WO1999055964A1 - Procede de production de papier - Google Patents

Procede de production de papier Download PDF

Info

Publication number
WO1999055964A1
WO1999055964A1 PCT/SE1999/000679 SE9900679W WO9955964A1 WO 1999055964 A1 WO1999055964 A1 WO 1999055964A1 SE 9900679 W SE9900679 W SE 9900679W WO 9955964 A1 WO9955964 A1 WO 9955964A1
Authority
WO
WIPO (PCT)
Prior art keywords
process according
suspension
polysaccharide
paper
cationic
Prior art date
Application number
PCT/SE1999/000679
Other languages
English (en)
Inventor
Michael Persson
Hans Hällström
Joakim CARLÉN
Original Assignee
Akzo Nobel N.V.
Eka Chemicals Ab
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
Family has litigation
First worldwide family litigation filed litigation Critical https://patents.darts-ip.com/?family=8236970&utm_source=google_patent&utm_medium=platform_link&utm_campaign=public_patent_search&patent=WO1999055964(A1) "Global patent litigation dataset” by Darts-ip is licensed under a Creative Commons Attribution 4.0 International License.
Priority to PL344040A priority Critical patent/PL200811B1/pl
Priority to CA002329027A priority patent/CA2329027C/fr
Priority to JP2000546103A priority patent/JP2002513103A/ja
Priority to DK99927017T priority patent/DK1080271T3/da
Priority to AU44016/99A priority patent/AU747089B2/en
Application filed by Akzo Nobel N.V., Eka Chemicals Ab filed Critical Akzo Nobel N.V.
Priority to NZ507605A priority patent/NZ507605A/xx
Priority to BR9909947-0A priority patent/BR9909947A/pt
Priority to EP99927017A priority patent/EP1080271B1/fr
Priority to DE69908938T priority patent/DE69908938T2/de
Priority to AT99927017T priority patent/ATE243281T1/de
Publication of WO1999055964A1 publication Critical patent/WO1999055964A1/fr
Priority to NO20005242A priority patent/NO20005242L/no

Links

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
  • 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 polysaccha ⁇ des like cationic starch and cationic guar gums are widely used as drainage and retention aids
  • the polysacc arides can be used alone or in combination with other polymers and/
  • Cationic polysaccharides are usually prepared by the reaction of a polysaccharide with a quaternising agent, e g 3-chloro-2-hydroxypropyl t ⁇ methylammonium chloride 2,3-epoxypropyl trimethyl ammonium chloride, and 2-chloroethyl t ⁇ methyl ammonium chloride
  • a quaternising agent e g 3-chloro-2-hydroxypropyl t ⁇ methylammonium chloride 2,3-epoxypropyl trimethyl ammonium chloride, and 2-chloroethyl t ⁇ methyl ammonium chloride
  • U S Patent Nos 4,388,150, 4,755,259, 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 European Patent No 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
  • 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
  • the invention further 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 dry strength agent comprising a cationic or ampho
  • 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
  • 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 carboxy c 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 covalentiy 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 Examples of suitable hydrophobic aliphatic groups include linear, branched and cyclic alkyl groups like ethyl, propyl, e g n
  • Particularly suitable polysaccharides according to the invention include those comprising the general structural formula (I)
  • 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 an alkyleneoxy group or hydroxy propylene group (- CH 2 - CH(OH) - CH 2 - ),
  • 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,
  • 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
  • the degree of anionic substitution (DS A ) can be from 0 to
  • 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 propylene oxide and butylene oxide 5 alkyl halides, e g decyl bromide and docecyl bromide, aralkyl hahdes, e g benzyl chloride and benzyl bromide, the reaction products of epichlorohyd ⁇ n and dialkylamines having at least one substituent comprising a hydrophobic group as defined above, including 3-d ⁇ alkyl- am ⁇ no-1 ,2-epoxypropanes, and cationic agents such as, for example, the reaction product of epichlorohyd ⁇ n and tertiary amines having at least one substituent comprising a hydro- phobic group as defined above, including t ⁇ alkylamines, alkaryldialkylamines, e g dimethyl- benzylamine, arylamine
  • 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 S ⁇ 0 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 polysi cic acid
  • the silica- based sols can also be modified and contain other elements, e g aluminium and/or boron, which can be present in the aqueous phase and/or in the silica-based particles
  • Suitable 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 silic
  • 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 Patent No 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 7 particles with a specific surface area in the range of from 300 to 1000 m 2 /g, suitably from
  • 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 Her & 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 polysihcic 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 poly- aluminosi cate and polyaluminosi cate 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 montmo ⁇ llonite/bentonite, hecto ⁇ te beide te 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 Patent Nos 4,753,710, 5,071 ,512, and 5,607,552, which are hereby incorporated herein by reference
  • 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 copolyme ⁇ zed with nonionic monomers like (meth)acrylam ⁇ de 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
  • 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 8 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)acrylam ⁇ des 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
  • Aluminium compounds that can be used according to this invention include alum alummates, 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 sulfunc 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 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 Patent No 5,858,174, which is hereby incorporated herein by reference
  • the dry strength agent and drainage and retention a ⁇ d(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 Generally 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 9 suitably 2% by weight
  • 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 S ⁇ 0 2 and based on dry stock substance preferably within the range of from 0 01 to 0 2% by weight
  • the total amount added is suitably within the range of from 0 005 to 0 5% by weight, calculated as S ⁇ 0 2 and based on dry stock substance preferably within the range of from 0 01 to 0 2% by weight
  • LMW cationic organic polymer in the process it can be added in an amount of at least
  • 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 0 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
  • the values referred to above are suitably determined by measuring the conductivity of the cellulosic suspension that is fed into or present in the headbox of the paper machine or, alternatively by measuring the conductivity of white water obtained by dewatering the suspension
  • High conductivity levels mean high contents of salts (electrolytes), where the various salts can be based on mono-, di- and multivalent
  • 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
  • the term ' paper as used herein 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, chemo- 11 thermomechanical 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%, suit
  • Cationised polysaccharides were prepared by reacting native potato starch with a quaternising agent according to the general procedure described in European Patent Application No. 189 935.
  • the quaternising agents are commercially available from for example Degussa, or were prepared according to the general procedure described in U.S. Patent No. 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: P1: Cationised starch obtained by quarternisation of native potato starch with 3- chloro-2-hydroxypropyl dimethyl benzyl ammonium chloride to 0.8% N.
  • P2 Cationised starch obtained by quarternisation of native potato starch with 3-chloro-
  • Ref. 1 Cationised starch obtained by quarternization of native potato starch with 3- chloro-2-hydroxypropyl trimethyl ammonium chloride to 0.8% N.
  • Ref. 2 Cationised starch obtained by quarternization of native potato starch with 2,3- epoxypropyl trimethyl ammonium chloride to 1.3% N.
  • Analyser 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.
  • First pass retention 12 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. Patent No. 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 Si0 2 and based on dry stock system.
  • 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 Si0 2 on dry stock system.
  • 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 Si0 2 on dry stock system. 14 Table 3
  • Example 5 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
  • 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 S ⁇ 0 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

Landscapes

  • Paper (AREA)
  • Polarising Elements (AREA)
  • Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
  • Polymers With Sulfur, Phosphorus Or Metals In The Main Chain (AREA)

Abstract

L'invention concerne un procédé de production de papier à partir d'une suspension contenant des fibres cellulosiques, et d'éventuelles charges. Ce procédé consiste à ajouter à la suspension un auxiliaire de drainage et de rétention contenant un polysaccharide cationique ou amphotérique, à former et à déshydrater la suspension sur un fil. Le polysaccharide cationique a un groupe hydrophobe. L'invention concerne également un procédé de production de papier à partir d'une suspension contenant des fibres cellulosiques, et éventuellement des charges. Ce procédé consiste à ajouter à la suspension un agent de résistance sec contenant un polysaccharide cationique ou amphotérique, à former et à déshydrater la suspension sur un fil. Le polysaccharide contient un groupe hydrophobe.
PCT/SE1999/000679 1998-04-27 1999-04-26 Procede de production de papier WO1999055964A1 (fr)

Priority Applications (11)

Application Number Priority Date Filing Date Title
AT99927017T ATE243281T1 (de) 1998-04-27 1999-04-26 Verfahren zur herstellung von papier
CA002329027A CA2329027C (fr) 1998-04-27 1999-04-26 Procede de production de papier
JP2000546103A JP2002513103A (ja) 1998-04-27 1999-04-26 紙の生産方法
DK99927017T DK1080271T3 (da) 1998-04-27 1999-04-26 Fremgangsmåde til fremstillingen af papir
AU44016/99A AU747089B2 (en) 1998-04-27 1999-04-26 A process for the production of paper
PL344040A PL200811B1 (pl) 1998-04-27 1999-04-26 Sposób wytwarzania papieru
NZ507605A NZ507605A (en) 1998-04-27 1999-04-26 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, where the polysaccharide has a hydrophobic group comprising an aromatic group
BR9909947-0A BR9909947A (pt) 1998-04-27 1999-04-26 Processo para produção de papel
EP99927017A EP1080271B1 (fr) 1998-04-27 1999-04-26 Procede de production de papier
DE69908938T DE69908938T2 (de) 1998-04-27 1999-04-26 Verfahren zur herstellung von papier
NO20005242A NO20005242L (no) 1998-04-27 2000-10-18 Fremgangsmåte ved fremstilling av papir

Applications Claiming Priority (4)

Application Number Priority Date Filing Date Title
US8325398P 1998-04-27 1998-04-27
US60/083,253 1998-04-27
EP98850067.4 1998-04-27
EP98850067A EP0953680A1 (fr) 1998-04-27 1998-04-27 Procédé pour la fabrication du papier

Publications (1)

Publication Number Publication Date
WO1999055964A1 true WO1999055964A1 (fr) 1999-11-04

Family

ID=8236970

Family Applications (3)

Application Number Title Priority Date Filing Date
PCT/SE1999/000677 WO1999055965A1 (fr) 1998-04-27 1999-04-26 Procede de production de papier
PCT/SE1999/000679 WO1999055964A1 (fr) 1998-04-27 1999-04-26 Procede de production de papier
PCT/SE1999/000678 WO1999055962A2 (fr) 1998-04-27 1999-04-26 Procede de production de papier

Family Applications Before (1)

Application Number Title Priority Date Filing Date
PCT/SE1999/000677 WO1999055965A1 (fr) 1998-04-27 1999-04-26 Procede de production de papier

Family Applications After (1)

Application Number Title Priority Date Filing Date
PCT/SE1999/000678 WO1999055962A2 (fr) 1998-04-27 1999-04-26 Procede de production de papier

Country Status (18)

Country Link
EP (4) EP0953680A1 (fr)
JP (3) JP4307721B2 (fr)
CN (3) CN1155754C (fr)
AT (3) ATE257530T1 (fr)
AU (3) AU750335B2 (fr)
BR (3) BR9909945B1 (fr)
CA (3) CA2329027C (fr)
CZ (3) CZ20003937A3 (fr)
DE (3) DE69914078T2 (fr)
DK (3) DK1084295T3 (fr)
ES (3) ES2196815T3 (fr)
ID (3) ID27307A (fr)
NZ (3) NZ507604A (fr)
PL (3) PL200673B1 (fr)
PT (3) PT1080271E (fr)
RU (3) RU2185470C1 (fr)
WO (3) WO1999055965A1 (fr)
ZA (3) ZA200005552B (fr)

Cited By (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1243693A2 (fr) * 2001-03-22 2002-09-25 Voith Paper Patent GmbH Procédé pour charger des fibres en suspension avec un additif
US6551457B2 (en) 2000-09-20 2003-04-22 Akzo Nobel N.V. Process for the production of paper
JP2004506105A (ja) * 2000-08-07 2004-02-26 アクゾ　ノーベル　エヌ．ブイ． 紙の製造方法
WO2004031478A1 (fr) * 2002-10-01 2004-04-15 Akzo Nobel N.V. Produit de polysaccharide cationise
US6818100B2 (en) 2000-08-07 2004-11-16 Akzo Nobel N.V. Process for sizing paper
EP1835075A1 (fr) * 2006-03-17 2007-09-19 Weyerhaeuser Company Procédé de fabrication d'un carton multicouche
US7303654B2 (en) 2002-11-19 2007-12-04 Akzo Nobel N.V. Cellulosic product and process for its production
US7608644B2 (en) * 2001-12-21 2009-10-27 Akzo Nobel N.V. Aqueous silica-containing composition
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
WO2012007363A1 (fr) * 2010-07-12 2012-01-19 Akzo Nobel Chemicals International B.V. Composition de fibre cellulosique
US20180073197A1 (en) * 2010-03-19 2018-03-15 Fibria Celulose S/A Methods of Making Paper and Paper with Modified Cellulose Pulps

Families Citing this family (30)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100403840B1 (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
GB0019415D0 (en) * 2000-08-09 2000-09-27 Ciba Spec Chem Water Treat Ltd Noval monomers, polymers thereof and the use of the polymers
MXPA04005533A (es) * 2001-12-21 2004-09-13 Akzo Nobel Nv Composicion que contiene silice acuosa y proceso para la produccion de papel.
PL214002B1 (pl) * 2002-01-31 2013-06-28 Akzo Nobel Nv Sposób wytwarzania papieru i tektury
US20040084162A1 (en) 2002-11-06 2004-05-06 Shannon Thomas Gerard Low slough tissue products and method for making same
BR0316393A (pt) * 2002-11-19 2005-09-27 Akzo Nobel Nv Produto celulósico e processo para a sua produção
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
AU2005231671B2 (en) * 2004-04-07 2008-08-07 Akzo Nobel Chemicals International B.V. Silica-based sols and their production and use
GB0425101D0 (en) * 2004-11-15 2004-12-15 Ciba Spec Chem Water Treat Ltd Papermaking process
BRPI0515831B1 (pt) * 2004-12-22 2017-03-28 Akzo Nobel Nv processo para 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
PT1969183E (pt) 2005-12-30 2015-03-06 Akzo Nobel Nv Processo para a produção de papel
EP1936032A1 (fr) 2006-12-18 2008-06-25 Akzo Nobel N.V. Procédé de production d'un produit en papier
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
WO2014087644A1 (fr) * 2012-12-07 2014-06-12 日本曹達株式会社 Procédé de production d'un polymère
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
KR102511422B1 (ko) * 2016-09-07 2023-03-17 케미라 오와이제이 종이, 보드 등의 제조 방법 및 조성물의 용도
EP3555364B1 (fr) * 2016-12-16 2020-10-14 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

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4388150A (en) * 1980-05-28 1983-06-14 Eka Aktiebolag Papermaking and products made thereby
US4687519A (en) * 1985-12-20 1987-08-18 National Starch And Chemical Corporation Paper size compositions
EP0335575A2 (fr) * 1988-03-28 1989-10-04 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
EP0752496A2 (fr) * 1995-07-07 1997-01-08 Eka Chemicals AB Procédé de production de papier

Family Cites Families (5)

* 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
FI81860C (fi) * 1984-01-27 1990-12-10 Nalco Chemical Co Nytt foerfarande foer limning av papper.
GB9313956D0 (en) * 1993-07-06 1993-08-18 Allied Colloids Ltd Production of paper
JP3626492B2 (ja) * 1993-07-07 2005-03-09 ポリコム・インコーポレイテッド 会話の品質向上のための背景雑音の低減
AU729008B2 (en) * 1996-05-01 2001-01-25 Nalco Chemical Company Improved papermaking process

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4388150A (en) * 1980-05-28 1983-06-14 Eka Aktiebolag Papermaking and products made thereby
US4687519A (en) * 1985-12-20 1987-08-18 National Starch And Chemical Corporation Paper size compositions
EP0335575A2 (fr) * 1988-03-28 1989-10-04 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
EP0752496A2 (fr) * 1995-07-07 1997-01-08 Eka Chemicals AB Procédé de production de papier

Cited By (24)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7488402B2 (en) 2000-08-07 2009-02-10 Akzo Nobel N.V. Process for production of paper
JP2004506105A (ja) * 2000-08-07 2004-02-26 アクゾ　ノーベル　エヌ．ブイ． 紙の製造方法
US7318881B2 (en) 2000-08-07 2008-01-15 Akzo Nobel N.V. Process for sizing paper
US6818100B2 (en) 2000-08-07 2004-11-16 Akzo Nobel N.V. Process for sizing paper
US6846384B2 (en) 2000-08-07 2005-01-25 Akzo Nobel N.V. Process for sizing paper
US6918995B2 (en) 2000-08-07 2005-07-19 Akzo Nobel N.V. Process for the production of paper
CN1302176C (zh) * 2000-08-07 2007-02-28 阿克佐诺贝尔公司 生产纸的方法
US6551457B2 (en) 2000-09-20 2003-04-22 Akzo Nobel N.V. Process for the production of paper
EP1243693A3 (fr) * 2001-03-22 2003-12-10 Voith Paper Patent GmbH Procédé pour charger des fibres en suspension avec un additif
EP1243693A2 (fr) * 2001-03-22 2002-09-25 Voith Paper Patent GmbH Procédé pour charger des fibres en suspension avec un additif
US7608644B2 (en) * 2001-12-21 2009-10-27 Akzo Nobel N.V. Aqueous silica-containing composition
WO2004031478A1 (fr) * 2002-10-01 2004-04-15 Akzo Nobel N.V. Produit de polysaccharide cationise
US7303654B2 (en) 2002-11-19 2007-12-04 Akzo Nobel N.V. Cellulosic product and process for its production
EP1835075A1 (fr) * 2006-03-17 2007-09-19 Weyerhaeuser Company Procédé de fabrication d'un carton multicouche
EP2199462A1 (fr) 2008-12-18 2010-06-23 Coöperatie Avebe U.A. Processus de fabrication de papier
US8585865B2 (en) 2008-12-18 2013-11-19 Cooperatie Avebe U.A. Process for making paper
WO2010071435A1 (fr) 2008-12-18 2010-06-24 Coöperatie Avebe U.A. Procede de fabrication de papier
EA019646B1 (ru) * 2008-12-18 2014-05-30 Коперати Авебе У.А. Способ производства бумаги
AU2009327706B2 (en) * 2008-12-18 2012-11-01 Cooperatie Avebe U.A. A process for making paper
US20180073197A1 (en) * 2010-03-19 2018-03-15 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
EP2402503A1 (fr) 2010-06-30 2012-01-04 Akzo Nobel Chemicals International B.V. Procédé de production d'un produit cellulosique
WO2012007363A1 (fr) * 2010-07-12 2012-01-19 Akzo Nobel Chemicals International B.V. Composition de fibre cellulosique

Also Published As

Publication number Publication date
DE69908939D1 (de) 2003-07-24
ID27490A (id) 2001-04-12
PT1080271E (pt) 2003-10-31
CN1155754C (zh) 2004-06-30
DE69908938D1 (de) 2003-07-24
BR9909946A (pt) 2001-03-06
EP1080271B1 (fr) 2003-06-18
DK1080272T3 (da) 2003-10-06
JP2002513102A (ja) 2002-05-08
CZ301092B6 (cs) 2009-11-04
WO1999055962A3 (fr) 1999-12-16
ATE243281T1 (de) 2003-07-15
CN1300332A (zh) 2001-06-20
DE69914078T2 (de) 2004-10-14
DE69908939T2 (de) 2004-05-13
ZA200005552B (en) 2001-05-11
ES2201725T3 (es) 2004-03-16
PL201054B1 (pl) 2009-03-31
ZA200005551B (en) 2001-05-11
CZ20003938A3 (cs) 2001-07-11
PL200673B1 (pl) 2009-01-30
JP4307721B2 (ja) 2009-08-05
PT1084295E (pt) 2004-04-30
RU2194106C2 (ru) 2002-12-10
ES2211166T3 (es) 2004-07-01
EP1080272B1 (fr) 2003-06-18
CA2329028A1 (fr) 1999-11-04
DK1084295T3 (da) 2004-04-26
BR9909945A (pt) 2000-12-26
EP1080272A1 (fr) 2001-03-07
CA2329191C (fr) 2006-06-27
RU2000129670A (ru) 2004-03-27
CZ301693B6 (cs) 2010-05-26
ES2196815T3 (es) 2003-12-16
CA2329027C (fr) 2005-02-15
CA2329191A1 (fr) 1999-11-04
PT1080272E (pt) 2003-10-31
CA2329027A1 (fr) 1999-11-04
JP2002513103A (ja) 2002-05-08
JP3890194B2 (ja) 2007-03-07
EP0953680A1 (fr) 1999-11-03
DE69908938T2 (de) 2003-12-18
CN1298466A (zh) 2001-06-06
CN1139691C (zh) 2004-02-25
PL200811B1 (pl) 2009-02-27
ATE243282T1 (de) 2003-07-15
RU2185470C1 (ru) 2002-07-20
PL344053A1 (en) 2001-09-24
BR9909946B1 (pt) 2009-12-01
EP1084295A2 (fr) 2001-03-21
RU2194818C2 (ru) 2002-12-20
CA2329028C (fr) 2005-11-22
DK1080271T3 (da) 2003-09-22
WO1999055962A2 (fr) 1999-11-04
CN1299425A (zh) 2001-06-13
CZ20003939A3 (cs) 2001-12-12
PL344079A1 (en) 2001-09-24
PL344040A1 (en) 2001-09-24
AU748735B2 (en) 2002-06-13
EP1080271A1 (fr) 2001-03-07
EP1084295B1 (fr) 2004-01-07
AU4301499A (en) 1999-11-16
BR9909945B1 (pt) 2009-08-11
BR9909947A (pt) 2000-12-26
CZ20003937A3 (cs) 2001-12-12
AU747089B2 (en) 2002-05-09
NZ507605A (en) 2003-01-31
JP2002513104A (ja) 2002-05-08
ID27307A (id) 2001-03-22
AU4401699A (en) 1999-11-16
ATE257530T1 (de) 2004-01-15
AU750335B2 (en) 2002-07-18
NZ507606A (en) 2003-07-25
WO1999055965A1 (fr) 1999-11-04
ID27899A (id) 2001-05-03
ZA200005550B (en) 2001-05-11
DE69914078D1 (de) 2004-02-12
CN1205386C (zh) 2005-06-08
AU4401599A (en) 1999-11-16
NZ507604A (en) 2003-09-26

Similar Documents

Publication Publication Date Title
EP1080271B1 (fr) Procede de production de papier
US8157962B2 (en) Process for the production of cellulosic product
US20060142465A1 (en) Aqueous composition
WO2004031478A1 (fr) Produit de polysaccharide cationise
KR100403840B1 (ko) 제지 방법
US20020139502A1 (en) Process for the production of paper
US7306700B1 (en) Process for the production of paper
US20040138438A1 (en) Cationised polysaccharide product
MXPA00010570A (es) Proceso para la produccion de papel
US20040104004A1 (en) Cationised polysaccharide product

Legal Events

Date Code Title Description
WWE Wipo information: entry into national phase

Ref document number: 99805532.8

Country of ref document: CN

AK Designated states

Kind code of ref document: A1

Designated state(s): AL AM AT AU AZ BA BB BG BR BY CA CH CN CU CZ DE DK EE ES FI GB GE GH GM HR HU ID IL IN IS JP KE KG KP KR KZ LC LK LR LS LT LU LV MD MG MK MN MW MX NO NZ PL PT RO RU SD SE SG SI SK SL TJ TM TR TT UA UG US UZ VN YU ZA ZW

AL Designated countries for regional patents

Kind code of ref document: A1

Designated state(s): GH GM KE LS MW SD SL SZ UG ZW AM AZ BY KG KZ MD RU TJ TM AT BE CH CY DE DK ES FI FR GB GR IE IT LU MC NL PT SE BF BJ CF CG CI CM GA GN GW ML MR NE SN TD TG

121 Ep: the epo has been informed by wipo that ep was designated in this application
DFPE Request for preliminary examination filed prior to expiration of 19th month from priority date (pct application filed before 20040101)
WWE Wipo information: entry into national phase

Ref document number: 44016/99

Country of ref document: AU

WWE Wipo information: entry into national phase

Ref document number: 2000/05552

Country of ref document: ZA

Ref document number: 200005552

Country of ref document: ZA

WWE Wipo information: entry into national phase

Ref document number: 507605

Country of ref document: NZ

ENP Entry into the national phase

Ref document number: 2329027

Country of ref document: CA

WWE Wipo information: entry into national phase

Ref document number: 1020007011564

Country of ref document: KR

WWE Wipo information: entry into national phase

Ref document number: PV2000-3937

Country of ref document: CZ

WWE Wipo information: entry into national phase

Ref document number: 1999927017

Country of ref document: EP

Ref document number: 09696834

Country of ref document: US

WWE Wipo information: entry into national phase

Ref document number: PA/a/2000/010570

Country of ref document: MX

REG Reference to national code

Ref country code: DE

Ref legal event code: 8642

WWP Wipo information: published in national office

Ref document number: 1999927017

Country of ref document: EP

WWP Wipo information: published in national office

Ref document number: 1020007011564

Country of ref document: KR

WWP Wipo information: published in national office

Ref document number: PV2000-3937

Country of ref document: CZ

WWG Wipo information: grant in national office

Ref document number: 44016/99

Country of ref document: AU

WWG Wipo information: grant in national office

Ref document number: 1999927017

Country of ref document: EP

WWG Wipo information: grant in national office

Ref document number: 1020007011564

Country of ref document: KR