US4104209A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Highly porous ion exchange resins prepared by suspension polymerization in the presence of linear polymer
Assignee: Sybron Chemical Holdings Inc
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Filing: 1976-07-06
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Granted: 1978-08-01
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Expires: 1996-07-06
Abstract
Abstract A process for the preparation of an ion exchange resin of higher porosity and purity is described. The porosity is achieved by inserting polar, preferably hydrolyzable linear polymer into the polymerizing phase. The insert is later extracted from the polymerized beads.
Inventors
- 👤 John A. Mikes
- 👤 Albert H. Greer
- 👤 Amos Norwood
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-27 08:55
CPC Classifications
C; C08; C08J; C08J9/00; C08J9/26; B; B01; B01J; B01J39/00; B01J39/08; B01J39/16; B01J39/18; B01J39/20; C08F; C08F2/00; C08F2/12; C08F2/16; C08F2/18; C08F2/20; C08J2357/00
Claims Analysis
Total Claims: 7
Claim 1
Independent Claim
295 words
A process for the preparation of crosslinked copolymer beads suitable for conversion to ion exchange resins having improved mechanical properties, improved chemical properties and porosity of 0.14 to 0.85 ml/g by octane absorption which comprises the steps of (a) forming a liquid monomer phase comprising: i. a mixture of mono-olefinic monomer(s) and at least one poly-olefinic monomer which are miscible and copolymerizable, said mono-olefinic monomer selected from a group consisting of mono-vinyl aromatic hydrocarbons, mono-vinyl heterocylic compounds, and (meth)acrylic esters, and said polyolefinic monomers selected from the group consisting of polyvinyl aromatic hydrocarbons, poly(meth)acrylates and polyvinyl heterocylic compounds, ii. from 5-20 parts by weight of total monomers of a linear polymer component selected from a group consisting of cellulose acetate butyrate, cellulose acetate, cellulose nitrate, polycaprolactam, polyvinyl pyridine and aliphatic polyesters, dispersed and preferably dissolved in the monomer phase, iii. optionally an inert solvent selected from either C 6 -C 10 hydrocarbons or C 3 -C 6 monohydric alcohols, such solvent being included in amounts of 0-50 percent by weight based on the total monomer weight, iv. an initiator component providing free radical selected from a group consisting of peroxides, hydroperoxides, azo/nitrile compounds, and (b) forming a aqueous phase comprising: i. a major portion of water ii. salts of alkali and/or alkali earth metals iii. hydrophilic polymer(s) selected from a group consisting of gelatin, casein, starch, polyvinyl alcohol, maleic acid copolymer(s), poly(meth)acrylic acid derivatives; and (c) combining said monomer phase (a) and said aqueous phase (b) to form a suspension of said monomer phase in said aqueous phase and (d) heating said suspension to polymerization temperature of between 50° C and 90° C while stirring said dispersion to form a multiplicity of macroporous polymer beads, and (e) separating said macroporous beads from the aqueous phase.
Claim 2
Dependent Claim
295 words
A process for the preparation of crosslinked copolymer beads suitable for conversion to ion exchange resins having improved mechanical properties, improved chemical properties and porosity of 0.14 to 0.85 ml/g by octane absorption which comprises the steps of (a) forming a liquid monomer phase comprising: i. a mixture of mono-olefinic monomer(s) and at least one poly-olefinic monomer which are miscible and copolymerizable, said mono-olefinic monomer selected from a group consisting of mono-vinyl aromatic hydrocarbons, mono-vinyl heterocylic compounds, and (meth)acrylic esters, and said polyolefinic monomers selected from the group consisting of polyvinyl aromatic hydrocarbons, poly(meth)acrylates and polyvinyl heterocylic compounds, ii. from 5-20 parts by weight of total monomers of a linear polymer component selected from a group consisting of cellulose acetate butyrate, cellulose acetate, cellulose nitrate, polycaprolactam, polyvinyl pyridine and aliphatic polyesters, dispersed and preferably dissolved in the monomer phase, iii. optionally an inert solvent selected from either C 6 -C 10 hydrocarbons or C 3 -C 6 monohydric alcohols, such solvent being included in amounts of 0-50 percent by weight based on the total monomer weight, iv. an initiator component providing free radical selected from a group consisting of peroxides, hydroperoxides, azo/nitrile compounds, and (b) forming a aqueous phase comprising: i. a major portion of water ii. salts of alkali and/or alkali earth metals iii. hydrophilic polymer(s) selected from a group consisting of gelatin, casein, starch, polyvinyl alcohol, maleic acid copolymer(s), poly(meth)acrylic acid derivatives; and (c) combining said monomer phase (a) and said aqueous phase (b) to form a suspension of said monomer phase in said aqueous phase and (d) heating said suspension to polymerization temperature of between 50° C and 90° C while stirring said dispersion to form a multiplicity of macroporous polymer beads, and (e) separating said macroporous beads from the aqueous phase.
Claim 3
Dependent Claim
38 words
The process of claim 1 wherein the porosity of the resulting macroporous beads is increased subsequent to the polymerization by removing the added linear polymer component by leaching and/or heating the beads dispersed in an alkaline aqueous medium.
Claim 4
Dependent Claim
37 words
The process of claim 1 wherein the porosity of the resulting macroporous beads is increased subsequent to the polymerization by removing the added linear polymer component by leaching and/or heating the beads in an acidic aqueous medium.
Claim 5
Dependent Claim
44 words
The process of claim 1 wherein the porosity of the resulting macroporous beads is increased subsequent to the polymerization by removing the added linear polymer component by leaching and/or heating the beads in an organic liquid which is a solvent of said linear polymer.
Claim 6
Dependent Claim
55 words
The process of claim 1 wherein the porosity of the resulting macroporous beads is increased subsequent to the polymerization by removing the added linear polymer component by decomposing and/or removing said linear polymer by reaction media used for the chemical transformation of the beads into ion exchangers, adsorbents, and macroporous polymer beads of other purposes.
Claim 7
Dependent Claim
18 words
The process of claim 1 wherein said mono olefinic monomer is styrene and said polyolefinic monomer is divinylbenzene.
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) | 1981-07-31 | 1982-01-30 | 1982-08-01 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1985-07-31 | 1986-01-30 | 1986-08-01 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1989-07-31 | 1990-01-30 | 1990-08-01 | $7700.00 | Window Closed / Lapsed |