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
  • 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
• • 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
  • D21H17/20—Macromolecular organic compounds
  • D21H17/33—Synthetic macromolecular compounds
  • D21H17/34—Synthetic macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds
  • D21H17/37—Polymers of unsaturated acids or derivatives thereof, e.g. polyacrylates
• • 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
  • D21H17/70—Inorganic compounds forming new compounds in situ, e.g. within the pulp or paper, by chemical reaction with other substances added separately
• • 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
  • D21H21/00—Non-fibrous material added to the pulp, characterised by its function, form or properties; Paper-impregnating or coating material, characterised by its function, form or properties
  • D21H21/06—Paper forming aids
  • D21H21/08—Dispersing agents for fibres
• • 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
  • D21H23/00—Processes or apparatus for adding material to the pulp or to the paper
  • D21H23/02—Processes or apparatus for adding material to the pulp or to the paper characterised by the manner in which substances are added
  • D21H23/04—Addition to the pulp; After-treatment of added substances in the pulp

Definitions

• the present invention relates to a method of producing a fibrous web, comprising a filler, according to the preamble of Claim 1.
• a filler is added to a slush comprising vegetable fibres, after which the fibre slush forms a fibre web, which is dried at the paper or cardboard machine.
• the present invention also relates to use according to Claim 14.
• FI Patent Specification 100729 describes a filler which is used in paper-making and which comprises porous aggregates formed of calcium carbonate particles which have been precipitated onto the surface of the fines.
• characteristic of this new filler is that the calcium carbonate has been precipitated onto fines fibrils which are prepared by a process of refining from cellulose fibres and/or mechanical pulp fibre.
• the size distribution of the fines fraction is in most cases equivalent to the fraction PlOO of the wire screen.
• this filler is also called by its product name "SuperFill".
• the calcium carbonate percentage of the paper can be increased by using the filler, in which case the grammage of the paper can be decreased.
• the presented product gives a considerable advantage.
• Graphic papers mean types of paper that are used for instance for posters, book-covers, advertisements, maps, illustrated books, and as archival papers. In other words, they are used for purposes where the smoothness, the gloss and the quality of the colour are important properties.
• the purpose of the present invention is to eliminate the disadvantages associated with the known art and to generate a completely new way of producing paper and similar fibre products.
• the purpose of the present invention is to generate a method which can be used to produce fibre products possessing good mechanical and graphical properties.
• Another purpose of the present invention is to generate a solution for increasing the light-scattering coefficient of paper at low fresh filler percentages.
• the present invention is based on the idea that the uniformity of the filler distribution is increased by dosing dispersant into the composite filler, in which case the agglomeration of the calcium carbonate crystals is reduced and thus the light-scattering is increased.
• dispersants have earlier been used mainly to improve the pumpability of the filler slurries.
• the literature mentions that dispersant can be used to increase the uniformity of the filler distribution Weigl, J. and Ritter, E., "Dietician der Operachengrosse und -form von F ⁇ llerstoffen endeavor deren Vertechniken bei der SC- Textilhergna,itchblatt f ⁇ r Textilfabrikation, 1995, no 17, pages 739-747.
• EP Published Patent Application 0 892 019 describes how CaCC « 3 , or another white pigment which turns insoluble, is precipitated onto the fine fibres (fibrils). After that, a further pigment is added in order that the precipitated pigment will bind the second pigment and the fine fibre together, with the result that a composite pigment is generated, one which binds better to paper than does the expensive pigment (TiO 2 ) by itself.
• a composite filler is used as a filler in papers and cardboards in order to improve the light-scattering properties of the fibrous web.
• This filler is brought into contact with the dispersant before it is mixed with the fibre slush.
• the fibrous web for instance paper or cardboard
• the fibrous web is mainly characterized by what is stated in the characterization part of Claim 1.
• the present invention can considerably improve the light-scattering properties of paper and cardboard, without decreasing the retentive properties of the filler.
• Figure 1 shows a bar chart of the light-scattering coefficient of papers which comprise three different fillers.
• a fibrous web comprising filler is prepared at for instance a paper or cardboard machine using a method which is known per se. The production is described in more detail below.
• the filler in the fibrous web is a composite material, one which comprises cellulose or lignocellulose fibrils, onto which light-scattering material particles have been precipitated.
• the filler is brought into contact with the dispersant before it is mixed into the fibre slush. At least most of the dispersant is attached to the material particles of the filler.
• the amount of the dispersant varies depending on the dispersant and the material particles.
• the upper limit of the addition of the dispersant in practice it is possible to proceed as follows: a water dispersion of mineral particles (without fibril matrices) is formed, after which dispersant is added to the dispersion.
• the upper limit of the addition of the dispersant is the same amount as that which produces the minimum viscosity of the slurry.
• the graph of the viscosity as a function of the dispersant amount is U-shaped, in which case, in the present invention, the amount of dispersant to be added is chosen as an amount which corresponds to the bottom of the U.
• the dispersant used can be conventional anionic polymers, such as anionic polyacrylate - for example anionic sodium polyacrylate, or polyphosphate.
• Sodium polyacrylates are marketed under the product names Fennodispo A 40 and A 41 (supplier Kemira Oyj), in which A stands for acrylate and 40 and 41, respectively, indicate the percentage of its aqueous solution.
• Fennodispo A 40 and A 41 supplied Kemira Oyj
• A stands for acrylate and 40 and 41, respectively, indicate the percentage of its aqueous solution.
• Another corresponding product is Dispex N40, which is a sodium polyacrylate, too, and the supplier of which is Ciba Specialty Chemicals. Aminoalcohols can be used as well.
• the amounts to be added are approximately 0.05-1 weight % of the dry weight of the fibrous web.
• the suitable amount to be added is approximately 0.08-0.5 weight %, especially approximately 0.1-0.35 weight %, most suitably approximately 0.1-0.3 weight %. These limits relate especially to anionic polyacrylate, especially anionic sodium polyacrylate.
• the present invention is particularly suitable for fibrous webs which comprise small or average amounts of filler.
• the total percentage of the filler is at maximum approximately 25 weight %, especially at maximum approximately 20 weight %, preferably at maximum approximately 15 weight %, of the dry matter of the web.
• the minimum percentage is approximately 0.1 weight %.
• the amount of fresh feed of the filler comprising composite filler is most suitably approximately 0.1-15, preferably approximately 0.5-12 weight %, of the dry matter of the web to be prepared.
• the filler used in the present invention is derived especially from the fibrils obtained from the chemical pulp.
• chemical pulp means a pulp which has been treated with cooking chemicals in order to delignify the cellulose fibres.
• the fibrils have been obtained by refining a pulp which has been prepared using the sulphate process or another alkaline method.
• the present invention is suitable not only for modifying chemical pulps but also for modifying fibrils obtained from chemi- mechanical and mechanical pulps.
• the average thickness of the cellulose or lignocellulose fibrils is less than 5 ⁇ m, generally less than 1 ⁇ m.
• the initial material of the fibrils i.e. cellulose or other fibre-based fines
• the initial material of the fibrils is fibrillated by refining it using a pulp refiner.
• the desired fraction can be separated by using a screen, but it is not always necessary to grade the fines.
• the fractions P50-P400 are suitable fibril fractions.
• refiners having grooved blades are used.
• the light-scattering particles of the filler are inorganic or organic salts, which can be formed from their initial materials by precipitation in an aqueous intermediate agent.
• Such compounds are calcium carbonate, calcium oxalate, calcium sulphate, barium sulphate and mixtures of them.
• the material particles have been precipitated onto the fibres.
• the amount of the inorganic salt compound relative to the amount of the fibrils is approximately 0.0001-95 weight %, preferably approximately 0.1-90 weight %, most suitably approximately 60-80 weight %, calculated from the amount of filler and approximately 0.1-80 weight %, preferably approximately 0.5-50 weight % calculated from the paper.
• the filler is produced by precipitating the mineral pigment onto the surface of the fines fibrils which are prepared from cellulose fibre and/or mechanical pulp fibre.
• Precipitation of for instance calcium carbonate can be carried out in such a way that an aqueous solution of calcium hydroxide, which may comprise solid calcium hydroxide, and a compound which comprises carbonate ions and is at least partially dissolved in water, are fed into the water slush of fibrils. It is also possible to introduce carbon dioxide gas into the aqueous phase. In the presence of calcium hydroxide this carbon dioxide generates calcium carbonate. Beaded calcium carbonate crystal aggregates are formed, which are kept together by the fibrils, i.e.
• the fines filaments and in which the calcium carbonate particles are precipitated and are attached to the filaments of the fines.
• the fines filaments form beaded filaments, which mainly resemble pearl necklaces in a pile, hi the water (the slush), the ratio between the effective volume and the mass of the aggregates is very large compared with the corresponding ratio of calcium carbonate that is used as a conventional filler.
• effective volume here means the volume which the pigment requires.
• the diameter of the calcium carbonate particles in the aggregates is approximately 0.1 -5 ⁇ m, typically approximately 0.2-3 ⁇ m.
• the sizes of fibrils correspond especially to the fractions P50 (or PlOO) - P400 of the wire screen.
• at least 80 %, preferably even 90 %, of the precipitated light-scattering pigment particles are attached to the fibrils.
• the volumetric efficiency of the pigment particles is at least 60 weight % (of the filler weight), preferably 70 weight % or more, but less than 85 weight %. Within this range, a good dewatering at the paper or cardboard machine is achieved and a constant air permeance in the fibrous web, too.
• the composite filler is modified by means of a dispersant before it is fed to the paper machine or cardboard machine.
• the modification can be done simply by mixing a predetermined amount of dispersant with the filler in a mixing tank, wherein the dispersant is allowed to be adsorbed or otherwise be attached during mixing to at least the mineral particles of the filler.
• the mixing time is especially approximately 1 minute - 24 hours, most suitably approximately 5 minutes - 10 hours.
• the mixing is carried out especially at a relatively high dry matter percentage, which can even be increased due to addition of the dispersant. Typically, the dry matter percentage is approximately 40-80 weight %.
• continuous mixers can be used, too, in which the mixing of the filler slurry and the dispersant is carried out in pipelines, possibly aided by static mixers inside them.
• the bulk of the dispersant that is fed into the filler dispersion typically at least 80 weight %, preferably at least 90 weight %, is attached to the filler sufficiently well that it will not be essentially detached from it in the conditions of the headbox.
• any free dispersant remaining would easily become attached to, for instance, particle-like fillers which might be circulating in the short or the long circulation water coming from the paper or the cardboard machine to the headbox. If a conventional filler is dispersed, the retention of such a filler decreases significantly.
• any (part of the) dispersant that remains unattached is preferably circulated back to the elutriation phase of the composite filler in order to attach it as efficiently as possible to the very same filler.
• the dispersed composite filler is fed and mixed into the fibre slush, hi this case, the fibre raw material of the paper or cardboard pulp is first slushed to a suitable consistency in a way which is known per se (typically to a solids percentage of approximately 0.1-1 %).
• the above-mentioned filler generally approximately 1-25 weight % of the weight of the fibres of the fibre pulp, is added into the fibre slush most suitably in the headbox of the paper or cardboard machine, hi practice, at least when coated paper and cardboard qualities are being produced, the amount of pigments in the broke is so large that the amount of the fresh feed must be limited to less than 15 weight % of the dry weight of the fibres fed into the headbox.
• the percentage of the composite filler in the total amount of filler of the web is at least 20 weight %, preferably at least approximately 30 weight %, most suitably at least 40 weight % and especially 50 weight %. More preferably, 75-100 weight % of the filler is composite filler.
• the fibre pulp is webbed to form the paper or cardboard web. After that, the web is led from the press section to the drying section, where it is dried in a way which is known per se.
• the fibrous web is dried and may be coated and optionally after-treated, for instance by calendering.
• a multi-layer webbing technique can be used to produce such products.
• Suitable pulp feeding architectures have been described for instance in FI Patent Specification 105 118 and EP Published Patent Application 824 157.
• the multi-layer headbox is used most suitably together with a gap former.
• a slice jet formed by the headbox is fed in between two wires and the water is removed from the pulp through the wires in two different directions.
• a gap former it is possible to make the fines gather on the surfaces of the layer thereby producing an arc- shaped filler distribution - like the shape of a smile.
• a desired multilayer structure is generated simply by feeding the paper or cardboard pulp in layers in between the wires by the means described above.
• This technique can also be used to manufacture products in which the thicknesses of the layers are smaller than when a regular multilayer technique is used.
• the paper or cardboard product generated according to the present invention can be coated or it can be delivered uncoated.
• the coating can be carried out as either a single coating or as a double coating, thus the coating pastes can be used as single coating pastes and as pre-coating and surface coating pastes. Triple coatings are possible, too.
• the coating colour according to the present invention comprises 10-100 parts by weight of at least one pigment or a mixture of pigments, 0.1-30 parts by weight of at least one binder and 1-10 parts by weight of other additives known per se.
• pigments are 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 of them.
• 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 plastic 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, together with barium sulphate and zinc oxide, should be mentioned.
• 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 cardboard can be carried out with a conventional coating apparatus, i.e. by blade coating, or film coating or surface spraying (JET application).
• a coating layer is formed, the grammage of which is 5-30 g/m2.
• the uncoated side can be treated for instance with surface sizing.
• the products can be calendered off-line.
• the calendering can be carried out already at the paper machine (on-line).
• cellulose-bearing material means, in general, paper or cardboard or a corresponding cellulose-bearing material, which is sourced from lignocellulose-bearing raw-material, especially wood or annual or perennial plants.
• the material in question can be wood-containing or wood-free and it can be prepared from mechanical, chemi-mechanical or chemical pulp. The pulp and the mechanical pulp can be bleached or unbleached.
• the material can also comprise recycled fibres, especially recycled paper or recycled cardboard.
• the grammage of the web formed of the material may typically vary between 35 and 500 g/m2, especially between approximately 50 and 450 g/m 2 .
• the grammage of the base paper is 20-250 g/m 2 , preferably 30-80 g/m 2 .
• a base paper of this type which has a grammage of approximately 50-70 g/m 2 , with a 2-20 g coating/m 2 /side and by calendering the paper, a product is generated having a grammage of 50-110 g/m 2 , a brightness of at least 90 % and an opacity of at least 90 %.
• the following non-restrictive examples illustrate the present invention. The results of measurements of the paper properties in the examples are determined using the following standard methods:
• the dispersant dose (as a percentage of the pigments) is determined by measuring the viscosity of the PCC filler slurry as a function of the dose (Table 2). A suitable dose range was obtained from the minimum point of the viscosity. The levels used were 0.10, 0.15 and 0.20 parts of the calcium carbonate.
• the viscosity response does not necessarily show up in this kind of measurements. Therefore, measurements of the concentrated commercial PCC, which has the same crystal structure as SuperFill, were also carried out. It is probable that, using an appropriate accuracy, the best working dose is the same regardless of the composition of the slurry.
• the materials are mainly adsorbed onto the calcium carbonate, not onto the fines of the paper pulp.
• the dose selected was 0.2 parts (of calcium carbonate) of dispersant (Kemira's Fennodispo A40), which is added to the SuperFill filler.
• the filler level was approximately 11 %, and the ratio between the hardwood pulp and the softwood pulp is, as mentioned above, 70/30, and the beating degrees SR 22.2 (hardwood) and 25.3 (softwood).
• the dispersion of SuperFill substantially improves the light-scattering coefficient compared with the same SuperFill filler which is not dispersed.
• the effect of the dispersion is significant, especially at low or middle range percentages of filler.

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• Inorganic Chemistry (AREA)
• Paper (AREA)

Priority Applications (5)

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Country Status (9)

Cited By (5)

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Citations (7)

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• 2005
  • 2005-06-23 FI FI20050683A patent/FI122674B/sv not_active IP Right Cessation
• 2006
  • 2006-06-21 BR BRPI0612278-7A patent/BRPI0612278A2/pt not_active IP Right Cessation
  • 2006-06-21 RU RU2007145593/12A patent/RU2393285C2/ru not_active IP Right Cessation
  • 2006-06-21 CN CNA200680022555XA patent/CN101203644A/zh active Pending
  • 2006-06-21 US US11/922,595 patent/US20090114356A1/en not_active Abandoned
  • 2006-06-21 CA CA2611272A patent/CA2611272C/en not_active Expired - Fee Related
  • 2006-06-21 EP EP06764448A patent/EP1893807A4/en active Pending
  • 2006-06-21 JP JP2008517521A patent/JP5033125B2/ja not_active Expired - Fee Related
  • 2006-06-21 WO PCT/FI2006/000222 patent/WO2006136651A1/en active Application Filing

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