EP0522940A1 - Process for the preparation of paper and paper obtained therefrom - Google Patents

Process for the preparation of paper and paper obtained therefrom Download PDF

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Publication number
EP0522940A1
EP0522940A1 EP92401913A EP92401913A EP0522940A1 EP 0522940 A1 EP0522940 A1 EP 0522940A1 EP 92401913 A EP92401913 A EP 92401913A EP 92401913 A EP92401913 A EP 92401913A EP 0522940 A1 EP0522940 A1 EP 0522940A1
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Prior art keywords
weight
silica
chosen
paper
mixtures
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German (de)
French (fr)
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EP0522940B1 (en
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Lucien Bourson
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Arkema France SA
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Elf Atochem SA
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Classifications

    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21HPULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
    • D21H17/00Non-fibrous material added to the pulp, characterised by its constitution; Paper-impregnating material characterised by its constitution
    • D21H17/63Inorganic compounds
    • D21H17/66Salts, e.g. alums
    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21HPULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
    • D21H17/00Non-fibrous material added to the pulp, characterised by its constitution; Paper-impregnating material characterised by its constitution
    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21HPULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
    • D21H17/00Non-fibrous material added to the pulp, characterised by its constitution; Paper-impregnating material characterised by its constitution
    • D21H17/20Macromolecular organic compounds
    • D21H17/21Macromolecular organic compounds of natural origin; Derivatives thereof
    • D21H17/24Polysaccharides
    • D21H17/28Starch
    • D21H17/29Starch cationic
    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21HPULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
    • D21H17/00Non-fibrous material added to the pulp, characterised by its constitution; Paper-impregnating material characterised by its constitution
    • D21H17/63Inorganic compounds
    • D21H17/67Water-insoluble compounds, e.g. fillers, pigments
    • D21H17/68Water-insoluble compounds, e.g. fillers, pigments siliceous, e.g. clays

Definitions

  • the suspension containing the cellulose fibers can be raw or bleached pulp, bleached chemical pulp of softwoods or hardwoods or annual plants, unbleached chemical pulp of softwoods or hardwoods, mechanical pulps (SGW, TMP, CTMP, %) unbleached or bleached, de-inked bleached or unbleached pasta, pasta already containing additives, and mixtures thereof.
  • the cationic starch - mentioned as component c) 1) - used according to the present invention is a mixture of one or more products sold under the generic name of cationic starch.
  • Starch has an average molecular weight of 2.104 to 2.105, preferably 3.104 to 12.104.
  • Cationic starches have a degree of substitution (D.S.) of between 0.01 and 0.1.
  • the cationic starches are, for example, those described in Kirk Othmer, 3rd edition, volume 21, page 503. Preferably, they represent by weight from 0.2 to 1.7% of the weight of the fibrous suspension entering the headbox .
  • the PAC is present in the fibrous composition entering the headbox at a rate of 0.01 to 0.3% by weight, relative to the weight of said fibrous composition, said percentage being expressed relative to Al2O3.
  • the PAC is from WAC.
  • the WAC corresponds to formula IV.
  • the mineral filler -component a) mentioned above- may be one or more of the following conventionally used fillers, given by way of illustration: clay, CaCO3, hydrated alumina, talc, TiO2, etc.
  • the mineral filler represents less than 40% by weight, preferably from 10 to 25% by weight, of the weight of said fibrous composition.
  • the preferred mineral filler is formed of CaCO3.
  • the sizing agent - component b) mentioned above - can be one or more of the following agents conventionally used in neutral medium: dimeric alkyl ketenes (AKD), fluorinated phosphates, carboxylic anhydrides, styrene / maleic anhydride copolymers, and their derivatives .
  • the amount of sizing agent used is less than 10% by weight, preferably between 0.01 and 2% by weight of commercial product with 6% of active material, relative to the weight of said composition.
  • the bonding agent preferably used is AKD.

Abstract

Process for the manufacture of paper, characterised in that the following are added to the fibrous composition entering the flow box: a) an inorganic filler, b) an adhesion promoter, and c) a retaining system consisting of: c)1) cationic starch, c)2) aluminium polychloride, and c)3) silica of anionic nature. The products c)1), c)2) and c)3) have the following respective weight percentages on a weight basis in relation to the weight of the composition entering the flow box: 0.15 to 1.7 %, 0.05 to 0.25 % expressed as percentage of Al2O3, and 0.01 to 0.3 % expressed as percentage of SiO2. The cationic starch has a molecular weight of 3x10<4> to 12x10<4> and a degree of substitution of 0.01 to 0.1.

Description

La présente invention concerne un procédé de fabrication de papier et se rapporte également au papier ainsi obtenu.The present invention relates to a process for manufacturing paper and also relates to the paper thus obtained.

La pâte à papier brute constituée essentiellement de fibres de cellulose est mise sous forme d'une suspension aqueuse diluée qui est amenée dans la caisse de tête de la machine à papier d'où elle est distribuée sur une toile filtrante sur laquelle se forme la feuille de papier. Cette feuille est ensuite essorée puis séchée. Les qualités et les propriétés du papier obtenues sont déterminées notamment par les conditions de marche de la machine à papier, la pâte brute, les différents additifs qu'on ajoute dans la suspension avant la formation de la feuille et aussi les produits qu'on couche sur la feuille de papier en aval de la toile filtrante.The raw paper pulp consisting essentially of cellulose fibers is put in the form of a dilute aqueous suspension which is brought into the headbox of the paper machine from where it is distributed on a filter cloth on which the sheet is formed. of paper. This sheet is then wrung and dried. The qualities and properties of the paper obtained are determined in particular by the operating conditions of the paper machine, the raw pulp, the various additives that are added to the suspension before the sheet is formed and also the products that are coated. on the sheet of paper downstream of the filter cloth.

Parmi les produits ajoutés à la suspension de fibres entrant en caisse de tête, on peut citer les charges minérales, les agents de collage, les agents visant à améliorer les propriétés mécaniques du papier, les colorants, etc. Les charges minérales, telles que CaCO₃, TiO₂, etc, rendent la feuille de papier opaque, ce qui facilite l'écriture et l'impression. Les agents de collage, tels que ceux de la famille des alkylcétènes dimères, sont ajoutés pour rendre la feuille résistante aux liquides, par conséquent permettre à la feuille de papier collée d'être utilisée pour l'écriture et l'impression.Among the products added to the suspension of fibers entering the headbox, there may be mentioned mineral fillers, bonding agents, agents intended to improve the mechanical properties of the paper, dyes, etc. Mineral fillers, such as CaCO₃, TiO₂, etc., make the sheet of paper opaque, which facilitates writing and printing. Sizing agents, such as those of the dimeric alkyl ketene family, are added to make the sheet resistant to liquids, therefore allowing the glued sheet of paper to be used for writing and printing.

L'une des qualités des papiers, cartons et autres est la régularité des caractéristiques. Parmi celles-ci, "l'épair" ou "formation de la feuille" est d'une grande importance et est représentative de la qualité générale du papier. En effet, l'épair représente la plus ou moins grande homogénéité de la répartition des fibres dans le plan et l'épaisseur de la feuille. La qualité de l'épair aura donc une incidence considérable sur la qualité générale de l'impression dans le cas, par exemple, des papiers impression-écriture, et sur les propriétés mécaniques dans le cas, par exemple, des papiers d'emballage. Afin d'améliorer l'épair, de plus en plus d'additifs sont ajoutés à la suspension entrant en caisse de tête. Mais pour répondre aux exigences de plus en plus sévères des normes de pollution, les papeteries sont conduites à diminuer leur consommation en eau, ce qui provoque une augmentation de la charge polluante associée à ce type d'industrie (Matières en Suspension MES, Demande Biologique en Oxygène DBO, Demande Chimique en Oxygène DCO, Salinité, etc...) ainsi que d'autres problèmes, tels que des problèmes de poix et plus généralement ceux liés à la présence de déchets anioniques (dénommés en anglais "anionic trash"). Les caractéristiques du papier devant cependant rester identiques, et les problèmes de lutte pour l'environnement devant être résolus, l'une des méthodes proposées dans l'art antérieur consiste à augmenter la rétention des éléments au sein de la feuille en cours de formation sur la toile filtrante. Ce résultat est atteint, jusqu'à un certain point, par l'adjonction d'agents rétenteurs à la suspension de fibres entrant en caisse de tête. Malheureusement, cette méthode soit varie en efficacité, soit conduit à une détérioration importante de l'épair du papier selon les produits utilisés.One of the qualities of paper, cardboard and others is the regularity of the characteristics. Among these, "the air" or "leaf formation" is of great importance and is representative of the general quality of the paper. In fact, the epair represents the greater or lesser homogeneity of the distribution of the fibers in the plane and the thickness of the sheet. The quality of the air will therefore have a considerable impact on the general quality of the printing in the case, for example, of printing-writing papers, and on the mechanical properties in the case, for example, of packaging papers. In order to improve the look, more and more additives are added to the suspension entering the headbox. But to meet the increasingly stringent requirements of pollution standards, paper mills are led to reduce their water consumption, which causes an increase in the pollutant load associated with this type of industry (MES suspended matter, Biological Demand in Oxygen BOD, Chemical Demand in Oxygen COD, Salinity, etc ...) as well as other problems, such as pitch problems and more generally those related to the presence of anionic waste (called in English "anionic trash") . The characteristics of the paper having however to remain identical, and the problems of fight for the environment having to be resolved, one of the methods proposed in the prior art consists in increasing the retention of the elements within the sheet being formed on the filter cloth. This result is achieved, to a certain extent, by the addition of retention agents to the suspension of fibers entering the headbox. Unfortunately, this method either varies in efficiency or leads to a significant deterioration in the appearance of the paper depending on the products used.

La présente invention a donc pour objet un nouveau procédé de fabrication de papiers et autres, dans lequel, en plus de la charge minérale et de l'agent de collage est mélangé à la suspension ou composition de fibres entrant en caisse de tête, un nouveau système rétenteur ternaire. L'état de la technique en la matière est essentiellement formé des documents suivants:

  • EP-A-348 366 décrit un système ternaire comprenant de l'amidon cationique, du polychlorure d'aluminium, et un polymère d'acide silicique. Il n'est fait nullement mention de silice à caractère anionique et d'autre part l'acide polysilicique doit avoir une aire spécifique donnée (> 1 050 m²/g).
  • WO 88/6 659 décrit un système ternaire comprenant un polymère cationique, du polychlorure d'aluminium, et de la silice. Le polymère cationique est de préférence du polyacrylamide et l'amidon cationique n'est pas cité.
  • EP-A-285 486 décrit un système rétenteur à base d'amidon cationique et de polychlorure d'aluminium. La charge minérale peut être par exemple de la silice. Néanmoins, cette demande ne décrit pas spécialement le système rétenteur ternaire selon la présence invention.
  • US-A-4 643 801 décrit un système rétenteur à base d'amidon cationique, d'un polymère anionique à poids moléculaire élevé et de silice selon des rations en poids amidon/silice de 100/1 à 1/1 et polymère anionique/silice de 20/1 à 1/10. Un composé d'aluminium peut aussi être ajouté. Le présent système rétenteur ternaire seul n'est cependant pas décrit.
The present invention therefore relates to a new process for manufacturing papers and the like, in which, in addition to the mineral filler and the bonding agent is mixed with the suspension or composition of fibers entering the headbox, a new ternary retention system. The state of the art in this area is essentially composed of the following documents:
  • EP-A-348 366 describes a ternary system comprising cationic starch, poly aluminum chloride, and a polymer of silicic acid. There is no mention of anionic silica and on the other hand the polysilicic acid must have a given specific area (> 1050 m² / g).
  • WO 88/6659 describes a ternary system comprising a cationic polymer, poly aluminum chloride, and silica. The cationic polymer is preferably polyacrylamide and the cationic starch is not mentioned.
  • EP-A-285 486 describes a retention system based on cationic starch and poly aluminum chloride. The mineral filler can for example be silica. However, this application does not specifically describe the ternary retention system according to the invention presence.
  • US-A-4 643 801 describes a retention system based on cationic starch, a high molecular weight anionic polymer and silica according to starch / silica weight rations of 100/1 to 1/1 and anionic polymer / silica from 20/1 to 1/10. An aluminum compound can also be added. The present ternary retention system alone is however not described.

Dans "Polyaluminium hydroxychloride application in neutral pH rosin sizing of paper", B.H. Wortley et J.C. Steelhammer, est mentionné un système rétenteur comprenant de l'amidon cationique, de la bentonite et un polymère anionique, mais il n'est pas mentionné ni suggéré l'emploi de PAC dans ce système rétenteur particulier.In "Polyaluminium hydroxychloride application in neutral pH rosin sizing of paper", BH Wortley and JC Steelhammer, is mentioned a retentive system comprising cationic starch, bentonite and an anionic polymer, but it is not mentioned nor suggested l use of PAC in this particular retention system.

Aucune des publications ci-dessus seule ou en combinaison avec d'autres références ne décrit ni ne suggère l'emploi d'un système rétenteur du type de celui de la présente invention ni ne décrit ou suggère les effets surprenants et inattendus obtenus grâce à ce nouveau système rétenteur.None of the above publications alone or in combination with other references describes or suggests the use of a retention system of the type of that of the present invention or describes or suggests the surprising and unexpected effects obtained thanks to this. new retention system.

La présente invention a pour but, entre autres, tout en conservant la qualité de l'épair ainsi que les autres caractéristiques du papier, d'obtenir des taux de rétention élevés ainsi que de permettre un égouttage amélioré. La présente invention permet de réaliser une charge plus importante, notamment en produits sensibles aux acides, et conduit à des rejets moins polluants. Ainsi, la présente invention a pour objet un procédé de fabrication de papier, dans lequel on ajoute à la composition ou suspension fibreuse entrant en caisse de tête:

  • a) une charge minérale,
  • b) un agent de collage, et
  • c) un système rétenteur ternaire constitué de:
    • c)1) amidon cationique,
    • c)2) polychlorure d'aluminium, et
    • c)3) silice à caractère anionique.
The object of the present invention is, among other things, while retaining the quality of the air as well as the other characteristics of the paper, to obtain high retention rates as well as to allow improved drainage. The present invention makes it possible to carry out a greater charge, in particular in products sensitive to acids, and leads to less polluting releases. Thus, the subject of the present invention is a process for manufacturing paper, in which the following is added to the fiber composition or suspension entering the headbox:
  • a) a mineral filler,
  • b) a bonding agent, and
  • c) a ternary retention system consisting of:
    • c) 1) cationic starch,
    • c) 2) poly aluminum chloride, and
    • c) 3) anionic silica.

La suspension contenant les fibres de cellulose peut être de la pâte brute ou blanchie, des pâtes chimiques blanchies de résineux ou de feuillus ou de plantes annuelles, des pâtes chimiques écrues de résineux ou de feuillus, des pâtes mécaniques (SGW, TMP, CTMP, ...) écrues ou blanchies, des pâtes désencrées blanchies ou non-blanchies, des pâtes contenant déjà des additifs, et leurs mélanges.The suspension containing the cellulose fibers can be raw or bleached pulp, bleached chemical pulp of softwoods or hardwoods or annual plants, unbleached chemical pulp of softwoods or hardwoods, mechanical pulps (SGW, TMP, CTMP, ...) unbleached or bleached, de-inked bleached or unbleached pasta, pasta already containing additives, and mixtures thereof.

L'amidon cationique -mentionné à titre de composant c)1)- utilisé selon la présente invention est un mélange d'un ou plusieurs produits commercialisés sous le nom générique d'amidon cationique. L'amidon a un poids moléculaire moyen de 2.10⁴ à 2.10⁵, de préférence de 3.10⁴ à 12.10⁴. Les amidons cationiques ont un degré de substitution (D.S.) compris entre 0,01 à 0,1. Les amidons cationiques sont, par exemple, ceux décrits dans Kirk Othmer, 3ème édition, volume 21, page 503. De préférence, ils représentent en poids de 0,2 à 1,7% du poids de la suspension fibreuse entrant en caisse de tête.The cationic starch - mentioned as component c) 1) - used according to the present invention is a mixture of one or more products sold under the generic name of cationic starch. Starch has an average molecular weight of 2.10⁴ to 2.10⁵, preferably 3.10⁴ to 12.10⁴. Cationic starches have a degree of substitution (D.S.) of between 0.01 and 0.1. The cationic starches are, for example, those described in Kirk Othmer, 3rd edition, volume 21, page 503. Preferably, they represent by weight from 0.2 to 1.7% of the weight of the fibrous suspension entering the headbox .

Le polychlorure d'aluminium ou "PAC" -mentionné à titre de composant c)2)- utilisé selon la présente invention désigne les produits qu'on appelle habituellement polychlorure d'aluminium, polychlorure basique d'aluminium, polychlorosulfate basique d'aluminium, et consiste de préférence en un ou plusieurs des produits suivants:

  • 1. le sel de formule:

            Aln(OH)mCl3n-m   (I)

       dans laquelle n est quelconque, 3n-m est positif, m et n sont des nombres entiers positifs;
    ledit sel pouvant contenir en outre un anion polyvalent Y choisi parmi les anions des acides sulfurique, phosphorique, polyphosphorique, silicique, chromique, carboxylique, et sulfonique, le rapport molaire Y/A1 étant de préférence compris entre 0,015 et 0,4;
  • 2. le sel de formule:

            Aln(OH)mCl3n-m-2k(SO₄)k   (II)

       dans laquelle k, m et n sont des entiers positifs, et 3n > m + 2k, la basicité ou le rapport m/3n est compris entre 0,3 et 0,7 et k/n = 0,01 à 0,03;
    ce produit peut être préparé selon le procédé décrit dans le US-A-3 929 666;
  • 3. le sel de formule:

            [Aln(OH)3n-m 2-pClm(SO₄)p]z   (III)

       dans laquelle (3n-m-2p)/3n = 0,4 à 0,7; p = 0,04 à 0,25n; m/p = 8 à 35; k, m, n, et p sont des nombres entiers et z est au moins 1;
    ce produit est décrit dans GB-A-2 128 977;
  • 4. le chlorosulfate d'aluminium basique de formule:

            AlnOHm(SO₄)kCl3n-m-2k   (IV)

       dans laquelle la basicité ou le rapport molaire (m/3n)x100 est compris entre 40% environ et 65% environ
    qui présente un rapport équivalent Al/équivalent CI compris entre 2,8 et 5, une masse moléculaire apparente MA, mesurée par diffusion de lumière classique, et des diamètres hydrodynamiques apparents 0̸Z et 0̸W, mesurés par diffusion quasi-élastique de la lumière, présentant les valeurs respectives suivantes: MA = 7000-35000
    Figure imgb0001
    0̸Z(Å) = 350-2500
    Figure imgb0002
    0̸W(Å) = 200-1200;
    Figure imgb0003
    ce produit est décrit dans FR-A-2 584 699.
Poly aluminum chloride or "PAC" - mentioned as component c) 2) - used according to the present invention designates the products which are usually called poly aluminum chloride, basic aluminum polychloride, basic aluminum polychlorosulfate, and preferably consists of one or more of the following products:
  • 1. the salt of formula:

    Al n (OH) m Cl 3n-m (I)

    where n is arbitrary, 3n-m is positive, m and n are positive integers;
    said salt possibly also containing a polyvalent anion Y chosen from anions of sulfuric, phosphoric, polyphosphoric, silicic, chromic, carboxylic and sulfonic acids, the molar ratio Y / A1 preferably being between 0.015 and 0.4;
  • 2. the salt of formula:

    Al n (OH) m Cl 3n-m-2k (SO₄) k (II)

    in which k, m and n are positive integers, and 3n> m + 2k, the basicity or the ratio m / 3n is between 0.3 and 0.7 and k / n = 0.01 to 0.03;
    this product can be prepared according to the method described in US-A-3,929,666;
  • 3. the salt of formula:

    [Al n (OH) 3n-m 2-p Cl m (SO₄) p ] z (III)

    in which (3n-m-2p) / 3n = 0.4 to 0.7; p = 0.04 to 0.25n; m / p = 8 to 35; k, m, n, and p are whole numbers and z is at least 1;
    this product is described in GB-A-2 128 977;
  • 4. basic aluminum chlorosulfate of formula:

    Al n OH m (SO₄) k Cl 3n-m-2k (IV)

    in which the basicity or the molar ratio (m / 3n) x100 is between approximately 40% and approximately 65%
    which has an equivalent Al / equivalent CI ratio between 2.8 and 5, an apparent molecular mass MA, measured by conventional light scattering, and apparent hydrodynamic diameters 0̸Z and 0̸W, measured by quasi-elastic light scattering, having the following respective values: MA = 7000-35000
    Figure imgb0001
    0̸Z (Å) = 350-2500
    Figure imgb0002
    0̸W (Å) = 200-1200;
    Figure imgb0003
    this product is described in FR-A-2 584 699.

De préférence, le PAC est présent dans la composition fibreuse entrant en caisse de tête à raison de 0,01 à 0,3% en poids, par rapport au poids de ladite composition fibreuse, ledit pourcentage étant exprimé par rapport à Al₂O₃. De préférence, le PAC est du WAC. Le WAC correspond à la formule IV.Preferably, the PAC is present in the fibrous composition entering the headbox at a rate of 0.01 to 0.3% by weight, relative to the weight of said fibrous composition, said percentage being expressed relative to Al₂O₃. Preferably, the PAC is from WAC. The WAC corresponds to formula IV.

La silice à caractère anionique -mentionnée à titre de composant c)3)- utilisée dans la présente invention est un mélange d'une ou plusieurs silices choisies dans le groupe consistant en: sol de silice, gel de silice, silice microparticulaire, silico-aluminate, bentone et bentonite. De préférence, la silice est présente dans la composition fibreuse, à raison de 0,01 à 0,3% en poids, par rapport au poids de ladite composition fibreuse, le pourcentage étant exprimé en pourcentage de matière active, c'est-à-dire en SiO₂. La silice à caractère anionique employée de préférence est celle qui est sous la forme d'un sol de silice, avantageusement à 15% de SiO₂.The anionic silica - mentioned as component c) 3) - used in the present invention is a mixture of one or more silicas chosen from the group consisting of: silica sol, silica gel, microparticulate silica, silico- aluminate, bentone and bentonite. Preferably, the silica is present in the fibrous composition, in an amount of 0.01 to 0.3% by weight, relative to the weight of said fibrous composition, the percentage being expressed as a percentage of active material, that is to say - say in SiO₂. The silica with an anionic character preferably used is that which is in the form of a silica sol, advantageously at 15% of SiO₂.

La charge minérale -le composant a) mentionné ci-dessus-peut être l'une ou plusieurs des charges classiquement utilisées suivantes, données à titre illustratif: argile, CaCO₃, alumine hydratée, talc, TiO₂, etc. La charge minérale représente moins de 40% en poids, de préférence de 10 à 25% en poids, du poids de ladite composition fibreuse. La charge minérale préférée est formée de CaCO₃.The mineral filler -component a) mentioned above-may be one or more of the following conventionally used fillers, given by way of illustration: clay, CaCO₃, hydrated alumina, talc, TiO₂, etc. The mineral filler represents less than 40% by weight, preferably from 10 to 25% by weight, of the weight of said fibrous composition. The preferred mineral filler is formed of CaCO₃.

L'agent de collage -le composant b) mentionné ci-dessus-peut être un ou plusieurs des agents suivants classiquement utilisés en milieu neutre: alkylcétènes dimères (AKD), phosphates fluorés, anhydrides carboxyliques, copolymères styrène/anhydride maléique, et leurs dérivés. La quantité d'agent de collage employée est inférieure à 10% en poids, de préférence comprise entre 0,01 et 2% en poids de produit commercial à 6% de matière active, par rapport au poids de ladite composition. L'agent de collage employé de préférence est l'AKD.The sizing agent - component b) mentioned above - can be one or more of the following agents conventionally used in neutral medium: dimeric alkyl ketenes (AKD), fluorinated phosphates, carboxylic anhydrides, styrene / maleic anhydride copolymers, and their derivatives . The amount of sizing agent used is less than 10% by weight, preferably between 0.01 and 2% by weight of commercial product with 6% of active material, relative to the weight of said composition. The bonding agent preferably used is AKD.

Les composants a), b), c)1), c)2) et c)3) mentionnés ci-dessus peuvent être ajoutés séparément ou en mélange de deux ou plusieurs d'entre eux.Components a), b), c) 1), c) 2) and c) 3) mentioned above can be added separately or as a mixture of two or more of them.

La suspension fibreuse peut aussi contenir des additifs classiques, tels que des colorants, des azurants optiques, des agents de renforcement mécaniques, des antimousses, des antislimes (agent anti-dépôt), ainsi que des produits choisis dans le groupe consistant en: les polyacrylamides, les polyéthylèneimines, la carboxyméthylcellulose, les résines urée-formol, les résines mélamines- formol, les résines aminopolyamideépichlorhydrine, les résines polyamide-épichlorhydrine.The fibrous suspension can also contain conventional additives, such as dyes, optical brighteners, mechanical reinforcing agents, defoamers, antislimes (anti-deposition agent), as well as products chosen from the group consisting of: polyacrylamides , polyethyleneimines, carboxymethylcellulose, urea-formaldehyde resins, melamine-formaldehyde resins, aminopolyamideepichlorohydrin resins, polyamide-epichlorohydrin resins.

De préférence, les composants ajoutés sont :

  • a) de 5 à 30% de CaCOH₃,
  • b) de 0,01 à 1% d'AKD, et
  • c) 1. de 0,2 à 1,7% d'amidon cationique de poids moléculaire 2.10⁴ à 12.10⁵ et de degré de substitution de 0,01 à 0,1; c)2. de 0,1 à 3% de WAC en produit commercial à 10% de Al₂O₃; et c)3. de 0,01 à 0,3% de sol de silice, exprimé en % de SiO₂.
Preferably, the added components are:
  • a) from 5 to 30% of CaCOH₃,
  • b) from 0.01 to 1% of AKD, and
  • c) 1. from 0.2 to 1.7% of cationic starch with molecular weight 2.10⁴ to 12.10⁵ and degree of substitution from 0.01 to 0.1; c) 2. from 0.1 to 3% of WAC in commercial product to 10% of Al₂O₃; and c) 3. from 0.01 to 0.3% silica sol, expressed as% of SiO₂.

Les exemples suivants sont illustratifs de la présente invention et ne doivent en aucun cas être considérés comme limitatifs de celle-ci. Dans ces exemples, le WAC est un produit commercialisé par ATOCHEM et correspond à un polychlorure d'aluminium de formule IV à 10% de Al₂O₃. La silice est sous la forme de sol de silice et est disponible dans le commerce sous la dénomination CECASOL de CECA. L'amidon cationique est celui fabriqué par ROQUETTE et commercialisé sous la dénomination HICAT 142. L'agent de collage AKD est fabriqué par HERCULES et commercialisé sous la dénomination AQUAPEL.The following examples are illustrative of the present invention and should in no way be taken to limit it. In these examples, WAC is a product marketed by ATOCHEM and corresponds to a poly aluminum chloride of formula IV at 10% Al 10O₃. The silica is in the form of a silica sol and is commercially available under the name CECASOL from CECA. The cationic starch is that manufactured by ROQUETTE and marketed under the name HICAT 142. The AKD sizing agent is manufactured by HERCULES and marketed under the name AQUAPEL.

Exemple 1Example 1

Le papier à fabriquer est du papier impression-écriture support pour autocopiant.

. machine utilisée
table plate équipée d'un former BEL BOND
. vitesse
590 m/mn
. laize
3 m
. grammage
50 g/m²
Figure imgb0004

Les essais effectués sur le produit obtenu, dans les conditions consignées dans le Tableau ci dessous, conduisent aux résultats donnés dans ce tableau:
Figure imgb0005
The paper to be produced is carbonless printing-writing paper.
. machine used
flat table equipped with a BEL BOND former
. speed
590 m / min
. width
3 m
. grammage
50 g / m²
Figure imgb0004

The tests carried out on the product obtained, under the conditions recorded in the Table below, lead to the results given in this table:
Figure imgb0005

Entre l'essai 1 et l'essai 2, on note l'amélioration très importante de l'épair provoquée par l'utilisation du WAC à la place de la silice, résultat conforme à ce qu'attend l'homme de l'art.Between test 1 and test 2, there is a very significant improvement in the air caused by the use of WAC instead of silica, a result in accordance with what one skilled in the art expects. .

L'essai 3 montre la synergie que développe l'association de faibles quantités de silice en présence du WAC. A épair équivalent la rétention est accrue de 10 points soit un accroissement de 15 à 20%. Il en résulte une moindre pollution de l'eau des circuits et une plus grande facilité de traitement des eaux de rejets pour un coût inférieur.Test 3 shows the synergy that the association of small quantities of silica develops in the presence of WAC. At equivalent thickness retention is increased by 10 points, ie an increase of 15 to 20%. This results in less pollution of the water in the circuits and greater ease of treatment of waste water at a lower cost.

Exemple 2: Example 2 :

Le papier à fabriquer est du papier impression-écriture. La machine est identique à l'exemple 1.

. Vitesse machine
540 m/mn
. Grammage
60 g/m²
The paper to be produced is printing-writing paper. The machine is identical to Example 1.
. Machine speed
540 m / min
. Weight
60 g / m²

Composition fibreuse: Fibrous composition :

. KBR
40%
. KBR
60%
. Charges
CaCO₃
. Taux de charge
11%
. Amidon cationique
0,5%
. Collage: colle AKD
0,15% (en produit commercial)

Les essais effectués sur le produit obtenu, dans les conditions consignées dans le Tableau ci-dessous, conduisent aux résultats donnés dans ce tableau:
Figure imgb0006
. KBR
40%
. KBR
60%
. Charges
CaCO₃
. The taxes
11%
. Cationic starch
0.5%
. Bonding: AKD glue
0.15% (in commercial product)

The tests carried out on the product obtained, under the conditions recorded in the Table below, lead to the results given in this table:
Figure imgb0006

Exemple 3: Example 3 :

La machine est la même que dans l'exemple 2

. Vitesse
520 m/mn
. Grammage
70 g/m²
The machine is the same as in Example 2
. Speed
520 m / min
. Weight
70 g / m²

Composition fibreuse: Fibrous composition :

. KBR
35%
. KBF
65%
. Charge
CaCO₃
. Taux de charge
14%
. Amidon cationique
0,6%
. Collage: colle AKD
0,15% (en produit commercial)

Les essais effectués sur le produit obtenu, dans les conditions consignées dans le Tableau ci dessous, conduisent aux résultats donnés dans ce tableau:
Figure imgb0007
. KBR
35%
. KBF
65%
. Charge
CaCO₃
. The taxes
14%
. Cationic starch
0.6%
. Bonding: AKD glue
0.15% (in commercial product)

The tests carried out on the product obtained, under the conditions recorded in the Table below, lead to the results given in this table:
Figure imgb0007

Claims (16)

1.- Procédé de fabrication de papiers caractérisé en ce que l'on ajoute à la composition fibreuse entrant en caisse de tête: a) une charge minérale, b) un agent de collage, et c) un système rétenteur constitué de: c)1) amidon cationique, c)2) polychlorure d'aluminium, et c)3) silice à caractère anionique 1.- A process for the production of papers, characterized in that the fiber composition entering the headbox is added: a) a mineral filler, b) a bonding agent, and c) a retention system consisting of: c) 1) cationic starch, c) 2) poly aluminum chloride, and c) 3) anionic silica 2.- Procédé selon la revendication 1, caractérisé en ce que les produits c)1), c)2) et c)3) présentent en poids, par rapport au poids de la composition entrant en caisse de tête, les pourcentages pondéraux respectifs suivants: 0,2 à 1,7%, 0,01 à 0,3% exprimé en pourcentage d'Al₂O₃, et 0,01 à 0,3% exprimé en pourcentage de SiO₂. 2.- Method according to claim 1, characterized in that the products c) 1), c) 2) and c) 3) have by weight, relative to the weight of the composition entering the headbox, the respective weight percentages following: 0.2 to 1.7%, 0.01 to 0.3% expressed as a percentage of Al₂O₃, and 0.01 to 0.3% expressed as a percentage of SiO₂. 3.- Procédé selon la revendication 1 ou 2, caractérisé en ce que l'amidon cationique présente un poids moléculaire de 3.10⁴ à 12.10⁴ et un degré de substitution de 0,01 à 0,1. 3.- Method according to claim 1 or 2, characterized in that the cationic starch has a molecular weight of 3.10⁴ to 12.10⁴ and a degree of substitution from 0.01 to 0.1. 4.- Procédé selon la revendication 1, 2 ou 3, caractérisé en ce que le polychlorure d'aluminium est choisi parmi le groupe consistant en les sels de formules I, II, III, et IV suivants,
et leurs mélanges:

        Aln(OH)mCl3n-m   (I)

   dans laquelle m et n sont des nombres entiers positifs et 3n-m est positif; ledit sel pouvant contenir en outre un anion polyvalent Y choisi parmi les anions des acides sulfurique, phosphorique, polyphosphorique, silicique, chromique, carboxylique, et sulfonique, le rapport molaire Y/A1 étant, de préférence, compris entre 0,015 et 0,4;

        Aln(OH)mCl3n-m-2k(SO₄)k   (II)

   dans laquelle k, m et n sont des entiers positifs, et 3n > m + 2k, la basicité m/3n est comprise entre 0,3 et 0,7 et k/n = 0,01 à 0,03;

        [Aln(HO)3n-m-2pClm(SO₄)p]z   (III)

   dans laquelle (3n-m-2p)/3n = 0,4 à 0,7; p = 0,04 à 0,25n; m/p = 8 à 35, k, m, n, et p sont des nombres entiers et z est au moins 1;

        AlnOHm(SO₄)kCl3n-m-2k   (IV)

   dans laquelle la basicité (m/3n)100 est comprise entre 40% environ et 65% environ et présentant un rapport équivalent Al/équivalent Cl compris entre 2,8 et 5, une masse moléculaire apparente MA mesurée par diffusion de lumière classique et des diamètres hydrodynamiques apparents 0̸Z et 0̸W mesurés par diffusion quasi-élastique de la lumière de valeurs suivantes: MA = 7000-35000
Figure imgb0008
0̸Z(Å) = 350-2500
Figure imgb0009
0̸W(Å) = 200-1200.
Figure imgb0010
4.- Method according to claim 1, 2 or 3, characterized in that the aluminum polychloride is chosen from the group consisting of the salts of formulas I, II, III, and IV below,
and their mixtures:

Al n (OH) m Cl 3n-m (I)

in which m and n are positive integers and 3n-m is positive; said salt possibly also containing a polyvalent anion Y chosen from anions of sulfuric, phosphoric, polyphosphoric, silicic, chromic, carboxylic and sulfonic acids, the molar ratio Y / A1 preferably being between 0.015 and 0.4;

Al n (OH) m Cl 3n-m-2k (SO₄) k (II)

in which k, m and n are positive integers, and 3n> m + 2k, the basicity m / 3n is between 0.3 and 0.7 and k / n = 0.01 to 0.03;

[Al n (HO) 3n-m-2p Cl m (SO₄) p ] z (III)

in which (3n-m-2p) / 3n = 0.4 to 0.7; p = 0.04 to 0.25n; m / p = 8 to 35, k, m, n, and p are whole numbers and z is at least 1;

Al n OH m (SO₄) k Cl 3n-m-2k (IV)

wherein the basicity (m / 3n) 100 is between approximately 40% and approximately 65% and having an Al equivalent / Cl equivalent ratio between 2.8 and 5, an apparent molecular mass MA measured by conventional light scattering and apparent hydrodynamic diameters 0̸Z and 0̸W measured by quasi-elastic light scattering of the following values: MA = 7000-35000
Figure imgb0008
0̸Z (Å) = 350-2500
Figure imgb0009
0̸W (Å) = 200-1200.
Figure imgb0010
5.- Procédé selon l'une quelconque des revendications 1 à 4, caractérisé en ce que la silice à caractère anionique est choisie parmi le groupe consistant en: sol de silice, gel de silice, silice microparticulaire, silico-aluminate, bentone et bentonite et leurs mélanges. 5.- Method according to any one of claims 1 to 4, characterized in that the anionic silica is chosen from the group consisting of: silica sol, silica gel, microparticulate silica, silico-aluminate, bentone and bentonite and their mixtures. 6.- Procédé selon l'une quelconque des revendications 1 à 5, caractérisé en ce que le polychlorure d'aluminium est du WAC. 6.- Method according to any one of claims 1 to 5, characterized in that the poly aluminum chloride is WAC. 7.- Procédé selon l'une quelconque des revendications 1 à 6, caractérisé en ce que la silice à caractère anionique est un sol de silice. 7.- Method according to any one of claims 1 to 6, characterized in that the anionic silica is a silica sol. 8.- Procédé selon l'une quelconque des revendications 1 à 7, caractérisé en ce que la quantité de charge minérale a) est inférieure à 40% en poids, de préférence comprise entre 5 et 30% en poids, par rapport au poids de ladite composition fibreuse. 8.- Method according to any one of claims 1 to 7, characterized in that the amount of mineral filler a) is less than 40% by weight, preferably between 5 and 30% by weight, relative to the weight of said fibrous composition. 9.- Procédé selon l'une quelconque des revendications 1 à 8, caractérisé en ce que la charge minérale est choisie parmi l'argile, le carbonate de calcium, le dioxyde de titane, le talc, l'alumine hydratée, et leurs mélanges. 9.- Method according to any one of claims 1 to 8, characterized in that the mineral filler is chosen from clay, calcium carbonate, titanium dioxide, talc, hydrated alumina, and their mixtures . 10.- Procédé selon l'une quelconque des revendications 1 à 9, caractérisé en ce que la quantité d'agent de collage b) est inférieure à 10% en poids, de préférence comprise entre 0,01 et 2% en poids, par rapport au poids de ladite composition. 10.- Method according to any one of claims 1 to 9, characterized in that the amount of bonding agent b) is less than 10% by weight, preferably between 0.01 and 2% by weight, relative to the weight of said composition. 11.- Procédé selon l'une quelconque des revendications 1 à 10, caractérisé en ce que l'agent de collage est choisi dans le groupe consistant en: alkyl cétène dimères (AKD), phosphates fluorés, anhydrides d'acides carboxyliques, copolymères styrène/anhydride maléique, leurs dérivés, et leurs mélanges. 11.- Method according to any one of claims 1 to 10, characterized in that the bonding agent is chosen from the group consisting of: alkyl ketene dimers (AKD), fluorinated phosphates, anhydrides of carboxylic acids, styrene copolymers / maleic anhydride, their derivatives, and mixtures thereof. 12.- Procédé selon l'une quelconque des revendications 1 à 11, caractérisé en ce que la charge minérale est du CaCO₃. 12.- Method according to any one of claims 1 to 11, characterized in that the mineral filler is CaCO₃. 13.- Procédé selon l'une quelconque des revendications 1 à 12, caractérisé en ce que l'agent de collage est de l'AKD. 13.- Method according to any one of claims 1 to 12, characterized in that the bonding agent is AKD. 14.- Procédé selon l'une quelconque des revendications 1 à 13, caractérisé en ce qu'on ajoute de plus à ladite composition fibreuse un composant optionnel choisi parmi les polyéthylèneimines, la carboxyméthylcellulose, les résines urée-formol, les résines mélamine-formol, les résines aminopolyamide-épichlorhydrine, les résines polyamide-épichlorhydrine et leurs mélanges. 14.- Method according to any one of claims 1 to 13, characterized in that one additionally adds to said fibrous composition an optional component chosen from polyethyleneimines, carboxymethylcellulose, urea-formaldehyde resins, melamine-formaldehyde resins , aminopolyamide-epichlorohydrin resins, polyamide-epichlorohydrin resins and mixtures thereof. 15.- Procédé selon l'une quelconque des revendications 1 à 14, caractérisé en ce que les composants ajoutés sont: a) de 5 à 30% de CaCO₃, b) de 0,01 à 1% d'AKD, et c)1. de 0,2 à 1,7% d'amidon cationique de poids moléculaire 2.10⁴ à 12.10⁵ et de degré de substitution de 0,01 à 0,1; c)2. de 0,1 à 3% de WAC en produit commercial à 10% de Al₂O₃; et c)3. de 0,01 à 0,3% de sol de silice, exprimé en % de SiO₂. 15.- Method according to any one of claims 1 to 14, characterized in that the added components are: a) from 5 to 30% of CaCO₃, b) from 0.01 to 1% of AKD, and c) 1. from 0.2 to 1.7% of cationic starch with molecular weight 2.10⁴ to 12.10⁵ and degree of substitution from 0.01 to 0.1; c) 2. from 0.1 to 3% of WAC in commercial product to 10% of Al₂O₃; and c) 3. from 0.01 to 0.3% silica sol, expressed as% of SiO₂. 16.- Papier, caractérisé en ce qu'il est obtenu par le procédé selon l'une quelconque des revendications 1 à 15. 16.- Paper, characterized in that it is obtained by the process according to any one of claims 1 to 15.
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Cited By (10)

* Cited by examiner, † Cited by third party
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EP0608986A1 (en) * 1993-01-26 1994-08-03 Ciba Specialty Chemicals Water Treatments Limited Production of filled paper
US5501774A (en) * 1993-01-26 1996-03-26 Allied Colloids Limited Production of filled paper
EP0683267A3 (en) * 1994-05-18 1996-07-03 Minnesota Mining & Mfg Fluorine-containing phosphates, and their use in papermaking.
US5891305A (en) * 1995-03-31 1999-04-06 Roquette Freres Process for the manufacture of paper
EP0786476A1 (en) 1996-01-23 1997-07-30 Roquette Frˬres Composition and process for bonding plane structures
ES2132011A1 (en) * 1996-08-07 1999-08-01 Fernandez Galo Polo Process for preparing board or similar agglomerates
US6074530A (en) * 1998-01-21 2000-06-13 Vinings Industries, Inc. Method for enhancing the anti-skid or friction properties of a cellulosic fiber
WO2007078245A1 (en) * 2005-12-30 2007-07-12 Akzo Nobel N.V. A process for the production of paper
EP2322714A1 (en) * 2005-12-30 2011-05-18 Akzo Nobel N.V. A process for the production of paper
US10982391B2 (en) 2016-06-01 2021-04-20 Ecolab Usa Inc. High-efficiency strength program used for making paper in higher charge demand system

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GR3021763T3 (en) 1997-02-28
DK0522940T3 (en) 1996-11-11
FI923194A0 (en) 1992-07-10
NO922672D0 (en) 1992-07-07
CA2073610A1 (en) 1993-01-13
IE922269A1 (en) 1993-01-13
EP0522940B1 (en) 1996-09-18
US5501771A (en) 1996-03-26
CA2073610C (en) 1996-09-17
ES2092074T3 (en) 1996-11-16
NO922672L (en) 1993-01-13
FR2678961B1 (en) 1993-10-15
FI923194A (en) 1993-01-13
DE69213850D1 (en) 1996-10-24
DE69213850T2 (en) 1997-02-20
FR2678961A1 (en) 1993-01-15
NO179255B (en) 1996-05-28
JPH05195486A (en) 1993-08-03
ATE143075T1 (en) 1996-10-15

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