FLUIDIZED BED INSTALLATION
20190134584 ยท 2019-05-09
Inventors
Cpc classification
B01J2/003
PERFORMING OPERATIONS; TRANSPORTING
B01J8/36
PERFORMING OPERATIONS; TRANSPORTING
B01D39/08
PERFORMING OPERATIONS; TRANSPORTING
B01J8/1872
PERFORMING OPERATIONS; TRANSPORTING
F26B3/08
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
B01J8/26
PERFORMING OPERATIONS; TRANSPORTING
B01D39/12
PERFORMING OPERATIONS; TRANSPORTING
B01J2/16
PERFORMING OPERATIONS; TRANSPORTING
B01J8/34
PERFORMING OPERATIONS; TRANSPORTING
International classification
B01J2/16
PERFORMING OPERATIONS; TRANSPORTING
B01D39/12
PERFORMING OPERATIONS; TRANSPORTING
B01D39/08
PERFORMING OPERATIONS; TRANSPORTING
B01J2/00
PERFORMING OPERATIONS; TRANSPORTING
F26B3/08
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
Abstract
The invention relates to a fluidized bed installation (1), comprising at least two chambers (2, 3, 4), wherein each chamber (2, 3, 4) has a main body (5) and a gas inlet (6) and a gas outlet (7), wherein each main body (5) has an inlet (8) and an outlet (9) for a solid (19), wherein the inlet (8) of a first chamber (2) is connected to a feed (10) of the fluidized bed installation (1), the outlet (9) of the first chamber (2) is connected to the inlet (8) of a second chamber (4), and the outlet (9) of the second chamber (4) is connected to a discharge (11) of the fluidized bed installation (1), and wherein a valve (12) is arranged between two connected chambers (2, 3, 4) and/or at the feed (10) and/or at the discharge (11) such that either continuous operation or semi-continuous operation of the fluidized bed installation (1) is enabled.
Claims
1. A fluidized bed installation (1) comprising at least two chambers (2, 3, 4), the at least two chambers including a first chamber (2) and a second chamber (4), wherein each of the at least two chambers (2, 3, 4) has a main body (5), a gas inlet (6) and a gas outlet (7), wherein each main body (5) has an inlet (8) and an outlet (9) for a solid (19), wherein the inlet for a solid (8) of the first chamber (2) is connected to a feed line (10) of the fluidized bed installation (1), the outlet for a solid (9) of the first chamber (2) is connected to the inlet for a solid (8) of the second chamber (4) and the outlet for a solid (9) of the second chamber (4) is connected to a discharge line (11) of the fluidized bed installation (1), and wherein a valve (12) is arranged between two the first and second chambers (2, 3, 4) and/or on the feed line (10) and/or on the discharge line (11), so as optionally to allow continuous or semicontinuous operation of the fluidized bed installation (1), for a solid
2. The fluidized bed installation (1) as claimed in claim 1, characterized in that the at least two chambers include at least one third chamber (3) arranged between the outlet for a solid (9) of the first chamber (2) and the inlet for a solid (8) of the second chamber (4), such that the inlet for a solid of the third chamber (3) is connected to the outlet for a solid (9) of the first chamber (2) and the outlet for a solid (9) of the third chamber (3) is connected to the inlet (8) of the second chamber (4).
3. The fluidized bed installation (1) as claimed in claim 1, characterized in that the valve (12) includes a weir.
4. The fluidized bed installation (1) as claimed in claim 1, characterized in that the main body (5) has a base (13) and a lid (14), wherein the base (13) comprises the gas inlet (6) and the lid (14) comprises the gas outlet (7).
5. The fluidized bed installation (1) as claimed in claim 4, characterized in that the base (13) comprises a gas distributor, wherein the gas distributor has a plurality of outlet orifices (20) via which a gas introduced through the gas inlet (6) may be introduced into the main body (5).
6. The fluidized bed installation (1) as claimed in claim 5, characterized in that the outlet orifices (20) are arranged toroidally.
7. The fluidized bed installation (1) as claimed in claim 4, characterized in that the base (13) has spray nozzles via which a liquid may be introduced into the main body (5).
8. The fluidized bed installation (1) as claimed in claim 4, characterized in that the lid (14) has a filter element (15), wherein the filter element (15) prevents the solid (19) from leaving the main body (5) through the gas outlet (7).
9. The fluidized bed installation (1) as claimed in claim 8, characterized in that the filter element (15) comprises a woven textile filter and/or a metal mesh filter and/or a gas/solid cyclone.
10. The fluidized bed installation (1) as claimed in claim 1, further comprising a mill, which is integrated into the discharge line (11).
Description
BRIEF DESCRIPTION OF THE DRAWINGS
[0016] Exemplary embodiments of the invention are described in detail below with reference to the accompanying drawings, in which:
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DETAILED DESCRIPTION
[0027]
[0028] A solid, in particular in powder form, may be fed to the individual chambers 2, 3, 4 via the feed line 10. As a result of the series connection, the solid firstly enters the first chamber 2, then the third chambers 3, and finally the second chamber 4.
[0029] Inside the individual chambers 2, 3, 4 the solid comes into contact with a gas, in particular with air. This is shown in
[0030] Each chamber 2, 3, 4 comprises a main body 5 and a base 13 and a lid 14. The base 13 is provided with a gas inlet 6, while the lid 14 comprises a gas outlet 7. Gas, in particular air, may be introduced into the main body via the gas inlet 6. A solid may moreover be introduced into the main body 5 via the respective inlets 8 of the chambers 2, 3, 4. Through contact with the flowing gas, the preferably pulverulent solid is set in motion and assumes a fluid-like state within the main body 5. The gas flows from the gas inlet 6 to the gas outlet 7 and leaves the respective chamber 2, 3, 4 via the gas outlet 7. To prevent solid from likewise leaving the chamber 2, 3, 4, the lid 14 comprises a filter element 15. The filter element 15 is advantageously a metal mesh filter. The metal mesh filter is in particular supplied with compressed air at regular intervals, in order to clean the metal mesh filter 15.
[0031] The base 13 has a gas distributor with a plurality of outlet orifices 20 (cf.
[0032]
[0033]
[0034] For reliable closure of the valve 12, moreover, a seal 18 is provided. The individual chambers 2, 3, 4 may thus be completely separated from one another. Once the chambers 2, 3, 4 have been separated, a semicontinuous mode of operation is possible for the fluidized bed installation 1. To this end, the first chamber 2 is filled with a solid 19, wherein the solid 19 remains in the first chamber 2 until a predefined product quality is achieved. Only then is the valve 12 between the first chamber 2 and the second chamber 3 preferably opened, in order to allow transfer of the solid between the first chamber 2 and the third chamber 3. The same applies to all the third chambers 3 and the fourth chamber 4. If, on the other hand, the valves 12 are open, a continuous operating mode is possible for the fluidized bed installation. The continuous operating mode is achieved in particular in that a solid 19 is constantly added via the feed line 10, while a solid and/or the finished product is continuously removed via the discharge line 11. Transfer between the individual chambers 2, 3, 4 takes place, in particular, due to a differential pressure between the chambers 2, 3, 4 and/or due to differences in height.
[0035]
[0036] In
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[0038] Finally,
[0039] In one further preferred embodiment, the fluidized bed installation additionally comprises a distribution system, wherein the distribution system is separately configured to introduce solid into and remove it from each individual chamber 2, 3, 4. This in particular enables batch operation of the fluidized bed installation 1, in that a solid 19 may be introduced into each chamber 2, 3, 4 individually and also removed again individually therefrom.
[0040] The fluidized bed installation 1 according to the present invention has the following advantages: [0041] choice between continuous and semi-continuous process control [0042] individually controllable chambers 2, 3, 4 for different process conditions in the individual main bodies 5, in particular with regard to temperature, air, gas velocities and spraying rates [0043] variable process length and thus flexibility of product residence time and throughput [0044] possibility of drying and granulation inside a fluidized bed installation 1 due to the separate chambers 2, 3, 4 [0045] step by step granulation or drying in mini batches, in order to ensure conservative process control [0046] continuous coating, since a different coating substance can be atomized in each chamber 2, 3, 4 in order in particular to multiply functionalize drugs [0047] bottom spray method with rotating particle bed with uniform distribution of spray liquid and permanent product wall movement to minimize incrustation of the main body 5; the bottom spray method is achieved in particular by mounting spray nozzles in the bases 13 of the chambers 2, 3, 4.