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US4147627A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for scale control using mixtures of polycationic and polyanionic polymers

Assignee: Wyeth Holdings LLC
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Filing: 1977-02-07
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Granted: 1979-04-03
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Expires: 1997-02-07
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Abstract

Abstract Magnesium hydroxide scale formation in evaporative desalination units is inhibited by adding to the saline water being processed a mixture of certain polycationic and polyanionic polymers.

Inventors

  • 👤 Richard M. Goodman

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-30 18:43
CPC Classifications
C; C02; C02F; C02F5/00; C02F5/08; C02F5/10

Claims Analysis

Total Claims: 15
Claim 1
Independent Claim 232 words
A process for inhibiting formation of magnesium hydroxide scale or sludge in evaporative desalination units which comprises adding to the saline water being processed in said units an effective amount of a mixture of (1) a polyanionic polymer containing at least about 50 mole percent or repeating units derived from an acrylic acid and any balance of repeating units derived from one or more monomers compatible therewith, the acid units being in the form of at least one member selected from the group consisting of free acid radical, ammonium salt, and alkali metal salts, and (2) a polycationic polymer selected from the group consisting of (a) dimethylaminepolyamine-epichlorohydrin reaction product wherein the amount of said polyamine is from 0 to about 15 mole percent of the total amine content and the amount of said epichlorohydrin is from at least the molar equivalent of the total amine content up to the full functional equivalent of said amine content, (b) poly(dimethyldiallylammonium chloride), (c) quaternarized derivatives of poly(dimethylaminoethylmethacrylate), and (d) poly[oxyethylene(dimethylimino)ethylene(dimethylimino)ethylene dichloride], said polyanionic polymer having a molecular weight in the range of about 500 and about 50,000, said polycationic polymer having a molecular weight in the range of about 1,500 and 500,000, and the molar ratio of said polycationic polymer to said polyanionic polymer based on the average molecular weight of the repeating units therein being in the range of about 2:1 and about 25:1.
Claim 2
Dependent Claim 232 words
A process for inhibiting formation of magnesium hydroxide scale or sludge in evaporative desalination units which comprises adding to the saline water being processed in said units an effective amount of a mixture of (1) a polyanionic polymer containing at least about 50 mole percent or repeating units derived from an acrylic acid and any balance of repeating units derived from one or more monomers compatible therewith, the acid units being in the form of at least one member selected from the group consisting of free acid radical, ammonium salt, and alkali metal salts, and (2) a polycationic polymer selected from the group consisting of (a) dimethylaminepolyamine-epichlorohydrin reaction product wherein the amount of said polyamine is from 0 to about 15 mole percent of the total amine content and the amount of said epichlorohydrin is from at least the molar equivalent of the total amine content up to the full functional equivalent of said amine content, (b) poly(dimethyldiallylammonium chloride), (c) quaternarized derivatives of poly(dimethylaminoethylmethacrylate), and (d) poly[oxyethylene(dimethylimino)ethylene(dimethylimino)ethylene dichloride], said polyanionic polymer having a molecular weight in the range of about 500 and about 50,000, said polycationic polymer having a molecular weight in the range of about 1,500 and 500,000, and the molar ratio of said polycationic polymer to said polyanionic polymer based on the average molecular weight of the repeating units therein being in the range of about 2:1 and about 25:1.
Claim 3
Dependent Claim 61 words
The process of claim 1 wherein the polycationic is the reaction product of dimethylamine-polyamine-epichlorohydrin wherein the amount of the said polyamine is from 0 to about 15 mole percent of the total amine content and the amount of said epichlorohydrin is from at least the molar equivalent of the total amine content up to the full functional equivalent of said content.
Claim 4
Dependent Claim 21 words
The process of claim 2 wherein the polycationic polymer is the reaction product of dimethylamine and epichlorohydrin in equal molar ratio.
Claim 5
Dependent Claim 21 words
The process of claim 2 wherein the polycationic polymer has a molecular weight in the range of about 10,000 and 500,000.
Claim 6
Dependent Claim 12 words
The process of claim 1 wherein the polycationic polymer is poly(dimethyldiallylammonium chloride).
Claim 7
Dependent Claim 21 words
The process of claim 6 wherein the polycationic polymer has a molecular weight in the range of about 10,000 and 200,000.
Claim 8
Dependent Claim 16 words
The process of claim 1 wherein the polycationic polymer is a quaternarized derivative of poly(dimethylaminoethyl methacrylate).
Claim 9
Dependent Claim 20 words
The process of claim 7 wherein the polycationic polymer has a molecular in the range of about 10,000 and 100,000.
Claim 10
Dependent Claim 12 words
The process of claim 1 wherein the polycationic polymer is poly[oxyethylene(dimethylimino)ethylene(dimethylimino)ethylene dichloride].
Claim 11
Dependent Claim 20 words
The process of claim 9 wherein the polycationic polymer has a molecular weight in the range of 3,000 and 50,000.
Claim 12
Dependent Claim 18 words
The process of claim 1 wherein the polyanionic polymer contains at least 10 mole percent of acrylonitrile units.
Claim 13
Dependent Claim 16 words
The process of claim 11 wherein the polyanionic polymer has a molecular weight of about 1,000.
Claim 14
Dependent Claim 16 words
The process of claim 11 wherein the polyanionic polymer has a molecular weight of about 8,000.
Claim 15
Dependent Claim 28 words
The process of claim 1 wherein the polyanionic polymer is a copolymer of at least 10 mole percent acrylamide and the polycationic polymer is selected from group (a).

References Cited (Backward Citations)

US2783200A Cited
US3377274A Cited
US3463730A Cited
GB1297515A Cited
US3658710A Cited
US3738945A Cited
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JPS4940794A Cited
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USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1982-04-02 1982-10-02 1983-04-03 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1986-04-02 1986-10-02 1987-04-03 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1990-04-02 1990-10-02 1991-04-03 $7700.00 Window Closed / Lapsed

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