US2008274997A1PendingUtilityA1

Stable Granulates Containing S-adenosylmethionine and Process for Preparation Thereof

Assignee: CHEMISTRY & HEALTH INT BVPriority: Dec 12, 2001Filed: Jul 10, 2008Published: Nov 6, 2008
Est. expiryDec 12, 2021(expired)· nominal 20-yr term from priority
A61K 9/1611A61K 9/5026A61P 1/16A61K 9/1694A61K 9/2077A61K 9/145A61K 31/7076A61K 9/1652
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Claims

Abstract

A fluid bed granulation process for manufacturing non-hygroscopic, stable granulates containing a water-soluble salt of S-adenosylmethionine is described. Said process comprises: a) the simultaneous, sequential or alternate dispersion of at least a solution of a water-soluble salt of SAMe (A) and of a solution of a coating agent (B), on a fluid bed granulation carrier (C) and b) the fluid bed granulation of the mixture. Granulates obtainable by said process and solid oral pharmaceutical forms obtainable by said granulates are disclosed.

Claims

exact text as granted — not AI-modified
1 . A process for manufacturing granulates containing a water-soluble salt of S-adenosylmethionine characterized by comprising:
 a) the simultaneous, sequential or alternate dispersion of at least a solution of a water-soluble salt of SAMe (A) and of a solution of a coating agent (B), on a fluid bed granulation carrier (C) and   b) the fluid bed granulation of the mixture so obtained at a temperature not above 62° C.   
     
     
         2 . A process according to  claim 1  wherein said fluid bed granulation is performed at a temperature from 48 and 52° C. 
     
     
         3 . A process according to  claim 1  wherein the water-soluble salt of SAMe (A) is a salt of SAMe, simple or mixed, selected among sulfate, tosylate and 1,4-butandisulfonate. 
     
     
         4 . A process according to  claim 3  wherein said salt is SAMe disulfate tosylate. 
     
     
         5 . A process according to  claim 1  wherein said solutions are aqueous solutions. 
     
     
         6 . A process according to  claim 1  wherein the solution of the water-soluble salt of SAMe (A) has a concentration from 10 to 25% by weight, preferably from 15 to 20% by weight. 
     
     
         7 . A process according to  claim 1  wherein the coating agent (B) is selected from the group comprising chitins, carragenins, cellulose and chemically modified celluloses, gum or xanthane. 
     
     
         8 . A process according to  claim 7  wherein the coating agent (B) is a hydroxypropylmethylcellulose. 
     
     
         9 . A process according to  claim 1  wherein the solution of the coating agent (B) has a concentration from 5 to 15% by weight, preferably from 7 to 10% by weight. 
     
     
         10 . A process according to  claim 1  wherein the fluid bed granulation carrier (C) is selected among starch, cellulose and maltodextrin, preferably said carrier is microcrystalline cellulose. 
     
     
         11 . A process according to  claim 1  wherein the fluid bed granulation carrier (C) is characterized by a granulometry from 50 to 500μ, preferably from 100 to 200μ. 
     
     
         12 . A process according to  claim 1  characterized by comprising an additional coating step with a gastro-resistant coating agent. 
     
     
         13 . A granulate obtainable according to the process of  claim 1 . 
     
     
         14 . A granulate, according to  claim 13 , comprising up to 60% by weight, preferably from 48 and 55% by weight, of a water-soluble salt of SAMe (A), 5-15% by weight of a coating agent (B) and 25-45% by weight of carrier (C). 
     
     
         15 . Oral pharmaceutical compositions containing a granulate according to  claim 13 .

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