Patent US4943349A successfully refreshed from Google Patents.
US4943349A
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US
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Process for preparing a sheet material with improved on-machine retention
Assignee: Papeteries de Gascogne SA
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Filing: 1987-02-20
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Granted: 1990-07-24
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Expires: 2007-02-20
Abstract
Abstract Process for using papermaking techniques for preparing a sheet material with improved on-machine retention, sheet material thus obtained and its application, notably in the field of printing and writing, packaging and coverings. The invention relates to a process for using papermaking techniques to make a sheet material. This material copmrises, in addition to the fibres, an organic binder, a non-binding mineral filler and a flocculant, as well as various conventional additives, this process being characterized by the fact that the mineral filler and the binder are flocculated beforehand before being incorporated into the fibre suspension. The material thus prepared has enhanced mineral filler retention and physical properties and can be used as printing and writing medium, covering medium, packaging medium or for obtaining complexes for industrial or foodstuffs use.
Inventors
- 👤 Daniel Gomez
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-06 19:49
CPC Classifications
D; D21; D21H; D21H17/00; D21H17/63; D21H17/67; D21H17/69
Claims Analysis
Total Claims: 12
Claim 1
Independent Claim
293 words
A process using paper-making techniques for producing a fibrous sheet comprising fibers, an organic binder, a non-binding mineral filler and a flocculant, designed to improve the retention of the mineral filler in the sheet, sheet formation and the sheet's physical properties, which comprises the following steps in the following order: dispersing a non-binding mineral filler in an aqueous medium at a concentration from 150 to 600 g/l, mixing an anionic organic binder selected from the group consisting of native starches, chemically, enzymatically or thermally modified starches, dextrines, casein, animal glue, vegetable proteins, cellulose esters, alginates carboxylated or uncarboxylated styrene-butadiene latexes, acrylic latexes, styrene acrylics, vinyl acetates, neoprene Iatexes, acrylonitrile latexes and vinyl chloride latexes with the dispersed filler under agitation, continuously in a mixer in order to obtain an aqueous dispersion of mineral filler particles coated with binder which, after dilution, has a concentration from 50 to 200 g/l before flocculation; carrying out continuously ionic destabilization of said aqueous dispersion of mineral filler particles coated with binder by means of a cationic flocculant selected from the group consisting of aqueous solutions of polyethylenimine, polyamido-amine, cross-linked polyalkylamine, modified polyacrylamides, polyaluminium chloride and quaternary ammonium compounds in order to obtain improved flocculation control and good uniformity of the floc particle size, which favors formation, appearance, uniformity of surface and dimensional stability of the sheet; then continuously introducing the mineral filler/organic binder flocs in aqueous suspension into the refined pulp storage vat, conveying the mixture thus prepared to the head box and subsequently subjecting it to the draining, wet pressing and drying usual treatments of the paper manufacturing process for obtaining the fibrous sheet wherein the amount of binder lies between 1 and 40 parts by weight per 100 parts by weight of fibers and filler.
Claim 2
Dependent Claim
293 words
A process using paper-making techniques for producing a fibrous sheet comprising fibers, an organic binder, a non-binding mineral filler and a flocculant, designed to improve the retention of the mineral filler in the sheet, sheet formation and the sheet's physical properties, which comprises the following steps in the following order: dispersing a non-binding mineral filler in an aqueous medium at a concentration from 150 to 600 g/l, mixing an anionic organic binder selected from the group consisting of native starches, chemically, enzymatically or thermally modified starches, dextrines, casein, animal glue, vegetable proteins, cellulose esters, alginates carboxylated or uncarboxylated styrene-butadiene latexes, acrylic latexes, styrene acrylics, vinyl acetates, neoprene Iatexes, acrylonitrile latexes and vinyl chloride latexes with the dispersed filler under agitation, continuously in a mixer in order to obtain an aqueous dispersion of mineral filler particles coated with binder which, after dilution, has a concentration from 50 to 200 g/l before flocculation; carrying out continuously ionic destabilization of said aqueous dispersion of mineral filler particles coated with binder by means of a cationic flocculant selected from the group consisting of aqueous solutions of polyethylenimine, polyamido-amine, cross-linked polyalkylamine, modified polyacrylamides, polyaluminium chloride and quaternary ammonium compounds in order to obtain improved flocculation control and good uniformity of the floc particle size, which favors formation, appearance, uniformity of surface and dimensional stability of the sheet; then continuously introducing the mineral filler/organic binder flocs in aqueous suspension into the refined pulp storage vat, conveying the mixture thus prepared to the head box and subsequently subjecting it to the draining, wet pressing and drying usual treatments of the paper manufacturing process for obtaining the fibrous sheet wherein the amount of binder lies between 1 and 40 parts by weight per 100 parts by weight of fibers and filler.
Claim 3
Dependent Claim
45 words
The process of claim 1, wherein the non-binding mineral filler is selected from the group consisting of talc, kaolin, natural or precipitated calcium carbonate, or calcium carbonate from recovery operations on the black liquor extracted from digestion of draft pulps, alumina hydrates and titanium dioxide.
Claim 4
Dependent Claim
28 words
The process of claim 1, wherein the amount of binder used lies between 1 and 25 parts by weight per 100 parts by weight of fibers and filler.
Claim 5
Dependent Claim
32 words
The process of claim 1, wherein the flocculating agent is incorporated in an amount of between 0.006 and 5 parts by weight per 100 parts by weight of mineral filler and binder.
Claim 6
Dependent Claim
32 words
The process of claim 1, wherein the flocculating agent is incorporated in an amount of between 0.01 and 2 parts by weight per 100 parts by weight of mineral filler and binder.
Claim 7
Dependent Claim
73 words
The process of claim 1 wherein at least one conventional paper industry additive selected from the group consisting of an anti-foam agent, an optical blueing agent, a dyeing or shading agent, a wet strength agent, a fungicide and/or bactericide, a dispersing agent, a lubricating agent, and a viscosity regulator is added in the refined pulp storage vat or continuously in the head circuit after incorporation of the flocculated mineral filler and organic binder.
Claim 8
Dependent Claim
19 words
The process of claim 1 where in a pH regulator and a sizing agent are incorporated into the pulp.
Claim 9
Dependent Claim
31 words
The process of claim 1 wherein the ionic destabilization of the homogeneous filler-binder bath is obtained by incorporating continuously into said bath a cationic flocculant previously diluted one to ten times.
Claim 10
Dependent Claim
34 words
The process of claim 1 wherein, before incorporation of the mineral filler/organic binder flocs into the pulp, the anionic strength of the latter is increased by adding, with agitation, an anionic type retention agent.
Claim 11
Dependent Claim
23 words
The process of claim 9, wherein the retention agent of anionic type is selected from high molecular weight modified polyacrylamides and sodium polyacrylates.
Claim 12
Dependent Claim
40 words
The process of claim 1 wherein the aqueous dispersion of mineral filler particles coated with binder is a stable coating bath containing a mineral or organic dispersant in an amount from 0.02 to 1% by weight of the mineral filler.
References Cited (Backward Citations)
US4181567A
Cited
US4210490A
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1993-07-23 | 1994-01-22 | 1994-07-24 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1997-07-23 | 1998-01-22 | 1998-07-24 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 2001-07-23 | 2002-01-22 | 2002-07-24 | $7700.00 | Window Closed / Lapsed |