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EP1392920B1 - Nappe fibreuse enduite et procede de production de ladite nappe - Google Patents

Nappe fibreuse enduite et procede de production de ladite nappe Download PDF

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Publication number
EP1392920B1
EP1392920B1 EP02716870A EP02716870A EP1392920B1 EP 1392920 B1 EP1392920 B1 EP 1392920B1 EP 02716870 A EP02716870 A EP 02716870A EP 02716870 A EP02716870 A EP 02716870A EP 1392920 B1 EP1392920 B1 EP 1392920B1
Authority
EP
European Patent Office
Prior art keywords
filler
fibrous web
fibrils
light scattering
coating
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
EP02716870A
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German (de)
English (en)
Other versions
EP1392920A1 (fr
Inventor
Petri Silenius
Jari Meuronen
Markku Leskelä
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Metsa Board Oyj
Original Assignee
M Real Oyj
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
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Classifications

    • D—TEXTILES; PAPER
    • D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21H—PULP 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
    • D21H17/00—Non-fibrous material added to the pulp, characterised by its constitution; Paper-impregnating material characterised by its constitution
    • D21H17/63—Inorganic compounds
    • D21H17/67—Water-insoluble compounds, e.g. fillers, pigments
    • D21H17/69—Water-insoluble compounds, e.g. fillers, pigments modified, e.g. by association with other compositions prior to incorporation in the pulp or paper
    • D—TEXTILES; PAPER
    • D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21H—PULP 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
    • D21H11/00—Pulp or paper, comprising cellulose or lignocellulose fibres of natural origin only
    • D21H11/16—Pulp or paper, comprising cellulose or lignocellulose fibres of natural origin only modified by a particular after-treatment
    • D—TEXTILES; PAPER
    • D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21H—PULP 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
    • D21H15/00—Pulp or paper, comprising fibres or web-forming material characterised by features other than their chemical constitution
    • D21H15/02—Pulp or paper, comprising fibres or web-forming material characterised by features other than their chemical constitution characterised by configuration
    • D21H15/10—Composite fibres
    • D21H15/12—Composite fibres partly organic, partly inorganic

Definitions

  • the present invention relates to a coated fibrous web according to the preamble of claim 1.
  • This kind of a fibrous web generally comprises a base web with a filler, having a pigment-containing coating layer on at least one surface.
  • the present invention relates also to the method according to the preamble of claim 12 for producing a coated fibrous web.
  • the printability of paper and board - properties of the printing surface and the printing process - are improved by coating the paper with different mineral coatings.
  • the purpose of the coating is to cover the fibres and the fibre flocks of the paper and board and, by these measures, to decrease the roughness of the surface and the size of the pores of the surface.
  • the coatings usually consist of pigments and binders, as well as of various additives.
  • the coatability of paper in other words the capability of the base paper to be covered with a coating, has become even more important with the increased demand for lightweight paper grades. Although the coverage can be affected by the properties of the coating mix and the coating manner, the qualities of the base paper are also important. Good formation and smoothness as well as suitable air resistance and porosity are properties of the base paper that are the most important factors affecting the coatability, especially when good quality is aspired with a small amount of coating.
  • the fibre web to be coated usually contains filler. The filler improves the formation of the paper web by filling the spaces between the fibres. Also the opacity of the web can be improved with the help of the filler.
  • Finnish Patent Specification No. 100729 discloses a papermaking filler comprising porous aggregates formed by precipitated calcium carbonate particles on the surface of fines. What characterises this new kind of filler is that, according to the patent specification, the calcium carbonate is precipitated on fine fibrils produced by refining cellulose fibres and/or mechanical pulp fibres. The size distribution of the fines fraction corresponds mainly to the wire screen fraction P100.
  • fillers consisting at least partly of cellulose or lignocellulose fibrils, over which light scattering material particles has been precipitated, can be used as fillers.
  • These particles are typically inorganic salts precipitating in an aqueous phase, such as calcium carbonate, calcium sulphate, barium sulphate and calcium oxalate.
  • the method according to the present invention is mainly characterised by what is stated in the characterising part of claim 1.
  • the method according to the present invention is characterised by what is stated in the characterising part of the claim 12.
  • the present invention provides considerable advantages.
  • a composite filler consisting of fibrils and mineral pigments has been found to provide the base paper with properties that are, as far as coatability is concerned, better than what can be achieved with fillers that are at the present commercially available.
  • the composite filler used in the present invention surprisingly can improve considerably the formation of the fibre web without impairing retention, a very smooth coating substrate can be obtained by means of the present invention.
  • the smoothness of the surface can also be improved.
  • the fines-based carrier fraction makes the surface of the base paper denser so that the coating does not penetrate too much into the fibre network. Due to these reasons, even a small amount of coating provides good coverage and a high quality of the coating, improving the cost efficiency.
  • the filler used in the present invention is based on fibrils obtained from chemical pulp.
  • chemical pulp refers to a pulp, which has been treated with cooking chemicals for delignification of the cellulose fibres.
  • fibrils have been obtained by refining a pulp produced by the sulphate process or by another alkaline pulping process.
  • the present invention can also be applied to modification of fibrils obtained from chemimechanical and mechanical pulp, in addition to chemical pulps.
  • the average thickness of cellulose or lignocellulose fibrils is smaller than 5 ⁇ m, conventionally smaller than 1 ⁇ m.
  • the fibrils are characterized by at least one of the following criteria:
  • the source material for the fibrils i.e. the fines based on cellulose or other fibers, is fibrillated by beating it in a pulp refiner.
  • the desired fraction may, when necessary, be separated by using a screen, but fines need not always be screened.
  • Suitable fibril fractions include wire screen fractions P50 - P400.
  • refiners with grooved blades are used.
  • the light-scattering material particles in the filler are inorganic or organic salts that can be formed from their source materials by precipitation in an aqueous medium.
  • Such compounds include calcium carbonate, calcium oxalate, calcium sulphate, barium sulphate, and mixtures thereof.
  • the material particles are deposited on the fibrils.
  • the amount of an inorganic salt compound in proportion to the fibril amount is approx. 0.0001 - 95 % by weight, preferably approx. 0.1 - 90 % by weight, most suitably approx. 60 - 80 % by weight, calculated from the amount of filler, and approx. 0.1 - 80 % by weight, preferably approx. 0.5 - 50 % by weight, of the paper.
  • the filler is produced by precipitating a mineral pigment on the surface of fine fibrils prepared from cellulose fibres and/or mechanical pulp fibres.
  • the precipitation of calcium carbonate can be carried out by feeding into an aqueous slush of fibrils an aqueous calcium hydroxide solution which possibly contains a solid calcium hydroxide, and a compound which contains carbonate ions and is at least partly dissolved in water (e.g. sodium carbonate or ammonium carbonate). It is also possible to introduce into the aqueous phase carbon dioxide gas that, in the presence of calcium hydroxide, produces calcium carbonate. There are formed string-of pearls-like calcium carbonate crystal aggregates, which are held together by fibrils, i.e.
  • the diameter of the calcium carbonate particles in the aggregates is about 0.1 to 5 ⁇ m, typically about 0.2 to 3 ⁇ m.
  • the fibrils correspond to wire screen fractions P50 (or P100) to P400.
  • the filler at least 80 %, preferably up to 90 %, of the light scattering pigments are attached to the fibrils.
  • the paper pulp is slushed by a process known per se (typically to solids content of about 0.1 to 1 %) and it is spread on the wire.
  • the above-mentioned filler is added to the fibre slush most suitably in the headbox of a paper or board machine, usually in an amount of about 1 to 100 % by weight of fibres of pulp. In other words, the amount of the filler can be up to equal to - or greater than - the amount of the actual pulp.
  • the pulp is webbed in a paper or board machine to form a paper or board web.
  • the fibre web is dried and coated and possibly processed further, for example, by calendering.
  • Coating can be carried out as single-coating or double-coating, whereupon the coating colour can be used as single-coat mixes and as so called precoating and surface-coat mixes. Also triple coatings are possible.
  • the coating colour according to the present invention contains from 10 to 100 parts by weight of at least one pigment or mixture of pigments, from 0.1 to 30 parts by weight of at least one binder and from 1 to 10 parts by weight of other additives known per se.
  • the typical composition of a precoating mixture is as follows: Coating pigment (for example, coarse calcium carbonate) 100 parts by weight Binder 1 - 20 % of the weight of the pigments Additives and auxiliary agents 0.1 - 10 % of the weight of the pigments Water the rest
  • Water is added to the precoating mix so that the solids content is generally from 40 to 70 %.
  • the composition of the surface-coat mixture or single-coat mixture is as follows: Coating pigment I (for example, fine carbonate) 10 - 90 parts by weight Coating pigment II (for example fine kaolin) 10 - 90 parts by weight Pigment total 100 parts by weight Binder 1 - 20 parts by weight Additives and auxiliary agents 0.1 - 10 parts by weight Water the rest
  • Water is added to this kind of a coating colour so that the dry solids content is typically from 50 to 75 %.
  • pigments that have a steep particle size distribution, so that the case at maximum 35 % of the pigment particles are smaller than 0.5 ⁇ m, preferably at maximum 15 % are smaller than 0.2 ⁇ m.
  • the present invention is applicable to any pigment.
  • Precipitated calcium carbonate, ground calcium carbonate, calcium sulphate, calcium oxalate, aluminium silicate, kaolin (hydrous aluminium silicate), aluminium hydroxide, magnesium silicate, talc (hydrous magnesium silicate), titanium dioxide and barium sulphate, and mixtures thereof can be mentioned as examples of the pigments.
  • Synthetic pigments can also be used.
  • the main pigments are kaolin, calcium carbonate, precipitated calcium carbonate and gypsum, which in general constitute over 50 % of the dry solids in the coating mix.
  • Calcined kaolin, titanium dioxide, satin white, aluminium hydroxide, sodium silicoaluminate and plastics pigments are additional pigments, and their amounts are in general less than 25 % of the dry solids in the mix.
  • special pigments special-quality kaolins and calcium carbonates, as well as barium sulphate and zinc oxide, should be mentioned.
  • the present invention is applied especially preferably to calcium carbonate, calcium sulphate, aluminium silicate and aluminium hydroxide, magnesium silicate, titanium dioxide and/or barium sulphate, as well as mixtures thereof, in which case, especially preferably, the principal pigment in the pre-coat mixes is calcium carbonate or gypsum and in surface-coat mixes and single-coat mixes the principal pigment consists of mixtures of calcium carbonate or gypsum and kaolin.
  • binders generally employed in paper production as binders in the coating colours.
  • binders it is also possible to use mixtures of binders.
  • typical binders include synthetic latexes made up of polymers or copolymers of ethylenically unsaturated compounds, e.g. copolymers of the butadienestyrene type, which possibly also have a comonomer containing a carboxyl group, such as acrylic acid, itaconic acid or maleic acid, and polyvinyl acetate having comonomers that contain carboxyl groups.
  • the water-soluble polymers starch, CMC, hydroxyethyl cellulose and polyvinyl alcohol as binders.
  • additives and auxiliary agents such as dispersants (e. g. sodium salt of polyacrylic acid), agents affecting the viscosity and water retention of the mix (e. g. CMC, hydroxyethyl cellulose, polyacrylates, alginates, benzoate), so-called lubricants, hardeners used for improving water-resistance, optical auxiliary agents, anti-foaming agents, pH control agents, and preservatives in the coating composition.
  • dispersants e. g. sodium salt of polyacrylic acid
  • agents affecting the viscosity and water retention of the mix e. g. CMC, hydroxyethyl cellulose, polyacrylates, alginates, benzoate
  • so-called lubricants so-called lubricants
  • hardeners used for improving water-resistance e. hydroxyethyl cellulose, polyacrylates, alginates, benzoate
  • hardeners used for improving water-resistance
  • optical auxiliary agents
  • lubricants include sulpfonate oils, esters, amines, calcium or ammonium stearates; of agents improving water resistance, glyoxal; of optical auxiliary agents, diaminostilbene disulfonic acid derivatives; of anti-foaming agents, phosphate esters, silicones, alcohols, ethers, vegetable oils; of pH control agents, sodium hydroxide, ammonia; and finally of preservatives, formaldehyde, phenol, quaternary ammonium salts.
  • the coating mix can be applied to the material web in a manner known per se.
  • the method according to the present invention for coating paper and/or board can be carried out with a conventional coating apparatus, i.e. by blade coating, or by film coating or JET application.
  • a coating layer having a grammage of 5-30 g/m 2 is formed at least on one surface, preferably on both surfaces.
  • An uncoated side can be treated, for example, by web sizing.
  • coated and optionally calendared cellulose-containing material webs having excellent printing properties, good smoothness and high opacity and brightness, can be produced.
  • cellulose-containing material we refer to the paper or board or a corresponding cellulosic material derived from a lignocellulose-containing raw material, in particular from wood or from annual or perennial plants.
  • the said material can be wood-containing or wood-free, and it can be produced from mechanical, semi-mechanical (chemimechanical) or chemical pulp. Chemical pulp or mechanical pulp may be bleached or unbleached.
  • the material may also contain recycled fibers, in particular recycled paper or recycled board.
  • the material may also contain recycled fibers, in particular recycled paper or recycled board.
  • the grammage of the material web ranges typically from 35 to 500 g/m 2 , typically it is about 50 to 450 g/m 2 .
  • the grammage of the base paper is 20-250 g/m 2 , preferably 30-80 g/m 2 .
  • the grammage of which is approx. 50-70 g/m 2
  • 10-20 g of coating/m 2 /side and by calendering the paper a product that has a grammage of 70-110 g/m 2 , a brightness of at least 90 %, an opacity of at least 90 % is obtained.
  • An especially preferred product is a coated offset paper in which high gloss and high opacity and bulk are combined.
  • the present invention is suitable also for production of coated fine paper, possibly also for those that contain mechanical pulp.
  • Birch sulphate pulp was refined with a Valmet JC-01 refiner to produce pulp that is suitable for production of the filler.
  • the consistency of refining was about 4 % and the total energy consumption was 343 kWh/t and the specific edge load was 0,5 J/m.
  • Carbonating was performed in tap water according to the FI Patent Specification No. 100729 .
  • the water slurry was obtained, the dry matter content of which was 2.22 % and total amount 248 m 3 .
  • the final product had CaCO 3 content of 69.7 % and a specific surface area 10.6 m 2 /kg.
  • Example 1 The product produced in Example 1 was used as a filler in coated fine papers.
  • Table 2 presents the results that were obtained in the test where fine paper was produced on the pilot machine (FEX) of STFI in Sweden: Table 2.
  • a base paper that has a grammage of 56 g/m 2 was produced in factory conditions for coating.
  • the slush consisted of a mixture of birch pulp (74 %) and pine pulp (24 %). After refining, the SR value of the pine was 32 to 34° and that of birch was 22 to 25 °. The SR value of the pulp in the headbox was 35 to 40°.
  • the wire compartment of the paper machine had a hybride wire of Valmet (Sym-former), and the wet pressing compartment consisted of a Valmet Sym-Press II that has a triple compressor and a conventional drying section.
  • Nanoparticles and cationic starch (Compozil Plus: EKA NP 780 nanoparticle and EKA PL 1510 C-PAM, supplier: EKA Chemicals) were used as retention chemicals.
  • the dosage amounts in the case of talc and PCC were as follows: nanoparticle 280 g/t, polymer 70 g/t, and with SuperFill: nanoparticle 280 g/t, polymer 50 g/t.
  • the amounts of cationic starch and resin adhesive used were 8 kg/t and 5.2 g/t.
  • the alum was administered for talc at 13 kg/t and with PCC and SuperFill at 19 kg/t.
  • the coulter-oil porosity was measured from the base paper samples. No significant differences were observed in the pore size distribution with low filler contents. 75 % of all pores were in the range of 1.2 to 1.8 ⁇ m (around the maximum point). When the filler content was increased to 20 %, significant differences were observed. In the case of PCC, the median of the pore size increased as the amount of filler was increased. The median decreased and the distribution narrowed with the SuperFill filler, whereupon 75 % of the values were around 0.8 ⁇ m. The same effect can be seen with talc but in a smaller scale.
  • the median of the pore size was only 60 % of the corresponding value of the PCC, and the width of the pore size distribution (75 % of values) was only 34 % of values obtained with the PCC.
  • the SuperFill provides paper, the surface of which is more enclosed than the surface of the paper filled with PCC, which facilitates the coating and improves the quality of paper due to the better coverage.
  • better glossier and smoother surface is obtained as the coating pigments cannot penetrate into the base paper as easily.
  • the base paper described hereinbefore was coated one-side and the other side was surface-sized.
  • the ABC single-blade coater of BTG was used for coating.
  • the surface sizing was performed in the same unit by film transferring on the backing-roll of the coater.
  • the machine velocity was 750 m/min and length of the reeler of the web was 252 cm.
  • Online-coating was carried out after the fourth drying group and the coating was dried with drying cylinders (the 5 th drying group).
  • the coated and calendered paper that contains SuperFill has about 5 % units better gloss and 0.1 pps units better smoothness than a corresponding paper filled with talc. This is a very good result, taking into account that the coater amounts of the SuperFill papers were even slightly smaller. The light scattering factor and brightness of the SuperFill papers were also considerably better than the corresponding papers filled with talc..

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  • Chemical & Material Sciences (AREA)
  • Inorganic Chemistry (AREA)
  • Paper (AREA)
  • Yarns And Mechanical Finishing Of Yarns Or Ropes (AREA)

Claims (16)

  1. Bande fibreuse revêtue, comprenant
    - une bande de base contenant une charge, qui comprend une couche de revêtement contenant un pigment au moins sur l'une des surfaces,
    caractérisée en ce que
    - la charge de la bande de base est au moins partiellement constituée de fibrilles de cellulose ou de lignocellulose, sur lesquelles des particules d'un matériau diffusant la lumière ont été précipitées.
  2. Bande fibreuse selon la revendication 1, caractérisée en ce que la charge comprend des fibrilles de cellulose ou de lignocellulose qui ont une épaisseur moyenne inférieure à 5 µm, produites par raffinage et tamisage de fibres végétales.
  3. Bande fibreuse selon la revendication 2, caractérisée en ce que les particules de matériau diffusant la lumière sont précipitées sur des fibrilles qui correspondent à une fraction traversant un tamis de 50 mesh et/ou ayant une épaisseur moyenne de 0,01 à 5 µm et une longueur moyenne de 10 à 1500 µm.
  4. Bande fibreuse selon l'une quelconque des revendications 1 à 3, caractérisée en ce que les particules de matériau diffusant la lumière sont des sels inorganiques qui peuvent être formés à partir de leurs matériaux sources par précipitation dans un milieu aqueux.
  5. Bande fibreuse selon la revendication 4, caractérisée en ce que les particules de matériau diffusant la lumière sont du carbonate de calcium, de l'oxalate de calcium, du sulfate de calcium, du sulfate de baryum ou leurs mélanges.
  6. Bande fibreuse selon l'une quelconque des revendications 1 à 5, caractérisée en ce que les particules de matériau sont précipitées sur les fibrilles.
  7. Bande fibreuse selon la revendication 6, caractérisée en ce que la quantité de particules de matériau diffusant la lumière par rapport à la quantité de fibrilles est de 0,0001 à 95 % en poids, de préférence d'environ 0,1 à 90 % en poids, de la manière la plus appropriée d'environ 60 à 80 % en poids, par rapport à la quantité de charge, et d'environ 0,1 à 60 % en poids, de préférence de 0,5 à 50 % en poids du papier.
  8. Bande fibreuse selon l'une quelconque des revendications précédentes, caractérisée en ce qu'elle est revêtue avec du carbonate de calcium, du gypse, du silicate d'aluminium, du kaolin, de l'hydroxyde d'aluminium, du silicate de magnésium, du talc, de l'oxyde de titane, du sulfate de baryum, de l'oxyde de zinc, un pigment synthétique ou leurs mélanges.
  9. Bande fibreuse selon l'une quelconque des revendications précédentes, caractérisée en ce que la charge, qui comprend des fibrilles de cellulose ou de lignocellulose, sur lesquelles les particules de matériau diffusant la lumière ont été précipitées, forme 10 à 100 % en poids de la charge de la bande de base.
  10. Bande fibreuse selon l'une quelconque des revendications précédentes, caractérisée en ce que la charge, qui comprend des fibrilles de cellulose ou de lignocellulose, sur lesquelles les particules de matériau diffusant la lumière ont été précipitées, forme 10 à 100 % en poids du matériau fibreux de la bande de base.
  11. Bande fibreuse selon l'une quelconque des revendications précédentes, caractérisée en ce qu'elle comprend du papier revêtu, contenant du bois ou sans bois.
  12. Procédé de fabrication d'une bande fibreuse, selon lequel une couche de revêtement contenant un pigment est appliquée au moins sur une surface d'une bande de base contenant un matériau fibreux, caractérisé par la formation de la bande de base à partir d'une boue du matériau fibreux, à laquelle un produit comprenant des fibrilles de cellulose ou de lignocellulose, sur lesquelles des particules d'un matériau diffusant la lumière ont été déposées, est ajouté en tant que charge.
  13. Procédé selon la revendication 12, caractérisé par l'utilisation d'une charge qui comprend des fibrilles de cellulose ou de lignocellulose ayant une épaisseur moyenne inférieure à 5 µm produites par raffinage et tamisage de fibres végétales.
  14. Procédé selon la revendication 12, caractérisé par l'utilisation d'une charge, dont les particules de matériau diffusant la lumière ont été déposées sur des fibrilles, qui correspond à une fraction qui traverse un tamis de 50 mesh et/ou ayant une épaisseur moyenne de 0,1 à 10 µm et une longueur moyenne de 10 à 1 500 µm.
  15. Procédé selon l'une quelconque des revendications 12 à 14, caractérisé par l'utilisation d'une charge dans laquelle au moins 80 % des particules de pigment diffusant la lumière sont attachées aux fibrilles.
  16. Procédé selon la revendication 12, caractérisé par le revêtement de la bande de base dans une machine à papier avec un mélange de revêtement contenant un pigment.
EP02716870A 2001-04-24 2002-04-24 Nappe fibreuse enduite et procede de production de ladite nappe Expired - Lifetime EP1392920B1 (fr)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
FI20010846 2001-04-24
FI20010846A FI117870B (fi) 2001-04-24 2001-04-24 Päällystetty kuiturata ja menetelmä sen valmistamiseksi
PCT/FI2002/000341 WO2002092909A1 (fr) 2001-04-24 2002-04-24 Nappe fibreuse enduite et procede de production de ladite nappe

Publications (2)

Publication Number Publication Date
EP1392920A1 EP1392920A1 (fr) 2004-03-03
EP1392920B1 true EP1392920B1 (fr) 2012-03-21

Family

ID=8561046

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Application Number Title Priority Date Filing Date
EP02716870A Expired - Lifetime EP1392920B1 (fr) 2001-04-24 2002-04-24 Nappe fibreuse enduite et procede de production de ladite nappe

Country Status (10)

Country Link
US (1) US20040173329A1 (fr)
EP (1) EP1392920B1 (fr)
JP (1) JP2004525281A (fr)
CN (1) CN100519936C (fr)
AT (1) ATE550485T1 (fr)
AU (1) AU2002247793B2 (fr)
CA (1) CA2444085C (fr)
FI (1) FI117870B (fr)
NZ (1) NZ529161A (fr)
WO (1) WO2002092909A1 (fr)

Families Citing this family (21)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FI115475B (fi) * 2002-10-24 2005-05-13 M Real Oyj Menetelmä paperin ja kartongin valmistamiseksi
FI20030976L (fi) * 2003-06-30 2004-12-31 M Real Oyj Päällystetty pohjapaperi ja menetelmä päällystetyn pohjapaperin valmistamiseksi
FR2879225B1 (fr) * 2004-12-15 2007-02-16 Honnorat Rech S & Services Sar Papier brillant
FI122674B (fi) * 2005-06-23 2012-05-15 M Real Oyj Menetelmä kuituradan valmistamiseksi
GB2427868A (en) * 2005-07-04 2007-01-10 Samuel Michael Baker Cellulosic products having oleophobic and hydrophobic properties
EP2092118A1 (fr) 2006-12-11 2009-08-26 International Paper Company Composition d'encollage de papier, papier encollé et procédé d'encollage de papier
SI2805986T1 (en) 2009-03-30 2018-04-30 Fiberlean Technologies Limited Process for the production of nano-fibrillary cellulose gels
HUE026741T2 (en) 2009-03-30 2016-07-28 Omya Int Ag Process for the preparation of nano-fibrous cellulose suspensions
GB0908401D0 (en) 2009-05-15 2009-06-24 Imerys Minerals Ltd Paper filler composition
FI124142B (fi) 2009-10-09 2014-03-31 Upm Kymmene Corp Menetelmä kalsiumkarbonaatin ja ksylaanin saostamiseksi, menetelmällä valmistettu tuote ja sen käyttö
DK2386682T3 (da) 2010-04-27 2014-06-23 Omya Int Ag Fremgangsmåde til fremstilling af strukturerede materialer under anvendelse af nano-fibrillære cellulosegeler
EP2386683B1 (fr) 2010-04-27 2014-03-19 Omya International AG Procédé de fabrication de matériaux composites à base de gel
GB201019288D0 (en) 2010-11-15 2010-12-29 Imerys Minerals Ltd Compositions
EP2460935A1 (fr) 2010-12-01 2012-06-06 SAPPI Netherlands Services B.V. Procédé de production de dihydrate de sulfate de calcium à base de substrats de papier et/ou couleurs de revêtement
FI20125569L (fi) * 2012-05-28 2013-11-29 Nordkalk Oy Ab Saostettua karbonaattia sisältävän komposiittirakenteen valmistus ja käyttö
FI126571B (fi) * 2012-06-28 2017-02-28 Nordkalk Oy Ab Päällystyskoostumuksen käyttö maalina
EP3362508B1 (fr) 2015-10-14 2019-06-26 FiberLean Technologies Limited Matériau formable en feuille 3d
EP3400333B1 (fr) * 2016-01-05 2020-03-25 Stora Enso Oyj Procede pour la prouction d'une composite comprenant du mfc et une composite produi par le procede
RU2727605C1 (ru) 2016-04-05 2020-07-22 Фиберлин Текнолоджис Лимитед Бумажные и картонные продукты
US11846072B2 (en) 2016-04-05 2023-12-19 Fiberlean Technologies Limited Process of making paper and paperboard products
KR102137796B1 (ko) 2016-04-22 2020-07-24 파이버린 테크놀로지스 리미티드 미세섬유화 셀룰로스를 포함하는 섬유 및 그로부터 제조된 섬유 및 부직포 물질의 제조 방법

Family Cites Families (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
SE461860B (sv) * 1989-02-13 1990-04-02 Mo Och Domsjoe Ab Foerfarande foer framstaellning av papper och bestruket papper varvid baspappret innehaaller precipiterat kalciumkarbonat
US5731034A (en) * 1990-12-04 1998-03-24 Ecc International Limited Method of coating paper
US5223090A (en) * 1991-03-06 1993-06-29 The United States Of America As Represented By The Secretary Of Agriculture Method for fiber loading a chemical compound
FR2689530B1 (fr) * 1992-04-07 1996-12-13 Aussedat Rey Nouveau produit complexe a base de fibres et de charges, et procede de fabrication d'un tel nouveau produit.
DE4335194A1 (de) * 1993-10-15 1995-04-20 Basf Ag Wäßrige Pigmentanschlämmungen und ihre Verwendung bei der Herstellung von füllstoffhaltigem Papier
EP0772702A4 (fr) * 1995-05-18 1998-07-01 Huber Corp J M Procede de preparation de fibres de papier pigmentees et de produits fibreux
FI100729B (fi) * 1995-06-29 1998-02-13 Metsae Serla Oy Paperinvalmistuksessa käytettävä täyteaine ja menetelmä täyteaineen va lmistamiseksi
FI100670B (fi) * 1996-02-20 1998-01-30 Metsae Serla Oy Menetelmä täyteaineen lisäämiseksi selluloosakuituperäiseen massaan
FI108283B (fi) * 1997-01-13 2001-12-31 M Real Oyj Menetelmä paperin ja kartongin päällystämiseksi
US5952082A (en) * 1997-07-18 1999-09-14 Consolidated Papers, Inc. Electrophotographic recording medium and method
FI106140B (fi) * 1997-11-21 2000-11-30 Metsae Serla Oyj Paperinvalmistuksessa käytettävä täyteaine ja menetelmä sen valmistamiseksi
FI111401B (fi) * 2000-01-28 2003-07-15 M Real Oyj Menetelmä kalanteroidun paperiradan valmistamiseksi sekä kalanteroitu paperituote
FI117874B (fi) * 2000-01-28 2007-03-30 M Real Oyj Menetelmä paperiradan päällystämiseksi sekä päällystyskoostumus

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WO2002092909A1 (fr) 2002-11-21
AU2002247793B2 (en) 2008-05-01
FI20010846A0 (fi) 2001-04-24
CN100519936C (zh) 2009-07-29
NZ529161A (en) 2005-04-29
CN1520484A (zh) 2004-08-11
JP2004525281A (ja) 2004-08-19
CA2444085A1 (fr) 2002-11-21
US20040173329A1 (en) 2004-09-09
ATE550485T1 (de) 2012-04-15
FI20010846L (fi) 2002-10-25
FI117870B (fi) 2011-06-27
EP1392920A1 (fr) 2004-03-03
CA2444085C (fr) 2011-11-22

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