SYSTEM AND METHOD FOR CONTINUOUS PROCESSING OF POWDER PRODUCTS
20220258114 · 2022-08-18
Assignee
Inventors
- Joris Vanderputten (Buizingen, BE)
- Jozef Verheyen (Mortsel, BE)
- Kris Schoeters (Kessel-Lo, BE)
- Nicolas Walter (Hamburg, DE)
- Sven Kolbe (Büchen, DE)
Cpc classification
B30B11/08
PERFORMING OPERATIONS; TRANSPORTING
B30B15/308
PERFORMING OPERATIONS; TRANSPORTING
A61J3/07
HUMAN NECESSITIES
B30B15/304
PERFORMING OPERATIONS; TRANSPORTING
B01F33/8051
PERFORMING OPERATIONS; TRANSPORTING
B01F33/8052
PERFORMING OPERATIONS; TRANSPORTING
International classification
Abstract
A system for continuous processing of powder products includes a first inlet configured to input a first dry powder product, a second inlet configured to input a second dry powder product, and a dry powder mixing device that mixes the first dry powder product together with the second dry powder product to form a product mixture. An outlet dispenses the product mixture from the dry powder mixing device. A production machine is included and has a powder feed frame comprising a feed frame inlet connected to the outlet of the dry powder mixing device. The outlet of the dry powder mixing device is positioned at a lower level than the feed frame inlet. A product conveying device is connected between the outlet of the dry powder mixing device and the feed frame inlet to continuously convey the product mixture from the dry powder mixing device to the feed frame inlet.
Claims
1-31. (canceled)
32. A system for continuous processing of powder products, the system comprising: a first inlet configured to input a first dry powder product; a second inlet configured to input a second dry powder product; a dry powder mixing device comprising, an inlet configured to connect to the first inlet to accept the first dry powder product and further configured to connect to the second inlet to accept the second dry powder product, wherein the dry powder mixing device is configured to mix the first dry powder product together with the second dry powder product to form a product mixture, and an outlet configured to dispense the product mixture from the dry powder mixing device; a production machine comprising a powder feed frame comprising, a feed frame inlet connected to the outlet of the dry powder mixing device, wherein the outlet of the dry powder mixing device is positioned at a lower level than the feed frame inlet of the production machine, and a feed frame outlet; and a product conveying device connected between the outlet of the dry powder mixing device and the feed frame inlet of the production machine, wherein the product conveying device is configured to continuously convey the product mixture from the outlet of the dry powder mixing device to the feed frame inlet of the production machine.
33. The system according to claim 32, wherein the continuous processing of powder products comprises a continuous production of solid dosage forms in direct processing, wherein the production machine is configured to continuously produce solid dosage forms from the product mixture, and wherein the production machine further comprises an outlet for discharging the solid dosage forms.
34. The system according to claim 33, wherein the production machine is one of: (1) a tablet press; (2) a capsule filling machine; (3) and a granulation device.
35. The system according to claim 32, wherein the first inlet for the first dry powder product and the second inlet for the second dry powder product are arranged at a height level that is at least one of: (1) a same height level; and (2) a lower height level than one of: (a) the production machine; and (b) the product conveying device.
36. The system according to claim 32, wherein a height difference between the outlet of the dry powder mixing device and the feed frame inlet of the production machine is more than 1.50 m, and wherein an overall height of the system is less than 2.50 m.
37. The system according to claim 32, wherein the product conveying device is a pneumatic vacuum dense phase product conveying device, wherein a conveying line pressure drop of the pneumatic vacuum dense phase product conveying device is more than 0.5 bar, and wherein a cycle mass of the pneumatic vacuum dense phase product conveying device is no more than 2 kg in weight.
38. The system according to claim 32, wherein the product conveying device comprises a product conveying hose configured to convey the product mixture.
39. The system according to claim 37, wherein a solids loading ratio of the pneumatic vacuum dense phase product conveying device is more than 15.
40. The system according to claim 32, further comprising, an inlet hopper positioned at the inlet of the product conveying device, and a conical diameter reduction configured to reduce a diameter from the inlet hopper to the conveying line of the product conveying device.
41. The system according to claim 32, further comprising at least one of: (1) an inlet hopper positioned at the inlet of the product conveying device; and (2) an outlet hopper positioned at the outlet of the product conveying device, wherein a volume of either the inlet or the outlet hopper is no more than 0.5 liters in volume.
42. The system according to claim 32, further comprising an outlet hopper positioned at the outlet of the product conveying device, wherein a ratio of a height of the outlet hopper to a diameter of the outlet hopper is at least 2.
43. The system according to claim 42, wherein a positive pressure is applied in the outlet hopper.
44. The system according to claim 32, wherein the feed frame inlet comprises a vent opening.
45. The system according to claim 32, further comprising an inlet hopper of the product conveying device, wherein the inlet hopper comprises a vent opening.
46. The system according to claim 45, wherein the vent opening comprises a venting tube.
47. The system according to claim 32, further comprising a plurality of feeding and dosing devices, wherein each of the first inlet, the second inlet, and the inlet of the dry powder mixing device is connected to one of the plurality of feeding and dosing devices.
48. The system according to claim 47, wherein the plurality of feeding and dosing devices, and the dry powder mixing device comprise a feeding, dosing and mixing module, wherein the feeding, dosing and mixing module is arranged in a module housing.
49. A method for continuous processing of powder products, the method comprising: continuously providing a first dry powder product and a second dry powder product to a dry powder mixing device; continuously mixing the first dry powder product with the second dry powder product in the powder mixing device to form a product mixture; continuously providing the product mixture to an outlet of the powder mixing device; conveying the product mixture from the outlet of the powder mixing device to a feed frame inlet of a production machine using a conveying device, wherein the outlet of the powder mixing device is positioned at a height below that of the feed frame inlet; continuously processing the product mixture with the production machine; and discharging processed product from the production machine.
50. The method of claim 49, wherein the conveying device is arranged in a connection between the outlet of the dry powder mixing device and the feed frame inlet of the production machine.
51. The method according to claim 49, wherein the discharging of the processed product comprises discharging solid dosage forms of the product mixture from the production machine.
Description
BRIEF DESCRIPTION OF THE DRAWINGS
[0051] Embodiments of the invention are explained in more detail below with reference to drawings. The drawings schematically show:
[0052]
[0053]
[0054]
[0055]
[0056]
[0057]
[0058] In the drawings the same reference numerals shall denote the same parts.
DETAILED DESCRIPTION OF THE INVENTION
[0059]
[0060] In
[0061] The feeding and dosing devices 34, 36, 38 and 40 are on the other hand connected with a mixing device 50. The mixing device 50 may generally be any type of dry powder mixer or blender. Mixing device 50 has a first inlet 52 which is connected with the feeding and dosing devices 34, 36, 38. A second inlet 54 of the mixing device 50 is connected with the feeding and dosing device 40. The mixing device 50 further has an outlet 56 which is connected with the inlet 24 of the product conveying device 22. The outlet 20 of the product conveying device 22 is connected with a feed frame inlet 58 of a feed frame 60 of the tablet press 10. The outlet 20 of the product conveying device 22 and the feed frame inlet 58 of the feed frame 60 of the tablet press 10 are connected through a vertical tube 62. The tablet press 10 further has an outlet 64 for discharging produced tablets.
[0062] In the following the inventive method carried out with the inventive system will be explained. During production the first, second and third powder product, provided at the first, second and third inlet 26, 28 and 30 are continuously provided to the first inlet 52 of the mixing device 50 through the feeding and dosing devices 34, 36 and 38. The fourth powder product provided at the fourth inlet 32 is continuously provided to the second inlet 54 of the mixing device 50 through the feeding and dosing device 40. The mixing device 50 continuously produces and provides at its outlet 56 a powder product mixture of the four powder products. The product mixture is continuously fed to the inlet 24 of the product conveying device 22. As can be seen for example in
[0063] According to the above explained system configuration, it is possible to restrict the overall height of the system to less than 3.50 m, preferably less than 3 m, more preferably less than 2.50 m. To this end the product mixture may be vertically lifted by the product conveying device 22 over a height of more than 1.50 m, for example roughly 2 m. It can be seen in
[0064] In
[0065] In the embodiment shown in
[0066] The vacuum dense phase product conveying device 22 shown in
[0067] This intermittent conveying process leads to an intermittent rising and lowering of powder level in the feed frame inlet 58 of the production machine 10, as explained above. In order to avoid an undesired underpressure in the feed frame inlet 58 a vertical venting tube 78 with a venting opening at its top, is provided at the feed frame inlet 58 of the production machine 10. At the top of the venting tube 78 a dust extraction shroud 80 and a dust extraction hose 82 is provided leading to a dust extraction system for extracting any powder dust potentially exiting the venting tube 78 through the venting opening.
[0068] Since a similar problem with regard to a rising and lowering pressure due to the intermittent conveying exists at the inlet hopper 68 of the product conveying device 22, a corresponding venting tube 78 with a venting opening at its top is arranged at the inlet hopper 68, as can be seen in
[0069] For feeding dry powder product to the dry powder mixing device 50 the system shown in
[0070] The production process with the system shown in
[0071] A further embodiment of an inventive system is shown in
[0072] Like the system shown in
[0073] Furthermore, all systems shown in the drawings may be contained systems, for example with a containment level for product toxicity level OEB 3 or higher, measured for example according to the SMEPAC test.
LIST OF REFERENCE NUMERALS
[0074] 10 production machine [0075] 12 production machine housing [0076] 14 module housing [0077] 16 system housing [0078] 18 windows [0079] 20 outlet of product conveying device [0080] 22 product conveying device [0081] 24 inlet of product conveying device [0082] 26 first inlet [0083] 28 second inlet [0084] 30 third inlet [0085] 32 fourth inlet [0086] 34, 36, 38, 40 feeding and dosing devices [0087] 42, 44, 46, 48 refill systems [0088] 50 mixing device [0089] 52 first inlet of mixing device [0090] 54 second inlet of mixing device [0091] 56 outlet of mixing device [0092] 58 feed frame inlet of production machine [0093] 60 feed frame of production machine [0094] 62 vertical tube [0095] 64 outlet of production machine [0096] 66 doors [0097] 68 inlet hopper [0098] 69 outlet hopper [0099] 70 product conveying hose [0100] 72 conical diameter reduction [0101] 74 vacuum hose [0102] 76 vacuum generation device [0103] 78 tube with vent opening [0104] 80 dust extraction shroud [0105] 82 dust extraction hose [0106] 84, 86, 88 housings for technical components [0107] 90 rear wall