US4390670A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Acrylate/maleate copolymers, their preparation and use as antiscalants
Assignee: Pfizer Inc
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Filing: 1981-02-09
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Granted: 1983-06-28
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Expires: 2001-02-09
Abstract
Abstract Substantially homogeneous acrylate/maleate copolymers of number average molecular weight of 500 to 5000 are prepared by copolymerizing 35 to 65 mole percent acrylic or methacrylic acid with 65 to 35 mole percent maleic anhydride at 80 DEG to 150 DEG C. in the presence of a polymerization initiator and a chain-transfer solvent such that both the monomers and the formed polymer remain in solution and the mole ratio of the acrylic or methacrylic acid monomer to the maleic anhydride monomer in the solvent is maintained below about 0.2 throughout the polymerization. The copolymers in hydrolyzed form are employed at a level of from about 0.1 to 100 ppm for prevention of alkaline calcium and magnesium scale formation, such as during seawater evaporative desalination.
Inventors
- 👤 Stanley W. Walinsky
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-31 20:12
CPC Classifications
C; C02; C02F; C02F5/00; C02F5/08; C02F5/10; C08; C08F; C08F220/00; C08F220/02; C08F220/04; C08F220/06; C08F222/00; C08F222/04; C08F222/06
Claims Analysis
Total Claims: 6
Claim 1
Independent Claim
186 words
A process for preparing a substantially homogeneous acrylate-maleate copolymer of number average molecular weight from about 500 to 5000, which comprises: copolymerizing from about 35 to 65 mole percent acrylic or methacrylic acid monomer with from about 65 to 35 mole percent maleic anhydride monomer over a period of from about 0.3 to 10 hours at a temperature of from about 80° to 150° C. in the presence of from about 5 to 25 weight percent polymerization initiator, based on the total weight of said monomers, and from about 45 to 90 weight percent of chain-transfer solvent, based on the total weight of said monomers, initiator and solvent, said maleic anhydride monomer, said initiator and up to about 10 percent of said acrylic or methacrylic acid monomer being dissolved in said solvent and the remainder of said acrylic or methacrylic acid monomer being introduced over said period at a rate such that said monomer and said copolymer remain in solution in said solvent, said solvent being selected from the group consisting of ketones, esters and ethers having from 4 to 10 carbon atoms, and mixtures thereof.
Claim 2
Dependent Claim
186 words
A process for preparing a substantially homogeneous acrylate-maleate copolymer of number average molecular weight from about 500 to 5000, which comprises: copolymerizing from about 35 to 65 mole percent acrylic or methacrylic acid monomer with from about 65 to 35 mole percent maleic anhydride monomer over a period of from about 0.3 to 10 hours at a temperature of from about 80° to 150° C. in the presence of from about 5 to 25 weight percent polymerization initiator, based on the total weight of said monomers, and from about 45 to 90 weight percent of chain-transfer solvent, based on the total weight of said monomers, initiator and solvent, said maleic anhydride monomer, said initiator and up to about 10 percent of said acrylic or methacrylic acid monomer being dissolved in said solvent and the remainder of said acrylic or methacrylic acid monomer being introduced over said period at a rate such that said monomer and said copolymer remain in solution in said solvent, said solvent being selected from the group consisting of ketones, esters and ethers having from 4 to 10 carbon atoms, and mixtures thereof.
Claim 3
Dependent Claim
25 words
The process of claim 1 wherein the resulting copolymer solution is maintained at said temperature for from about 10 to 120 minutes following said addition.
Claim 4
Dependent Claim
11 words
The process of claim 1 wherein said initiator is di-t-butyl peroxide.
Claim 5
Dependent Claim
29 words
The process of claim 1 wherein from about 40 to 50 mole percent methacrylic acid monomer is copolymerized with from about 60 to 50 mole percent maleic anhydride monomer.
Claim 6
Dependent Claim
86 words
The process of claim 2 wherein from about 40 to 45 mole percent methacrylic acid monomer is added over a period of from about 2 to 4 hours to a solution of from about 60 to 55 mole percent maleic anhydride monomer, 10 to 20 weight percent di-t-butyl peroxide and 50 to 60 weight percent methyl isobutyl ketone at a temperature of from about 110° to 120° C., and said solution is held at that temperature for from about 15 to 90 minutes following said addition.
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) | 1986-06-27 | 1986-12-27 | 1987-06-28 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1990-06-27 | 1990-12-27 | 1991-06-28 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1994-06-27 | 1994-12-27 | 1995-06-28 | $7700.00 | Window Closed / Lapsed |