# US 5,350,584 A · Spheronization process using charged resins

> Agents: this data is available as JSON from the patentgrep API and MCP server — see https://patentgrep.com/llms.txt

- Number: US 5,350,584 A
- Document ID: US5350584A
- Status: Granted
- Kind: A
- Application number: 07/906,226
- Filed: 1992-06-26
- Granted: 1994-09-27
- Earliest claimed: 1992-06-26
- Assignees: Merck & Co., Inc.
- Inventors: Gregory A. McClelland; Gaylen M. Zentner
- Web page: https://patentgrep.com/patent/US5350584A

## CPC

- A61K 9/1694: {resulting in granules or microspheres of the matrix type containing more than 5% of excipient}
- A61K 9/1635: {obtained by reactions only involving carbon-to-carbon unsaturated bonds, e.g. polyvinyl pyrrolidone, poly(meth)acrylates}
- A61K: PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES (devices or methods specially adapted for bringing pharmaceutical products into particular physical or administering forms A61J3/00; chemical aspects of, or use of materials for deodorisation of air, for disinfection or sterilisation, or for bandages, dressings, absorbent pads or surgical articles A61L; soap compositions C11D)

## Abstract

The invention comprises a novel process for the spheronization of charged resins. Spherical multiparticlates are produced which range in size from 0.3 mm to 3 mm in diameter. The spherical particle product is microcrystalline-free. The process consists of the steps of mixing followed by wet granulation, spheronization and drying.

## Claims

### Claim 1

A process for the production of microcrystalline cellulose free multiparticulate comprise a medicament and a charged resin, comprising the steps of:
(a) adding a charged resin and an excipient to a mixing vessel;
(b) mixing the charged resin and excipient of (a) to obtain a uniform formulation;
(c) adding a granulating solution to wet the dry mixture of (b);
(d) granulating the mixture until a uniform, wet granulation results;
(e) extruding the wet granulation of (d) through a screen to produce strands;
(f) spheronizing the strands of (e) to produce microcrystalline cellulose free spherical multiparticulates;
(g) collecting and drying the spherical multiparticulates.

### Claim 2 (depends on 1)

The process of claim 1 wherein a medicament is added to the dry ingredients.

### Claim 3 (depends on 1)

The process for the production of spherical multiparticulates of claim 1 wherein the charged resin is chosen from the group consisting of sodium polystyrene sulfonate, the chloride salt of cholestyramine resin USP, the acid form of methacrylic acid-divinyl benzene, carboxypolymethylenes prepared from acrylic acid cross-linked with allyl ethers of sucrose or pentaerythritol, and sodium polyacrylate.

### Claim 4 (depends on 1)

The process for the production of spherical multiparticulates of claim 1 wherein the medicament is selected from the group consisting of simvastatin, lovastatin, pravastatin, diltiazem, and the pharmaceutically active salts and crystal forms of these compounds.

### Claim 5 (depends on 1)

The process for the production of spherical multiparticulates of claim 1 wherein the excipients are osmotically active agents.

### Claim 6 (depends on 5)

The process for the production of spherical multiparticulates of claim 5 wherein the osmotically active agents are selected from the group consisting of sodium chloride, sodium dodecyl sulfate, disodium phosphate, monosodium phosphate, citric acid, trisodium citrate, adipic acid, mannitol, sucrose, and lactose.

### Claim 7 (depends on 1)

The process for the production of spherical multiparticulates of claim 1 wherein the dry material is mixed from about 1 to about 60 minutes.

### Claim 8 (depends on 1)

The process for the production of spherical multiparticulates of claim 1 wherein the mixing is accomplished using a planetary mixer.

### Claim 9 (depends on 1)

The process for the production of spherical multiparticulates of claim 1 wherein the granulating solvent is water.

### Claim 10 (depends on 1)

The process for the production of spherical multiparticulates of claim 1 wherein the granulating solvent is a mixture of water and ethanol.

### Claim 11 (depends on 1)

The process for the production of spherical multiparticulates of claim 1 wherein a component of the formulation is dissolved in the granulating solvent prior to the wet granulation step.

### Claim 12 (depends on 1)

The process for the production of spherical multiparticulates of claim 1 wherein the extrusion occurs through a screen having openings of from about 0.5 mm to about 3 mm.

### Claim 13 (depends on 1)

The process for the production of spherical multiparticulates of claim 1 wherein the spheronizer comprises a friction plate which rotates at speeds of from about 500 rpm to about 2000 rpm.