US2004014590A1PendingUtilityA1

Methods for extractin and reaction using supercritical fluids

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Assignee: BOEHRINGER INGELHEIM PHARMAPriority: Oct 14, 1997Filed: Jul 16, 2003Published: Jan 22, 2004
Est. expiryOct 14, 2017(expired)· nominal 20-yr term from priority
A61P 9/06A61M 15/00B01D 11/0203A61M 2209/02A61K 9/4883A61J 3/07A61K 9/0075A61P 11/08A61K 9/0073A61K 9/48B01D 11/02Y02C20/40
53
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Claims

Abstract

Methods for removing soluble material from confined spaces within substrates such as containers, capsules and porous powders comprising extraction with supercritical fluids, the pressure of which is preferably modulated between an upper level and a lower level within a relatively narrow range of fluid pressure and density. The method permits enhanced extraction efficiency, catalytic reaction rates and ability to maintain catalyst activity.

Claims

exact text as granted — not AI-modified
What is claimed is:  
     
         1 . A method for extracting material from a porous substrate comprising the steps of: 
 a) exposing the substrate to a supercritical fluid in which said material is substantially soluble but said substrate is not;    b) repeatedly modulating the pressure of said supercritical fluid between two or more pressure levels such that the relative difference between the uppermost and lowermost levels of density of said supercritical fluid at such pressure levels is not more than about 30%.    
     
     
         2 . The method of  claim 1  wherein said method is conducted at near-critical or supercritical conditions.  
     
     
         3 . The method of  claim 1  wherein said method is conducted at a temperature in the range of about 0.8 to about 2 times the critical temperature of the fluid in degrees Kelvin.  
     
     
         4 . The method of  claim 1  wherein the uppermost pressure level of said two or more pressure levels is within the range of about 0.5 to about 30 times the critical pressure of the supercritical fluid.  
     
     
         5 . The method of  claim 1  wherein the uppermost pressure level of said two or more pressure levels is within the range of about 1 to about 10 times the critical pressure of the supercritical fluid.  
     
     
         6 . The method of  claim 1  wherein said method is conducted at a temperature in the range of about 1 to about 1.1 times the critical temperature of the fluid in degrees Kelvin.  
     
     
         7 . The method of  claim 1  wherein said supercritical fluid is maintained at conditions such that the relative difference between the density level achieved at the uppermost pressure level and the lowermost pressure level of said two or more pressure levels is no more than about 5%.  
     
     
         8 . The method of  claim 1  wherein said pressure modulation is repeated multiple times.  
     
     
         9 . The method of  claim 1  wherein said pressure modulation is repeated at least 5 times.  
     
     
         10 . The method of  claim 1  wherein said pressure modulation is repeated at least 20 times.  
     
     
         11 . The method of  claim 1  wherein said pressure modulation is repeated at least 50 times.  
     
     
         12 . The method of  claim 1  wherein said pressure modulation is repeated until more than 50% of the material is removed from said substrate.  
     
     
         13 . The method of  claim 1  wherein said pressure modulation is repeated until more than 75% of the material is removed from said substrate.  
     
     
         14 . The method according to  claim 1  wherein the supercritical fluid is or contains carbon dioxide.  
     
     
         15 . The method according to  claim 1  wherein said substrate is sensitive to large changes in pressure, temperature or density.  
     
     
         16 . The method according to  claim 1 , wherein said substrate is a porous matrix.  
     
     
         17 . The method according to  claim 1 , wherein said substrate defines a porous structure selected from: powders, adsorbents and absorbents.

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