Process for the preparation of porous polymer beads

• US 4,940,734 A
• Filed: 11/23/1988
• Issued: 07/10/1990
• Est. Priority Date: 11/23/1988
• Status: Expired due to Fees

• Current Assignee: American Colloid Company (Minerals Technologies Incorporated)
• Original Assignee: American Colloid Company (Minerals Technologies Incorporated)
• Inventors: Ley, David A., Hiscock, Laura J., Cooke, Michael T.
• Primary Examiner(s): Hoke, Veronica P.
• Application Number:
  US07/275,170
• Time in Patent Office: 594 Days
• Field of Search: 521/84.1, 521/89, 521/60, 521/63, 521/64, 521/142, 521/143, 521/144, 521/147, 521/149, 530/413
• US Class Current: 521/84.1
• CPC Class Codes: B01J 20/26 Synthetic macromolecular compounds
• CPC Class Codes: C08J 2333/20 Homopolymers or copolymers of acrylonitrile C08J2355/02 takes precedence
• CPC Class Codes: C08J 3/12 Powdering or granulating
• CPC Class Codes: C08J 9/28 by elimination of a liquid phase from a macromolecular composition or article, e.g. drying of coagulum

Abstract

Isotropic porous polymer beads having controllable surface porosity and large pore diameters from about 0.002 to about 5 microns are produced from solutions of an acrylonitrile polymer or a copolymer by a thermally-induced phase separation process including intensively shearing the polymer solution into small droplets. The use of mixed solvent non-solvent combinations as solvents for the polymers, and preferably reducing the polymer content in solution to below 10 percent produces high pore content, substantially spherical beads having a morphology ideally suited to the chromatography of large molecules, such as proteins, and for enzyme-binding.

Claims

1. A process for the preparation of porous polymer beads with controllable surface porosity wherein said beads are substantially nonswellable in water and have substantially uniform pores of not substantially greater than about 5 microns in diameter, said process comprising

(i) heating and mixing an acrylonitrile homopolymer or copolymer thereof with a mixture comprising a solvent and a non-solvent for the polymer to form a homogeneous solution having a polymer solids concentration range of from 0.5 to less than 20 percent:

(ii) breaking the homogeneous solution into droplets using a high shearing technique;

(iii) cooling the droplets, optionally in the presence of an inert liquid, to bring about phase separation and solidification of the polymer in the droplets;

(iv) separating the solidified droplets from any inert liquid and removing the solvent non-solvent mixture from the solidified droplets to produce porous beads.

2. A process as defined in claim 1 wherein step (i) further comprises dispersing the solution in a hot inert liquid and step (ii) comprises breaking the homogeneous dispersion into droplets by use of a static mixer.

3. A process as defined in claim 1 wherein step (ii) comprises breaking the homogeneous solution into droplets by use of an ultrasonic nozzle.

4. A process as defined in claim 1 wherein step (ii) comprises breaking the homogeneous solution into droplets by use of an atomization nozzle.

5. A process as defined in claim 1 wherein step (ii) comprises breaking the homogeneous solution into droplets through the use of laminar jets.

6. A process as defined in claim 1 wherein step (i) further comprises dispersing the solution in a hot inert liquid and step (ii) comprises breaking the homogeneous dispersion into droplets by homogenization.

7. A process as defined in claim 1 wherein said solvent comprises dimethyl sulfone, the non-solvent comprises urea, water, propylene glycol, ethylene glycol or a mixture thereof and step (i) is carried out at a temperature of at least about 130°

C.

8. A process as defined in claim 1 wherein the inert liquid comprises mineral oil, kerosene, heptane, or a mixture thereof.

9. A process as defined in claim 1 wherein the inert liquid is extracted from the solidified droplets with a non-solvent for the polymer, said non-solvent comprising acetone, methanol, water, or a mixture thereof.

10. A process for the production of porous beads as defined in claim 1 wherein said polyacrylonitrile copolymer comprises an acrylonitrile copolymerized with a (C₂ -C₆) monoolefin, a vinylaromatic, a vinylaminoaromatic, a vinyl halide, a (C₁ -C₆) alkyl (meth)acrylate, a (meth)acrylamide, a vinyl pyrrolidone, a vinyl pyridine, a (C₁ -C₆)hydroxyalkyl (meth)acrylate, a (meth)acrylic acid, an acrylamidomethylpropylsulfonic acid, an N-hydroxy- containing (C₁ -C₆) alkyl(meth)acrylamide, or a mixture of any of the foregoing.

11. A process as defined in claim 1 further comprising the step of at least partially filling the pores of said porous beads with a compound.

12. A process as defined in claim 11 wherein said compound is selected from the group consisting of a protein, an enzyme, a hormone, a peptide, a polysaccharide, a nucleic acid, a dye, a pigment or a mixture of any of the foregoing.

13. A process as defined in claim 12 wherein said compound comprises a protein.

14. A process as defined in claim 12 wherein the pore diameter of said porous beads is at least about 3 times the diameter of said compound.

15. A process as defined in claim 1 wherein the homogeneous solution of step (i) contains less than about 10 weight percent total polymer or copolymer solids and the porous polymer beads are substantially skinless.

16. The product of the process as defined in claim 1 wherein the pore volume is not substantially less than about 1.5 ml/g.

17. A product as defined in claim 16 wherein said beads are substantially spherical.

18. A product as defined in claim 16 wherein said beads comprise a copolymer of from about 45 to about 99.5 mole percent of acrylonitrile.

19. A product as defined in claim 16 wherein the beads are substantially isotropic.

20. A product of the process as defined in claim 15.