IP Library Granted Patent US 8,029,647
Granted Patent B2
US 8,029,647 · App. 11/574,677 · Granted Oct 4, 2011

Method for the production of paper, paperboard and cardboard

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Quick Facts
Patent No.
US 8,029,647
App. No.
11/574,677
Granted
Oct 4, 2011
Kind
B2
Abstract

Process for the production of paper, board and cardboard by draining a paper stock on a wire with sheet formation and drying of the sheets, the sheet formation being carried out in the absence of finely divided inorganic flocculants and (a) polymers comprising vinylamine units and/or polyvinylformamide having a molar mass M w of, in each case, at least 1 million and (b) at least one cationic or nonionic polyacrylamide and/or one cationic or nonionic polymethacrylamide having a molar mass M w of, in each case, at least 2.5 million being used as retention aids.

Claims (48)

1. A process for producing paper, board or cardboard comprising:

draining a paper stock on a wire with sheet formation which is carried out in the absence of a finely divided inorganic flocculant and in the presence of a retention aid to obtain a sheet, wherein the retention aid comprises:

(a) at least one hydrolyzed polyvinylformamide having a degree of hydrolysis of 0.5-50% and a weight average molar mass M w of at least 1,200,000, which is prepared by homopolymerizing N-vinylformamide to give poly-N-vinylformamide and subsequently hydrolyzing 0.5-50% of the vinylformamide units to vinylamine units, which is cationic, and which has a charge density of 0.2-4 meq/g; and

(b) at least one cationic poly(meth)acrylamide copolymer having a weight average molar mass M w of at least 3,000,000 and comprising 70-93 mol. % of acrylamide and 7-30 mol. % of at least one cationic monomer, wherein the cationic monomer is selected from the group consisting of dimethylaminoethyl acrylate and dimethylaminoethyl methacrylate, including free bases, salts and/or quaternized forms thereof,

wherein a weight ratio of component (b) to component (a) is 0.25-0.4; and

drying the sheet obtained from said sheet formation.

2. The process according to claim 1 , wherein the cationic monomer is dimethylaminoethyl acrylate methochloride.

3. The process according to claim 1 , wherein the retention aid comprises:

(a) 0.001-0.8 wt. % of the hydrolyzed polyvinylfomamide; and

(b) 0.001-0.8 wt. % of the cationic poly(meth)acrylamide copolymer.

4. The process according to claim 1 , wherein the retention aid comprises:

(a) 0.01-0.5 wt. % of the hydrolyzed polyvinylformamide; and

(b) 0.01-0.2 wt. % of the cationic poly(meth)acrylamide copolymer.

5. The process according to claim 1 , wherein the hydrolyzed polyvinylformamide has a degree of hydrolysis of 1-40%.

6. The process according to claim 1 , wherein the hydrolyzed polyvinylformamide has a degree of hydrolysis of 2-30%.

7. The process according to claim 1 , wherein the cationic poly(meth)acrylamide copolymer has a weight average molar mass M w of 5,000,000 to 15,000,000.

8. The process according to claim 1 , wherein the retention aid comprises:

(b) a mixture comprising: the cationic poly(meth)acrylamide copolymer; and at least one nonionic poly(meth)acrylamide copolymer having a weight average molar mass M w of at least 3,000,000.

9. The process according to claim 8 , wherein the retention aid comprises:

(a) 0.001-0.8 wt. % of the hydrolyzed polyvinylformamide; and

(b) 0.001-0.8 wt. % of the mixture.

10. The process according to claim 8 , wherein the retention aid comprises:

(a) 0.01-0.5 wt. % of the hydrolyzed polyvinylformamide; and

(b) 0.01-0.2 wt. % of the mixture.

11. A process for producing paper, board or cardboard comprising:

draining a paper stock on a wire with sheet formation which is carried out in the absence of a finely divided inorganic flocculant and in the presence of a retention aid to obtain a sheet, wherein the retention aid comprises:

(a) at least one hydrolyzed polyvinylformamide having a weight average molar mass M w of at least 1,200,000, which is prepared by homopolymerizing N-vinylformamide to give poly-N-vinylformamide and subsequently hydrolyzing the vinylformamide units to vinylamine units, which is cationic, and which has a charge density of 0.2-4 meq/g; and

(b) at least one cationic poly(meth)acrylamide copolymer having a weight average molar mass M w of at least 3,000,000 and comprising 70-93 mol. % of acrylamide and 7-30 mol. % of at least one cationic monomer, wherein the cationic monomer is selected from the group consisting of dimethylaminoethyl acrylate and dimethylaminoethyl methacrylate, including free bases, salts and/or quaternized forms thereof,

wherein a weight ratio of component (b) to component (a) is 0.25-0.4; and

drying the sheet obtained from said sheet formation.

12. The process according to claim 11 , wherein the cationic monomer is dimethylaminoethyl acrylate methochloride.

13. The process according to claim 11 , wherein the retention aid comprises:

(a) 0.001-0.8 wt. % of the hydrolyzed polyvinylformamide; and

(b) 0.001-0.8 wt. % of the cationic poly(meth)acrylamide copolymer.

14. The process according to claim 11 , wherein the retention aid comprises:

(a) 0.01-0.5 wt. % of the hydrolyzed polyvinylformamide; and

(b) 0.01-0.2 wt. % of the cationic poly(meth)acrylamide copolymer.

15. The process according to claim 11 , wherein the hydrolyzed polyvinylformamide has a degree of hydrolysis of 0.5-50%.

16. The process according to claim 11 , wherein the hydrolyzed polyvinylformamide has a degree of hydrolysis of 1-40%.

17. The process according to claim 11 , wherein the cationic poly(meth)acrylamide copolymer has a weight average molar mass M w of 5,000,000 to 15,000,000.

18. The process according to claim 11 , wherein the retention aid comprises:

(b) a mixture comprising: the cationic poly(meth)acrylamide copolymer; and at least one nonionic poly(meth)acrylamide copolymer having a weight average molar mass M w of at least 3,000,000.

19. The process according to claim 18 , wherein the retention aid comprises:

(a) 0.001-0.8 wt. % of the hydrolyzed polyvinylformamide; and

(b) 0.001-0.8 wt. % of the mixture.

20. The process according to claim 18 , wherein the retention aid comprises:

(a) 0.01-0.5 wt. % of the hydrolyzed polyvinylformamide; and

(b) 0.01-0.2 wt. % of the mixture.

Assignments (13)
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 →
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 (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 →
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 (ABL) Recorded Sep 14, 2022
From: SOLENIS TECHNOLOGIES, L.P.; INNOVATIVE WATER CARE, LLC
To: BANK OF AMERICA, N.A, AS COLLATERAL AGENT
Reel/Frame 061432/0958 →
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 →
SECURITY AGREEMENT (TERM) Recorded Sep 13, 2022
From: SOLENIS TECHNOLOGIES, L.P.; INNOVATIVE WATER CARE, LLC
To: GOLDMAN SACHS BANK USA, AS COLLATERAL AGENT
Reel/Frame 061431/0851 →
SECURITY AGREEMENT (NOTES) Recorded Sep 13, 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 061431/0865 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Mar 9, 2022
From: BASF SE
To: SOLENIS TECHNOLOGIES, L.P.
Reel/Frame 059206/0621 →
CHANGE IN LEGAL FORM Recorded Aug 16, 2012
From: BASF AKTIENGESELLSCHAFT
To: BASF SE
Reel/Frame 028801/0481 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Dec 5, 2007
From: LEDUC, MARC; BLUM, RAINER; LEIFERT, PETER
To: BASF AKTIENGESELLSCHAFT
Reel/Frame 020200/0293 →