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EP0130160A2 Expired / Lapsed EP ⏱️ 0.0 years remaining

Small particle formation

Assignee: Ohio State University Research Foundation
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Filing: 1984-06-12
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Granted: —
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Expires: 2004-06-12
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Abstract

Abstract The present invention is concerned with the formation of small particles of organic compounds whose solubility in water is independent of temperature and greater at a first pH than at a second pH. upon precipitation by pH change with or without a change in temperature, but in the presence of a surfactant mixture.

Inventors

  • 👤 Sylvan Gerald Frank
  • 👤 Arne Folke Brodin
  • 👤 Chih-Ming James Chen
  • 👤 Ratnesh Shrivastava

Bibliographic Details

Application Number —
Jurisdiction EP
Data Source google_patents
Last Synchronized 2026-11-06 04:44
CPC Classifications
A; A61; A61K; A61K9/00; A61K9/14; A61K9/16; A61K9/1682; A61K9/1688; C; C21; C21C; C21C1/00; C21C1/04; B; B01; B01J; B01J13/00; B01J13/02; B01J13/06; B01J13/10

Claims Analysis

Total Claims: 11
Claim 1
Independent Claim 138 words
A process for forming small particles of a weakly acidic organic compound whose solubility in water is greater at a first pH than at a second pH which process comprises: (a) dissolving said compound in water in the presence of sufficient base to raise the pH to said first pH and above the pKa of the compound preferably about 2 pH units, together with an anionic surfactant which maintains its ionic condition between the first and second pH and an amphoteric surfactant whose cationic nature increases from the first pH to said second pH; and (b) stirring and titrating the solution, with a titrant effective to reduce the pH of said solution to said second pH to cause the concurrent formation of a coacervate of the anionic and amphoteric surfactants, and precipitation of the compound as small particles.
Claim 2
Dependent Claim 138 words
A process for forming small particles of a weakly acidic organic compound whose solubility in water is greater at a first pH than at a second pH which process comprises: (a) dissolving said compound in water in the presence of sufficient base to raise the pH to said first pH and above the pKa of the compound preferably about 2 pH units, together with an anionic surfactant which maintains its ionic condition between the first and second pH and an amphoteric surfactant whose cationic nature increases from the first pH to said second pH; and (b) stirring and titrating the solution, with a titrant effective to reduce the pH of said solution to said second pH to cause the concurrent formation of a coacervate of the anionic and amphoteric surfactants, and precipitation of the compound as small particles.
Claim 3
Dependent Claim 138 words
A process for forming small particles of a weakly basic organic compound whose solubility in water is greater at a first pH than at a second pH which process comprises: (a) dissolving said compound in water in the presence of sufficient acid to lower the pH to said first pH and below the pKa of the compound preferably about 2 pH units, together with a cationic surfactant which maintains its ionic condition between the first and second pH and an amphoteric surfactant whose anionic nature increases from the first pH to said second pH; and (b) stirring and titrating the solution, with a titrant effective to raise the pH of said solution to said second pH to cause the concurrent formation of a coacervate of the cationic and amphoteric surfactants, and precipitation of the compound as small particles.
Claim 4
Dependent Claim 138 words
A process for forming small particles of a weakly basic organic compound whose solubility in water is greater at a first pH than at a second pH which process comprises: (a) dissolving said compound in water in the presence of sufficient acid to lower the pH to said first pH and below the pKa of the compound preferably about 2 pH units, together with a cationic surfactant which maintains its ionic condition between the first and second pH and an amphoteric surfactant whose anionic nature increases from the first pH to said second pH; and (b) stirring and titrating the solution, with a titrant effective to raise the pH of said solution to said second pH to cause the concurrent formation of a coacervate of the cationic and amphoteric surfactants, and precipitation of the compound as small particles.
Claim 5
Dependent Claim 14 words
A process according to claims 1 or 2, wherein the compound is pharmaceutically active.
Claim 6
Dependent Claim 29 words
A process according to claim 3, wherein the pharmaceutically active compound is selected from the group consisting of sulfadiazine, lidocaine, salicylic acid, felodipine, sulbactam pivoxil, chlorzoxazone, theophylline and erythromycin.
Claim 7
Dependent Claim 27 words
The process according to claim 1 or 2 wherein the amphoteric surfactant is selected from the group consisting of imidazoline derived amphoterics, betaines and amino acid amphoterics.
Claim 8
Dependent Claim 24 words
A process according to claim 5, wherein the amphoteric surfactant is selected from the group consisting of cocamidopropyl betaine, lauramidopropyl betaine, disodium and lauriminodipropionate.
Claim 9
Dependent Claim 41 words
A process according to claim 1, wherein the anionic surfactant is selected from the group consisting of sodium lauryl sulfate, sodium alkyl sulfates having alkyl groups containing 8-18 carbon atoms and dialkyl sodium sulfosuccinates having alkyl groups containing 6-8 carbon atoms.
Claim 10
Dependent Claim 54 words
A process according to claim 2, wherein the cationic surfactant is selected from the group consisting of alkyltrimethylammonium halides containing alkyl groups containing 11-18 carbon atoms, alkylpyridinium halides containing alkyl groups containing 8-18 carbon atoms, benzylalkyldimethylammonium halides containing alkyl groups with 8-18 carbon atoms and alkyldimethylethylammonium halides containing alkyl groups containing 8-18 carbon atoms.
Claim 11
Dependent Claim 38 words
A process according to claims 1 or 2, wherein the ratio of compound to amphoteric surfactant and the cationic or anionic surfactant is about 0.15:1:1 to 4.4:1:1, and up to the maximum solubilizing capacity for a particular system.

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