Process for production of polymer particles

• US 5,583,166 A
• Filed: 02/21/1995
• Issued: 12/10/1996
• Est. Priority Date: 02/20/1991
• Status: Expired due to Term

• Current Assignee: Idemitsu Kosan Company Limited
• Original Assignee: Idemitsu Petrochemical Co., Ltd. (Idemitsu Kosan Company Limited)
• Inventors: Okamoto, Masaya, Koyama, Yoshinari, Kunishi, Noriyuki
• Primary Examiner(s): Michl, Paul R.
• Assistant Examiner(s): MERRIAM, ANDREW EDWIN
• Application Number:
  US08/391,264
• Time in Patent Office: 658 Days
• Field of Search: 524/464, 528/501, 528/497, 528/498, 528/491, 523/340
• US Class Current: 523/340
• CPC Class Codes: B29B 9/08 by agglomerating smaller particles
• CPC Class Codes: B29K 2069/00 Use of PC, i.e. polycarbonates or derivatives thereof, as moulding material
• CPC Class Codes: C08J 3/12 Powdering or granulating
• CPC Class Codes: C08J 3/14 by precipitation from solutions C08J3/122 takes precedence

Abstract

An efficient method of obtaining polymer particles by evaporating an organic solvent while maintaining a solution of a polymer in the organic solvent in contact with polymer particles, using a simple apparatus and a simple procedure. The polymer particles (powder) produced by the method have a small particle diameter, a high bulk density, a small amount of residual solvent, and are thus excellent in quality. The method includes introducing the organic solvent solution of the polymer into a particle producing zone which does not substantially contain steam, wherein an atmosphere is maintained in which the organic solvent is vaporizable and the particles are stirred. The organic solvent is evaporated, while maintaining the solution in contact with the polymer particles. Additionally a breaker is used in combination with a mixer; a poor solvent is employed; polymer particles are recycled; or a horizontal particle producing vessel is utilized.

Claims

1. A process for producing polymer particles from an organic solvent solution consisting essentially of an organic solvent, a poor solvent, and polymer particles being dissolved in said organic solvent solution, the process comprising:

(a) initially introducing said polymer particles into a particle producing zone, and stirring said polymer particles under conditions in which said organic solvent would be vaporizable,

(b) introducing said organic solvent solution having a polymer concentration of 3 to 70% by weight, onto said polymer particles which are maintained in said particle producing zone, said particle producing zone not substantially containing steam, said solution being added in an amount of not more than 250% by weight per hour based on the amount of the polymer particles which are initially held in said particle producing zone, said poor solvent being selected from the group consisting of benzene, toluene, xylene, pentane, hexane, heptane, octane, acetone and methyl ethyl ketone, said poor solvent being in an amount of 5 to 50% by weight based on the weight of said polymer in said organic solvent solution, wherein said polymer is not precipitated by said amount of said poor solvent, and

(c) evaporating said organic solvent, while maintaining said organic solvent solution of said polymer in contact with said polymer particles which are maintained in said particle producing zone, to produce said polymer particles.

2. The process as claimed claim 1 wherein the particle producing zone is a complete mixing particle producing vessel.

4. The process as claimed in claim 1 wherein the organic solvent is methylene chloride.

5. The process as claimed in claim 1 wherein the polymer is selected from the group consisting of polycarbonate and polyarylate.

6. The process according to claim 1 wherein the polymer is polyester polycarbonate.

7. The process as claimed in claim 5 wherein the organic solvent is methylene chloride.

8. The process as claimed in claim 6 wherein the organic solvent is methylene chloride.

9. The process as claimed in claim 1 wherein the polymer is selected from the group consisting of polycarbonate, polyarylate and polyamide;

the organic solvent is selected from the group consisting of methylene chloride., chloroform, chlorobenzene, dioxane and tetrahydrofuran; and

the process is carried out at a temperature of 0 to 200°

C., an absolute pressure of 0.1 to 11 kg/cm² and with a residence time of polymer in the particle producing zone of 0.01 to 10 hours.

10. The process as claimed in claim 9 wherein the polymer is dissolved in the organic solvent in a concentration of 10 to 60% by weight;

the temperature is 30 to 150°

C. and the pressure is 0.5 to 5 kg/cm².

11. The process as claimed in claim 10 wherein the polymer is polycarbonate having a particle diameter of 50 μ

m to 3 mm.

12. The process as claimed in claim 1 wherein the organic solvent solution is added in an amount of not more than 100% by weight per hour based on the amount of the polymer particles held in the polymer producing zone.

14. The process as claimed in claim 1 wherein the process is continuous and the polymer particles are stirred homogeneously.

16. The process as claimed in claim 1 wherein part of the polymer particles produced in the particle producing zone is continuously recycled to said particle producing zone.

3. A process for producing polymer particles from an organic solvent solution consisting essentially of an organic solvent, a poor solvent, and polymer particles being dissolved in said organic solvent solution, the process comprising:

(a) initially introducing said polymer particles into a horizontal vessel having a horizontal particle producing zone, and stirring said polymer particles under conditions in which said organic solvent would be vaporizable,

(b) introducing said organic solvent solution into said horizontal particle producing zone, said organic solvent solution being divided into a plurality of streams for introducing said organic solvent solution through a plurality of points in said horizontal particle producing zoned and onto said polymer particles which are maintained in said horizontal particle producing zone, said organic solvent solution having a polymer concentration of 3 to 70% by weight, said particle producing zone not substantially containing steam, said solution being added in an amount of not more than 250% by weight per hour based on the amount of the polymer particles which are initially held in said horizontal particle producing zone, said poor solvent being selected from the group consisting of benzene, toluene, xylene, pentane, hexane, heptane, octane, acetone and methyl ethyl ketone, said poor solvent being in an amount of 5 to 50% by weight based on the weight of said polymer in said organic solvent solution, wherein said polymer is not precipitated by said amount of said poor solvent and

(c) evaporating said organic solvent, while maintaining said organic solvent solution of said polymer in contact with said polymer particles which are maintained in said horizontal particle producing zone, to produce said polymer particles.

13. The process as claimed in claim 3 wherein the organic solvent solution is added in an amount of not more than 100% by weight per hour based on the amount of the polymer particles held in the polymer producing zone.

15. The process as claimed in claim 3 wherein the process is continuous and the polymer particles are stirred homogeneously.