Fluid Bed Granulation Process and Apparatus
A fluid bed granulation process and apparatus, wherein a suitable fluid bed of a particulate material is maintained in a granulator ( 1 ) fed by an input flow (F) comprising a growth liquid (L) and by a flow (S1) of seeds adapted to promote the granulation, and wherein a part (F2) of said input flow (F) is taken upstream the feeding of the fluid bed, and used in a seeds generator ( 33 ), to produce the seeds for the fluid bed.
1 . A fluid bed granulation process of a given substance, comprising the steps of:
providing a fluid bed of a particulate material comprising granules of said substance and solid particles of an appropriate substance working as seeds for the granulation process;
feeding an input flow (F) comprising a growth liquid (L) containing said substance, to said process;
feeding a flow (S1) of said seeds into the fluid bed, to promote the growth of granules and to maintain the fluidized mass;
taking a flow of solid granules as output of the process carried out in the fluid bed;
wherein a first portion (F1) of said input flow (F) is fed directly to the fluid bed, and a second portion (F2) of said input flow (F) is used to generate at least a part of said flow (S1) of seeds.
2 . The process according to claim 1 , wherein said second portion (F2) is a minor portion of said input flow.
3 . The process according to claim 2 , wherein the ratio between said second portion (F2) and the input flow (F) is equal to d 3 /D 3 , where d is the mean value of a characterizing dimension of said seeds and D is the mean value of a characterizing dimension of the solid granules obtained at the output of the fluid bed.
4 . The process according to claim 1 , wherein said second portion (F2) of the input flow is solidified by depositing liquid drops on a cooled conveyor belt, obtaining solid pastilles with a suitable diameter.
5 . The process according to claim 1 , wherein said second portion (F2) of the input flow is solidified in a prilling tower.
6 . The process according to claim 1 , wherein said second portion (F2) of input flow is used to generate the full flow (S1) of seeds to the fluid bed.
7 . The process according to claim 6 , wherein the output flow of the fluid bed is directly taken as final product of the granulation, without further screening and separation of waste granules.
8 . The process according to claim 1 , wherein said first portion (F1) of the input fluid flow is fed to the fluid bed along a continuous, longitudinal feeding line on one or both sides of the fluid bed.
9 . The process according to claim 1 , wherein said first portion (F1) of the input fluid flow is fed to the fluid bed in discrete and predetermined feeding zones (Z′), aligned in a main flowing direction of the fluid bed, and alternate to non-feeding zones (Z″) of the same fluid bed, said feeding zones (Z′) acting substantially as wetting zones of the particulate material by the fluid flow, and said non-feeding zones (Z″) acting substantially as drying and consolidation zones of the growing particles.
10 . The process according to claim 1 , wherein a vortex condition is induced and maintained in the fluid bed; with a transversal vortex (V) or a double transversal vortex (V 1 , V 2 ) arrangement, the axis of the vortex (V; V 1 , V 2 ) being substantially parallel to a main flow direction of the fluid bed.
11 . A granulation apparatus, adapted to operate according to the process of claim 1 , comprising at least a granulator where said fluid bed is formed and maintained, and feeding means of an input flow (F) containing a growth liquid, characterized by said feeding means comprising first feeding means for directly feeding the granulator with the growth liquid, and second feeding means connected to a seed generator, said generator being adapted to convert a portion of said input flow (F) into solid seeds (S1), the output of said seed generator being connected to the granulator and feeding said seeds (S1) to said granulator.