Process for the manufacture of paper and paperboard

Patent metadata

Field	Value
Publication number	US-10113270-B2
Application number	US-201414760381-A
Country	US
Kind code	B2
Filing date	Jan 9, 2014
Priority date	Jan 11, 2013
Publication date	Oct 30, 2018
Grant date	Oct 30, 2018

Abstract

Process for the Manufacture of Paper and Paperboard The present invention relates to a process of making paper or paperboard in which a cellulosic thin stock is provided and subjected to one or more shear stages and then drained and a moving screen to form a sheet which is dried, wherein the process employs a retention system which is applied to the thin stock, said retention system comprising as components i) a blend of different cationic polymers and ii) a microparticulate material, in which the blend of cationic polymers comprises, a) a cationic polymer having a charge density of from 0.5 and below 3 mEq per gram and a molar mass of greater than 700,000 Da, which cationic polymer is selected from polymers containing vinyl amine units and polyethylenimine, b) a cationic polymer having a charge density of below 3 mEq per gram and an intrinsic viscosity of at least 3 dl/g, wherein one of the components of the retention system is dosed into the thin stock after the final shearing stage and the other is dosed into the thin stock before the final shearing stage.

First claim

The invention claimed is:

1. A process of making paper or paperboard, comprising subjecting a cellulosic thin stock to one or more shear stages and then draining through a moving screen to form a sheet which is dried,
wherein the process employs a retention system which is applied to the thin stock, the retention system comprising as components
i) a blend of different cationic polymers, and
ii) a microparticulate material, which microparticulate material is selected from colloidal silica and bentonite,
in which the blend of cationic polymers comprises:
a) from 50 ppm to 3000 ppm dose rate of a cationic polymer having a charge density of from 1 to 2 mEq per gram and a molar mass of from greater than 700,000 Da to 3 million Da, which cationic polymer is selected from polymers comprising vinyl amine units, and
b) from 50 ppm to 1000 ppm dose rate of a cationic polymer haying a charge density of below 3 mEq per grain and an intrinsic viscosity of at least 10 dl/g, which cationic polymer is a cationic polyacrylamide comprising acrylamide and from 5 to 10 mole % of at least one water-soluble cationic ethylenically unsaturated monomer,
wherein i) the blend of cationic polymers is dosed into the thin stock prior to the final shearing stage and ii) the microparticulate material is dosed into the thin stock after the final shearing stage, and
wherein the ppm dose rate is based on the active weight of the cationic polymer relative to a dry weight of the cellulosic thin stock suspension,
wherein one of the components of the retention system is dosed into the thin stock after the final shearing stage and the other is dosed into the thin stock before the final shearing stage.

2. The process according to claim 1 , wherein a) the cationic polymer having a charge density of from 1 to 2 mEq per gram and molar mass of from greater than 700,000 Da to 3 million Da comprises polyvinylamine and partially hydrolysed polyvinyl carboxamides.

3. The process according to claim 1 , wherein b) the at least one water-soluble cationic ethylenically unsaturated monomer is selected from the group consisting of quaternary or acid salts of &alkyl amino alkyl (meth) acrylates, quaternary or acid salts of dalkyl amino alkyl (meth) actylamides and dialkyl diallyl ammonium halides.

4. The process according to claim 1 , wherein the molar mass of the cationic polymer a) is from 1.5 to 2.5 million Da.

5. The process according to claim 1 , wherein b) the at least one water-soluble cationic ethylenically unsaturated monomer of the cationic polyacrylamide is a methyl chloride quaternary ammonium salt of dimethylamino ethyl acrylate.

6. The process according to claim 1 , wherein
a dose amount of the cationic polymer b) is from 50 ppm to 600 ppm,
wherein the dose amount is based on the active weight of the cationic polymer relative to the dry weight of the cellulosic thin stock suspension.

Assignees

• Basf Se

Inventors

• Gray Christopher Alan
• Moormann-Schmitz Antonius
• Meixner Hubert
• Sanchez Cerro Luis Miguel
• Muehlenbernd Thomas
• Jehn-Rendu Christian

Classifications

• D21H17/44

  cationic · CPC title

• D21H17/45 Primary

  Nitrogen-containing groups · CPC title

• D21H11/20

  Chemically or biochemically modified fibres · CPC title

• D21H17/56

  Polyamines; Polyimines; Polyester-imides · CPC title

• D21H17/68

  siliceous, e.g. clays · CPC title