A method for treating starch in pulp, paper and board making processes
US-2019024306-A1 · Jan 24, 2019 · US
US11976418B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11976418-B2 |
| Application number | US-202117498818-A |
| Country | US |
| Kind code | B2 |
| Filing date | Oct 12, 2021 |
| Priority date | Oct 12, 2021 |
| Publication date | May 7, 2024 |
| Grant date | May 7, 2024 |
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The present invention provides a novel method and composition for enhancing the efficiency of starch adsorption (i.e., starch trapping) from starch-containing furnishes comprising high content of recycled fibers for use in paper making processes such as pulp, paper, or board production. A novel polymer coagulation system is disclosed in which two quick inversion cationic emulsion polymers (starch trapping polymers A and B) are co-mixed at optimal blend ratios to meet specific recycled fiber and process water requirements for different recycled fiber plants and added to furnishes prior to formation of paper or board in a paper machine. Co-mixed solutions of starch trapping polymers A and B provide synergistic enhancements in (i) starch trapping efficiency and (ii) starch retention in the produced paper or board over equivalent dosage levels of singly administered polymer A, polymer B, or conventional starch trapping products, without over-flocculation or formation of stickies.
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What is claimed is: 1. A method for treating starch-containing fiber stock, the method comprising: (a) providing a starch-containing fiber stock comprising recycled fibers and/or mill broke fibers; (b) providing or obtaining a synthetic starch trapping polymer A having polymer standard viscosity of between 3 to 3.5 cPs and comprising 15-23 mol %, 17-22 mol %, 19-21 mol %, or 20 mol % of one or more cationic monomers; and (c) providing or obtaining a synthetic starch trapping polymer B having polymer standard viscosity of between 1.5 to 2.0 cPs and comprising 25-45 mol %, 28-42 mol %, or 30-40 mol % of one or more cationic monomers; (d) inverting said synthetic starch trapping polymers A and B; and (e) adding said synthetic starch trapping polymers A and B to said starch-containing fiber stock, thereby forming a treated fiber stock; wherein said synthetic starch trapping polymers A and B: (i) comprise quick inversion reverse phase cationic emulsion polymers, (ii) are added to said starch-containing fiber stock at an optimal blend ratio of polymer A/polymer B; and (iii) are added to said starch-containing fiber stock at a combined dosage of said synthetic starch trapping polymers A and B that is sufficient to elicit a synergistic or additive increase in starch trapping efficiency, compared to the administration the same dosage of polymer A or polymer B alone. 2. The method of claim 1 , wherein: said synthetic starch trapping polymers A and B are obtained by reverse phase emulsion polymerization of a monomer blend comprising non-ionic monomers, 15-50 mol-% cationic monomers, 2-30 ppm or at most 50 ppm of a crosslinking agent, and a chain transfer agent, wherein ppm denotes mg of solute per liter of solution; (ii) said synthetic starch trapping polymer A comprises 20 mol % cationic monomer content; (iii) said synthetic starch trapping polymer B comprises 30-40 mol % cationic monomer content; (iv) said synthetic starch trapping polymer A has a standard viscosity of 3-3.5 cPs when measured by a Brookfield viscometer with UL adapter at 25° C. on a 0.1% by weight polymer solution in 1 M NaCl; (v) said starch trapping polymer B has a standard viscosity of 1.5-2 cPs when measured by a Brookfield viscometer with UL adapter at 25° C. on a 0.1% by weight polymer solution in 1 M NaCl; (vi) the cationic monomers are selected from the group consisting of diallyldimethylammonium chloride (DADMAC); acryloyloxyethyltrimethyl ammonium chloride (Q9); methacrylates of N,N-dialkylaminoalkyl compounds; and quaternaries and salts thereof, such as N, N-dimethylaminoethylacrylate methyl-chloride salt; monomers of N,N-dialkylaminoalkyl (meth)acrylamides; and salts and quaternaries thereof, such as N,N-dialkylaminoethylacrylamides; methacrylamidopropyltrimethylammonium chloride; and 1-methacryloyl-4-methyl piperazine; (vii) the nonionic monomers are selected from the group consisting of acrylamide; methacrylamide; N-alkyl acrylamides, such as N-methylacrylamide, N,N-dialkylacrylamides, such as N,N-dimethylacrylamide; methyl acrylate; methyl methacrylate; acrylonitrile; N-vinylmethylacetamide or formamide; N-vinyl acetate or vinyl pyrrolidone; (viii) said synthetic starch trapping polymer A is a quick inversion cationic emulsion polyacrylamide co-polymer comprising cationic quaternary amine side chains; (ix) said synthetic starch trapping polymer B is a quick inversion cationic emulsion polyacrylamide co-polymer comprising cationic quaternary amine side chains; (x) said synthetic starch trapping Polymer A comprises a quick inversion cationic emulsion polyacrylamide co-polymer comprising acrylamide and acryloyloxyethyltrimethyl ammonium chloride (Q9); (xi) said synthetic starch trapping Polymer B comprises a quick inversion cationic emulsion polyacrylamide co-polymer comprising acrylamide and acryloyloxyethyltrimethyl ammonium chloride (Q9); or (xii) any combination of (i) to (xi). 3. The method of claim 1 , wherein the method further comprises, prior step (e), co-mixing of said synthetic starch trapping polymers A and B at said optimal blend ratio of polymer A/polymer B, wherein said synthetic starch trapping polymer A and synthetic starch trapping polymer B are co-mixed during the emulsion inverting step (d) and/or during polymer makedown, wherein said optimal blend ratio is optimal for starch removal, and wherein said co-mixing does not require conventional polymer inverting and/or aging tanks. 4. The method of claim 1 , wherein: (i) said optimal blend ratio of polymer A/polymer B ranges from 90/10 to 50/50 when trapping starch from a recycled fiber containing a percent by mass of a dry fines ranging from 0.1-5% or 0.1-0.2%; (ii) said optimal blend ratio of polymer A/polymer B ranges from 80/20 to 60/40 when trapping starch from a recycled fiber stock containing a percent by mass of a dry fines ranging from 0.1-5% or 0.1-0.2%; (iii) said optimal blend ratio of polymer A/polymer B is 70/30 when trapping starch from a recycled fiber stock containing a percent by mass of a dry fines ranging from 0.1-5% or 0.1-0.2%; (iv) said optimal blend ratio of polymer A/polymer B ranges from 10/90 to 1/99 when trapping starch from a recycled fiber stock containing a percent by mass of a dry fines ranging from 5-15%; (v) said optimal blend ratio of polymer A/polymer B is less than 1/99 when trapping starch from a recycled fiber stock containing a percent by mass of a dry fines ranging from 5-15%; or (vi) any combination of (i) to (v), wherein said fines comprise particle sizes smaller than 0.76 micron. 5. The method of claim 1 , wherein said starch-containing fiber stock: (i) is obtained from a papermaking machine which uses recycled paper; (ii) comprises a over 50% by weight of recycled fibers, and/or mill broke, based on dry paper or board; (iii) comprises fibers originating from recycled paper, old corrugated containerboard (OCC), mixed office waste (MOW), old magazine (OMG), unbleached kraft pulp, neutral sulphite semi chemical (NCCS) pulp and/or mechanical pulp; (iv) comprises at least 50%, 60%, 70%, 80%, 90% or 100% recycled fibers and/or pretreated fiber stock from a papermaking process using a paper machine that uses at least 60%, 70%, 80%, 90% or 100% recycled fibers; (v) comprises OCC recycled fibers comprising 5% native size press starch and starch gel that may be reclaimed for use in the manufacture of paper or board; (vi) comprises starch derived from recycled fibers and/or mill broke fibers in the starch-containing stock and/or comprises starch that is added to the treated fiber stock; or (vii) any combination of (i) to (vi). 6. The method of claim 1 , wherein: (i) the method is effected prior to the use of the treated fiber stock in a papermaking process or other industrial process using cationic functional polymers or other papermaking chemicals; (ii) said synthetic starch trapping polymers A and B are added to said starch-containing fiber stock prior to washing and/or cleaning and/or thickening, wherein said starch-containing fiber stock has a consistency (i.e., percent oven dry mass in the stock) of less than 4%, 2%, or 1%; (iii) said synthetic starch trapping polymers A and B are added to said starch-containing fiber stock prior to forming and/or pressing and/or drying, wherein said starch-containing fiber stock has a consistency (i.e., percent oven dry mass in the stock) of 15-35%; or (iv) any combination of (i) to (iii). 7. The method of claim 1 , wherein: said combined dosage of synthetic starch trapping polymers A and B ranges from 0.1-2.72 kg (as is)/ton of produced paper or board; (ii) said combined dosage of synthetic starch trapping polymers A and B ranges from 0.52-0.87 kg (as is)/ton of produced paper or board; (iii) said treated fi
Other processes for obtaining cellulose, e.g. cooking cotton linters (obtaining fibres for spinning D01C); {Processes characterised by the choice of cellulose-containing starting materials} · CPC title
cationic · CPC title
Chemicals therefor · CPC title
Chemicals therefor · CPC title
Secondary fibres (working-up waste paper D21C5/02) · CPC title
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