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EP1309758A1 - Procede de production de papier - Google Patents

Procede de production de papier

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Publication number
EP1309758A1
EP1309758A1 EP01958740A EP01958740A EP1309758A1 EP 1309758 A1 EP1309758 A1 EP 1309758A1 EP 01958740 A EP01958740 A EP 01958740A EP 01958740 A EP01958740 A EP 01958740A EP 1309758 A1 EP1309758 A1 EP 1309758A1
Authority
EP
European Patent Office
Prior art keywords
polymer
anionic
cationic
process according
polymers
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
EP01958740A
Other languages
German (de)
English (en)
Other versions
EP1309758B1 (fr
Inventor
Sten FRÖLICH
Fredrik Solhage
Erik Lindgren
Hans Johansson-Vestin
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Akzo Nobel NV
Nouryon Pulp and Performance Chemicals AB
Original Assignee
Akzo Nobel NV
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
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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
    • D21H23/76—Processes or apparatus for adding material to the pulp or to the paper characterised by choice of auxiliary compounds which are added separately from at least one other compound, e.g. to improve the incorporation of the latter or to obtain an enhanced combined effect
    • D21H23/765—Addition of all compounds to the pulp
    • 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
    • D21H21/14—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 characterised by function or properties in or on the paper
    • D21H21/16—Sizing or water-repelling agents
    • 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
    • D21H17/29—Starch cationic
    • 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
    • D21H17/46—Synthetic macromolecular compounds obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds
    • D21H17/47—Condensation polymers of aldehydes or ketones

Definitions

  • This invention relates to papermaking and more specifically to a process for the production of paper in which cationic and anionic polymers having aromatic groups are added to a papermaking stock.
  • the process provides improved drainage and retention.
  • 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.
  • the obtained water usually referred to as white water and containing fine particles such as fine fibres, fillers and additives, is usually recycled 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 cellulose fibres so that they are retained with the fibres.
  • a wide variety of drainage and retention aids are known in the art, for example anionic, non-ionic, cationic and amphoteric organic polymers, anionic and cationic inorganic materials, and many combinations thereof.
  • WO 99/55964 and WO 99/55965 disclose the use of drainage and retention aids comprising cationic organic polymers having aromatic groups.
  • the cationic organic polymers can be used alone or in combination with various anionic materials such as, for example, anionic organic and inorganic condensation polymers, e.g. sulphonated melamine-formaldehyde and silica- based particles.
  • the present invention relates to a process for the production of paper from an aqueous suspension containing cellulosic fibres, and optional fillers, which comprises separately adding to the suspension a cationic organic polymer having an aromatic group and an anionic polymer having an aromatic group, the anionic polymer being selected from step-growth polymers, polysaccharides, and naturally occurring aromatic polymers and modifications thereof; forming and draining the suspension on a wire, with the proviso that if the anionic polymer is selected from step- growth polymers, it is not an anionic melamine-sulphonic acid condensation polymer.
  • the invention further relates to a process for the production of paper from an aqueous suspen- sion containing cellulosic fibres, and optional fillers, which comprises separately adding to the suspension a cationic organic polymer having an aromatic group and an anionic polymer having an aromatic group, forming and draining the suspension on a wire, with the proviso that the anionic polymer is not an anionic polystyrene sulphonate or anionic melamine-sulphonic acid condensation polymer.
  • the invention thus relates to a process as further defined in the claims.
  • drainage and retention aids refers to two or more components which, when added to an aqueous cellulosic suspension, give better drainage and/or retention than is obtained when not adding the said two or more components.
  • the present invention results in improved drainage and/or retention in the production of paper from all types of stocks, in particular stocks having high contents of salts (high conductivity) and colloidal substances, and/or in papermaking processes with a high degree of white water closure, i.e. extensive white water recycling and limited fresh water supply.
  • the present invention makes it possible to increase the speed of the paper machine and to use a lower dosage of additives to give a corresponding drainage and/or retention effect, thereby leading to an improved papermaking process and economic benefits.
  • the present invention also provides paper with improved dry strength.
  • the cationic organic polymer having an aromatic group according to the present invention can be derived from natural or synthetic sources, and it can be linear, branched or cross-linked.
  • the cationic polymer is water-soluble or water-dispersable.
  • suitable cationic polymers include cationic polysaccharides, e.g.
  • Cationic starches and cationic acrylamide- based polymers having an aromatic group are particularly preferred cationic polymers.
  • the cationic organic polymer according to the invention has one or more aromatic groups and the aromatic groups can be of the same or different types.
  • the aromatic group of the cationic organic polymer can be present in the polymer backbone (main chain) or in a substituent group that is attached to the polymer backbone, preferably in a substituent group.
  • suitable aromatic groups include aryl, aralkyl and alkaryl 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, preferably benzyl.
  • cationically charged groups that can be present in the cationic polymer as well as in monomers used for preparing the cationic polymer include quaternary ammonium groups, tertiary amino groups and acid addition salts thereof.
  • the cationic organic polymer having an aromatic group is a polysaccharide represented by 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.
  • R and R 2 are each H or, preferably, a hydrocarbon group, suitably alkyl, having from 1 to 3 carbon atoms, preferably 1 to 2 carbon atoms;
  • Q is a substituent containing an aromatic group, suitably a phenyl or substituted phenyl group, which can be attached to the nitrogen by means of an alkylene group usually having from 1 to 3 carbon atoms, suitably 1 to 2 carbon atoms, and preferably Q is a benzyl group (-CH 2 -C 6 H 5 );
  • n is an integer, usually from about 2 to about 300,000, suitably from 5 to 200,000 and preferably from 6 to 125,000 or, alternatively, R 1f R 2 and Q 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.
  • Suitable polysaccharides represented by the general formula (I) include those mentioned above.
  • Cationic polysaccharides according to the invention may also contain anionic groups, preferably in a minor amount. Such anionic groups may be introduced in the polysaccharide by means of chemical treatment or be present in the native polysaccharide.
  • the cationic organic polymer having an aromatic group is a chain-growth polymer.
  • chain-growth polymer refers to a polymer obtained by chain-growth polymerization, also being referred to as chain reaction polymer and chain reaction polymerization, respectively.
  • Suitable chain-growth polymers include vinyl addition polymers prepared by polymerization of one or more monomers having a vinyl group or ethylenically unsaturated bond, for example a polymer obtained by polymerizing a cationic monomer or a monomer mixture comprising a cationic monomer represented by the general structural formula (II):
  • R 3 is H or CH 3 ;
  • R-* and R 2 are each H or, preferably, a hydrocarbon group, suitably alkyl, having from 1 to 3 carbon atoms, preferably 1 to 2 carbon atoms;
  • a 2 is O or NH;
  • B 2 is an alkyl or alkylene group having from 2 to 8 carbon atoms, suitably from 2 to 4 carbon atoms, or a hydroxy propylene group;
  • Q is a substituent containing an aromatic group, suitably a phenyl or substituted phenyl group, which can be attached to the nitrogen by means of an alkylene group usually having from 1 to 3 carbon atoms, suitably 1 to 2 carbon atoms, and preferably Q is a benzyl group (-CH 2 -C 6 H 5 ); and
  • X " is an anionic counterion, usually a halide like chloride.
  • Suitable monomers represented by the general formula (II) include quaternary monomers obtained by treating dialkylaminoalkyl (meth)acrylates, e.g. dimethylaminoethyl (meth)acrylate, diethylaminoethyl (meth)acrylate and dimethylaminohydroxy- propyl (meth)acrylate, and dialkylaminoalkyl (meth)acrylamides, e.g. dimethylaminoethyl (meth)acrylamide, diethylaminoethyl (meth)acrylamide, dimethylaminopropyl (meth)- acrylamide, and diethylaminopropyl (meth)acrylamide, with benzyl chloride.
  • dialkylaminoalkyl (meth)acrylates e.g. dimethylaminoethyl (meth)acrylate, diethylaminoethyl (meth)acrylate and dimethylaminohydroxy- propyl
  • Preferred cationic monomers of the general formula (I) include dimethylaminoethylacrylate benzyl chloride quaternary salt and dimethylaminoethylmethacrylate benzyl chloride quaternary salt.
  • the monomer of formula (II) can be copolymerized with one or more non-ionic, cationic and/or anionic monomers.
  • Suitable copolymerizable non-ionic monomers include (meth)acrylamide; acrylamide-based monomers like N-alkyl (meth)acrylamides, N,N-dialkyl (meth)acrylamides and dialkylaminoalkyl (meth)acrylamides, acrylate-based monomers like dialkylaminoalkyl (meth)acrylates, and vinylamides.
  • Suitable copolymerizable cationic monomers include acid addition salts and quaternary salts of dimethylaminoethyl (meth)acrylate and diallyldimethylammonium chloride.
  • the cationic organic polymer may also contain anionic groups, preferably in a minor amount.
  • Suitable copolymerizable anionic monomers include acrylic acid, methacrylic acid and various sulphonated vinylic monomers such as styrenesulphonate.
  • Preferred copolymerizable monomers include acrylamide and methacrylamide, i.e. (meth)acrylamide, and the cationic or amphoteric organic polymer is preferably an acrylamide-based polymer.
  • Cationic vinyl addition polymers according to this invention can be prepared from a monomer mixture generally comprising from 1 to 99 mole%, suitably from 2 to 50 mole% and preferably from 5 to 20 mole% of cationic monomer having an aromatic group and from 99 to 1 mole%, suitably from 98 to 50 mole%, and preferably from 95 to 80 mole% of other copolymerizable monomers which preferably comprises acrylamide or methacrylamide ((meth)acrylamide), the monomer mixture suitably comprising from 98 to 50 mole% and preferably from 95 to 80 mo!e% of (meth)acrylamide, the sum of percentages being 100.
  • suitable cationic step-growth polymers include cationic polyurethanes which can be prepared from a monomer mixture comprising aromatic isocyanates and/or aromatic alcohols.
  • suitable aromatic isocyanates include diisocyanates, e.g. toluene-2,4- and 2,6-diisocyanates and diphenylmethane-4,4'- diisocyanate.
  • suitable aromatic alcohols include dihydric alcohols, i.e. diols, e.g. bisphenol A, phenyl diethanol amine, glycerol monoterephthalate and trimethylol- propane monoterephthalate. Monohydric aromatic alcohols such as phenol and derivaties thereof may also be employed.
  • the monomer mixture can also contain non-aromatic isocyanates and/or alcohols, usually diisocyanates and diols, for example any of those known to be useful in the preparation of polyurethanes.
  • suitable monomers containing cationic groups include cationic diols such as acid addition salts and quaternization products of N-alkandiol dialkylamines and N-alkyl dialkanolamines like 1,2- propanediol-3-dimethylamine, N-methyl diethanolamine, N-ethyl diethanolamine, N-propyl diethanolamine, N-n-butyl diethanolamine and N-t-butyl diethanolamine, N-stearyl di- ethanolamine and N-methyl dipropanolamine.
  • the quaternization products can be derived from alkylating agents like methyl chloride, dimethyl sulphate, benzyl chloride and epichlorohydrin.
  • the weight average molecular weight of the cationic polymer can vary within wide limits dependent on, inter alia, the type of polymer used, and usually it is at least about 5,000 and often at least 10,000. More often, it is above 150,000, normally above 500,000, suitably above about 700,000, preferably above about 1,000,000 and most preferably above about 2,000,000.
  • the upper limit is not critical; it can be about 200,000,000, usually 150,000,000 and suitably 100,000,000.
  • the cationic organic polymer can have a degree of cationic substitution (DS C ) varying over a wide range dependent on, inter alia, the type of polymer used; DS C can be from 0.005 to 1.0, usually from 0.01 to 0.5, suitably from 0.02 to 0.3, preferably from 0.025 to 0.2; and the degree of aromatic substitution (DS Q ) can be from 0.001 to 0.5, usually from 0.01 to 0.5, suitably from 0.02 to 0.3 and preferably from 0.025 to 0.2.
  • DS C degree of cationic substitution
  • DS Q degree of aromatic substitution
  • the degree of anionic substitution can be from 0 to 0.2, suitably from 0 to 0.1 and preferably from 0 to 0.05, the cationic polymer having an overall cationic charge.
  • the charge density of the cationic polymer is within the range of from 0.1 to 6.0 meqv/g of dry polymer, suitably from 0.2 to 5.0 and preferably from 0.5 to 4.0.
  • Suitable cationic organic polymers having an aromatic group include those described in International Patent Publication Nos. WO 99/55964, WO 99/55965 and WO 99/67310, which are hereby incorporated herein by reference.
  • Anionic polymers having an aromatic group according to the invention can be selected from step-growth polymers, chain-growth polymers, polysaccharides, naturally occurring aromatic polymers and modifications thereof.
  • step-growth polymer refers to a polymer obtained by step-growth polymerization, also being referred to as step-reaction polymer and step-reaction polymerization, respectively.
  • the anionic polymer is selected from step-growth polymers, polysaccharides and naturally occurring aromatic polymers and modifications thereof, most preferably step- growth polymers.
  • the anionic polymers according to the invention can be linear, branched or cross-linked.
  • the anionic polymer is water-soluble or water-dispersable.
  • the anionic polymer is preferably organic.
  • the anionic polymer according to the invention has one or more aromatic groups and the aromatic groups can be of the same or different types.
  • the aromatic group of the anionic polymer can be present in the polymer backbone or in a substituent group that is attached to the polymer backbone (main chain).
  • suitable aromatic groups include aryl, aralkyl and alkaryl groups and derivatives thereof, e.g. phenyl, tolyl, naphthyl, phenylene, xylylene, benzyl, phenylethyl and derivatives of these groups.
  • anionically charged groups that can be present in the anionic polymer as well as in the monomers used for preparing the anionic polymer include groups carrying an anionic charge and acid groups carrying an anionic charge when dissolved or dispersed in water, the groups herein collectively being referred to as anionic groups, such as phosphate, phosphonate, sulphate, sulphonic acid, sulphonate, carboxylic acid, carboxylate, alkoxide and phenolic groups, i.e. hydroxy-substituted phenyls and naphthyls.
  • Groups carrying an anionic charge are usually salts of an alkali metal, alkaline earth or ammonia.
  • suitable anionic step-growth polymers include condensation polymers, i.e. polymers obtained by step-growth condensation polymerization, e.g. condensates of an aldehyde such as formaldehyde with one or more aromatic compounds containing one or more anionic groups, and optional other co- monomers useful in the condensation polymerization such as urea and melamine.
  • suitable aromatic compounds containing anionic groups comprises benzene and naphthalene-based compounds containing anionic groups such as phenolic and naphtholic compounds, e.g. phenol, naphthol, resorcinol and derivatives thereof, aromatic acids and salts thereof, e.g.
  • phenylic, phenolic, naphthylic and naphtholic acids and salts usually sulphonic acids and sulphonates, e.g. benzene sulphonic acid and sulphonate, xylen sulphonic acid and sulphonates, naphthalene sulphonic acid and sulphonate, phenol sulphonic acid and sulphonate.
  • suitable anionic step- growth polymers according to the invention include anionic benzene-based and naphthalene-based condensation polymers, preferably naphthalene-sulphonic acid based and naphthalene-sulphonate based condensation polymers.
  • anionic step-growth polymers examples include addition polymers, i.e. polymers obtained by step-growth addition polymerization, e.g. anionic polyurethanes which can be prepared from a monomer mixture comprising aromatic isocyanates and/or aromatic alcohols.
  • suitable aromatic isocyanates include diisocyanates, e.g. toluene-2,4- and 2,6-diisocyanates and diphenyl- methane-4,4'-diisocyanate.
  • suitable aromatic alcohols include dihydric alcohols, i.e. diols, e.g.
  • the monomer mixture can also contain non- aromatic isocyanates and/or alcohols, usually diisocyanates and diols, for example any of those known to be useful in the preparation of polyurethanes.
  • suitable monomers containing anionic groups include the monoester reaction products of triols, e.g. trimethylolethane, trimethylolpropane and glycerol, with dicarboxylic acids or anhydrides thereof, e.g.
  • succinic acid and anhydride terephthalic acid and anhydride, such as glycerol monosuccinate, glycerol monoterephthalate, trimethylolpropane monosuccinate, trimethylolpropane monoterephthalate, N,N-bis-(hydroxyethyl)-glycine, di-(hydroxy- methyl)propionic acid, N,N-bis-(hydroxyethyl)-2-aminoethanesulphonic acid, and the like, optionally and usually in combination with reaction with a base, such as alkali metal and alkaline earth hydroxides, e.g. sodium hydroxide, ammonia or an amine, e.g.
  • a base such as alkali metal and alkaline earth hydroxides, e.g. sodium hydroxide, ammonia or an amine, e.g.
  • suitable anionic chain-growth polymers include anionic vinyl addition polymers obtained from a mixture of vinylic or ethylenically unsaturated monomers comprising at least one monomer having an aromatic group and at least one monomer having an anionic group, usually co-polymerized with non-ionic monomers such as acrylate- and acrylamide-based monomers.
  • suitable anionic monomers include (meth)acrylic acid and paravinyl phenol (hydroxy styrene).
  • anionic polysaccharides examples include starches, guar gums, celluloses, chitins, chitosans, glycans, galactans, glucans, xanthan gums, pectins, mannans, dextrins, preferably starches, guar gums and cellulose derivatives, suitable starches including potato, corn, wheat, tapioca, rice, waxy maize and barley, preferably potato.
  • the anionic groups in the polysaccharide can be native and/or introduced by chemical treatment.
  • the aromatic groups in the polysaccharide can be introduced by chemical methods known in the art.
  • Naturally occurring aromatic anionic polymers and modifications thereof i.e. modified naturally occurring aromatic anionic polymers, according to the invention include naturally occuring polyphenolic substances that are present in wood and organic extracts of bark of some wood species and chemical modifications thereof, usually sulphonated modifications thereof.
  • the modified polymers can be obtained by chemical processes such as, for example, sulphite pulping and kraft pulping.
  • suitable anionic polymers of this type include lignin-based polymers, preferably sulphonated lignins, e.g. ligno- sulphonates, kraft lignin, sulphonated kraft lignin, and tannin extracts.
  • the weight average molecular weight of the anionic polymer can vary within wide limits dependent on, inter alia, the type of polymer used, and usually it is at least about 500, suitably above about 2,000 and preferably above about 5,000.
  • the upper limit is not critical; it can be about 200,000,000, usually 150,000,000, suitably 100,000,000 and preferably 10,000,000.
  • the anionic polymer can have a degree of anionic substitution (DS A ) varying over a wide range dependent on, inter alia, the type of polymer used; DS A is usually from 0.01 to 2.0, suitably from 0.02 to 1.8 and preferably from 0.025 to 1.5; and the degree of aromatic substitution (DS Q ) can be from 0.001 to 1.0, usually from 0.01 to 0.8, suitably from 0.02 to 0.7 and preferably from 0.025 to 0.5.
  • the degree of cationic substitution (DS C ) can be, for example, from 0 to 0.2, suitably from 0 to 0.1 and preferably from 0 to 0.05, the anionic polymer having an overall anionic charge.
  • the anionic charge density of the anionic polymer is within the range of from 0.1 to 6.0 meqv/g of dry polymer, suitably from 0.5 to 5.0 and preferably from 1.0 to 4.0.
  • suitable anionic aromatic polymers include those described in U.S. Patent Nos. 4,070,236 and 5,755,930; and International Patent Application Publication Nos. WO 95/21295, WO 95/21296, WO 99/67310 and WO 00/49227, which are hereby incorporated herein by reference.
  • anionic and cationic polymers having aromatic groups examples include (i) cationic polysaccharides, preferably cationic starch, and anionic step-growth polymers, suitably anionic benzene-based and naphthalene-based condensation polymers and anionic polyurethanes, preferably anionic naphthalene-based condensation polymers; (ii) cationic polysaccharides, preferably cationic starch, and naturally occurring aromatic anionic polymers and modifiations thereof, suitably anionic lignin-based polymers, preferably sulphonated lignins;
  • cationic chain-growth polymers suitably cationic vinyl addition polymers, preferably cationic acrylamide-based polymers, and anionic step-growth polymers, suitably anionic benzene-based and naphthalene-based condensation polymers and anionic polyurethanes, preferably anionic naphthalene-based condensation polymers; and
  • cationic chain-growth polymers suitably cationic vinyl addition polymers, preferably cationic acrylamide-based polymers, and naturally occurring aromatic anionic polymers and modifiations thereof, suitably anionic lignin-based polymers, preferably sulphonated lignins.
  • the cationic and anionic polymers according to the invention are preferably separately added to the aqueous suspension containing cellulosic fibres, or stock, and not as a mixture containing said polymers.
  • the cationic and anionic polymers are added to the stock at different points.
  • the polymers can be added in any order. Usually the cationic polymer is firstly added to the stock and the anionic polymer is subsequently added, although the reverse order of addition may also be used.
  • the polymers can be added to the stock to be dewatered in amounts which can vary within wide limits depending on, inter alia, type of stock, salt content, type of salts, filler content, type of filler, point of addition, etc.
  • the polymers are added in an amount that give better drainage and/or retention than is obtained when not adding them and usually the cationic polymer is added to the stock prior to adding the anionic polymer.
  • the cationic polymer is usually added in an amount of at least 0.001%, often at least 0.005% by weight, based on dry stock substance, whereas the upper limit is usually 3% and suitably 2.0% by weight.
  • the anionic polymer is usually added in an amount of at least 0.001%, often at least 0.005% by weight, based on dry stock substance, whereas the upper limit is usually 3% and suitably 1.5% by weight.
  • the polymers having aromatic groups according to the invention can be used in conjunction with additional additive(s) that are beneficial to the overall drainage and/or retention performance, thereby forming drainage and retention aids comprising three or more components.
  • additional additive(s) that are beneficial to the overall drainage and/or retention performance, thereby forming drainage and retention aids comprising three or more components.
  • suitable stock additives of this type include anionic microparticulate materials, e.g., silica-based particles and clays of smectite type, low molecular weight cationic organic polymers, aluminium compounds, anionic vinyl addition polymers and combinations thereof, including the compounds and the use thereof disclosed in International Patent Application Publication Nos. WO 99/55964 and WO 99/55965, which are incorporated herein by reference.
  • LMW cationic organic polymers that can be used according to the invention include those commonly referred to as anionic trash catchers (ATC).
  • ATC anionic trash catchers
  • 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 poly- amines, polyamidoamines, polyethyleneimines, homo- and copolymers based on diallyl- dimethyl ammonium chloride, (meth)acrylamides and (meth)acrylates.
  • the molecular weight of the LMW cationic organic polymer is preferably lower; it 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 usually about 200,000.
  • Aluminium compounds that can be used according to the 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 sulphuric acid, phosphoric acid, organic acids such as citric acid and oxalic acid.
  • the process of this invention is applicable to all papermaking processes and cellulosic suspensions, and it is particularly useful in the manufacture of paper from a stock that has a high conductivity.
  • the conductivity of the stock that is dewatered on the wire is usually at least 2.0 mS/cm, suitably at least 3.5 mS/cm, and preferably at least 5.0 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) which can be derived from the materials used to form the stock, from various additives introduced into the stock, from the fresh water supplied to the process, 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.
  • salts electrophilic compounds
  • the present invention further encompasses papermaking processes where white water is extensively recycled, or recirculated, 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.
  • Recycling 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 of this invention.
  • 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 thick suspension containing cellulosic fibres to dilute it so as to form a thin suspension to be dewatered, before, simultaneous with or after mixing the suspension with white water.
  • Further additives which are conventional in papermaking can of course be used in combination with the polymers according to the invention, such as, for example, dry strength agents, wet strength agents, optical brightening agents, dyes, sizing agents like rosin-based sizing agents and cellulose-reactive sizing agents, e.g. alkyl and alkenyl ketene dimers, alkyl and alkenyl ketene multimers, and succinic anhydrides, 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 cellulosic fibre-containing 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 suspension can be based on fibres from chemical pulp such as sulphate, sulphite and organosolv pulps, mechanical pulp such as thermomechanical pulp, chemo-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.
  • chemical pulp such as sulphate, sulphite and organosolv pulps
  • mechanical pulp such as thermomechanical pulp, chemo-thermomechanical pulp, refiner pulp and groundwood pulp, from both hardwood and softwood
  • recycled fibres optionally from de-inked pulps, and mixtures thereof.
  • Example 1 Cationic polymers used in the tests were purchased on the market or prepared by generally known procedures.
  • the cationic polysaccharides used in the tests were prepared by reacting native potato starch with a quaternising agent according to the general procedure described in EP-A 0 189935 and WO 99/55964.
  • the cationic polymers used in the tests hereinafter also collectively referred to as cationic polymer, C1 to C3 according to the invention and C1-ref to C3-ref intended for comparison purposes, were the following: C1: Cationic starch obtained by quarternisation of native potato starch with 3-chloro- 2-hydroxypropyl dimethyl benzyl ammonium chloride to 0.5% N.
  • C2 Cationic starch obtained by quarternisation of native potato starch with 3-chloro-
  • C3 Cationic vinyl addition polymer prepared by polymerisation of acrylamide (90 mole%) and acryloxyethyldimethylbenzylammonium chloride (10 mole%), molecular weight about 6,000,000.
  • C1-ref Cationic starch obtained by quarternization of native potato starch with 2,3- epoxypropyl trimethyl ammonium chloride to 0.8% N.
  • C2-ref Cationic starch obtained by quarternization of native potato starch with 2,3- epoxypropyl trimethyl ammonium chloride to 0.5% N.
  • C3-ref Cationic vinyl addition polymer prepared by polymerisation of acrylamide (90 mole%) and acryloxyethyltrimethylammonium chloride (10 mole%), molecular weight about 6,000,000.
  • anionic polymers used in the tests were purchased on the market or prepared by generally known procedures.
  • the anionic polymers used in the tests hereinafter also collectively referred to as anionic polymer, A1 to A8 according to the invention and A1-ref to
  • A1 Anionic polycondensate of formaldehyde with naphthalene sulphonate, molecular weight about 20,000.
  • A2 Anionic polycondensate of formaldehyde with naphthalene sulphonate, molecular weight about 110,000.
  • A3 Anionic polycondensate of formaldehyde with naphthalene sulphonate, molecular weight about 40,000.
  • A4 Anionic polycondensate of formaldehyde with naphthalene sulphonate, molecular weight about 210,000.
  • A5 Anionic polyurethane obtained by reacting glycerol monostearate with toluene diisocyanate to form a pre-polymer containing terminal isocyanate groups which is then reacted with dimethylol propionic acid.
  • A6 Anionic polyurethane obtained by reacting phenyl diethanol amine with toluene diisocyanate to form a pre-polymer containing terminal isocyanate groups which is then reacted with dimethylol propionic acid and N-methyl diethanol amine.
  • A7 Anionic sulphonated kraft lignin.
  • A8 Anionic lignosulphonate.
  • A1-ref Anionic melamine-formaldehyde-sulphonate polycondensate.
  • A2-ref Anionic inorganic condensation polymer of silicic acid in the form of colloidal silica particles with a particle size of 5 nm.
  • a low molecular weight cationic organic polymer also referred to as ATC, which was used in some of the tests, was available on the market and producible by generally known procedures.
  • the ATC was the following:
  • ATC Cationic copolymer of dimethylamine, epichlorohydrin and ethylene diamine with a molecular weight of about 50,000.
  • Example 2 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
  • a standard stock was prepared from a furnish 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 25 g/l of a colloidal fraction, bleach water from a paper mill.
  • Stock volume was 800 ml and pH about 7.
  • Calcium chloride was added to the stock to adjust the conductivity to 0.5 mS/cm.
  • the obtained stock is referred to as standard stock. Additional amounts of calcium chloride were added to the standard stock in order to prepare a medium conductivity stock (2.0 mS/cm) and a high conductivity stock (5.0 mS/cm).
  • 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 cationic polymer to the stock following by stirring for 30 seconds, ii) adding anionic polymer to the stock followed by stirring for 15 seconds, iii) draining the stock while automatically recording the drainage time. If used, the ATC was added to the stock followed by stirring for 30 seconds prior to i) adding cationic polymer and ii) adding anionic polymer according to the procedure described above.
  • Table 1 shows the dewatering (drainage) effect at various dosages of the cationic polymer C1, calculated as dry polymer on dry stock system, and various dosages of the anionic polymers A1-ref, A1 and A2, calculated as dry polymer on dry stock system.
  • the standard stock was used in Test Nos. 1-5 and the high conductivity stock was used in Test Nos. 6-9.
  • Example 3 First pass retention was evaluated by means of a nephelometer by measuring the turbidity of the filtrate from the Dynamic Drainage Analyser (DDA), the white water, obtained by draining the stock obtained in Example 2. The results are shown in Table 2.
  • DDA Dynamic Drainage Analyser
  • Drainage performance was evaluated using the cationic and anionic polymers according to Example 1 and the medium conductivity stock and procedure according to
  • Example 7 Drainage performance was evaluated using the cationic and anionic polymers according to Example 1 and the high conductivity stock and procedure according to Example 2. The results are shown in Table 6. Table 6
  • Example 8 Drainage and retention performance was evaluated using the cationic and anionic polymers according to Example 1 and the standard conductivity stock and procedures according to Examples 2 and 3. The results are shown in Table 7.
  • Example 9 Drainage performance was evaluated using the cationic and anionic polymers and ATC according to Example 1 and the medium conductivity stock and procedure according to Example 2. The results are shown in Table 8. Table 8
  • Example 10 Drainage and retention performance was evaluated using the cationic and anionic polymers and ATC according to Example 1 and the medium conductivity stock and procedures according to Examples 2 and 3. The results are shown in Table 9.

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Abstract

La présente invention concerne un procédé de production de papier à partir d'une suspension aqueuse contenant des fibres cellulosiques, et éventuellement des charges. Ce procédé consiste à ajouter séparément à la suspension un polymère organique cationique ayant au moins un groupe aromatique et un polymère anionique ayant au moins un groupe aromatique, le polymère anionique étant sélectionné parmi des polymères à croissance étagée, des polysaccharides et des polymères aromatiques existant naturellement et leurs modifications ; à façonner et à drainer la suspension sur une toile, sachant que si le polymère anionique est un polymère à croissance étagée, il ne doit pas être un polymère à condensation de mélamine anionique et d'acide sulfonique. L'invention concerne également un procédé de production de papier à partir de fibres cellulosiques contenant une suspension aqueuse, et éventuellement des charges. Ce procédé consiste : - à ajouter séparément à la suspension un polymère organique cationique ayant au moins un groupe aromatique et un polymère anionique ayant au moins un groupe aromatique ; - à façonner et à drainer la suspension sur une toile sachant que le polymère anionique est ni un polystyrène de sulfonate anionique ni un polymère de condensation de mélamine anionique et d'acide sulfonique.
EP01958740A 2000-08-07 2001-08-02 Procede de production de papier Expired - Lifetime EP1309758B1 (fr)

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EP00850135 2000-08-07
EP00850136 2000-08-07
EP00850137 2000-08-07
EP00850135 2000-08-07
EP00850137 2000-08-07
EP00850136 2000-08-07
EP00850195 2000-11-16
EP00850195 2000-11-16
EP01958740A EP1309758B1 (fr) 2000-08-07 2001-08-02 Procede de production de papier
PCT/SE2001/001701 WO2002012626A1 (fr) 2000-08-07 2001-08-02 Procede de production de papier

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