Papermaking process of increasing ash content of a paper product and a paper product obtained by the same

Patent metadata

Field	Value
Publication number	US-10697121-B2
Application number	US-201515531211-A
Country	US
Kind code	B2
Filing date	Oct 27, 2015
Priority date	Nov 26, 2014
Publication date	Jun 30, 2020
Grant date	Jun 30, 2020

Abstract

A process for flocculating filler particles in water is provided. The process comprises adding a flocculant to a mixture comprising filler particles and water, wherein the flocculant has a reduced specific viscosity (“RSV”) of from about 5 dL/g to about 16 dL/g, a viscosity average molecular weight of from about 1,200,000 to about 7,500,000, and a cationic charge of from about 5 mol % to about 50 mol %. Flocs formed by flocculation of the filler particles and the flocculant have a median particle size of from about 10 μm to about 150 μm. The filler is not precipitated calcium carbonate alone. The flocs provided by the process are useful in increasing ash content of a paper product.

First claim

The invention claimed is:

1. A process for flocculating filler particles in water comprising:
adding an acrylamide-based polymer flocculant to a mixture comprising filler particles and water, wherein the acrylamide-based polymer flocculant has a reduced specific viscosity (“RSV”) of from about 5 dL/g to about 12 dL/g, a viscosity average molecular weight of from about 1,400,000 to about 5,000,000, and a cationic charge of from about 20 mol % to about 40 mol %;
wherein the acrylamide-based polymer flocculant is the only flocculant added to the mixture comprising filler particles and water;
wherein flocs formed by flocculation of the filler particles and the acrylamide-based polymer flocculant have a median particle size of from about 10 μm to about 150 μm;
wherein the filler is not precipitated calcium carbonate alone.

2. The process of claim 1 , wherein the median particle size of the flocs formed by flocculation of the filler particles and the acrylamide-based polymer flocculant is from about 30 μm to about 120 μm.

3. The process of claim 1 , wherein the flocs have a size distribution, and the size distribution spans less than 2 μm.

4. The process of claim 1 , wherein an amount of the acrylamide-based polymer flocculant added to the mixture is from about 0.2 kg to about 4 kg per ton of the filler particles.

5. The process of claim 1 , wherein the acrylamide-based polymer flocculant is a polymer formed by acrylamide and one or more monomers selected from acryloyloxyethyl trimethyl ammonium chloride, dimethylaminoethyl methacrylate, dimethylaminoethyl acrylate, diethylaminoethyl acrylate, diethylaminoethyl methacrylate, diallyldimethylammonium chloride, and quaternary ammonium salt formed of dimethyl sulfate and methyl chloride or benzyl chloride.

6. The process of claim 5 , wherein the polymer is a copolymer or terpolymer formed by two or more of the monomers.

7. The process of claim 6 , wherein the acrylamide-based polymer flocculant is a copolymer of acrylamide and acryloyloxyethyl trimethyl ammonium chloride, and/or a copolymer of acrylamide and diallyldimethylammonium chloride.

8. The process of claim 1 , wherein the filler is one or more materials selected from a group of calcium carbonate, kaolin, titanium dioxide, talcum powder, silica, silicate, aluminum hydroxide, barium sulfate and calcium sulfate; wherein, when the filler is calcium carbonate, the filler particles comprise at least 10 wt % ground calcium carbonate.

9. The process of claim 1 , wherein the mixture comprising the filler particles and water is an aqueous dispersion of the filler particles.

10. The process of claim 1 , wherein the acrylamide-based polymer flocculant is added to the mixture with a rotating mixing apparatus having a distribution head rotated by a driver, the distribution head arranged in a container containing an aqueous slurry of the filler particles and has a rotation plane associated with the rotation thereof, and the distribution head has, along a circumference, which surrounds a rotation axis, distributed outlets and mixing blades, the acrylamide-based polymer flocculant is passed from the outlets into the slurry, the outlets are formed as openings, the mixing blades are formed as strips extending transverse to the rotation plane, having a length equal to at least half of an inner diameter of a slurry pipe.

11. The process of claim 1 , wherein the acrylamide-based polymer flocculant has a RSV of from about 9 dL/g to about 11 dL/g.

12. The process of claim 1 , wherein the acrylamide-based polymer flocculant has a viscosity average molecular weight of from about 3,300,000 to about 4,400,000.

13. The process of claim 1 , further comprising adding the flocs to a papermaking wet end.

14. The process of claim 13 , further comprising:
adding an enhancer selected from starch and a modified substance thereof, chitosan, guar gum, hydroxymethyl cellulose, formaldehyde resin, polyethyleneimine, polyvinyl alcohol, or a combination thereof to the papermaking wet end.

Assignees

• Ecolab Usa Inc

Inventors

• Rao Qinglong
• Zhao Yulin
• Cheng Weiguo
• Ashton Stephen B
• Todorovic Aleksandar
• Smith Alan

Classifications

• D21H21/10

  Retention agents or drainage improvers · CPC title

• D21H17/37 Primary

  Polymers of unsaturated acids or derivatives thereof, e.g. polyacrylates · CPC title

• D21H17/44

  cationic · CPC title

• D21H17/45

  Nitrogen-containing groups · CPC title

• D21H21/06

  Paper forming aids · CPC title