IP Library Granted Patent US 10,850,238
Granted Patent B2
US 10,850,238 · App. 15/565,938 · Granted Dec 1, 2020

Processes for reducing the fouling of surfaces

Inventors: Rupert Konradi (Ladenburg, DE); Cristina Cepraga (Mannheim, DE); Claudia Staudt (Alzey, DE); Bernhard Von Vacano (Mannheim, DE); Matthias Kellermeier (Mannheim, DE); Peter Stengel (Schwanheim, DE); Roelf-Peter Baumann (Mannheim, DE); Laurent Marty (Heidelberg, DE); Jelan Kuhn (Mannheim, DE); Sarah-Jane Schauksdat (Hirschhorn, DE); Ludger Wegmann (Ludwigshafen, DE); Erik Bohrer (Maxdorf, DE)
Assignee: SOLENIS TECHNOLOGIES, L.P.
B01D67/0088A01N25/10A01N25/34B01D65/08B01D69/06B01D69/08B01D71/28B01D71/40B01D71/80C08F283/06C09D5/1668C09D151/08B01D71/52
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Quick Facts
Patent No.
US 10,850,238
App. No.
15/565,938
Granted
Dec 1, 2020
Kind
B2
Abstract

Process for reducing the fouling of a surface O, wherein an aqueous solution S of at least one polymer P comprising styrene and at least one ester E of (meth)acrylic acid and polyethylene oxide in a molar ratio of 0.05:1 to 50:1 is applied to said surface O.

Claims (49)

1. A process for reducing fouling of a surface O, the process comprising:

preparing an aqueous solution S comprising at least one polymer P formed from styrene and polyethylene glycol methacrylic ester by solution polymerization in water, ethanol, 1-propanol, isopropanol, or combinations thereof, wherein the aqueous solution S comprises at least 50% by weight of water; and

applying the aqueous solution S to the surface O,

wherein the polymer P has a number average molecular weight Mn of from 8,830 to 50,700 g/mol, wherein the polyethylene glycol methacrylic ester has a number average molecular weight Mn of from 550 to 2,000 g/mol, and wherein the polymerization reaction is carried out using a molar ratio of styrene:polyethylene glycol methacrylic ester of from 20:1 to 1:4.

2. The process according to claim 1 , wherein the surface O is a membrane M.

3. The process according to claim 1 , wherein the polymer P has a number average molecular weight Mn of from 10,900 to 29,000.

4. The process according to claim 1 , wherein the polymer P is a statistical copolymer.

5. The process according to claim 1 , wherein the aqueous solution S comprises 0.001 to 1% by weight of said at least one polymer P.

6. The process according to claim 1 , wherein the at least one polymer P is applied to the surface O in intervals of 1 day to 24 months.

7. The process according to claim 2 , wherein the membrane M is a RO, FO, NF, UF or MF membrane.

8. The process according to claim 1 , wherein said process is used in treating industrial or municipal waste water, sea water, brackish water, fluvial water, surface water or drinking water, desalination of sea or brackish water, dialysis, plasmolysis or processing of food and beverages.

9. The process of claim 1 wherein the solution polymerization occurs in water, ethanol, isopropanol, or combinations thereof, and the polymer P has a number average molecular weight Mn of from 10,500 to 18,500 g/mol.

10. The process of claim 1 wherein the solution polymerization occurs in a combination of water and 1-propanol.

11. The process of claim 1 wherein the solution polymerization occurs in a combination of water and isopropanol.

12. The process of claim 1 wherein the polyethylene glycol methacrylic ester has a number average molecular weight Mn of 550 g/mol, the solution polymerization occurs in a combination of water and 1-propanol, and the polymer P has a number average molecular weight Mn of from 10,900 to 50,700 g/mol.

13. The process of claim 12 wherein the polymerization reaction is carried out using a molar ratio of styrene:polyethylene glycol methacrylic ester of 1:1.

14. The process of claim 1 wherein the polyethylene glycol methacrylic ester has a number average molecular weight Mn of 1,000 g/mol, the solution polymerization occurs in a combination of water and 1-propanol, and the polymer P has a number average molecular weight Mn of from 10,900 to 50,700 g/mol.

15. The process of claim 14 wherein the polymerization reaction is carried out using a molar ratio of styrene:polyethylene glycol methacrylic ester of 1:1 to 1:4.

16. The process of claim 1 wherein the polyethylene glycol methacrylic ester has a number average molecular weight Mn of 2,000 g/mol, the solution polymerization occurs in a combination of water and 1-propanol, and the polymer P has a number average molecular weight Mn of from 10,900 to 50,700 g/mol.

17. A process for reducing fouling of a membrane, the process comprising:

preparing an aqueous solution S comprising at least one polymer P formed from styrene and polyethylene glycol methacrylic ester by solution polymerization in a combination of water and 1-propanol wherein the aqueous solution S comprises at least 50% by weight of water; and

applying the aqueous solution S to the membrane M to form a layer of the at least one polymer P on the membrane,

wherein the membrane M is a RO, FO, NF, UF or MF membrane,

wherein the layer is a self-assembled monolayer,

wherein the at least one polymer P is a statistical copolymer and has a number average molecular weight Mn of from 10,900 to 50,700 g/mol, wherein the polyethylene glycol methacrylic ester has a number average molecular weight Mn of 2,000 g/mol, wherein the polymerization reaction is carried out using a molar ratio of styrene:polyethylene glycol methacrylic ester of from 20:1 to 1:4, and

wherein the aqueous solution S comprises 0.001 to 1% by weight of the at least one polymer P.

18. The process according to claim 17 ,

wherein the at least one polymer P is applied to the surface O in intervals of 1 day to 24 months, and

wherein said process is used in treating industrial or municipal waste water, sea water, brackish water, fluvial water, surface water or drinking water, desalination of sea or brackish water, dialysis, plasmolysis or processing of food and beverages.

19. A process for reducing fouling of a membrane, the process comprising:

preparing an aqueous solution S comprising at least one polymer P formed from styrene and polyethylene glycol methacrylic ester by solution polymerization in a combination of water and isopropanol, wherein the aqueous solution S comprises at least 50% by weight of water; and

applying the aqueous solution S to the membrane M to form a layer of the at least one polymer P on the membrane,

wherein the membrane M is a RO, FO, NF, UF or MF membrane,

wherein the layer is a self-assembled monolayer,

wherein the at least one polymer P is a statistical copolymer and has a number average molecular weight Mn of from 10,500 to 18,500 g/mol, wherein the polyethylene glycol methacrylic ester has a number average molecular weight Mn of 2,000 g/mol, wherein the polymerization reaction is carried out using a molar ratio of styrene:polyethylene glycol methacrylic ester of 1:1, and

wherein the aqueous solution S comprises 0.001 to 1% by weight of the at least one polymer P.

20. The process according to claim 19 ,

wherein the at least one polymer P is applied to the surface O in intervals of 1 day to 24 months, and

wherein said process is used in treating industrial or municipal waste water, sea water, brackish water, fluvial water, surface water or drinking water, desalination of sea or brackish water, dialysis, plasmolysis or processing of food and beverages.

21. A process for reducing fouling of a membrane, the process comprising:

preparing an aqueous solution S comprising at least one polymer P formed from styrene and polyethylene glycol methacrylic ester by solution polymerization in a combination of water and 1-propanol, wherein the aqueous solution S comprises at least 50% by weight of water; and

applying the aqueous solution S to the membrane M to form a layer of the at least one polymer P on the membrane,

wherein the membrane M is a RO, FO, NF, UF or MF membrane,

wherein the layer is a self-assembled monolayer,

wherein the at least one polymer P is a statistical copolymer and has a number average molecular weight Mn of from 8,830 to 39,100 g/mol, wherein the polyethylene glycol methacrylic ester has a number average molecular weight Mn of 550 to 1,000 g/mol, wherein the polymerization reaction is carried out using a molar ratio of styrene:polyethylene glycol methacrylic ester of 1:1, and

wherein the aqueous solution S comprises 0.001 to 1% by weight of the at least one polymer P.

22. The process according to claim 21 ,

wherein the at least one polymer P is applied to the surface O in intervals of 1 day to 24 months, and

wherein said process is used in treating industrial or municipal waste water, sea water, brackish water, fluvial water, surface water or drinking water, desalination of sea or brackish water, dialysis, plasmolysis or processing of food and beverages.

Assignments (12)
SECURITY INTEREST Recorded Nov 14, 2025
From: CHEM-AQUA, INC.; DIVERSEY, INC.; DIVERSEY TASKI, INC.; INNOVATIVE WATER CARE, LLC; NCH CORPORATION; NCH LIFE SCIENCES LLC; SOLENIS TECHNOLOGIES, L.P.
To: THE BANK OF NEW YORK MELLON TRUST COMPANY, N.A., AS NOTES COLLATERAL AGENT
Reel/Frame 073570/0838 →
RELEASE OF SECURITY INTEREST Recorded Nov 14, 2025
From: THE BANK OF NEW YORK MELLON TRUST COMPANY, N.A., AS NOTES COLLATERAL AGENT
To: BIRKO CORPORATION; DIVERSEY, INC.; DIVERSEY TASKI, INC.; INNOVATIVE WATER CARE, LLC; SOLENIS TECHNOLOGIES, L.P.
Reel/Frame 073564/0864 →
SECURITY AGREEMENT (NOTES) Recorded Oct 10, 2025
From: DIVERSEY, INC.; DIVERSEY TASKI, INC.; INNOVATIVE WATER CARE, LLC; SOLENIS TECHNOLOGIES, L.P.
To: THE BANK OF NEW YORK MELLON TRUST COMPANY, N.A., AS NOTES COLLATERAL AGENT
Reel/Frame 073061/0885 →
RELEASE OF 2023 NOTES PATENT SECURITY INTERESTS Recorded Oct 10, 2025
From: THE BANK OF NEW YORK MELLON TRUST COMPANY, N.A.
To: BIRKO CORPORATION; DIVERSEY, INC.; DIVERSEY TASKI, INC.; INNOVATIVE WATER CARE, LLC; SOLENIS TECHNOLOGIES, L.P.
Reel/Frame 073074/0198 →
SECURITY AGREEMENT (2024 NOTES) Recorded Jun 24, 2024
From: BIRKO CORPORATION; DIVERSEY, INC.; DIVERSEY TASKI, INC.; INNOVATIVE WATER CARE, LLC; SOLENIS TECHNOLOGIES, L.P.
To: THE BANK OF NEW YORK MELLON TRUST COMPANY, N.A., AS NOTES COLLATERAL AGENT
Reel/Frame 067824/0278 →
2023 NOTES PATENT SECURITY AGREEMENT Recorded Jul 7, 2023
From: BIRKO CORPORATION; SOLENIS TECHNOLOGIES, L.P.; INNOVATIVE WATER CARE, LLC; DIVERSEY, INC.; DIVERSEY TASKI, INC.; INNOVATIVE WATER CARE GLOBAL CORPORATION
To: BANK OF NEW YORK MELLON TRUST COMPANY, N.A.
Reel/Frame 064225/0170 →
SECURITY AGREEMENT (NOTES) Recorded Sep 14, 2022
From: SOLENIS TECHNOLOGIES, L.P.; INNOVATIVE WATER CARE, LLC
To: THE BANK OF NEW YORK MELLON TRUST COMPANY, N.A. AS COLLATERAL AGENT
Reel/Frame 061432/0821 →
NOTES SECURITY AGREEMENT Recorded Nov 10, 2021
From: INNOVATIVE WATER CARE, LLC; SOLENIS TECHNOLOGIES, L.P.
To: THE BANK OF NEW YORK MELLON TRUST COMPANY, N.A.
Reel/Frame 058103/0066 →
TERM LOAN PATENT SECURITY AGREEMENT Recorded Nov 10, 2021
From: INNOVATIVE WATER CARE, LLC; SOLENIS TECHNOLOGIES, L.P.
To: GOLDMAN SACHS BANK USA
Reel/Frame 058102/0407 →
ABL PATENT SECURITY AGREEMENT Recorded Nov 10, 2021
From: INNOVATIVE WATER CARE, LLC; SOLENIS TECHNOLOGIES, L.P.
To: BANK OF AMERICA, N.A.
Reel/Frame 058102/0122 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Mar 26, 2019
From: BASF SE
To: SOLENIS TECHNOLOGIES, L.P.
Reel/Frame 048697/0892 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Apr 3, 2018
From: KONRADI, RUPERT; CEPRAGA, CRISTINA; STAUDT, CLAUDIA; VON VACANO, BERNHARD; KELLERMEIER, MATTHIAS; STENGEL, PETER; BAUMANN, ROELF-PETER; MARTY, LAURENT; KUHN, JELAN; SCHAUKSDAT, SARAH-JANE; WEGMANN, LUDGER; BOHRER, ERIK
To: BASF SE
Reel/Frame 045423/0695 →
Priority Claims (1)
EP 15163306 · Apr 13, 2015 · regional
Continuity (1)
Related Publication 20180056245A1 · Mar 1, 2018