US2010326615A1PendingUtilityA1
Papermaking And Products Made Thereby With High Solids Glyoxalated-Polyacrylamide And Silicon-Containing Microparticle
Est. expiryJun 29, 2029(~2.9 yrs left)· nominal 20-yr term from priority
Inventors:Chen Lu
D21H 17/375D21H 17/13D21H 17/45D21H 21/10D21H 17/68
39
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Claims
Abstract
Enhancement of papermaking drainage and retention properties of aqueous cellulosic suspensions used for production of paper or paper board with a retention/drainage additive system including high solids glyoxalated polyacrylamide polymers in combination with silicon-containing microparticles is described.
Claims
exact text as granted — not AI-modified1 . A process for making paper comprising adding silicon-containing microparticles and a glyoxalated polyacrylamide polymer comprising at least about 25% by weight cationic monomer to an aqueous suspension containing cellulosic fibers, and forming said suspension into a water-laid web and drying said web to form paper, wherein the added amount of silicon-containing microparticles is effective to increase fiber retention and de-watering rate as compared to paper made with the suspension absent the silicon-containing microparticles.
2 . The process of claim 1 , wherein the glyoxalated polyacrylamide polymer is a reaction product of glyoxal and a base polymer comprising the acrylamide monomer and the cationic monomer.
3 . The process of claim 2 , wherein said base polymer has an average molecular weight range from 500 Daltons to 20,000 Daltons.
4 . The process of claim 2 , wherein said base polymer has a charge density of 1 meg/g or greater.
5 . The process of claim 2 , wherein said base polymer has a charge density of from 1 meg/g to 4.5 meg/g.
6 . The process of claim 2 , wherein said base polymer has a charge density of from 1.5 to 3.5 meg/g.
7 . The process according to claim 1 , wherein the paper comprises from about 0.05 to about 2.5 pounds said silicon-containing microparticles/ton dry fiber.
8 . The process according to claim 1 , wherein the silicon-containing microparticles are selected from silica microparticles and bentonite microparticles.
9 . The process according to claim 1 , wherein the silicon-containing microparticles comprise amorphous silica microparticles.
10 . The process according to claim 1 , wherein said silicon-containing microparticles comprise colloidal silica comprising a surface area from 300 m 2 /g to 1000 m 2 /g and an S-value of from 80% to 20%.
11 . The process according to claim 1 , wherein said silicon-containing microparticles comprise bentonite microparticles.
12 . The process according to claim 1 , wherein the microparticles have an absolute particle size of not greater than about 750 nm.
13 . The process according to claim 1 , wherein at least 90% of the microparticles have an absolute particle size of not greater than about 750 nm.
14 . The process according to claim 1 , wherein the paper comprises from about 0.5 to about 12 pounds said polymer/ton dry fiber.
15 . The process according to claim 1 , wherein said adding comprises introducing an aqueous polymer composition comprising said glyoxalated polyacrylamide polymer, wherein the polymer composition comprises (a) at least 10%, by weight, said glyoxalated polyacrylamide polymer, and (b) water, wherein the glyoxalated polyacrylamide polymer comprises a reaction product between glyoxal and a cationic polyacrylamide base polymer, wherein the cationic polyacrylamide base polymer comprises from about 75% to about 10%, by weight, acrylamide monomer and from about 25% to about 90%, by weight, cationic monomer copolymerizable with said acrylamide monomer, and having sufficient glyoxal-reactive amide substituents and —CHOHCHO substituents to be thermosetting.
16 . The process according to claim 15 , wherein said polymer composition comprising about 5% to about 30%, by weight, said glyoxalated polyacrylamide polymer.
17 . The process according to claim 15 , wherein said polymer composition comprising about 7% to about 15%, by weight, said glyoxalated polyacrylamide polymer.
18 . The process according to claim 15 , wherein the cationic monomer is 2-vinylpyridine, 2-vinyl-N-methylpyridinium chloride, (p-vinylphenyl) trimethyl ammonium chloride, diallyldimethylammonium chloride, 2-(dimethylamino)ethyl acrylate, trimethyl(p-vinylbenzyl)ammonium chloride, p-dimethylaminoethylstyrene, dimethylaminopropyl acrylamide, 2-methylacroyloxyethyltrimethyl ammonium methylsulfate, or 3-acrylamido-3-methylbutyl trimethyl ammonium chloride, or any combination thereof.
19 . The process according to claim 15 , wherein the cationic monomer is diallyldimethyl-ammonium chloride.
20 . The process according to claim 15 , wherein the acrylamide monomer is acrylamide, methacrylamide, ethylacrylamide, crotonamide, N-methyl acrylamide, N-butyl acrylamide, or N-ethyl methacrylamide, or any combination thereof.
21 . The process according to claim 15 , wherein the cationic polyacrylamide base polymer comprises from about 70% to about 20%, by weight, acrylamide monomer and from about 30% to about 80%, by weight, cationic monomer copolymerizable with said acrylamide monomer.
22 . The process according to claim 15 , wherein the polymer is a reaction product of glyoxal and a base polymer comprising the acrylamide monomer and the cationic monomer in a weight ratio ranging from about 0.01 to 0.6:1.
23 . The process according to claim 22 , wherein the base polymer has a molecular weight ranging from about 500 Daltons to about 100,000 Daltons.
24 . The process according to claim 1 , wherein the paper comprises a cellulosic fibrous non-woven web.
25 . A product comprising a paper made by the process of claim 1 containing the glyoxalated polyacrylamide polymer and silicon-containing microparticles.
26 . A product according to claim 25 , wherein the product is paper sheeting, paperboard, tissue paper, or wall board.
27 . A product according to claim 25 , wherein the product is newsprint or linerboard.Join the waitlist — get patent alerts
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