Patent US4564644A successfully refreshed from Google Patents.
US4564644A
Expired / Lapsed
US
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Ion exchange resins prepared by sequential monomer addition
Assignee: DIAMOND TECHNOLOGY PARTNERSHIP Co
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Filing: 1983-06-22
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Granted: 1986-01-14
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Expires: 2003-06-22
Abstract
Abstract A process for preparing copolymer beads suitable for conversion to ion exchange resins, comprising forming a polymeric matrix containing a plurality of free radicals, and continuously adding to said matrix, under conditions suitable for polymerizing a monomer feed which is imbibed by and polymerized within the matrices. Ion exchange resins prepared from beads made by such process exhibit improved osmotic and mechanical properties.
Inventors
- 👤 William I. Harris
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-31 14:05
CPC Classifications
C; C08; C08F; C08F257/00; C08F257/02; B; B01; B01J; B01J39/00; B01J39/08; B01J39/16; B01J39/18; B01J39/20; B01J41/00; B01J41/08; B01J41/12; B01J41/14; C08F285/00; C08F291/00
Claims Analysis
Total Claims: 22
Claim 1
Independent Claim
232 words
A process for preparing crosslinked copolymer beads comprising: (a) forming a suspension of particles of a crosslinked or noncrosslinked polymer in a continuous aqueous phase, then (b) swelling said polymer particles with a first monomer mix comprising from about 75 to about 99.5 parts by weight of a monoethylenically unsaturated monomer, about 0.5 to about 25 parts by weight of a polyethylenically unsaturated monomer and a sufficient amount of a substantially water-insoluble free radical initiator to catalyze the polymerization of said first monomer mix and a second monomer mix, then (c) polymerizing said first monomer mix within said polymer particles until about 40 to about 95 weight percent of said monomers are converted to polymer, then (d) continue adding to said suspension a second monomer mix, which second monomer mix comprises a monoethylenically unsaturated monomer but contains essentially no free radical initiator, said addition of said second monomer mix being made under conditions including a temperature sufficient to initiate the free radical polymerization of the monomer in said second monomer mix such that said monomer mix is imbibed by said polymer particles and the polymerization of said second monomer mix within said polymer particles is catalyzed by the free radical initiator contained in said first monomer mix and wherein the monomers of the second monomer mix, when polymerized, comprise from about 40 to about 90 weight percent of the product copolymer beads.
Claim 2
Dependent Claim
232 words
A process for preparing crosslinked copolymer beads comprising: (a) forming a suspension of particles of a crosslinked or noncrosslinked polymer in a continuous aqueous phase, then (b) swelling said polymer particles with a first monomer mix comprising from about 75 to about 99.5 parts by weight of a monoethylenically unsaturated monomer, about 0.5 to about 25 parts by weight of a polyethylenically unsaturated monomer and a sufficient amount of a substantially water-insoluble free radical initiator to catalyze the polymerization of said first monomer mix and a second monomer mix, then (c) polymerizing said first monomer mix within said polymer particles until about 40 to about 95 weight percent of said monomers are converted to polymer, then (d) continue adding to said suspension a second monomer mix, which second monomer mix comprises a monoethylenically unsaturated monomer but contains essentially no free radical initiator, said addition of said second monomer mix being made under conditions including a temperature sufficient to initiate the free radical polymerization of the monomer in said second monomer mix such that said monomer mix is imbibed by said polymer particles and the polymerization of said second monomer mix within said polymer particles is catalyzed by the free radical initiator contained in said first monomer mix and wherein the monomers of the second monomer mix, when polymerized, comprise from about 40 to about 90 weight percent of the product copolymer beads.
Claim 3
Dependent Claim
43 words
The process of claim 1 wherein the monoethylenically unsaturated monomer employed in step (b) and (d) comprises a monovinyl aromatic or an alkyl ester of acrylic or methacrylic acid and the polyethylenically unsaturated monomer comprises divinylbenzene, an alkylene diacrylate or an alkylene dimethacrylate.
Claim 4
Dependent Claim
31 words
A process of claim 1 wherein said second monomer mix is added continuously or intermittently such that the instantaneous conversion during said addition of monomer mix is at least 20 percent.
Claim 5
Dependent Claim
38 words
A process of claim 1 wherein the particles of (a) have a diameter in the range from about 10 to about 750 microns and the diameter of the copolymer bead ranges from about 50 to about 2000 microns.
Claim 6
Dependent Claim
23 words
A process of claim 1 which further comprises attaching active ion exhange groups to the copolymer beads to form an ion exchange resin.
Claim 7
Dependent Claim
61 words
The process of claim 1 wherein said copolymer beads, when fully aminated to form an anion exchange resin, exhibit a crush strength of at least 700 g/bead and a resistance to osmotic shock such that when said beads are contacted with 10 cycles of alternating 8M HCl and 8M NaOH, fewer than 15 percent by number of the beads are broken.
Claim 8
Dependent Claim
42 words
The process of claim 1 wherein the crosslinked copolymer bead has a core/shell morphology and the polymers of the shell have an average crosslink density which is less than or equal to the average crosslink density of the polymers of the core.
Claim 9
Dependent Claim
21 words
A process of claim 5 wherein the resin is an anion exchange resin, a cation exchange resin or a chelating resin.
Claim 10
Dependent Claim
11 words
Crosslinked copolymer beads prepared according to the process of claim 1.
Claim 11
Dependent Claim
44 words
A process of claim 8 wherein said cation exchange resin has a crush strength of at least 1500 g/bead and wherein fewer than 10 percent by number of said beads are broken when contacted with 10 cycles of alternating 8M HCl and 8M NaOH.
Claim 12
Dependent Claim
232 words
A process for preparing crosslinked copolymer beads comprising: (a) forming a suspension of particles of a crosslinked or noncrosslinked polymer in a continuous aqueous phase, then (b) swelling said polymer particles with a first monomer mix comprising from about 75 to about 99.5 parts by weight of a monoethylenically unsaturated monomer, about 0.5 to about 25 parts by weight of a polyethylenically unsaturated monomer and a sufficient amount of a substantially water-insoluble free radical initiator to catalyze the polymerization of said first monomer mix and a second monomer mix, then (c) polymerizing said first monomer mix within said polymer particles until about 20 to about 95 weight percent of said monomer are converted to polymer, then (d) continue adding to said suspension a second monomer mix, which second monomer mix comprises a monoethylenically unsaturated monomer but contains essentially no free radical initiator, said addition of said second monomer mix being made under conditions including a temperature sufficient to initiate the free radical polymerization of the monomer in said second monomer mix such that said monomer mix is imbibed by said polymer particles and the polymerization of said second monomer mix within said polymer particles is catalyzed by the free radical initiator contained in said first monomer mix and wherein the monomers of the second monomer mix, when polymerized, comprise from about 40 to about 90 weight percent of the product copolymer beads.
Claim 13
Dependent Claim
232 words
A process for preparing crosslinked copolymer beads comprising: (a) forming a suspension of particles of a crosslinked or noncrosslinked polymer in a continuous aqueous phase, then (b) swelling said polymer particles with a first monomer mix comprising from about 75 to about 99.5 parts by weight of a monoethylenically unsaturated monomer, about 0.5 to about 25 parts by weight of a polyethylenically unsaturated monomer and a sufficient amount of a substantially water-insoluble free radical initiator to catalyze the polymerization of said first monomer mix and a second monomer mix, then (c) polymerizing said first monomer mix within said polymer particles until about 20 to about 95 weight percent of said monomer are converted to polymer, then (d) continue adding to said suspension a second monomer mix, which second monomer mix comprises a monoethylenically unsaturated monomer but contains essentially no free radical initiator, said addition of said second monomer mix being made under conditions including a temperature sufficient to initiate the free radical polymerization of the monomer in said second monomer mix such that said monomer mix is imbibed by said polymer particles and the polymerization of said second monomer mix within said polymer particles is catalyzed by the free radical initiator contained in said first monomer mix and wherein the monomers of the second monomer mix, when polymerized, comprise from about 40 to about 90 weight percent of the product copolymer beads.
Claim 14
Dependent Claim
43 words
The process of claim 11 wherein the monoethylenically unsaturated monomer employed in step (b) and (d) comprises a monovinyl aromatic or an alkyl ester of acrylic or methacrylic acid and the polyethylenically unsaturated monomer comprises divinylbenzene, an alkylene diacrylate or an alkylene dimethacrylate.
Claim 15
Dependent Claim
31 words
A process of claim 11 wherein said second monomer mix is added continuously or intermittently such that the instantaneous conversion during said addition of monomer mix is at least 20 percent.
Claim 16
Dependent Claim
38 words
A process of claim 11 wherein the particles of (a) have a diameter in the range from about 10 to about 750 microns and the diameter of the copolymer bead ranges from about 50 to about 2000 microns.
Claim 17
Dependent Claim
23 words
A process of claim 11 which further comprises attaching active ion exchange groups to the copolymer beads to form an ion exchange resin.
Claim 18
Dependent Claim
61 words
The process of claim 11 wherein said copolymer beads, when fully aminated to form an anion exchange resin, exhibit a crush strength of at least 700 g/bead and a resistance to osmotic shock such that when said beads are contacted with 10 cycles of alternating 8M HCl and 8M NaOH, fewer than 15 percent by number of the beads are broken.
Claim 19
Dependent Claim
42 words
The process of claim 11 wherein the crosslinked copolymer bead has a core/shell morphology and the polymers of the shell have an average crosslink density which is less than or equal to the average crosslink density of the polymers of the core.
Claim 20
Dependent Claim
21 words
A process of claim 11 wherein the resin is an anion exchange resin, a cation exchange resin or a chelating resin.
Claim 21
Dependent Claim
11 words
Crosslinked copolymer beads prepared according to the process of claim 11.
Claim 22
Dependent Claim
44 words
A process of claim 11 wherein said cation exchange resin has a crush strength of at least 1500 g/bead and wherein fewer than 10 percent by number of said beads are broken when contacted with 10 cycles of alternating 8M HCl and 8M NaOH.
References Cited (Backward Citations)
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1989-01-13 | 1989-07-15 | 1990-01-14 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1993-01-13 | 1993-07-15 | 1994-01-14 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1997-01-13 | 1997-07-15 | 1998-01-14 | $7700.00 | Window Closed / Lapsed |