicks, C., Tarlet, D., Roloff, C., Bordas, R., Wunderlich, B., Michaelis, B., Thevenin, D.:
Improved 3-D particle tracking velocimetry with colored particles. J. Sign. Inf. Process. 2,
59–71 (2011)
26. Capart, H., Young, D., Zech, Y.: Voronoi imaging methods for the measurement of granular
flows. Exp. Fluids 32, 121–135 (2002)
27. You, C., Zhao, H., Cai, Y., Qi, H., Xu, X.: Experimental investigation of interparticle collision
rate in particulate flow. Int. J. Multiph. Flow 30, 1121–1138 (2004)
28. Charlou, C., Sauceau, M., Milhe, M., Arlabosse, P.: Application of Markov chains to the
modeling of sludge flow in an agitated indirect continuous dryer. In: Proceedings of European
Symposium on Drying (EuroDrying 2013), Paris (2013)