Lactose and cellulose-based tableting aid
The present invention concerns a process for producing a granulate based on lactose and cellulose (derivative), a granulate obtainable by the process and its use as a tabletting excipient.
1. A process for producing a granulate, comprising:
(i) suspending and/or at least partially dissolving lactose and optionally at least one cellulose derivative in at least one liquid, to form a solution or suspension; and
(ii) atomizing said solution or suspension in an environment above room temperature onto cellulose derivative particles and optionally lactose particles during which said atomized liquid is at least partially removed.
2. The process according to claim 1 , wherein said lactose is selected from the group consisting of lactose monohydrate and anhydrous lactose.
3. The process according to claim 1 , wherein the cellulose derivative is selected from the group consisting of cellulose whose hydroxyl groups are independently of one another at least partially alkylated, hydroxyalkylated, sulfonated, carboxyalkylated and/or xanthogenated.
4. The process according to claim 1 , wherein the cellulose derivative is selected from the group consisting of hypromellose (HPMC), hypromellose phthalate, hydroxypropyl cellulose (HPC), hydroxyethyl cellulose (HEC), ethyl cellulose (EC), carboxymethyl cellulose (CMC), carboxyethyl cellulose (CEC) and/or sodium and/or calcium salts thereof.
5. The process according to claim 1 , wherein said liquid is selected from the group consisting of water and organic solvents.
6. The process according to claim 1 , wherein said lactose and cellulose derivative in step (i) have a weight ratio of lactose/cellulose derivative of from about 100:0 to about 5:95.
7. The process according to claim 1 , wherein at least 5% by weight, based on total content of lactose, is present in a dissolved form in step (i).
8. The process according to claim 1 , wherein said suspension is characterized by an average particle size in a range of from 0.1 μm to about 1000 μm.
9. The process according to claim 1 , wherein said solution or suspension in step (ii) is atomized by a nozzle to form droplets having an average diameter of from 15 μm to 1250 μm.
10. The process according to claim 1 , wherein said solution or suspension is atomized in an environment at temperature of from about 30° C. to 250° C.
11. The process according to claim 10 , wherein said environment has a pressure of from about 0 bar to 1.0 bar.
12. The process according to claim 1 , wherein said solution or suspension is sprayed onto cellulose derivative particles and/or lactose particles having average diameter of from about 1 μm to about 500 μm.
13. The process according to claim 1 , wherein said cellulose derivative particles and lactose particles in step (ii) have a ratio of cellulose derivative particles/lactose particles in a range of from about 100:0 to about 5:95.
14. The process according to claim 1 , wherein said liquid of said solution or suspension is at least partially removed by a spray drying process.
15. The process according to claim 1 , wherein all of said cellulose derivative particles and optional lactose particles are present in a fluidized bed or a stationary fluidized bed.
16. The process according to claim 1 , wherein said liquid of said solution or suspension is at least partially removed in a fluidized bed granulation process.
17. The process according to claim 1 , wherein said liquid of said solution or suspension is at least partially removed in a wet granulation process.
18. The process according to claim 1 , wherein free liquid content in said granulate is less than 8% by weight, based on total mass of the granulate.
19. The process according to claim 1 , wherein said granulate has a ratio of lactose/cellulose derivative of from about 95:5 and 1:99.
20. The process according to claim 1 , wherein said granulate has a spherical or spheroid morphology.
21. The process according to claim 1 , wherein said granulate comprises granulate particles having a d 50 particle size distribution of from 25 μm to 750 μm.