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dc.contributor.author
Veliz Moraga, Sussy  
dc.contributor.author
Villa, Marta Patricia  
dc.contributor.author
Bertin, Diego Esteban  
dc.contributor.author
Cotabarren, Ivana María  
dc.contributor.author
Piña, Juliana  
dc.contributor.author
Pedernera, Marisa Noemi  
dc.contributor.author
Bucala, Veronica  
dc.date.available
2017-09-25T15:02:28Z  
dc.date.issued
2015-09-08  
dc.identifier.citation
Veliz Moraga, Sussy; Villa, Marta Patricia; Bertin, Diego Esteban; Cotabarren, Ivana María; Piña, Juliana; et al.; Fluidized-bed melt granulation: The effect of operating variables on process performance and granules properties; Elsevier Science; Powder Technology; 286; 8-9-2015; 654-667  
dc.identifier.issn
0032-5910  
dc.identifier.uri
http://hdl.handle.net/11336/25022  
dc.description.abstract
This paper addresses fluid-bed melt granulation (FBMG) for seeds and a binder of the same chemical nature, i.e. with an identical melting point. The purpose of this work is to study the impact of seed size, bed temperature, binder flowrate, and fluidization and atomization air flowrates on process parameters such as: mass balance closure; fines deposited on granulator walls and granulationefficiency; and on product properties such as: particle size distribution; percentages of particles effectively coated or agglomerated and granule crushing strength; among others. This is done to find the operating regions capable of avoiding lump formation or out-of-specification granule production.This work is focused on operating conditions and seed diameter ranges not addressed before. In particular, relatively large seed particles compared to the size of the droplets, high binder/seed mass ratios, and bottom spray are used. The specific method proposed to characterize the granular product into three categories (fines, pure coated particles, and agglomerated/coated granules), allowed to identify the main growth mechanisms for an extended range of operating conditions and seed sizes.The agglomeration rate was found to increase by decreasing the fluidization and atomization air flowrates and the bed temperature, as well as by increasing the binder flowrate. The agglomerated mass fraction presented a non-monotonic behavior as a function of the seed diameter, with a minimum at a seed mean diameter of about 0.26 cm. Even though the operating variables were widely disturbed, the main particle growth mechanism was pure coating for all the tested conditions. In fact, coated particles accounted for more than 68 wt% of the granular product. As a result, the final mass median size remained almost constant for all the studied cases. On the other hand, the span of the particle size distribution was extremely sensitive to the selected operating conditions. This contribution provides some valuable guidelines to avoid agglomeration in melt granulation processes designed to produce coated granules  
dc.format
application/pdf  
dc.language.iso
eng  
dc.publisher
Elsevier Science  
dc.rights
info:eu-repo/semantics/openAccess  
dc.rights.uri
https://creativecommons.org/licenses/by-nc-sa/2.5/ar/  
dc.subject
Melt Granulation  
dc.subject
Fluidized Bed  
dc.subject
Urea  
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Growth Mechanisms  
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Coating  
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Agglomeration  
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Otras Ingeniería Química  
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Ingeniería Química  
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INGENIERÍAS Y TECNOLOGÍAS  
dc.title
Fluidized-bed melt granulation: The effect of operating variables on process performance and granules properties  
dc.type
info:eu-repo/semantics/article  
dc.type
info:ar-repo/semantics/artículo  
dc.type
info:eu-repo/semantics/publishedVersion  
dc.date.updated
2017-05-03T20:05:03Z  
dc.journal.volume
286  
dc.journal.pagination
654-667  
dc.journal.pais
Países Bajos  
dc.journal.ciudad
Amsterdam  
dc.description.fil
Fil: Veliz Moraga, Sussy. Universidad Católica del Norte; Chile  
dc.description.fil
Fil: Villa, Marta Patricia. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Conicet - Bahía Blanca. Planta Piloto de Ingeniería Química. Universidad Nacional del Sur. Planta Piloto de Ingeniería Química; Argentina  
dc.description.fil
Fil: Bertin, Diego Esteban. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Conicet - Bahía Blanca. Planta Piloto de Ingeniería Química. Universidad Nacional del Sur. Planta Piloto de Ingeniería Química; Argentina  
dc.description.fil
Fil: Cotabarren, Ivana María. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Conicet - Bahía Blanca. Planta Piloto de Ingeniería Química. Universidad Nacional del Sur. Planta Piloto de Ingeniería Química; Argentina  
dc.description.fil
Fil: Piña, Juliana. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Conicet - Bahía Blanca. Planta Piloto de Ingeniería Química. Universidad Nacional del Sur. Planta Piloto de Ingeniería Química; Argentina  
dc.description.fil
Fil: Pedernera, Marisa Noemi. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Conicet - Bahía Blanca. Planta Piloto de Ingeniería Química. Universidad Nacional del Sur. Planta Piloto de Ingeniería Química; Argentina  
dc.description.fil
Fil: Bucala, Veronica. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Conicet - Bahía Blanca. Planta Piloto de Ingeniería Química. Universidad Nacional del Sur. Planta Piloto de Ingeniería Química; Argentina  
dc.journal.title
Powder Technology  
dc.relation.alternativeid
info:eu-repo/semantics/altIdentifier/doi/http://dx.doi.org/10.1016/j.powtec.2015.09.006  
dc.relation.alternativeid
info:eu-repo/semantics/altIdentifier/url/http://www.sciencedirect.com/science/article/pii/S0032591015300516