IP Library Granted Patent US 8,106,100
Granted Patent B2
US 8,106,100 · App. 12/086,001 · Granted Jan 31, 2012

Process for producing tablet by high-speed direct compression

Assignee: Asahi Kasei Chemicals Corporation
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Quick Facts
Patent No.
US 8,106,100
App. No.
12/086,001
Granted
Jan 31, 2012
Kind
B2
Abstract

A process for producing a tablet characterized by performing high-speed direct compression with a moving speed of a pestle of 800 mm/s or more while compressing a powder which contains at least 15 to 80% by mass of cellulose, an active ingredient and a lubricant and has an angle of repose of 50° C. or less, a compression degree of 20% or more and an elongation at break of 30 μm or more.

Claims (16)

1. A process for producing a tablet, characterized by comprising performing high-speed direct compression at a punch moving speed of 800 mm/s or more; while compacting a powder which comprises at least 15 to 80% by mass of cellulose, an active ingredient, and a lubricant and has an angle of repose of 50° or less, a compressibility of 20% or more, and a tensile elongation at break of 30 μm or more, wherein said powder is prepared without a fluidizer.

2. The process according to claim 1 , wherein the cellulose is crystalline cellulose of which an average degree of polymerization is 150 to 450, a rate of particles remaining on a sieve of 250 μm in mesh size is 10% by mass or less, average L/D of particles of 75 μm or smaller is 2.0 or more, a bulk density is 0.25 g/cm 3 or less, and an angle of repose is 43° or more.

3. The process according to claim 1 , wherein the powder requires flow energy of 400 mJ or less during aeration.

4. The process according to claim 3 , wherein the powder requires flow energy of 350 mJ or less during aeration.

5. The process according to claim 1 , wherein the powder has an angle of repose of 30 to 50°.

6. The process according to claim 1 , wherein the powder has a compressibility of 20 to 50%.

7. The process according to claim 1 , wherein the powder has a tensile elongation at break of 100 μm or less.

8. The process according to claim 3 , wherein the powder requires flow energy of 100 mJ or more during aeration.

9. The process according to claim 1 , wherein the compaction is performed with a stirring feeder attached to a tablet machine.

10. The process according to claim 2 , wherein the powder requires flow energy of 400 mJ or less during aeration.

11. The process according to claim 10 , wherein the powder requires flow energy of 350 mJ or less during aeration.

12. The process according to claim 2 , wherein the powder has an angle of repose of 30 to 50°.

13. The process according to claim 2 , wherein the powder has a compressibility of 20 to 50%.

14. The process according to claim 2 , wherein the powder has a tensile elongation at break of 100 μm or less.

15. The process according to claim 11 , wherein the powder requires flow energy of 100 mJ or more during aeration.

16. The process according to claim 10 , wherein the compaction is performed with a stirring feeder attached to a tablet machine.

Assignments (1)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jun 4, 2008
From: KAKIZAWA, MASAYUKI; GOMI, SHUNICHI; OZEKI, YUICHI
To: ASAHI KASEI CHEMICALS CORPORATION
Reel/Frame 021087/0747 →
Priority Claims (1)
JP 2005-352301 · Dec 6, 2005 · national
Continuity (1)
Related Publication 20090163604A1 · Jun 25, 2009