EP1080271B1 - Procede de production de papier - Google Patents

Procede de production de papier Download PDF

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Publication number
EP1080271B1
EP1080271B1 EP99927017A EP99927017A EP1080271B1 EP 1080271 B1 EP1080271 B1 EP 1080271B1 EP 99927017 A EP99927017 A EP 99927017A EP 99927017 A EP99927017 A EP 99927017A EP 1080271 B1 EP1080271 B1 EP 1080271B1
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EP
European Patent Office
Prior art keywords
process according
suspension
polysaccharide
anionic
wire
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EP99927017A
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German (de)
English (en)
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EP1080271A1 (fr
Inventor
Michael Persson
Hans Hällström
Joakim Carlen
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Akzo Nobel NV
Nouryon Pulp and Performance Chemicals AB
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Akzo Nobel NV
Eka Chemicals AB
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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
    • 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
    • D21H23/06—Controlling the addition
    • D21H23/08—Controlling the addition by measuring pulp properties, e.g. zeta potential, pH
    • 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
    • D21H21/10—Retention agents or drainage improvers
    • 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
    • D21H11/14—Secondary 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
    • D21H17/00—Non-fibrous material added to the pulp, characterised by its constitution; Paper-impregnating material characterised by its constitution
    • D21H17/01—Waste products, e.g. sludge
    • 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
    • D21H17/21—Macromolecular organic compounds of natural origin; Derivatives thereof
    • D21H17/24—Polysaccharides
    • 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
    • D21H17/21—Macromolecular organic compounds of natural origin; Derivatives thereof
    • D21H17/24—Polysaccharides
    • D21H17/28—Starch
    • 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
    • D21H17/21—Macromolecular organic compounds of natural origin; Derivatives thereof
    • D21H17/24—Polysaccharides
    • D21H17/31—Gums
    • D21H17/32—Guar or other polygalactomannan gum
    • 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
    • D21H17/375—Poly(meth)acrylamide
    • 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
    • D21H17/41—Synthetic macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds containing ionic groups
    • D21H17/44—Synthetic macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds containing ionic groups cationic
    • D21H17/45—Nitrogen-containing groups
    • D21H17/455—Nitrogen-containing groups comprising tertiary amine or being at least partially quaternised
    • 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
    • D21H17/68—Water-insoluble compounds, e.g. fillers, pigments siliceous, e.g. clays
    • 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
    • D21H23/06—Controlling the addition
    • D21H23/08—Controlling the addition by measuring pulp properties, e.g. zeta potential, pH
    • D21H23/10—Controlling the addition by measuring pulp properties, e.g. zeta potential, pH at least two kinds of compounds being added

Definitions

  • This invention relates to papermaking and more specifically to a process for the production of paper in which a cationic or amphoteric polysaccharide containing hydrophobic substitution is added to a papermaking stock.
  • the process provides improved drainage and retention as well as improved dry strength of the paper produced by the process.
  • an aqueous suspension containing cellulosic fibres, and optional fillers and additives referred to as stock
  • a headbox which ejects the stock onto a forming wire.
  • Water is drained from the stock through the forming wire so that a wet web of paper is formed on the wire, and the web is further dewatered and dried in the drying section of the paper machine.
  • white water which usually contains fine particles, e.g. fine fibres, fillers and additives, is usually recirculated in the papermaking process.
  • Drainage and retention aids are conventionally introduced into the stock in order to facilitate drainage and increase adsorption of fine particles onto the cellulosic fibres so that they are retained with the fibres on the wire.
  • Cationic and amphoteric polysaccharides like cationic starch and cationic guar gums are widely used as drainage and retention aids.
  • the polysaccharides can be used alone or in combination with other polymers and/or with anionic microparticulate materials such as, for example, anionic inorganic particles like colloidal silica.
  • Cationic and amphoteric polysaccharides are also widely used as dry strength agents which are introduced into the stock to produce paper with improved dry strength.
  • Cationic polysaccharides are usually prepared by the reaction of a polysaccharide with a quaternising agent, e.g. 3-chloro-2-hydroxypropyl trimethylammonium chloride, 2,3-epoxypropyl trimethyl ammonium chloride, and 2-chloroethyl trimethyl ammonium chloride.
  • a quaternising agent e.g. 3-chloro-2-hydroxypropyl trimethylammonium chloride, 2,3-epoxypropyl trimethyl ammonium chloride, and 2-chloroethyl trimethyl ammonium chloride.
  • U.S. -A- 4,388,150; 4,755,259; 4,840,705; 4,961,825; 5,127,994; 5,643,414; 5,447,604; 5,277,764; 5,607,552; 5,603,805; and 5,858,174; and EP-A-500,770 disclose the use of cationic and amphoteric polysaccharides and anionic inorganic particles as stock additives in papermaking. These additives are among the most efficient drainage and retention aids now in use.
  • a drainage and retention aid comprising a cationic and/or amphoteric polysaccharide containing a hydrophobic group substituent, i.e. a hydrophobe. It has also been found that the cationic and/or amphoteric polysaccharide containing a hydrophobic group provides improved dry strength of the paper.
  • the present invention relates to a process for the production of paper from a suspension containing cellulosic fibres, and optional fillers, which comprises adding to the suspension a drainage and retention aid comprising a cationic or amphoteric polysaccharide, forming and dewatering the suspension on a wire, wherein the polysaccharide has a hydrophobic group which comprises an aromatic group and the suspension that is dewatered on the wire has a conductivity of at least 0.75 mS/cm.
  • the invention further relates to a process for the production of paper from a suspension containing cellulosic fibres, and optional fillers, comprising adding to the suspension a drainage and retention aid comprising a cationic or amphoteric polysaccharide and a component selected from anionic microparticulate materials, water-soluble anionic vinyl addition polymers and combinations thereof, forming and dewatering the suspension on a wire, wherein the polysaccharide has a hydrophobic group comprising an aromatic group or the polysaccharide has the general structural formula (I): wherein P is a residue of a polysaccharide; A is a group attaching N to the polysaccharide residue; R 1 and R 2 are each H or alkyl having from 1 to 3 carbon atoms; R 3 is a hydrophobic hydrocarbon group containing at least 2 carbon atoms; n is an integer from 2 to 300,000, or, alternatively, R 1 , R 2 and R 3 together with N form an aromatic group containing from 5 to 12 carbon
  • the process further comprises forming and dewatering the suspension on a wire to obtain a wet web containing cellulosic fibres, or paper, and white water, recirculating the white water and optionally introducing fresh water to form a suspension containing cellulosic fibres, and optional fillers, to be dewatered to form paper, wherein the amount of fresh water introduced is less than 30 tons per ton of dry paper produced.
  • the process of this invention results in improved drainage and/or retention and hereby the present process makes it possible to increase the speed of the paper machine and to use lower a dosage of additive to give a corresponding drainage and retention effect, thereby leading to an improved papermaking process and economic benefits.
  • Further benefits observed with the present invention include improved dry strength of the paper produced using the polysaccharide having a hydrophobic group.
  • the process of this invention is suitably used for the treatment of cellulosic suspensions in closed mills wherein the white water is repeatedly recycled with the introduction of only low amounts of fresh water.
  • the process is further suitably applied to papermaking processes using cellulosic suspensions having high salt contents, and thus having high conductivity levels, for example processes with extensive white water recycling and limited fresh water supply and/or processes using fresh water having high salt contents.
  • the polysaccharide according to this invention can be selected from any polysaccharide known in the art including, for example, starches, guar gums, celluloses, chitins, chitosans, glycans, galactans, glucans, xanthan gums, pectins, mannans, dextrins, preferably starches and guar gums.
  • suitable starches include potato, com, wheat, tapioca, rice, waxy maize, etc.
  • the cationic polysaccharide is water-dispersable or, preferably, water-soluble.
  • the polysaccharide is capable of functioning as a drainage and retention aid (agent).
  • drainage and retention aid refers to one or more components (aids, agents, or additives) which, when being added to a stock, give better drainage and/or retention than is obtained when not adding the said one or more components.
  • the polysaccharide is capable of functioning as a dry strength agent.
  • dry strength agent refers to at least one component (aid, agent or additive) which, when being added to a stock, give better dry strength of the paper produced than is obtained when not adding the said component.
  • the polysaccharide is a hydrophobe substituted, cationic or amphoteric polysaccharide, i.e. a polysaccharide having one or more hydrophobic groups and one or more cationic groups, the cationic groups suitably being tertiary amino groups or, preferably, quaternary ammonium groups.
  • the polysaccharide may also contain one or more anionic groups which can be, for example, phosphate, phosphonate, sulphate, sulphonate or carboxylic acid groups and they are preferably phosphate groups. If present, the anionic groups can be native or introduced by means of chemical treatment in conventional manner; native potato starch contains a substantial amount of covalently bound phosphate monoester groups.
  • cationic groups are preferably present in a predominant amount.
  • the hydrophobic group of the polysaccharide can be attached to a heteroatom like oxygen present in the polysaccharide.
  • the hydrophobic group is attached to a heteroatom, e.g. nitrogen or oxygen, the heteroatom optionally being charged, for example when it is a nitrogen, or a group comprising such a heteroatom, e.g., amide, ester or ether, which, in turn, can be attached to the polysaccharide backbone (main chain), for example via a chain of atoms.
  • the hydrophobic group has at least 2, usually at least 3, suitably at least 4 and preferably at least 6 carbon atoms; and usually up to about 20, suitably up to 14 and preferably up to 12 carbon atoms.
  • the hydrophobic group can be selected from aromatic (aryl) groups, aliphatic hydrocarbon groups, and mixtures of such groups.
  • suitable hydrophobic aliphatic groups include linear, branched and cyclic alkyl groups like ethyl; propyl, e.g. n-propyl and iso-propyl; butyl, e.g. n-butyl, isobutyl and t-butyl; pentyl, e.g. n-pentyl, neo-penyl and iso-pentyl; hexyl, e.g. n-hexyl and cyclohexyl; octyl, e.g.
  • n-octyl decyl, e.g. n-decyl; and dodecyl, e.g. n-dodecyl; and tetradecyl.
  • suitable aromatic groups and groups comprising an aromatic group include aryl and aralkyl groups, e.g. phenyl, phenylene, naphthyl, phenylene, xylylene, benzyl and phenylethyl; nitrogen-containing aromatic (aryl) groups, e.g. pyridinium and quinolinium, as well as derivatives of these groups where one or more substituents attached to said aromatic groups can be selected from hydroxyl, halides, e.g. chloride, nitro, and hydrocarbon groups having from 1 to 4 carbon atoms.
  • Particularly suitable polysaccharides according to the invention include those comprising the general structural formula (I): wherein P is a residue of a polysaccharide; A is a group attaching N to the polysaccharide residue, suitably a chain of atoms comprising C and H atoms, and optionally O and/or N atoms, usually an alkylene group with from 2 to 18 and suitably 2 to 8 carbon atoms. optionally interrupted or substituted by one or more heteroatoms, e.g. O or N, e.g.
  • R 1 and R 2 are each H or, preferably, a hydrocarbon group, suitably alkyl, having from 1 to 3 carbon atoms, suitably 1 or 2 carbon atoms;
  • R 3 is a hydrophobic hydrocarbon group containing at least 2 carbon atoms, suitably 4 to 14 and preferably 6 to 12 carbon atoms, the hydrophobic group suitably being as defined above, preferably a group selected from alkyl and aralkyl groups, e.g.
  • n is an integer from about 2 to about 300,000, suitably from 5 to 200,000 and preferably from 6 to 125,000 or, alternatively, R 1 , R 2 and R 3 together with N form a aromatic group containing from 5 to 12 carbon atoms; and
  • X - is an anionic counterion, usually a halide like chloride.
  • the hydrophobic group modified cationic or amphoteric polysaccharide can have a degree of substitution varying over a wide range; the degree of cationic substitution (DS C ) can be from 0,01 to 0,5, suitably from 0,02 to 0,3, preferably from 0,025 to 0,2, the degree of hydrophobic substitution (DS H ) can be from from 0,01 to 0,5, suitably from 0,02 to 0,3. preferably from 0,025 to 0,2, and the degree of anionic substitution (DS A ) can be from 0 to 0,2, suitably from 0 to 0,1, preferably from 0 to 0,05.
  • the polysaccharides according to the invention can be prepared by subjecting a polysaccharide to cationic and hydrophobic modification in known manner using one or more agents containing a cationic group and/or a hydrophobic group, for example by reacting the agent with the polysaccharide in the presence of an alkaline substance such as an alkali metal or alkaline earth metal hydroxide.
  • the polysaccharide to be subjected to cationic and hydrophobic modification can be non-ionic, anionic, amphoteric or cationic.
  • Suitable modifying agents include non-ionic agents such as, for example, hydrophobe substituted succinic anhydrides; alkylene oxides, e.g.
  • alkyl halides e.g. decyl bromide and docecyl bromide
  • aralkyl halides e.g. benzyl chloride and benzyl bromide
  • the reaction products of epichlorohydrin and dialkylamines having at least one substituent comprising a hydrophobic group as defined above, including 3-dialkylamino-1,2-epoxypropanes
  • cationic agents such as, for example, the reaction product of epichlorohydrin and tertiary amines having at least one substituent comprising a hydrophobic group as defined above, including trialkylamines, alkaryldialkylamines, e.g.
  • Suitable cationic agents of this type include 2,3-epoxypropyl trialkylammonium halides and halohydroxypropyl trialkylammonium halides, e.g.
  • N-(3-chloro-2-hydroxypropyl)-N-(alkaryl)-N,N-di(lower alkyl)ammonium chloride where the alkaryl and lower alkyl groups are as defined above, particularly N-(3-chloro-2-hydroxypropyl)-N-benzyl-N,N-dimethylammonium chloride; and N-(3-chloro-2-hydroxypropyl) pyridinium chloride.
  • the polysaccharide is suitably rendered cationic by using any of the cationic agents known in the art before or after the hydrophobic modification.
  • Suitable cationic and/or hydrophobic modifying agents, hydrophobic group modified polysaccharides and methods for their preparation include those described in U.S. -A- 4,687,519 and 5,463,127; WO -A- 94/24169, EP-A- 189 935; and S.P. Patel, R.G. Patel and V.S. Patel, Starch/Stärke, 41(1989), No. 5, pp. 192-196.
  • the polysaccharide according to the invention is used in conjunction with at least one additional stock additive, in particular for further improving drainage and/or retention, thereby forming a drainage and retention aid comprising two or more components, usually referred to as drainage and retention aids.
  • the term "drainage and retention aids", as used herein, refers to two or more components (aids, agents or additives) which, when being added to a stock, give better drainage and/or retention than is obtained when not adding the components.
  • suitable stock additives of this type include anionic microparticulate materials, e.g. anionic organic particles and anionic inorganic particles, water-soluble anionic vinyl addition polymers, low molecular weight cationic organic polymers, aluminium compounds, and combinations thereof.
  • the polysaccharide is used in conjunction with an anionic microparticulate material, notably with anionic inorganic particles.
  • the polysaccharide is used in conjunction with anionic inorganic particles and a low molecular weight cationic organic polymer.
  • the polysaccharide is used in conjunction with anionic inorganic particles and an aluminium compound.
  • the anionic microparticulate material according to the invention can be selected from inorganic and organic particles.
  • Anionic inorganic particles that can be used according to the invention include anionic silica-based particles and clays of the smectite type. It is preferred that the anionic inorganic particles are in the colloidal range of particle size.
  • Anionic silica-based particles i.e. particles based on SiO 2 or silicic acid, are preferably used and such particles are usually supplied in the form of aqueous colloidal dispersions, so-called sols.
  • suitable silica-based particles include colloidal silica and different types of polysilicic acid.
  • the silica-based sols can also be modified and contain other elements, e.g.
  • silica-based particles of this type include colloidal aluminium-modified silica and aluminium silicates. Mixtures of such suitable silica-based particles can also be used. Drainage and retention aids comprising suitable anionic silica-based particles are disclosed in U.S.
  • Anionic silica-based particles suitably have an average particle size below about 50 nm, preferably below about 20 nm and more preferably in the range of from about 1 to about 10 nm.
  • the particle size refers to the average size of the primary particles, which may be aggregated or non-aggregated.
  • the specific surface area of the silica-based particles is suitably above 50 m 2 /g and preferably above 100 m 2 /g. Generally, the specific surface area can be up to about 1700 m 2 /g and preferably up to 1000 m 2 /g.
  • the specific surface area can be measured by means of titration with NaOH in known manner, e.g. as described by Sears in Analytical Chemistry 28(1956):12, 1981-1983 and in U.S. -A- 5,176,891. The given area thus represents the average specific surface area of the particles.
  • the anionic inorganic particles are silica-based particles having a specific surface area within the range of from 50 to 1000 m 2 /g, preferably from 100 to 950 m 2 /g.
  • Sols of silica-based particles these types also encompass modified sols like aluminium-containing silica-based sols and boron-containing silica-based sols.
  • the silica-based particles are present in a sol having an S-value in the range of from 8 to 45%, preferably from 10 to 30%, containing silica-based particles with a specific surface area in the range of from 300 to 1000 m 2 /g, suitably from 500 to 950 m 2 /g, and preferably from 750 to 950 m 2 /g, which sols can be modified with aluminium and/or boron as mentioned above.
  • the particles can be surface-modified with aluminium to a degree of from 2 to 25% substitution of silicon atoms.
  • the S-value can be measured and calculated as described by Iler & Dalton in J. Phys. Chem. 60(1956), 955-957. The S-value indicates the degree of aggregate or microgel formation and a lower S-value is indicative of a higher degree of aggregation.
  • the silica-based particles are selected from polysilicic acid and modified polysilicic acid having a high specific surface area, suitably above about 1000 m 2 /g.
  • the specific surface area can be within the range of from 1000 to 1700 m 2 /g and preferably from 1050 to 1600 m 2 /g.
  • the sols of modified polysilicic acid can contain other elements, e.g. aluminium and/or boron, which can be present in the aqueous phase and/or in the silica-based particles.
  • polysilicic acid is also referred to as polymeric silicic acid, polysilicic acid microgel, polysilicate and polysilicate microgel, which are all encompassed by the term polysilicic acid used herein.
  • Aluminium-containing compounds of this type are commonly also referred to as polyaluminosilicate and polyaluminosilicate microgel, which are both encompassed by the terms colloidal aluminium-modified silica and aluminium silicate used herein.
  • Clays of the smectite type that can be used in the process of the invention are known in the art and include naturally occurring, synthetic and chemically treated materials.
  • suitable smectite clays include montmorillonite/bentonite, hectorite, beidelite, nontronite and saponite, preferably bentonite and especially such bentonite which after swelling preferably has a surface area of from 400 to 800 m 2 /g.
  • Suitable clays are disclosed in U.S. -A- 4,753,710; 5,071,512; and 5,607,552.
  • Anionic organic particles that can be used according to the invention include highly cross-linked anionic vinyl addition polymers, suitably copolymers comprising an anionic monomer like acrylic acid, methacrylic acid and sulfonated or phosphonated vinyl addition monomers, usually copolymerized with nonionic monomers like (meth)acrylamide, alkyl (meth)acrylates, etc.
  • Useful anionic organic particles also include anionic condensation polymers, e.g. melamine-sulfonic acid sols.
  • LMW cationic organic polymers that can be used according to the invention include those commonly referred to and used as anionic trash catchers (ATC).
  • ATC's are known in the art as neutralizing and/or fixing agents for detrimental anionic substances present in the stock and the use thereof in combination with drainage and retention aids often provide further improved drainage and/or retention.
  • the LMW cationic organic polymer can be derived from natural or synthetic sources, and preferably it is an LMW synthetic polymer.
  • Suitable organic polymers of this type include LMW highly charged cationic organic polymers such as polyamines, polyamidoamines, polyethyleneimines, homo- and copolymers based on diallyldimethyl ammonium chloride, (meth)acrylamides and (meth)acrylates.
  • the molecular weight of the LMW cationic organic polymer is suitably at least 2,000 and preferably at least 10,000.
  • the upper limit of the molecular weight is usually about 700,000, suitably about 500,000 and preferably about 200,000.
  • Aluminium compounds that can be used according to this invention include alum, aluminates, aluminium chloride, aluminium nitrate and polyaluminium compounds, such as polyaluminium chlorides, polyaluminium sulphates, polyaluminium compounds containing both chloride and sulphate ions, polyaluminium silicate-sulphates, and mixtures thereof.
  • the polyaluminium compounds may also contain other anions than chloride ions, for example anions from sulfuric acid, phosphoric acid, organic acids such as citric acid and oxalic acid.
  • the components of drainage and retention aids according to the invention can be added to the stock in conventional manner and in any order.
  • an anionic microparticulate material it is preferred to add the hydrophobe substituted, cationic or amphoteric polysaccharide to the stock before adding the microparticulate material, even if the opposite order of addition may be used. It is further preferred to add the polysaccharide before a shear stage, which can be selected from pumping, mixing, cleaning, etc., and to add the anionic particles after that shear stage.
  • an LMW cationic organic polymer and/or an aluminium compound such components are preferably introduced into the stock prior to introducing the polysaccharide and anionic microparticulate material, if used.
  • the LMW cationic organic polymer and polysaccharide can be introduced into the stock essentially simultaneously, either separately or in admixture, e.g. as disclosed in U.S. -A- 5,858,174.
  • the dry strength agent and drainage and retention aid(s) according to the invention are added into the stock to be dewatered in amounts which can vary within wide limits depending on, inter alia, type and number of components, type of furnish, filler content, type of filler, point of addition, salt content, etc.
  • the component(s) are added in an amount that give better paper dry strength and/or drainage and/or retention than is obtained when not adding the component(s).
  • the hydrophobe substituted, cationic or amphoteric polysaccharide is usually added in an amount of at least 0,01%, often at least 0,1% by weight, based on dry stock substance, and the upper limit is usually 10% and suitably 2% by weight.
  • an anionic microparticulate material When using an anionic microparticulate material, it is usually added in an amount of at least 0.001% by weight, often at least 0.005% by weight, based on dry substance of the stock, and the upper limit is usually 1.0% and suitably 0.6% by weight.
  • the total amount added is suitably within the range of from 0.005 to 0.5% by weight, calculated as SiO 2 and based on dry stock substance, preferably within the range of from 0.01 to 0.2% by weight.
  • an LMW cationic organic polymer in the process it can be added in an amount of at least 0.05%, based on dry substance of the stock to be dewatered.
  • the amount is in the range of from 0.07 to 0.5%, preferably in the range from 0.1 to 0.35%.
  • the total amount introduced into the stock to be dewatered is dependent on the type of aluminium compound used and on other effects desired from it. It is for instance well known in the art to utilise aluminium compounds as precipitants for rosin-based sizing agents.
  • the total amount added is usually at least 0.05%, calculated as Al 2 O 3 and based on dry stock substance.
  • the amount is in the range of from 0.5 to 3.0%, preferably in the range from 0.1 to 2.0%.
  • the process of the invention is preferably used in the manufacture of paper from a suspension containing cellulosic fibers, and optional fillers, having a high conductivity.
  • the conductivity of the stock that is dewatered on the wire is at least 0.75 mS/cm. suitably at least 2.0 mS/cm, preferably at least 3.5 mS/cm. Very good drainage and retention results have been observed at conductivity levels above 5.0 mS/cm and even above 7.5 mS/cm. Conductivity can be measured by standard equipment such as, for example a WTW LF 539 instrument supplied by Christian Berner.
  • High conductivity levels mean high contents of salts (electrolytes), where the various salts can be based on mono-, di- and multivalent cations like alkali metals, e.g. Na + and K + . alkaline earths, e.g. Ca 2+ and Mg 2+ , aluminium ions, e.g.
  • the invention is particularly useful in the manufacture of paper from stocks having high contents of salts of di- and multivalent cations, and usually the cation content is at least 200 ppm, suitably at least 300 ppm and preferably at least 400 ppm.
  • the salts can be derived from the cellulosic fibres and fillers used to form the stock, in particular in integrated mills where a concentrated aqueous fibre suspension from the pulp mill normally is mixed with water to form a dilute suspension suitable for paper manufacture in the paper mill.
  • the salt may also be derived from various additives introduced into the stock, from the fresh water supplied to the process, or be added deliberately, etc. Further, the content of salts is usually higher in processes where white water is extensively recirculated, which may lead to considerable accumulation of salts in the water circulating in the process.
  • the present invention further encompasses papermaking processes where white water is extensively recirculated (recycled), i.e. with a high degree of white water closure, for example where from 0 to 30 tons of fresh water are used per ton of dry paper produced, usually less than 20, suitably less than 15, preferably less than 10 and notably less than 5 tons of fresh water per ton of paper.
  • Recirculation of white water obtained in the process suitably comprises mixing the white water with cellulosic fibres and/or optional fillers to form a suspension to be dewatered; preferably it comprises mixing the white water with a suspension containing cellulosic fibres, and optional fillers, before the suspension enters the forming wire for dewatering.
  • the white water can be mixed with the suspension before, between simultaneous with or after introducing the drainage and retention aids, if used: and before, simultaneous with or after introducing the polysaccharide.
  • Fresh water can be introduced in the process at any stage; for example, it can be mixed with cellulosic fibres in order to form a suspension, and it can be mixed with a suspension containing cellulosic fibres to dilute it so as to form the suspension to be dewatered, before or after mixing the stock with white water and before, between, simultaneous with or after introducing the components of drainage and retention aids, if used; and before, simultaneous with or after introducing the polysaccharide.
  • additives which are conventional in papermaking can of course be used in combination with the additives according to the invention, such as, for example, additional dry strength agents, wet strength agents, sizing agents, e.g. those based on rosin, ketene dimers and acid anhydrides, optical brightening agents, dyes, etc.
  • the cellulosic suspension, or stock can also contain mineral fillers of conventional types such as, for example, kaolin, china clay, titanium dioxide, gypsum, talc and natural and synthetic calcium carbonates such as chalk, ground marble and precipitated calcium carbonate.
  • the process of this invention is used for the production of paper.
  • paper as used herein, of course include not only paper and the production thereof, but also other sheet or web-like products, such as for example board and paperboard, and the production thereof.
  • the process can be used in the production of paper from different types of suspensions of cellulose-containing fibres and the suspensions should suitably contain at least 25% by weight and preferably at least 50% by weight of such fibres, based on dry substance.
  • the suspensions can be based on fibres from chemical pulp such as sulphate.
  • sulphite and organosolv pulps mechanical pulp such as thermomechanical pulp, chemothermomechanical pulp, refiner pulp and groundwood pulp, from both hardwood and softwood, and can also be based on recycled fibres, optionally from de-inked pulps, and mixtures thereof.
  • the invention is particularly useful in the manufacture of paper from suspensions based on pulps comprising recycled fibres and de-inked pulp, and the content of cellulosic fibres of such origin can be up to 100%, suitably from 20 to 100%.
  • Cationised polysaccharides were prepared by reacting native potato starch with a quaternising agent according to the general procedure described in EP-A- 189 935.
  • the quaternising agents are commercially available from for example Degussa, or were prepared according to the general procedure described in U.S. -A- 5,463,127.
  • the starches were dissolved in water and used as 0.5% aqueous solutions.
  • Polysaccharides according to the invention, P1 to P3, and polysaccharides intended for comparison purposes, Ref. 1 and Ref. 2, were prepared from the following starting materials:
  • Drainage performance was evaluated by means of a Dynamic Drainage Analyser (DDA), available from Akribi, Sweden, which measures the time for draining a set volume of stock through a wire when removing a plug and applying vacuum to that side of the wire opposite to the side on which the stock is present.
  • DDA Dynamic Drainage Analyser
  • First pass retention was evaluated by means of a nephelometer by measuring the turbidity of the filtrate, the white water, obtained by draining the stock.
  • the furnish used was based on 56% by weight of peroxide bleached TMP/SGW pulp (80/20), 14% by weight of bleached birch/pine sulphate pulp (60/40) refined to 200° CSF and 30% by weight of china clay.
  • To the stock was added 40 g/l of a colloidal fraction, bleach water from an SC mill, filtrated through a 5 ⁇ m screen and concentrated with an UF filter, cut off 200,000.
  • Stock volume was 800 ml and pH about 7. Calcium chloride was added to the stock to adjust the conductivity to 5.0 mS/cm (Test Nos. 1-3), and 7.5 mS/cm (Test Nos. 4-6).
  • the stock was stirred in a baffled jar at a speed of 1500 rpm throughout the test and chemicals additions were conducted as follows: i) adding polysaccharide to the stock following by stirring for 30 seconds, ii) adding anionic inorganic particles to the stock followed by stirring for 15 seconds, iii) draining the stock while automatically recording the drainage time.
  • the polysaccharides used in the test series were P1 and Ref. 1 according to Example 1.
  • the anionic inorganic particles used were silica-based particles of the type disclosed in U.S. -A- 5,368,833.
  • the sol had an S-value of about 25% and contained silica particles with a specific surface area of about 900 m 2 /g which were surface-modified with aluminium to a degree of 5%.
  • Table 1 shows the dewatering and retention effect at various dosages of cationized starch, calculated as dry starch on dry stock system, and silica-based particles, calculated as SiO 2 and based on dry stock system.
  • Test No. Starch Dosage [kg/t] SiO 2 Dosage [kg/t] Dewatering time [sec] Turbidity [NTU] P1 Ref. 1 P1 Ref. 1 1 7.5 3 17.0 20.6 51 61 2 10 3 16.0 20.0 54 54 3 15 3 15.0 21.0 48 52 4 7.5 1.5 18.1 22.3 53 64 5 10 1.5 16.6 22.1 55 60 6 15 1.5 15.5 24.0 50 58
  • the furnish was the same as used in Example 2.
  • Stock volume was 800 ml and pH about 7.
  • Calcium chloride was added to the stock to adjust the conductivity to 1.5 mS/cm (Test Nos. 1-3); 3.5 mS/cm (Test Nos. 4-5); and 5.0 mS/cm (Test Nos. 6-7).
  • the polysaccharides used for in the test series were P2 and Ref. 2 according to Example 1.
  • the anionic inorganic particles according to Example 2 were similarly used in this test series.
  • Table 2 shows the dewatering effect at various dosages of drainage and retention aids, calculated as dry starch and SiO 2 on dry stock system.
  • Test No. Starch Dosage [kg/t] SiO 2 Dosage [kg/t] Dewatering time [s] P2 Ref. 2 1 0 0 22.5 22.5 2 5 3 16.3 18.0 3 10 3 10.3 10.7 4 5 3 11.6 13.4 5 10 3 9.9 10.4 6 5 3 13.1 17.9 7 10 3 10.8 15.0
  • the dewatering effect was evaluated according to the procedure described in Example 2 except that the drainage and retention aids also comprised a low molecular weight cationic polyamine; ATC.
  • the polyamine was added to the stock followed by stirring for 30 seconds before addition of cationized polysaccharide and then anionic inorganic particles.
  • the furnish used was based on 70% deinked pulp, 15% by weight of peroxide bleached TMP/SGW pulp (80/20), and 15% by weight of bleached birch/pine sulphate pulp (60/40) refined to 200° CSF.
  • Stock volume was 800 ml and pH about 7.
  • Calcium chloride was added to the stock to adjust the conductivity to 1.0 mS/cm (Test No. 1), 2.0 mS/cm (Test No. 2), 4.0 mS/cm (Test Nos. 3-4) and 7.5 mS/cm (Test No 5).
  • the polysaccharides used for in the test series were P1, P2, Ref. 1 and Ref. 2 according to Example 1.
  • the anionic inorganic particles according to Example 2 were similarly used.
  • Table 3 shows the dewatering effect at various dosages of drainage and retention aids. calculated as dry polyamine, starch and SiO 2 on dry stock system.
  • Test No. ATC Dosage [kg/t] Starch Dosage [kg/t] SiO 2 Dosage [kg/t] Dewatering time [s] P1 P3 Ref. 1 Ref. 2 1 3 2.5 3 12.1 - 13.2 - 2 3 2.5 3 12.3 12.9 13 - 3 3 2.5 3 13.3 13.9 14.5 - 4 3 5 3 11.6 12.8 13 - 5 3 7.5 3 - 13.8 - 16
  • Dry strength performance was evaluated with a Dynamic Sheet Former (Formette Dynamique), supplied by Fibertech AB, Sweden, and a Tensile Strength Tester supplied by Lorentzen & Wettre, Sweden. Dewatering effect was evaluated according to the procedure described in Example 4.
  • Dynamic Sheet Former Formette Dynamique
  • Tensile Strength Tester supplied by Lorentzen & Wettre, Sweden. Dewatering effect was evaluated according to the procedure described in Example 4.
  • Example 2 The furnish according to Example 2 was used. Stock consistency was 0.3%. Conductivity of the stock was adjusted by addition of calcium chloride. Additives and order of addition according to Example 4 were used in this test series.
  • the polyamine was added in an amount of 3 kg/ton, calculated as dry polyamine on dry stock system.
  • the silica-based particles were added in an amount of 3 kg/ton, calculated as SiO 2 and based on dry stock system.
  • Paper sheets were formed in the Dynamic Sheet Former by adding the chemicals to the stock in the mixing chest, pumping the stock through a traversing nozzle into the rotating drum onto the water film on top of the wire, draining the stock to form a sheet, pressing and drying the sheet.
  • the sheets were cut into strips that were evaluated in the Tensile Strength Tester. The square mean value of the tensile strength index of the machine and cross direction of the paper sheets was calculated and compared.
  • Table 4 shows the dewatering time and tensile strength of the sheets obtained at various starch dosages, calculated as dry starch on dry stock system.

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Claims (20)

  1. Procédé de production de papier à partir d'une suspension contenant des fibres cellulosiques et d'éventuelles charges, lequel procédé comporte le fait d'ajouter à cette suspension un auxiliaire de drainage et de rétention comprenant un polysaccharide cationique ou amphotère, et le fait de mettre cette suspension en forme et de l'épaissir sur une toile, caractérisé en ce que ledit polysaccharide possède un groupe hydrophobe comportant un groupe aromatique et en ce que la suspension qui est épaissie sur la toile présente une conductivité d'au moins 0,75 mS/cm.
  2. Procédé de production de papier à partir d'une suspension contenant des fibres cellulosiques et d'éventuelles charges, lequel procédé comporte le fait d'ajouter à cette suspension un auxiliaire de drainage et de rétention comprenant un polysaccharide cationique ou amphotère et un composant choisi parmi des matériaux anioniques en microparticules, des polymères d'addition vinyliques anioniques et hydrosolubles et des combinaisons de tels matériaux, et le fait de mettre cette suspension en forme et de l'épaissir sur une toile, caractérisé en ce que ledit polysaccharide possède un groupe hydrophobe comportant un groupe aromatique ou possède la formule structurale générale (I) :
    Figure 00230001
    dans laquelle P représente un résidu de polysaccharide, A représente un groupe reliant l'atome d'azote au résidu de polysaccharide, R1 et R2 représentent chacun un atome d'hydrogène ou un groupe alkyle comportant 1 à 3 atomes de carbone, R3 représente un groupe hydrocarboné hydrophobe comportant au moins 2 atomes de carbone, n représente un nombre entier valant de 2 à 300 000, ou bien R1, R2 et R3 représentent, conjointement avec l'atome d'azote, un groupe aromatique comportant 5 à 12 atomes de carbone, et X- représente un contre-ion anionique, et en ce que la suspension qui est épaissie sur la toile présente une conductivité d'au moins 0,75 mS/cm.
  3. Procédé conforme à la revendication 2, caractérisé en ce que le groupe hydrophobe comporte un groupe aromatique.
  4. Procédé conforme à la revendication 1, 2 ou 3, caractérisé en ce que le groupe hydrophobe est un groupe benzyle.
  5. Procédé conforme à la revendication 2, caractérisé en ce que le groupe hydrophobe comporte un groupe alkyle.
  6. Procédé conforme à la revendication 5, caractérisé en ce que le groupe hydrophobe est un groupe butyle, pentyle, hexyle, octyle ou décyle.
  7. Procédé conforme à l'une des revendications précédentes, caractérisé en ce que le groupe hydrophobe comporte 4 à 14 atomes de carbone.
  8. Procédé conforme à l'une des revendications précédentes, caractérisé en ce que le groupe hydrophobe comporte 6 à 12 atomes de carbone.
  9. Procédé conforme à l'une des revendications précédentes, caractérisé en ce que le polysaccharide est choisi parmi les amidons et les gommes de guar.
  10. Procédé conforme à l'une des revendications précédentes, caractérisé en ce que le polysaccharide comporte un ou plusieurs groupes anioniques.
  11. Procédé conforme à l'une des revendications précédentes, caractérisé en ce que le polysaccharide est ajouté en une quantité qui représente au moins 0,1 % du poids de matières sèches de la pâte.
  12. Procédé conforme à l'une des revendications précédentes, caractérisé en ce que l'auxiliaire de drainage et de rétention comprend un matériau anionique en microparticules.
  13. Procédé conforme à la revendication 12, caractérisé en ce que le matériau anionique en microparticules est choisi parmi de la bentonite et des particules à base de silice.
  14. Procédé conforme à la revendication 12 ou 13, caractérisé en ce que le matériau anionique en microparticules est choisi parmi des particules à base de silice dont l'aire spécifique vaut plus de 50 m2/g.
  15. Procédé conforme à l'une des revendications précédentes, caractérisé en ce que l'auxiliaire de drainage et de rétention comprend en outre un polymère organique cationique à faible masse moléculaire.
  16. Procédé conforme à l'une des revendications précédentes, caractérisé en ce que la suspension contient des fibres cellulosiques recyclées.
  17. Procédé conforme à l'une des revendications précédentes, caractérisé en ce que la suspension contient de la pâte désencrée.
  18. Procédé conforme à l'une des revendications précédentes, caractérisé en ce que la suspension qui est épaissie sur la toile présente une conductivité d'au moins 2,0 mS/cm.
  19. Procédé conforme à la revendication 18, caractérisé en ce que la suspension qui est épaissie sur la toile présente une conductivité d'au moins 3,5 mS/cm.
  20. Procédé conforme à l'une des revendications précédentes, caractérisé en ce que le procédé comporte en outre le fait d'épaissir la suspension sur une toile, de manière à obtenir une bande humide de papier et de l'eau blanche, et le fait de recycler cette eau blanche, en y ajoutant éventuellement de l'eau neuve, pour former une suspension à épaissir contenant des fibres cellulosiques et d'éventuelles charges, la quantité d'eau neuve ajoutée valant moins de 30 tonnes par tonne de papier sec produite.
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PCT/SE1999/000679 WO1999055964A1 (fr) 1998-04-27 1999-04-26 Procede de production de papier
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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2011113119A1 (fr) * 2010-03-19 2011-09-22 Fibria Celulose S/A Procédé pour le traitement de pâtes de cellulose, pâte de cellulose ainsi obtenue et utilisation de biopolymère pour le traitement de pâtes de cellulose

Families Citing this family (41)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100403839B1 (ko) * 1998-04-27 2003-11-01 악조 노벨 엔.브이. 제지 방법
US6417268B1 (en) 1999-12-06 2002-07-09 Hercules Incorporated Method for making hydrophobically associative polymers, methods of use and compositions
US6818100B2 (en) 2000-08-07 2004-11-16 Akzo Nobel N.V. Process for sizing paper
MX252220B (es) † 2000-08-07 2007-12-09 Akzo Nobel Nv Proceso para encolado de papel.
GB0019415D0 (en) * 2000-08-09 2000-09-27 Ciba Spec Chem Water Treat Ltd Noval monomers, polymers thereof and the use of the polymers
AU2001288175A1 (en) 2000-09-20 2002-04-02 Akzo Nobel N.V. A process for the production of paper
DE10113998A1 (de) * 2001-03-22 2002-09-26 Voith Paper Patent Gmbh Verfahren zum Beladen von in einer Faserstoffsuspension enthaltenen Fasern mit einem Hilfsstoff
MXPA04005533A (es) 2001-12-21 2004-09-13 Akzo Nobel Nv Composicion que contiene silice acuosa y proceso para la produccion de papel.
US7156955B2 (en) * 2001-12-21 2007-01-02 Akzo Nobel N.V. Papermaking process using a specified NSF to silica-based particle ratio
PL214002B1 (pl) * 2002-01-31 2013-06-28 Akzo Nobel Nv Sposób wytwarzania papieru i tektury
CA2500545A1 (fr) * 2002-10-01 2004-04-15 Akzo Nobel N.V. Produit de polysaccharide cationise
US20040084162A1 (en) 2002-11-06 2004-05-06 Shannon Thomas Gerard Low slough tissue products and method for making same
KR20050083897A (ko) * 2002-11-19 2005-08-26 악조 노벨 엔.브이. 셀룰로오스계 제품 및 제조 공정
US7303654B2 (en) 2002-11-19 2007-12-04 Akzo Nobel N.V. Cellulosic product and process for its production
JP4179913B2 (ja) * 2003-03-31 2008-11-12 ソマール株式会社 紙の製造方法
KR20050058785A (ko) * 2003-12-12 2005-06-17 김재봉 벤토나이트를 함유하는 수용성 중합체 분산액 및 그의제조방법
CN101955188A (zh) * 2004-04-07 2011-01-26 阿克佐诺贝尔公司 二氧化硅基溶胶及使用该溶胶的生产纸的方法
GB0425101D0 (en) * 2004-11-15 2004-12-15 Ciba Spec Chem Water Treat Ltd Papermaking process
PT1834040E (pt) * 2004-12-22 2015-04-15 Akzo Nobel Nv Processo para a produção de papel
US7955473B2 (en) 2004-12-22 2011-06-07 Akzo Nobel N.V. Process for the production of paper
US20060254464A1 (en) 2005-05-16 2006-11-16 Akzo Nobel N.V. Process for the production of paper
US8273216B2 (en) 2005-12-30 2012-09-25 Akzo Nobel N.V. Process for the production of paper
JP5140000B2 (ja) 2005-12-30 2013-02-06 アクゾ ノーベル ナムローゼ フェンノートシャップ 紙の製造方法
CA2581898A1 (fr) * 2006-03-17 2007-09-17 Weyerhaeuser Company Methode de fabrication d'un carton multiplis a faible densite avec forte resistance d'adhesion interne
EP1936032A1 (fr) 2006-12-18 2008-06-25 Akzo Nobel N.V. Procédé de production d'un produit en papier
EP2199462A1 (fr) 2008-12-18 2010-06-23 Coöperatie Avebe U.A. Processus de fabrication de papier
EP2402503A1 (fr) 2010-06-30 2012-01-04 Akzo Nobel Chemicals International B.V. Procédé de production d'un produit cellulosique
JP2013531749A (ja) * 2010-07-12 2013-08-08 アクゾ ノーベル ケミカルズ インターナショナル ベスローテン フエンノートシャップ セルロース繊維組成物
FI125713B (fi) * 2010-10-01 2016-01-15 Upm Kymmene Corp Menetelmä märän paperirainan ajettavuuden parantamiseksi ja paperi
RU2483151C1 (ru) * 2011-11-10 2013-05-27 Российская Федерация, От Имени Которой Выступает Министерство Промышленности И Торговли Российской Федерации Способ изготовления бумаги для печати
JP6243853B2 (ja) * 2012-12-07 2017-12-06 日本曹達株式会社 重合体の製造方法
EP3059739A1 (fr) 2015-02-20 2016-08-24 Wicor Holding AG Élément d'isolation ayant une faible conductivité électrique destiné à l'isolation dans une zone de haute tension
EP3288041A1 (fr) 2016-08-23 2018-02-28 Wicor Holding AG Élément d'isolation électrique avec fibres chimiques pour une zone haute tension
CN109661493B (zh) * 2016-09-07 2021-11-16 凯米罗总公司 用于制造纸、纸板或类似物的方法和组合物的用途
WO2018109279A1 (fr) * 2016-12-16 2018-06-21 Kemira Oyj Composition de polymère et ses utilisations
EP3601669B1 (fr) * 2017-03-29 2023-09-13 Kemira Oyj Procédé de fabrication de papier, de carton ou analogue
WO2019004950A1 (fr) * 2017-06-30 2019-01-03 Scg Packaging Public Company Limited Matériau en feuille à haute résistance
RU2671752C1 (ru) * 2017-12-14 2018-11-06 Общество с ограниченной ответственностью "ПАННА" Водорастворимая бумага со схемой для вышивания и способ ее производства
CN109594402A (zh) * 2018-12-28 2019-04-09 江苏理文造纸有限公司 一种利用废水污泥制备牛皮挂面箱板纸的方法
CN109942721B (zh) * 2019-03-20 2021-04-02 淮海工学院 一种羟甲基脲改性阳离子多糖的水溶液
AT525216A1 (de) * 2021-07-15 2023-01-15 Berndorf Band Gmbh Pressvorrichtung mit einer Druckrolle

Family Cites Families (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4250269A (en) * 1979-11-26 1981-02-10 Buckman Laboratories, Inc. Water-soluble mixtures of quaternary ammonium polymers, nonionic and/or cationic vinyl-addition polymers, and nonionic and/or cationic surfactants
SE432951B (sv) * 1980-05-28 1984-04-30 Eka Ab Pappersprodukt innehallande cellulosafibrer och ett bindemedelssystem som omfattar kolloidal kiselsyra och katjonisk sterkelse samt forfarande for framstellning av pappersprodukten
AU577735B2 (en) * 1984-01-27 1988-09-29 Nalco Chemical Company Emulsion for paper sizing
US4687519A (en) * 1985-12-20 1987-08-18 National Starch And Chemical Corporation Paper size compositions
EP0335575B2 (fr) * 1988-03-28 2000-08-23 Ciba Specialty Chemicals Water Treatments Limited Fabrication de papier et carton
US5098520A (en) * 1991-01-25 1992-03-24 Nalco Chemcial Company Papermaking process with improved retention and drainage
GB9313956D0 (en) * 1993-07-06 1993-08-18 Allied Colloids Ltd Production of paper
EP0707763B1 (fr) * 1993-07-07 2001-08-29 Picturetel Corporation Reduction de bruits de fond pour l'amelioration de la qualite de voix
SE9502522D0 (sv) * 1995-07-07 1995-07-07 Eka Nobel Ab A process for the production of paper
AU729008B2 (en) * 1996-05-01 2001-01-25 Nalco Chemical Company Improved papermaking process

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2011113119A1 (fr) * 2010-03-19 2011-09-22 Fibria Celulose S/A Procédé pour le traitement de pâtes de cellulose, pâte de cellulose ainsi obtenue et utilisation de biopolymère pour le traitement de pâtes de cellulose
WO2011113126A3 (fr) * 2010-03-19 2011-11-17 Fibria Celulose S/A Procédé de production de pâtes de cellulose modifiées, pâte de cellulose ainsi obtenue et utilisation d'un biopolymère pour produire des pâtes de cellulose
US9096974B2 (en) 2010-03-19 2015-08-04 Fibria Celulose S/A Process for producing modified cellulose pulps, cellulose pulp thus obtained and use of biopolymer for producing cellulose pulps
US9828728B2 (en) 2010-03-19 2017-11-28 Fibria Celulose S/A Methods of making paper and paper with modified cellulose pulps
US10590608B2 (en) 2010-03-19 2020-03-17 Suzano S.A. Methods of making paper and paper with modified cellulose pulps
US11047092B2 (en) 2010-03-19 2021-06-29 Suzano S.A. Methods of making paper and paper with modified cellulose pulps

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EP1080272A1 (fr) 2001-03-07
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AU750335B2 (en) 2002-07-18
JP2002513104A (ja) 2002-05-08
RU2000129670A (ru) 2004-03-27
NZ507606A (en) 2003-07-25
CN1205386C (zh) 2005-06-08
EP1084295A2 (fr) 2001-03-21
EP0953680A1 (fr) 1999-11-03
EP1080272B1 (fr) 2003-06-18
DE69908938D1 (de) 2003-07-24
PL200811B1 (pl) 2009-02-27
CA2329191C (fr) 2006-06-27
JP2002513102A (ja) 2002-05-08
ID27899A (id) 2001-05-03
CZ20003938A3 (cs) 2001-07-11
BR9909946A (pt) 2001-03-06
AU4301499A (en) 1999-11-16
BR9909945B1 (pt) 2009-08-11
WO1999055962A2 (fr) 1999-11-04
ES2196815T3 (es) 2003-12-16
ATE243282T1 (de) 2003-07-15
ES2201725T3 (es) 2004-03-16
ZA200005551B (en) 2001-05-11
RU2194106C2 (ru) 2002-12-10
CA2329028A1 (fr) 1999-11-04
CN1300332A (zh) 2001-06-20
DE69914078T2 (de) 2004-10-14
PL344053A1 (en) 2001-09-24
ATE257530T1 (de) 2004-01-15
EP1084295B1 (fr) 2004-01-07
BR9909946B1 (pt) 2009-12-01
CN1155754C (zh) 2004-06-30
DE69908938T2 (de) 2003-12-18
CN1299425A (zh) 2001-06-13
PL344040A1 (en) 2001-09-24
WO1999055965A1 (fr) 1999-11-04
ZA200005550B (en) 2001-05-11
DE69908939T2 (de) 2004-05-13
PT1080271E (pt) 2003-10-31
BR9909945A (pt) 2000-12-26
CN1139691C (zh) 2004-02-25
ID27307A (id) 2001-03-22
WO1999055962A3 (fr) 1999-12-16
CA2329027C (fr) 2005-02-15
CA2329191A1 (fr) 1999-11-04
RU2185470C1 (ru) 2002-07-20
ZA200005552B (en) 2001-05-11
JP4307721B2 (ja) 2009-08-05
CZ301693B6 (cs) 2010-05-26
AU4401699A (en) 1999-11-16
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CZ20003939A3 (cs) 2001-12-12
EP1080271A1 (fr) 2001-03-07
CN1298466A (zh) 2001-06-06
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JP2002513103A (ja) 2002-05-08
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AU747089B2 (en) 2002-05-09
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DE69914078D1 (de) 2004-02-12
CZ301092B6 (cs) 2009-11-04
PL200673B1 (pl) 2009-01-30
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PL201054B1 (pl) 2009-03-31
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DE69908939D1 (de) 2003-07-24
WO1999055964A1 (fr) 1999-11-04
AU4401599A (en) 1999-11-16
JP3890194B2 (ja) 2007-03-07
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ATE243281T1 (de) 2003-07-15
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PT1080272E (pt) 2003-10-31

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