Method of preparing uniform size ion exchange resin particles by partial functionalization

• US 5,081,160 A
• Filed: 04/02/1991
• Issued: 01/14/1992
• Est. Priority Date: 04/02/1991
• Status: Expired due to Fees

• Current Assignee: The Dow Chemical Company (Dow, Inc.)
• Original Assignee: The Dow Chemical Company (Dow, Inc.)
• Inventors: Westphal, Natalie N., Harris, William I., Strom, Robert M., Gaidos, Robert E., Dorta, Antonio
• Primary Examiner(s): Schofer, Joseph L.
• Assistant Examiner(s): Zitomer, Fred
• Application Number:
  US07/679,465
• Time in Patent Office: 287 Days
• Field of Search: 521/29, 521/33, 521/36, 521/28, 521/30, 521/31, 521/32
• US Class Current: 521/29
• CPC Class Codes: B01J 39/20 obtained by reactions only involving unsaturated carbon-to-carbon bonds
• CPC Class Codes: B01J 41/14 obtained by reactions only involving unsaturated carbon-to-carbon bonds
• CPC Class Codes: B01J 45/00 Ion-exchange in which a complex or a chelate is formed; Use of material as complex or chelate forming ion-exchangers; Treatment of material for improving the complex or chelate forming ion-exchange properties ion-exchange chromatography processes B01D15/36

Abstract

A process is provided for preparing ion-exchange resin particles of relatively uniform size by partial functionalization of non-uniform copolymer beads with ion-exchange groups. The non-uniform copolymer beads are preferably functionalized in a manner such that the ion-exchange groups are substituted at available sites which are most accessible to diffusion by functionalizing agents. Due to the size difference between individual copolymer particles, a greater proportion of available sites is functionalized in a small particle when compared to that of a large particle. Due to the greater proportion of ion-exchange groups present in a small particle, the small particle swells relatively more than a larger particle. The result is effectively a narrowing of the size distribution for the partially functionalized resin particles. The relatively uniform resin particles obtained by the process have performance advantages, such as reduced pressure drops, improved exchange kinetics, rinse efficiencies, and separation efficiencies when compared to fully functionalize ion-exchange resins that are non-uniform in particle size.

Claims

1. A process for preparing improved ion-exchange resins that are derived from a plurality of cross-linked copolymer beads which are non-uniform in particle size, the process comprising:

contacting the copolymer beads with a functionalizing agent under conditions sufficient to substitute ion-exchange groups onto the copolymer beads; and

continuing the contact until a partially functionalized ion-exchange resin is obtained having a particle size distribution characterized by a standard deviation located substantially at the minimum point on a two-dimensional curve, the curve being defined by a plot of standard deviation versus contact time for the copolymer beads wherein standard deviation is plotted in reference to the vertical axis and contact time is plotted in reference to the horizontal axis.

2. The process of claim 1 wherein the ion-exchange groups are substituted at available sites which are most accessible to diffusion by the functionalizing agent.

3. The process of claim 1 wherein the ion-exchange groups are substituted substantially within a continuous shell disposed about a central, essentially unfunctionalized copolymer core.

4. The process of claim 1 wherein the partially functionalized ion-exchange resin has a volume average particle diameter of from about 125 to about 2000 μ

m.

5. The process of claim 1 wherein the copolymer beads have a volume average particle diameter of from about 100 to about 1600 μ

m.

6. The process of claim 1 wherein the copolymer beads are prepared from at least one monovinylidene monomer and a cross-linking monomer.

7. The process of claim 6 wherein the at least one monovinylidene monomer is styrene.

8. The process of claim 6 wherein the at least one monovinylidene monomer is vinylbenzylchloride.

9. The process of claim 6 wherein the cross-linking monomer is divinylbenzene.

10. The process of claim 6 wherein the cross-linked copolymer beads comprise from about 88 to about weight percent of the at least one monovinylidene monomer and from about 0.5 to about 12 weight percent of the cross-linking monomer, based on total weight of the monomers employed.

11. The process of claim 1 wherein the cross-linked copolymer beads are macroporous.

12. The process of claim 1 wherein the cross-linked copolymer beads are of a gel copolymer.

13. The process of claim 1 wherein the cross-linked copolymer beads have a β

of from about 1.5 to about 10 wherein β

is defined by the formula ##EQU7## wherein;

V_r is the volume of a copolymer bead which is substantially completely functionalized with ion-exchange groups and swollen with a solvent, typically water; and

V_p is the volume of the unreacted copolymer bead.

14. The process of claim 1 wherein the cross-linked copolymer beads have a β

of from about 3 to about 5 wherein β

is defined as in claim 13.

15. The process of claim 1 wherein the ion-exchange groups are cation-exchange groups, anion-exchange groups, or chelate-exchange groups.

16. The process of claim 1 wherein the ion-exchange groups are sulfonic acid groups.

17. The process of claim 1 wherein the partially functionalized ion-exchange resin has from about 10 to about 90 percent of the capacity of an otherwise similar resin which is substantially completely functionalized with the ion-exchange groups.

18. The process of claim 1 wherein the partially functionalized ion-exchange resin has from about 30 to about 70 percent of the capacity of an otherwise similar resin which is substantially completely functionalized with the ion-exchange groups.