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EP2315875B1 - Method for increasing the dry strength of paper, paperboard and cardboard - Google Patents

Method for increasing the dry strength of paper, paperboard and cardboard Download PDF

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Publication number
EP2315875B1
EP2315875B1 EP09781661.5A EP09781661A EP2315875B1 EP 2315875 B1 EP2315875 B1 EP 2315875B1 EP 09781661 A EP09781661 A EP 09781661A EP 2315875 B1 EP2315875 B1 EP 2315875B1
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units
polymer
acid
polymers
groups
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EP09781661.5A
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German (de)
French (fr)
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EP2315875A1 (en
Inventor
Hans-Joachim HÄHNLE
Christian Jehn-Rendu
Rainer Blum
Ellen KRÜGER
Norbert Schall
Martin Rübenacker
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BASF SE
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BASF SE
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Classifications

    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21HPULP 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
    • D21H21/00Non-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
    • D21H21/14Non-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
    • D21H21/18Reinforcing agents
    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21HPULP 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
    • D21H17/00Non-fibrous material added to the pulp, characterised by its constitution; Paper-impregnating material characterised by its constitution
    • D21H17/20Macromolecular organic compounds
    • D21H17/33Synthetic macromolecular compounds
    • D21H17/34Synthetic macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds
    • D21H17/37Polymers of unsaturated acids or derivatives thereof, e.g. polyacrylates
    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21HPULP 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
    • D21H17/00Non-fibrous material added to the pulp, characterised by its constitution; Paper-impregnating material characterised by its constitution
    • D21H17/20Macromolecular organic compounds
    • D21H17/33Synthetic macromolecular compounds
    • D21H17/34Synthetic macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds
    • D21H17/37Polymers of unsaturated acids or derivatives thereof, e.g. polyacrylates
    • D21H17/375Poly(meth)acrylamide
    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21HPULP 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
    • D21H17/00Non-fibrous material added to the pulp, characterised by its constitution; Paper-impregnating material characterised by its constitution
    • D21H17/20Macromolecular organic compounds
    • D21H17/33Synthetic macromolecular compounds
    • D21H17/34Synthetic macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds
    • D21H17/41Synthetic macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds containing ionic groups
    • D21H17/44Synthetic macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds containing ionic groups cationic
    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21HPULP 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
    • D21H17/00Non-fibrous material added to the pulp, characterised by its constitution; Paper-impregnating material characterised by its constitution
    • D21H17/20Macromolecular organic compounds
    • D21H17/33Synthetic macromolecular compounds
    • D21H17/46Synthetic macromolecular compounds obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds
    • D21H17/47Condensation polymers of aldehydes or ketones
    • D21H17/48Condensation polymers of aldehydes or ketones with phenols
    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21HPULP 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
    • D21H17/00Non-fibrous material added to the pulp, characterised by its constitution; Paper-impregnating material characterised by its constitution
    • D21H17/20Macromolecular organic compounds
    • D21H17/33Synthetic macromolecular compounds
    • D21H17/46Synthetic macromolecular compounds obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds
    • D21H17/54Synthetic macromolecular compounds obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds obtained by reactions forming in the main chain of the macromolecule a linkage containing nitrogen
    • D21H17/55Polyamides; Polyaminoamides; Polyester-amides
    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21HPULP 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
    • D21H17/00Non-fibrous material added to the pulp, characterised by its constitution; Paper-impregnating material characterised by its constitution
    • D21H17/20Macromolecular organic compounds
    • D21H17/33Synthetic macromolecular compounds
    • D21H17/46Synthetic macromolecular compounds obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds
    • D21H17/54Synthetic macromolecular compounds obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds obtained by reactions forming in the main chain of the macromolecule a linkage containing nitrogen
    • D21H17/56Polyamines; Polyimines; Polyester-imides

Definitions

  • the invention relates to a process for the production of paper, paperboard and cardboard with high dry strength by adding at least one cationic polymer and a polymeric anionic compound to a pulp, dewatering of the pulp under sheet formation and drying of the paper products.
  • CA patent 1 110 019 discloses a process for the production of paper with high dry strength, in which one adds to the paper material first a water-soluble cationic polymer, then dosed a water-soluble anionic polymer, then dewatered the paper stock on the paper machine with sheet formation and the paper products dried.
  • Suitable anionic polymers are, for example, hydrolyzed polyacrylamides which may have up to 30 mol% of acrylic acid units.
  • cationic polymers for example, water-soluble homo- and copolymers of cationic monomers such as vinylpyridine, vinylimidazolidine, diallylamines, ethyleneimine and basic acrylates and basic methacrylates are used.
  • the basic (meth) acrylates can each be copolymerized with acrylamide or methacrylamide.
  • These cationic polymers and also polyacrylamides can be modified to form other cationic polymers which are suitable for the process described, for example they can be subjected to a Mannich reaction or Hofmann degradation.
  • From the DE-A 35 06 832 discloses a process for the production of paper with high dry strength, in which one adds to the stock first a water-soluble cationic polymer and then a water-soluble anionic polymer.
  • Suitable anionic polymers are, for example, homopolymers or copolymers of ethylenically unsaturated C 3 -C 5 -carboxylic acids.
  • the copolymers contain at least 35 wt .-% of an ethylenically unsaturated C 3 - C 5 carboxylic acid (eg acrylic acid) in copolymerized form.
  • polyethyleneimine polyvinylamine, polydiallyldimethylammonium chloride and epichlorohydrin crosslinked condensation products of adipic acid and diethylenetriamine are described.
  • the JP-A 1999-140787 relates to a process for the production of corrugated board, wherein to improve the strength properties of a paper product to the pulp 0.05 to 0.5 wt .-%, based on dry pulp, of a polyvinylamine obtained by hydrolysis of polyvinylformamide having a degree of hydrolysis of 25 to 100 %, is added in combination with an anionic polyacrylamide, the stock is then dewatered to form sheets and the paper is dried.
  • a paper product having improved strength properties obtainable by applying to the surface of a paper product a polyvinylamine and a polymeric anionic compound which can form a polyelectrolyte complex with polyvinylamine, or a polymeric compound having aldehyde functions such as aldehyde group-containing polysaccharides.
  • a polyvinylamine and a polymeric anionic compound which can form a polyelectrolyte complex with polyvinylamine or a polymeric compound having aldehyde functions such as aldehyde group-containing polysaccharides.
  • WO 2004/061235 discloses a process for the production of paper, especially tissue, with particularly high wet and / or dry strengths, in which the paper stock is first added a water-soluble cationic polymer containing at least 1.5 meq / g of polymer to primary amino functionalities and a molecular weight of at least 10,000 daltons. Particular emphasis is placed here partially and fully hydrolyzed homopolymers of N-vinylformamide. Subsequently, a water-soluble anionic polymer is added which contains anionic and / or aldehydic groups.
  • WO 2006/120235 describes a process for producing papers having a filler content of at least 15% by weight, in which filler and fibers are treated together with cationic and anionic polymers, the treatment taking place alternately with cationic and anionic polymers and comprising at least 3 steps.
  • the invention has for its object to provide a further process for the production of paper, paperboard and cardboard with high dry strength available, the dry strength properties of the paper products compared to those of known products are further improved as possible. Another object of the invention is to achieve faster dewatering of the stock compared to known methods.
  • Examples of monomers of the formula I are N-vinylformamide, N-vinyl-N-methylformamide, N-vinylacetamide, N-vinyl-N-methylacetamide, N-vinyl-N-ethylacetamide, N-vinylpropionamide and N-vinyl-N-methylpropionamide and N-vinylbutyramide.
  • the monomers of group (i) can be used alone or mixed in the copolymerization with the monomers of the other groups.
  • Preferably used monomer of this group is N-vinylformamide.
  • These polymers may optionally be modified by copolymerizing the N-vinylcarboxamides (i) together with (ii) at least one other monoethylenically unsaturated monomer and then hydrolyzing the copolymers to form amino groups. If anionic monomers are used in the copolymerization, the hydrolysis of the copolymerized vinylcarboxamide units is carried out so far that the molar excess of amine units compared to the anionic units in the polymer is at least 5 mol%.
  • Examples of monomers of group (ii) are esters of ⁇ , ⁇ -ethylenically unsaturated mono- and dicarboxylic acids with C 1 -C 30 -alkanols, C 2 -C 30 -alkanediols and C 2 -C 30 -aminoalcohols, amides of ⁇ , ⁇ -ethylenically unsaturated monocarboxylic acids and their N-alkyl and N, N-dialkyl derivatives, nitriles of ⁇ , ⁇ -ethylenically unsaturated mono- and dicarboxylic acids, esters of vinyl alcohol and allyl alcohol with C 1 -C 30 monocarboxylic acids, N-vinyl lactams, nitrogen-containing Heterocycles with ⁇ , ⁇ -ethylenically unsaturated double bonds, vinyl aromatics, vinyl halides, vinylidene halides, C 2 -C 8 monoolefins and mixtures thereof
  • Suitable representatives are, for example, methyl (meth) acrylate (this notation symbolizes both "acrylates” and “methacrylates” here as well as in the following text), methyl methacrylate, Ethyl (meth) acrylate, ethyl ethacrylate, n-butyl (meth) acrylate, isobutyl (meth) acrylate, tert-butyl (meth) acrylate, tert-butyl methacrylate, n-o-cytriethyl (meth) acrylate, 1,1,3, 3-Tetramethylbutyl (meth) acrylate, ethylhexyl (meth) acrylate and mixtures thereof.
  • Suitable additional monomers of group (ii) are furthermore the esters of ⁇ , ⁇ -ethylenically unsaturated mono- and dicarboxylic acids with aminoalcohols, preferably C 2 -C 12 -aminoalcohols. These may be C 1 -C 8 -monoalkylated or -dialkylated on the amine nitrogen.
  • the acid component of these esters are z.
  • Preference is given to using acrylic acid, methacrylic acid and mixtures thereof.
  • N-methylaminomethyl (meth) acrylate N-methylaminoethyl (meth) acrylate, N, N-dimethylaminomethyl (meth) acrylate, N, N-dimethylaminoethyl (meth) acrylate, N, N-diethylaminoethyl (meth) acrylate, N , N-dimethylaminopropyl (meth) acrylate, N, N-diethylaminopropyl (meth) acrylate and N, N-dimethylaminocyclohexyl (meth) acrylate.
  • Suitable monomers of group (ii) are 2-hydroxyethyl (meth) acrylate, 2-hydroxyethyl methacrylate, 2-hydroxypropyl (meth) acrylate, 3-hydroxypropyl (meth) acrylate, 3-hydroxybutyl (meth) acrylate, 4-hydroxybutyl ( meth) acrylate, 6-hydroxyhexyl (meth) acrylate and mixtures thereof.
  • Suitable monomers of group (ii) are acrylamide, methacrylamide, N-methyl (meth) acrylamide, N-ethyl (meth) acrylamide, n-propyl (meth) acrylamide, N- (n-butyl) (meth) acrylamide, tert-butyl (meth) acrylamide, n-octyl (meth) acrylamide, 1,1,3,3-tetramethylbutyl (meth) acrylamide, ethylhexyl (meth) acrylamide and mixtures thereof.
  • monomers of group (ii) are nitriles of ⁇ , ⁇ -ethylenically unsaturated mono- and dicarboxylic acids such as, for example, acrylonitrile and methacrylonitrile.
  • the presence of units of these monomers in the copolymer leads during or after the hydrolysis to products which have amidine units, cf. eg EP-A 0 528 409 or DE-A 43 28 975 , Namely, in the hydrolysis of N-vinylcarboxylic acid amide polymers, amidine units are formed in a secondary reaction by reacting vinylamine units with an adjacent vinylformamide unit or, if a nitrile group is present as an adjacent group in the polymer.
  • the indication of vinylamine units in the amphoteric Copolymers or in unmodified homo- or copolymers always the sum of vinylamine and amidine units.
  • Suitable monomers of group (ii) are furthermore N-vinyllactams and derivatives thereof which, for. B. one or more C 1 -C 6 alkyl substituents (as defined above) may have.
  • N-vinylpyrrolidone N-vinylpiperidone, N-vinylcaprolactam, N-vinyl-5-methyl-2-pyrrolidone, N-vinyl-5-ethyl-2-pyrrolidone, N-vinyl-6-methyl-2-piperidone, N-vinyl-6-ethyl-2-piperidone, N-vinyl-7-methyl-2-caprolactam, N-vinyl-7-ethyl-2-caprolactam and mixtures thereof.
  • suitable monomers of group (ii) are N-vinylimidazoles and alkylvinylimidazoles, in particular methylvinylimidazoles such as 1-vinyl-2-methylimidazole, 3-vinylimidazoleN-oxide, 2- and 4-vinylpyridine N-oxides and betaine derivatives and quaternization products of these monomers and ethylene, propylene, isobutylene, butadiene, styrene, ⁇ -methylstyrene, vinyl acetate, vinyl propionate, vinyl chloride, vinylidene chloride, vinyl fluoride, vinylidene fluoride and mixtures thereof.
  • methylvinylimidazoles such as 1-vinyl-2-methylimidazole, 3-vinylimidazoleN-oxide, 2- and 4-vinylpyridine N-oxides and betaine derivatives and quaternization products of these monomers and ethylene, propylene, isobutylene, butad
  • the aforementioned monomers can be used individually or in the form of any mixtures. Typically, they are used in amounts of 1 to 90 mol%, preferably 10 to 80 mol% and particularly preferably 10 to 60 mol%.
  • amphoteric Copoylmerisaten come as other monoethylenically unsaturated monomers of group (ii) also anionic monomers into consideration, which are referred to above as monomers (ii, a). They may optionally be copolymerized with the neutral and / or cationic monomers (ii, b) described above. However, the amounts of anionic monomers (ii, a) is at most 45 mol%, so that the resulting amphoteric copolymer has a total cationic charge.
  • anionic monomers of group (ii, a) are ethylenically unsaturated C 3 to C 8 carboxylic acids such as acrylic acid, methacrylic acid, dimethacrylic acid, ethacrylic acid, maleic acid, fumaric acid, itoconic acid, mesaconic acid, citraconic acid, methylenemalonic acid, allylacetic acid, vinylacetic acid and crotonic acid.
  • monomers containing sulfo groups such as vinylsulfonic acid, acrylamido-2-methylpropanesulfonic acid and styrenesulfonic acid, and monomers containing phosphono groups, such as vinylphosphonic acid.
  • the monomers of this group can be used alone or in admixture with each other, in partially or completely neutralized form in the copolymerization.
  • neutralization for example, alkali metal or alkaline earth metal bases, ammonia, amines and / or alkanolamines are used. Examples of these are sodium hydroxide solution, potassium hydroxide solution, soda, potash, sodium bicarbonate, magnesium oxide, calcium hydroxide, calcium oxide, Triethanolamine, ethanolamine, morpholine, diethylenetriamine or tetraethylenepentamine.
  • a further modification of the copolymers is possible by using in the copolymerization monomers of group (iii) which contain at least two double bonds in the molecule, for. B. triallylamine, methylenebisacrylamide, glycol diacrylate, glycol dimethacrylate, glycerol triacrylate, pentaerythritol triallyl ether, at least two times with acrylic acid and / or methacrylic acid esterified polyalkylene glycols or polyols such as pentaerythritol, Sobit or glucose. If at least one monomer of the above group is used in the polymerization, the amounts used are up to 2 mol%, e.g. B. 0.001 to 1 mol%.
  • regulators are typically used 0.001 to 5 mol%. All regulators known in the literature can be used, eg. For example, sulfur compounds such as mercaptoethanol, 2-Ethylhexylthioglycolat, thioglycolic acid and dodecyl mercaptan and sodium hypophosphite, formic acid or Tribromchlormethan.
  • the polymers containing vinylamine units also include hydrolyzed graft polymers of, for example, N-vinylformamide on polyalkylene glycols, polyvinyl acetate, polyvinyl alcohol, polyvinylformamides, polysaccharides such as starch, oligosaccharides or monosaccharides.
  • the graft polymers are obtainable by free-radically polymerizing, for example, N-vinylformamide in aqueous medium in the presence of at least one of the stated grafting bases together with copolymerizable other monomers and then hydrolyzing the grafted vinylformamide units in a known manner to give vinylamine units.
  • the hydrolysis of the copolymers can be carried out in the presence of acids or bases or else enzymatically.
  • the vinylamine groups formed from the vinylcarboxamide units are present in salt form.
  • the hydrolysis of vinylcarboxylic acid amide copolymers is described in U.S. Pat EP-A 0 438 744 , Page 8, line 20 to page 10, line 3, described in detail.
  • the explanations made there apply correspondingly to the preparation of the cationic and / or amphoteric polymers containing vinylamine units to be used according to the invention and having a total cationic charge.
  • the polymers containing vinylamine units can also be used in the form of the free bases in the process according to the invention. Such polymers are useful, for example, in the hydrolysis of polymers containing vinylcarboxylic acid units with bases.
  • the polymers containing vinylamine units have, for example, K values (determined according to H. Fikentscher in 5% strength aqueous sodium chloride solution at pH 7, a polymer concentration of 0.5% by weight and a temperature of 25 ° C.) in the range from 20 to 250 , preferably 50 to 150.
  • the preparation of the homopolymers and copolymers containing vinylamine units described above can be carried out by solution, precipitation, suspension or emulsion polymerization. Preference is given to solution polymerization in aqueous media. Suitable aqueous media are water and mixtures of water and at least one water-miscible solvent, e.g. As an alcohol such as methanol, ethanol, n-propanol or isopropanol.
  • the cationic polymers are water-soluble.
  • the charge density of the cationic polymers (without counterions) is for example at least 1.0 meq / g and is preferably in the range of 4 to 10 meq / g.
  • polymers containing vinylamine units the reaction products which are obtainable by Hofmann degradation of homopolymers or copolymers of acrylamide or methacrylamide in an aqueous medium in the presence of sodium hydroxide solution and sodium hypochlorite and subsequent decarboxylation of the carbamate groups of the reaction products in the presence of an acid are also suitable .
  • Such polymers are for example made EP-A 0 377 313 and WO 2006/075115 known.
  • the preparation of polymers containing vinylamine groups is described, for example, in WO 2006/075115 , Page 4, line 25 to page 10, line 22 and in the examples on pages 13 and 14 are treated in detail.
  • acrylamide and / or methacrylamide units are homopolymers or copolymers of acrylamide and methacrylamide.
  • Suitable comonomers are, for example, dialkylaminoalkyl (meth) acrylamides, diallylamine, methyldiallylamine and also the salts of the amines and the quaternized amines.
  • Dimethyldiallylammonium salts acrylamidopropyltrimethylammonium chloride and / or Methacrylamidopropyltrimethylammoniumchlorid
  • N-vinylformamide N-vinylacetamide
  • N-vinylpyrrolidone vinyl acetate
  • acrylic and methacrylic acid esters Dimethyldiallylammonium salts, acrylamidopropyltrimethylammonium chloride and / or Methacrylamidopropyltrimethylammoniumchlorid, N-vinylformamide, N-vinylacetamide, N-vinylpyrrolidone, vinyl acetate and acrylic and methacrylic acid esters.
  • comonomers are optionally also anionic monomers such as acrylic acid, methacrylic acid, maleic anhydride, maleic acid, itaconic acid, acrylamidomethylpropanesulfonic acid, methallylsulfonic acid and vinylsulfonic acid and the alkali metal, Erdalkylimetall- and Ammonium salts of said acidic monomers into consideration, wherein not more than 5 mol% of these monomers are used in the polymerization.
  • the amount of water-insoluble monomers is chosen in the polymerization so that the resulting polymers are soluble in water.
  • comonomers may also be used crosslinkers, for. B. ethylenically unsaturated monomers containing at least two double bonds in the molecule such as triallylamine, methylenebisacrylamide, ethylene glycol diacrylate, ethylene glycol dimethacrylate, polyethylene glycol dimethacrylate, triallylamine and trimethylol trimethacrylate. If a crosslinker is used, the amounts used are, for example, 5 to 5000 ppm.
  • the polymerization of the monomers can be carried out by any known method, for. B. by free-radical initiated solution, precipitation or suspension polymerization. If appropriate, it is possible to work in the presence of customary polymerization regulators.
  • Hofmann degradation is for example from 20 to 40 wt .-% aqueous solutions of at least one acrylamide and / or methacrylamide units containing polymers.
  • the ratio of alkali metal hypochlorite to (meth) acrylamide units in the polymer is decisive for the resulting content of amine groups in the polymer.
  • the molar ratio of alkyl metal hydroxide to alkyl metal hypochlorite is, for example, 2 to 6, preferably 2 to 5.
  • the amount of alkali metal hydroxide required for the degradation of the polymer is calculated.
  • the Hofmann degradation of the polymer takes place z.
  • the aqueous reaction solution is passed into a reactor in which an acid is introduced for the decarboxylation of the reaction product.
  • the pH of the reaction product containing vinylamine units is adjusted to a value of 2 to 7.
  • the concentration of the decomposition products containing vinylamine units is, for example, more than 3.5% by weight, in most cases above 4.5% by weight.
  • the aqueous polymer solutions can be concentrated for example by means of ultrafiltration.
  • the polymers containing ethyleneimine units include all polymers obtainable by polymerization of ethyleneimine in the presence of acids, Lewis acids or haloalkanes, such as homopolymers of ethyleneimine or graft polymers of ethyleneimine, cf. US 2,182,306 or in US 3,203,910 , If desired, these polymers can subsequently be subjected to crosslinking. As crosslinkers z. B.
  • multifunctional epoxides such as bisglycol ethers of oligo- or polyethyleneoxides or other multifunctional alcohols such as glycerol or sugars, multifunctional carboxylic acid esters, mulifunctional isocyanates, polyfunctional acrylic or methacrylic acid esters, multifunctional acrylic or methacrylic acid amides, epichlorohydrin, multifunctional acid halides, multifunctional nitriles, ⁇ , ⁇ -chlorohydrin ethers of oligo- or polyethylene oxides or of other multifunctional alcohols such as glycerol or sugars, divinyl sulfone, maleic anhydride or ⁇ -halocarboxylic acid chlorides, multifunctional haloalkanes in particular ⁇ , ⁇ -dichloroalkanes.
  • Other crosslinkers are in WO 97/25367 , Pages 8 to 16 described.
  • polymers containing ethyleneimine units are made EP-A-0411400 . DE 2434816 and US 4,066,494 known.
  • a method for producing such compounds is, for example, in DE-A-2434816 wherein ⁇ , ⁇ -chlorohydrin ethers of oligo- or polyethylene oxides are used as crosslinkers application.
  • Reaction products of polyethylenimines with monobasic carboxylic acids to amidated polyethylenimines are known from the WO 94/12560 known.
  • Michael addition products of polyethyleneimines with ethylenically unsaturated acids, salts, esters, amides or nitriles of monoethylenically unsaturated carboxylic acids are the subject of WO 94/14873 , Phosphonomethylated polyethylenimines are described in detail in U.S. Pat WO 97/25367 described.
  • Carboxylated polyethyleneimines are obtainable, for example, by means of a plug synthesis by reacting polyethyleneimines with formaldehyde and ammonia / hydrogen cyanide and hydrolysing the reaction products.
  • Alkoxylated polyethyleneimines can be prepared by reacting Polyethyleiminen with alkylene oxides such as ethylene oxide and / or propylene oxide.
  • the polymers containing ethyleneimine units have, for example, molecular weights of from 10,000 to 3,000,000.
  • the cationic charge of the polymers containing ethyleneimine units is e.g. at least 4 meq / g. It is usually in the range of 8 to 20 meq / g.
  • the weight ratio of polymers containing (a) vinylamine units to polymers containing (b) ethyleneimine units in the process of the present invention is, for example, 10: 1 to 1:10, preferably 5: 1 to 1: 5.
  • the combination of polymers containing ethyleneimine units and polymers containing vinylamine units used in the inventive method for producing paper for example in an amount of 0.01 to 2.0 wt .-%, preferably 0.1 to 1.0 wt .-%, based on dry pulp.
  • Suitable monomers of group (1.1) are compounds which have an organic radical having a polymerizable, ⁇ , ⁇ -ethylenically unsaturated double bond and at least one sulfonic acid or phosphonic acid group per molecule. Also suitable are the salts and esters of the aforementioned compounds. The esters of phosphonic acids may be mono- or diesters. Suitable monomers (1.1) are furthermore esters of phosphoric acid with alcohols having a polymerizable, ⁇ , ⁇ -ethylenically unsaturated double bond. In this case, a proton of the phosphoric acid group or the other two protons of the phosphoric acid group can be neutralized by suitable bases or esterified with alcohols which have no polymerizable double bonds.
  • Suitable bases for the partial or complete neutralization of the acid groups of the monomers (1.1) are, for example, alkali metal or alkaline earth metal bases, ammonia, amines and / or alkanolamines. Examples of these are sodium hydroxide, potassium hydroxide, sodium carbonate, potassium carbonate, sodium hydrogencarbonate, potassium hydrogencarbonate, magnesium hydroxide, magnesium oxide, calcium hydroxide, calcium oxide, triethanolamine, ethanolamine, morpholine, diethylenetriamine or tetraethylenepentamine.
  • Suitable alcohols for the esterification of phosphoric acid are, for example, C 1 -C 6 -alkanols, such as, for example, methanol, ethanol, n-propanol, isopropanol, n-butanol, sec-butanol, tert-butanol, n-pentanol, n-hexanol and their isomers.
  • component (1.1) exclusively monomers in which all protons of the acid groups are esterified, such as.
  • component (1.2) at least one monoethylenically unsaturated mono- and / or dicarboxylic acid or a salt thereof is used for the polymerization, as described below as component (1.2). This ensures that the copolymers used according to the invention have anionic groups.
  • the abovementioned monomers (1.1) can be used individually or in the form of any desired mixtures in the preparation of the anionic polymers.
  • Suitable monomers of group (1.2) are monoethylenically unsaturated carboxylic acids having 3 to 8 carbon atoms and the water-soluble salts such as alkali metal, alkaline earth metal or ammonium salts of these carboxylic acids and the monoethylenically unsaturated carboxylic acid anhydrides.
  • This group of monomers includes, for example, acrylic acid, methacrylic acid, dimethacrylic acid, ethacrylic acid, ⁇ -chloroacrylic acid, maleic acid, maleic anhydride, fumaric acid, itaconic acid, mesaconic acid, citraconic acid, glutaconic acid, aconitic acid, methylenemalonic acid, allylacetic acid, vinylacetic acid and crotonic acid.
  • the monomers of group (1.2) can be used alone or mixed with each other, in partially or completely neutralized form in the homo- or copolymerization. Suitable bases for neutralization are the compounds mentioned above in component (1.1).
  • the water-soluble anionic polymer contains at least one monomer from the group (1) which is selected from the subgroups (1.1) and / or (1.2).
  • the water-soluble copolymer may also contain mixtures of monomers from subgroups (1.1) and (1.2) in copolymerized form.
  • the copolymers may contain at least one further monomer of group (2) in copolymerized form for modification.
  • These monomers are preferably selected from esters of ⁇ , ⁇ -ethylenically unsaturated mono- and dicarboxylic acids with C 1 -C 30 -alkanols, C 2 -C 30 -alkanediols and C 2 -C 30 -aminoalcohols, amides of ⁇ , ⁇ -ethylenically unsaturated monocarboxylic acids and their N-alkyl and N, N-dialkyl derivatives, esters of vinyl alcohol and allyl alcohol with C 1 -C 30 monocarboxylic acids, N-vinyl lactams, nitrogen-containing heterocycles having ⁇ , ⁇ -ethylenically unsaturated double bonds, vinyl aromatics, vinyl halides, vinylidene halides, C 2 C 8 monoolefins and mixtures thereof.
  • Suitable representatives of group (2) are z. Methyl (meth) acrylate, methyl methacrylate, ethyl (meth) acrylate, ethyl methacrylate, n-butyl (meth) acrylate, isobutyl (meth) acrylate, tert-butyl (meth) acrylate, tert-butyl methacrylate, n-ocytl ( meth) acrylate, 1,1,3,3-tetramethylbutyl (meth) acrylate, ethylhexyl (meth) acrylate and mixtures thereof.
  • Suitable additional monomers (2) are furthermore acrylic acid amide, methacrylamide, N-methyl (meth) acrylamide, N-ethyl (meth) acrylamide, n-propyl (meth) acrylamide, N- (n-butyl) (meth) acrylamide, tert. Butyl (meth) acrylamide, n-octyl (meth) acrylamide, 1,1,3,3-tetramethylbutyl (meth) acrylamide, ethylhexyl (meth) acrylamide and mixtures thereof.
  • 2-hydroxyethyl (meth) acrylate, 2-hydroxyethyl methacrylate, 2-hydroxypropyl (meth) acrylate, 3-hydroxypropyl (meth) acrylate, 3-hydroxybutyl (meth) acrylate, 4-hydroxybutyl (meth) are suitable.
  • Suitable monomers of group (2) are nitriles of ⁇ , ⁇ -ethylenically unsaturated mono- and dicarboxylic acids, such as, for example, acrylonitrile and methacrylonitrile.
  • Suitable monomers of group (2) are also N-vinyl lactams and derivatives thereof, the z. B. one or more C 1 -C 6 alkyl substituents (as defined above) may have. These include N-vinylpyrrolidone, N-vinylpiperidone, N-vinylcaprolactam, N-vinyl-5-methyl-2-pyrrolidone, N-vinyl-5-ethyl-2-pyrrolidone, N-vinyl-6-methyl-2-piperidone, N-vinyl-6-ethyl-2-piperidone, N-vinyl-7-methyl-2-caprolactam, N-vinyl-7-ethyl-2-caprolactam and mixtures thereof.
  • Suitable monomers of group (2) are ethylene, propylene, isobutylene, butadiene, styrene, ⁇ -methylstyrene, vinyl acetate, vinyl propionate, vinyl chloride, vinylidene chloride, vinyl fluoride, vinylidene fluoride and mixtures thereof.
  • the aforementioned monomers of group (2) can be used in the copolymerization with at least one anionic monomer, individually or in the form of any mixtures.
  • a further modification of the copolymers is possible by using in the copolymerization monomers of group (3) which contain at least two double bonds in the molecule, for.
  • group (3) which contain at least two double bonds in the molecule
  • methylenebisacrylamide glycol diacrylate, glycol dimethacrylate, glycerol triacrylate, pentaerythritol triallyl ether, at least two times with acrylic acid and / or methacrylic acid esterified polyalkylene glycols or polyols such as pentaerythritol, soba or glucose.
  • the amounts used are up to 2 mol%, z. B. 0.001 to 1 mol%.
  • regulators in the polymerization.
  • All known literature can be used Regulators such as mercaptoethanol, 2-ethylhexyl thioglycolate, thioglycolic acid, dodecyl mercaptan, sodium hypophosphite, formic acid and / or tribromochloromethane.
  • the anionic polymeric compound used is preferably homopolymers of ethylenically unsaturated C 3 - to C 5 -carboxylic acids, in particular polyacrylic acid and polymethacrylic acid, and also hydrolyzed homopolymers of maleic anhydride and of itaconic anhydride.
  • Preferred anionic copolymers comprise, for example, (1) 10 to 99% by weight of at least one ethylenically unsaturated C 3 to C 5 carboxylic acid and (2) 90 to 1% by weight of at least one amide, nitrile and / or one Esters of an ethylenically unsaturated C 3 - to C 5 -carboxylic acid in copolymerized form.
  • copolymers of acrylic acid and acrylamide Copoylmerisate of acrylic acid and acrylonitrile
  • copolymers of acrylic acid and N-vinylformamide copolymers of methacrylic acid and methacrylamide, copolymers of Methacrylic acid and N-vinylformamide
  • copolymers of acrylic acid and methacrylamide copolymers of acrylic acid and methacrylonitrile
  • copolymers of methacrylic acid and methacrylonitrile copolymers of methacrylic acid and methacrylonitrile and copolymers of acrylic acid, acrylamide and acrylonitrile.
  • the anionic polymers are water-soluble. They can be used in the form of the free acids and / or as alkali metal, alkaline earth metal or ammonium salt in the process according to the invention. They have, for example, a K value of 50 to 250 (determined according to H. Fikentscher in 5% strength by weight aqueous sodium chloride solution at 25 ° C. and pH 7).
  • the water-soluble anionic polymer is used in the process according to the invention in an amount of, for example, from 0.01 to 2.0% by weight, preferably from 0.05 to 1.0% by weight, in particular from 0.1 to 0.5% by weight. %, based on dry pulp, used.
  • the weight ratio of cationic polymers (a) polymers containing vinylamine units and (b) polymers containing ethyleneimine units to the water-soluble polymeric anionic compounds is for example 3: 1 to 1: 3 and is preferably 1: 1.
  • the pulps used for producing the pulps are all grades which are customary for this purpose, for example wood pulp, bleached and unbleached pulp and paper pulp from all annual plants.
  • Wood pulp includes, for example, groundwood, thermomechanical pulp (TMP), chemothermomechanical pulp (CTMP), pressure groundwood, semi-pulp, high yield pulp, and refiner mechanical pulp (RMP).
  • TMP thermomechanical pulp
  • CMP chemothermomechanical pulp
  • RMP refiner mechanical pulp
  • pulp for example, sulphate, sulphite and soda pulps come into consideration.
  • unbleached pulp also referred to as unbleached kraft pulp
  • Suitable annual plants For example, rice, wheat, sugar cane and kenaf are used to make paper stocks.
  • the inventive method is particularly suitable for the production of dry-proof papers from waste paper (comprising deinked waste paper), which is used either alone or in admixture with other fibers. It is also possible to start with fiber blends of a primary material and recycled coated broke, e.g. B. bleached pine sulfate in admixture with recycled coated broke.
  • the inventive method is for the production of paper, cardboard and cardboard from waste paper and in special cases from deinked waste paper of technical interest, because it significantly increases the strength properties of the recycled fibers. It is of particular importance for improving the strength properties of graphic papers and packaging papers.
  • the pH of the stock suspension is, for example, in the range of 4.5 to 8, most 6 to 7.5.
  • an acid such as sulfuric acid or aluminum sulphate.
  • the cationic polymers namely (a) polymers comprising vinylamine units and polymers containing ethyleneimine units, are preferably first metered into the pulp.
  • the cationic polymers can be added to the thick material (fiber concentration> 15 g / l, for example in the range from 25 to 40 g / l up to 60 g / l) or preferably to a thin material (fiber concentration ⁇ 15 g / l, eg in in the range of 5 to 12 g / l).
  • the point of addition is preferably in front of the screens, but it can also be between a shearing stage and a screen or afterwards.
  • the dosage of the cationic polymers (a) and (b) to the paper stock can be carried out, for example, successively, simultaneously or else as a mixture of (a) and (b).
  • the anionic component is usually added only after the addition of the cationic polymers (a) and (b) to the paper stock, but can also be metered simultaneously to the stock, but separately from the cationic polymers. Furthermore, it is also possible first to add the anionic and subsequently the cationic component or first to meter one of the cationic components (a) or (b) to the paper stock, then to add the anionic polymer and then to add the other cationic component.
  • the process chemicals commonly used in papermaking can be used in the usual amounts, for.
  • dehydrating agents other dry strength such as Starch, pigments, fillers, optical brighteners, defoamers, biocides and paper dyes.
  • the process according to the invention gives dry-proof papers whose dry strength relative to papers produced by known processes has an increased dry strength.
  • the dewatering rate is improved in comparison with known methods.
  • the percentages in the examples are by weight unless otherwise specified.
  • the K value of the polymers was after Fikentscher, Cellulose Chemie, Vol. 13, 58-64 and 71-74 (1932 ) at a temperature of 25 ° C in 5 wt .-% aqueous saline solutions at a pH of 7 and a polymer concentration of 0.5%.
  • a paper made of 100% waste paper (mixture of the grades: 1.02, 1.04,4.01) was pitched with drinking water at a consistency of 4% in a laboratory pulper without specks and ground in a laboratory refiner to a freeness of 40 ° SR. This substance was then diluted with drinking water to a consistency of 0.7%.
  • the polymers listed in the table were added successively to the above-described paper stock with stirring.
  • the polymer concentration of the aqueous solutions of cationic and anionic polymers was 1% each.
  • the amounts of polymers used in each case are given in percent by weight, based on the solids content of the paper stock.

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Description

Die Erfindung betrifft ein Verfahren zur Herstellung von Papier, Pappe und Karton mit hoher Trockenfestigkeit durch Zugabe mindestens eines kationischen Polymeren und einer polymeren anionischen Verbindung zu einem Papierstoff, Entwässern des Papierstoffs unter Blattbildung und Trocknen der Papierprodukte.The invention relates to a process for the production of paper, paperboard and cardboard with high dry strength by adding at least one cationic polymer and a polymeric anionic compound to a pulp, dewatering of the pulp under sheet formation and drying of the paper products.

Aus dem CA-Patent 1 110 019 ist ein Verfahren zur Herstellung von Papier mit hoher Trockenfestigkeit bekannt, bei dem man zum Papierstoff zunächst ein wasserlösliches kationisches Polymerisat zugibt, danach ein wasserlösliches anionisches Polymerisat dosiert, anschließend den Papierstoff auf der Papiermaschine unter Blattbildung entwässert und die Papierprodukte trocknet. Als anionische Polymerisate kommen beispielsweise hydrolysierte Polyacrylamide in Betracht, die bis zu 30 Mol-% Acrylsäure-Einheiten aufweisen können. Als kationische Polymere werden beispielsweise wasserlösliche Homo- und Copolymerisate von kationischen Monomeren wie Vinylpyridin, Vinylimidazolidin, Diallylamine, Ethylenimin sowie basische Acrylate und basische Methacrylate eingesetzt. Die basischen (Meth)acrylate können jeweils mit Acrylamid oder Methacrylamid copolymerisiert werden. Diese kationischen Polymeren sowie Polyacrylamide können zu weiteren, für das beschriebene Verfahren geeigneten kationischen Polymeren modifiziert werden, beispielsweise kann man sie einer Mannich-Reaktion oder einem Hofmann-Abbau unterwerfen.From the CA patent 1 110 019 discloses a process for the production of paper with high dry strength, in which one adds to the paper material first a water-soluble cationic polymer, then dosed a water-soluble anionic polymer, then dewatered the paper stock on the paper machine with sheet formation and the paper products dried. Suitable anionic polymers are, for example, hydrolyzed polyacrylamides which may have up to 30 mol% of acrylic acid units. As cationic polymers, for example, water-soluble homo- and copolymers of cationic monomers such as vinylpyridine, vinylimidazolidine, diallylamines, ethyleneimine and basic acrylates and basic methacrylates are used. The basic (meth) acrylates can each be copolymerized with acrylamide or methacrylamide. These cationic polymers and also polyacrylamides can be modified to form other cationic polymers which are suitable for the process described, for example they can be subjected to a Mannich reaction or Hofmann degradation.

Aus der DE-A 35 06 832 ist ein Verfahren zur Herstellung von Papier mit hoher Trockenfestigkeit bekannt, bei dem man zum Papierstoff zunächst ein wasserlösliches kationisches Polymerisat und anschließend ein wasserlösliches anionisches Polymerisat zugibt. Als anionische Polymerisate kommen beispielsweise Homo- oder Copolymerisate von ethylenisch ungesättigten C3 - C5-Carbonsäuren in Betracht. Die Copolymerisate enthalten mindestens 35 Gew.-% einer ethylenisch ungesättigten C3 - C5-Carbonsäure (z.B. Acrylsäure) einpolymerisiert. Als kationische Polymerisate werden in den Beispielen Polyethylenimin, Polyvinylamin, Polydiallyldimethylammoniumchlorid und mit Epichlorhydrin vernetzte Kondensationsprodukte aus Adipinsäure und Diethylentriamin beschrieben. Auch die Verwendung von partiell hydrolysierten Homo- und Copolymerisaten des N-Vinylformamids ist in Betracht gezogen worden.From the DE-A 35 06 832 discloses a process for the production of paper with high dry strength, in which one adds to the stock first a water-soluble cationic polymer and then a water-soluble anionic polymer. Suitable anionic polymers are, for example, homopolymers or copolymers of ethylenically unsaturated C 3 -C 5 -carboxylic acids. The copolymers contain at least 35 wt .-% of an ethylenically unsaturated C 3 - C 5 carboxylic acid (eg acrylic acid) in copolymerized form. As cationic polymers in the examples polyethyleneimine, polyvinylamine, polydiallyldimethylammonium chloride and epichlorohydrin crosslinked condensation products of adipic acid and diethylenetriamine are described. The use of partially hydrolyzed homo- and copolymers of N-vinylformamide has also been considered.

Die JP-A 1999-140787 betrifft ein Verfahren zur Herstellung von Wellpappe, wobei man zur Verbesserung der Festigkeitseigenschaften eines Papierprodukts zum Papierstoff 0,05 bis 0,5 Gew.-%, bezogen auf trockenen Papierstoff, eines Polyvinylamins, das durch Hydrolyse von Polyvinylformamid mit einem Hydrolysegrad von 25 bis 100 % zugänglich ist, in Kombination mit einem anionischen Polyacrylamid zugibt, den Papierstoff dann unter Blattbildung entwässert und das Papier trocknet.The JP-A 1999-140787 relates to a process for the production of corrugated board, wherein to improve the strength properties of a paper product to the pulp 0.05 to 0.5 wt .-%, based on dry pulp, of a polyvinylamine obtained by hydrolysis of polyvinylformamide having a degree of hydrolysis of 25 to 100 %, is added in combination with an anionic polyacrylamide, the stock is then dewatered to form sheets and the paper is dried.

Aus der WO 03/052206 ist ein Papierprodukt mit verbesserten Festigkeitseigenschaften bekannt, dass dadurch erhältlich ist, dass man auf die Oberfläche eines Papierprodukts ein Polyvinylamin und eine polymere anionische Verbindung, die mit Polyvinylamin einen Polyelektrolytkomplex bilden kann, oder eine polymere Verbindung mit Aldehydfunktionen wie Aldehydgruppen enthaltende Polysaccharide aufbringt. Man erhält nicht nur eine Verbesserung der Trocken- und Nassfestigkeit des Papiers, sondern beobachtet auch eine Leimungswirkung der Behandlungsmittel.From the WO 03/052206 For example, there is known a paper product having improved strength properties obtainable by applying to the surface of a paper product a polyvinylamine and a polymeric anionic compound which can form a polyelectrolyte complex with polyvinylamine, or a polymeric compound having aldehyde functions such as aldehyde group-containing polysaccharides. Not only does the paper improve its dry and wet strength, it also observes a sizing effect of the treating agents.

Aus der WO 2004/061235 ist ein Verfahren zur Herstellung von Papier, insbesondere Tissue, mit besonders hohen Naß- und/oder Trockenfestigkeiten bekannt, bei dem man zum Papierstoff zunächst ein wasserlösliches kationisches Polymerisat zugibt, dass mindestens 1,5 meq/g Polymer an primären Aminofunktionalitäten enthält und ein Molekulargewicht von wenigstens 10.000 Dalton aufweist. Besonders hervorgehoben werden hierbei partiell- und vollhydrolysierte Homopolymerisate des N-Vinylformamids. Anschließend wird ein wasserlösliches anionisches Polymerisat zugegeben, dass anionische und/oder aldehydische Gruppen enthält.From the WO 2004/061235 discloses a process for the production of paper, especially tissue, with particularly high wet and / or dry strengths, in which the paper stock is first added a water-soluble cationic polymer containing at least 1.5 meq / g of polymer to primary amino functionalities and a molecular weight of at least 10,000 daltons. Particular emphasis is placed here partially and fully hydrolyzed homopolymers of N-vinylformamide. Subsequently, a water-soluble anionic polymer is added which contains anionic and / or aldehydic groups.

In der DE-A 10 2004 056 551 wird ein weiteres Verfahren zur Verbesserung der Trockenfestigkeit von Papier beschrieben. Bei diesem Verfahren erfolgt eine getrennte Zugabe eines Vinylamineinheiten enthaltenden Polymeren und einer polymeren anionischen Verbindung zu einem Papierstoff, Entwässern des Papierstoffs und Trocknen der Papierprodukte, wobei man als polymere anionische Verbindung mindestens ein Copolymerisat einsetzt, das erhältlich ist durch Copolymerisieren von

  1. (a) mindestens eines N-Vinylcarbonsäureamids der Formel
    Figure imgb0001
    in der R1, R2 = H oder C1- bis C6-Alkyl bedeuten,
  2. (b) mindestens eines Säuregruppen enthaltenden monoethylenisch ungesättigten Monomeren und/oder deren Alkalimetall-, Erdalkalimetall- oder Ammoniumsalzen und gegebenenfalls
  3. (c) anderen monoethylenisch ungesättigten Monomeren, und gegebenenfalls
  4. (d) Verbindungen, die mindestens zwei ethylenisch ungesättigte Doppelbindungen im Molekül aufweisen.
In the DE-A 10 2004 056 551 Another method of improving the dry strength of paper is described. In this process, a separate addition of a Vinylamineinheiten polymers and a polymeric anionic compound to a pulp, dewatering of the pulp and drying of the paper products, wherein the polymeric anionic compound is at least one copolymer obtained by copolymerizing
  1. (a) at least one N-vinylcarboxamide of the formula
    Figure imgb0001
    in which R 1 , R 2 = H or C 1 - to C 6 -alkyl,
  2. (B) at least one acid group-containing monoethylenically unsaturated monomer and / or their alkali metal, alkaline earth metal or ammonium salts and optionally
  3. (c) other monoethylenically unsaturated monomers, and optionally
  4. (d) compounds having at least two ethylenically unsaturated double bonds in the molecule.

Aus der WO 2006/075115 ist die Verwendung von Hofmann-Abbauprodukten von Copolymeren des Acrylamids oder Methacrylamids in Kombination mit anionischen Polymeren mit einer anionischen Ladungsdichte von > 0,1 meq/g zur Herstellung von Papier und Karton mit einer hohen Trockenfestigkeit bekannt.From the WO 2006/075115 the use of Hofmann degradation products of copolymers of acrylamide or methacrylamide in combination with anionic polymers having an anionic charge density of> 0.1 meq / g for the production of paper and cardboard with a high dry strength is known.

In WO 2006/120235 wird ein Verfahren zur Herstellung von Papieren mit einem Füllergehalt von mindestens 15 Ges.-% beschrieben, bei dem Füller und Fasern gemeinsam mit kationischen und anionischen Polymeren behandelt werden, wobei die Behandlung abwechselnd mit kationischen und anionischen Polymeren erfolgt und mindestens 3 Schritte umfasst.In WO 2006/120235 describes a process for producing papers having a filler content of at least 15% by weight, in which filler and fibers are treated together with cationic and anionic polymers, the treatment taking place alternately with cationic and anionic polymers and comprising at least 3 steps.

Die WO 2006/090076 betrifft ebenfalls ein Verfahren zur Herstellung von Papier und Pappe mit hoher Trockenfestigkeit, wobei dem Papierstoff 3 Komponenten zugesetzt werden:

  1. a) ein Polymer mit primären Aminogruppen und einer Ladungsdichte von > 1,0 meq/g
  2. b) ein zweites, anderes kationisches Polymer mit einer Ladungsdichte von > 0,1 meq/g, das durch radikalische Polymerisation von kationischen Monomeren erhältlich ist, und
  3. c) ein anionisches Polymer mit einer Ladungsdichte von > 0,1 meq/g.
The WO 2006/090076 also relates to a process for the production of paper and paperboard having a high dry strength, wherein 3 components are added to the paper stock:
  1. a) a polymer with primary amino groups and a charge density of> 1.0 meq / g
  2. b) a second, different cationic polymer with a charge density of> 0.1 meq / g, which is obtainable by free-radical polymerization of cationic monomers, and
  3. c) an anionic polymer with a charge density of> 0.1 meq / g.

Der Erfindung liegt die Aufgabe zugrunde, ein weiteres Verfahren zur Herstellung von Papier, Pappe und Karton mit hoher Trockenfestigkeit zur Verfügung zu stellen, wobei die Trockenfestigkeitseigenschaften der Papierprodukte gegenüber denjenigen bekannter Produkte möglichst weiter verbessert sind. Eine weitere Aufgabe der Erfindung besteht darin, gegenüber bekannten Verfahren eine schnellere Entwässerung des Papierstoffs zu erreichen.The invention has for its object to provide a further process for the production of paper, paperboard and cardboard with high dry strength available, the dry strength properties of the paper products compared to those of known products are further improved as possible. Another object of the invention is to achieve faster dewatering of the stock compared to known methods.

Die Aufgaben werden erfindungsgemäß gelöst mit einem Verfahren zur Herstellung von Papier, Pappe und Karton mit hoher Trockenfestigkeit durch Zugabe mindestens eines wasserlöslichen kationischen Polymeren und mindestens einer wasserlöslichen polymeren anionischen Verbindung zu einem Papierstoff, Entwässern des Papierstoffs unter Blattbildung und Trocknen der Papierprodukte, wenn man als wasserlösliche kationische Polymere

  1. (a) Vinylamineinheiten enthaltende Polymere und
  2. (b) Ethylenimineinheiten enthaltende Polymere
in beliebiger Reihenfolge oder als Mischung zu einem Papierstoff dosiert und wobei das Gewichtsverhältnis von (a) Vinylamineinheiten enthaltenden Polymeren zu (b) Ethylenimineinheiten enthaltenden Polymeren 10 : 1 bis 1 : 10 beträgt und man als (a) Vinylamineinheiten enthaltende Polymere die Reaktionsprodukte einsetzt, die erhältlich sind
  • durch Polymerisieren mindestens eines Monomeren der Formel
    Figure imgb0002
    in der R1, R2 = H oder C1- bis C6-Alkyl bedeuten,
    und anschließende teilweise oder vollständige Abspaltung der Gruppen -CO-R1 aus den in das Polymerisat einpolymerisierten Einheiten der Monomeren (I) unter Bildung von Aminogruppen
    und/oder
  • durch Hofmann-Abbau von Polymeren, die Acrylamid- und/oder Methacrylamideinheiten aufweisen.
The objects are achieved according to the invention with a process for the production of paper, paperboard and cardboard with high dry strength by adding at least one water-soluble cationic polymer and at least one water-soluble polymeric anionic compound to a pulp, dewatering the pulp under sheet formation and drying the paper products, if water-soluble cationic polymers
  1. (a) polymers containing vinylamine units and
  2. (b) polymers containing ethyleneimine units
dosed in any order or as a mixture to form a pulp and wherein the weight ratio of (a) polymers containing vinylamine units to (b) polymers containing ethyleneimine units is from 10: 1 to 1:10 and the polymers containing (a) vinylamine units are the reaction products which are available
  • by polymerizing at least one monomer of the formula
    Figure imgb0002
    in which R 1 , R 2 = H or C 1 - to C 6 -alkyl,
    and subsequent partial or complete cleavage of the groups -CO-R 1 from the polymerized in the polymer units of the monomers (I) to form amino groups
    and or
  • by Hofmann degradation of polymers having acrylamide and / or methacrylamide units.

Polymerisate, die Vinylamineinheiten enthalten, sind bekannt, vgl. die zum Stand der Technik genannten DE-A 35 06 832 und DE-A 10 2004 056551 . Bei dem erfindungsgemäßen Verfahren setzt man als (a) Vinylamineinheiten enthaltende Polymere beispielsweise die Reaktionsprodukte ein, die erhältlich sind

  • durch Polymerisieren mindestens eines Monomeren der Formel
    Figure imgb0003
    in der R1, R2 = H oder C1- bis C6-Alkyl bedeuten,
    und anschließende teilweise oder vollständige Abspaltung der Gruppen -CO-R1 aus den in das Polymerisat einpolymerisierten Einheiten der Monomeren (I) unter Bildung von Aminogruppen
    und/oder
  • durch Hofmann-Abbau von Polymeren, die Acrylamid- und/oder Methacrylamideinheiten aufweisen.
Polymers containing vinylamine units are known, cf. those mentioned in the prior art DE-A 35 06 832 and DE-A 10 2004 056551 , In the inventive Methods are used as (a) vinylamine units containing polymers, for example, the reaction products that are available
  • by polymerizing at least one monomer of the formula
    Figure imgb0003
    in which R 1 , R 2 = H or C 1 - to C 6 -alkyl,
    and subsequent partial or complete cleavage of the groups -CO-R 1 from the polymerized in the polymer units of the monomers (I) to form amino groups
    and or
  • by Hofmann degradation of polymers having acrylamide and / or methacrylamide units.

Als (a) Vinylamineinheiten enthaltende Polymere setzt man beispielsweise die Reaktionsprodukte ein, die erhältlich sind durch Polymerisieren von

  1. (i) mindestens eines Monomeren der Formel
    Figure imgb0004
    in der R1, R2 = H oder C1- bis C6-Alkyl bedeuten,
  2. (ii) mindestens eines anderen monoethylenisch ungesättigten Monomeren und gegebenenfalls
  3. (iii) mindestens eines vernetzend wirkenden Monomeren mit mindestens zwei Doppelbindungen im Molekül
und anschließende teilweise oder vollständige Abspaltung der Gruppen -CO-R1 aus den in das Polymerisat einpolymerisierten Einheiten der Monomeren (I) unter Bildung von Aminogruppen.As (a) polymers containing vinylamine units, for example, the reaction products obtainable by polymerizing
  1. (i) at least one monomer of the formula
    Figure imgb0004
    in which R 1 , R 2 = H or C 1 - to C 6 -alkyl,
  2. (ii) at least one other monoethylenically unsaturated monomer and optionally
  3. (Iii) at least one crosslinking monomer having at least two double bonds in the molecule
and subsequent partial or complete cleavage of the groups -CO-R 1 from the polymerized in the polymer units of the monomers (I) to form amino groups.

Die Vinylamineinheiten enthaltenden Polymerisate können auch amphoter sein, wenn sie eine kationische Gesamtladung aufweisen. Der Gehalt an kationischen Gruppen im Polymeren soll dabei mindestens 5 Mol-%, vorzugsweise mindestens 10 Mol-% über dem Gehalt an anionischen Gruppen liegen. Solche Polymere sind beispielsweise erhältlich durch Polymerisieren von

  • (i) mindestens eines Monomeren der Formel
    Figure imgb0005
    in der R1, R2 = H oder C1- bis C6-Alkyl bedeuten,
  • (ii,a) mindestens jeweils einer monoethylenisch ungesättigten Sulfonsäure, einer monoethylenisch ungesättigten Phosphonsäure, einer monoethylenisch ungesättigten Carbonsäure mit 3 bis 8 C-Atomen im Molekül und/oder deren Alkalimetall-, Erdalkalimetall- oder Ammoniumsalzen und gegebenenfalls
  • (ii,b) mindestens eines anderen neutralen und/oder eines kationischen Monomeren und gegebenenfalls
  • (iii) mindestens eines vernetzend wirkenden Monomeren mit mindestens zwei Doppelbindungen im Molekül
und anschließende teilweise oder vollständige Abspaltung von Gruppen -CO-R1 aus den in das Polymerisat einpolymerisierten Monomeren der Formel I unter Bildung von Aminogruppen, wobei der Gehalt an Aminogruppen im Copolymerisat mindestens 5 Mol-% über dem Gehalt an einpolymerisierten Säuregruppen der Monomere (ii,a) beträgt.The polymers containing vinylamine units may also be amphoteric if they have a total cationic charge. The content of cationic groups in the polymer should be at least 5 mol%, preferably at least 10 mol% the content of anionic groups. Such polymers are obtainable, for example, by polymerizing
  • (i) at least one monomer of the formula
    Figure imgb0005
    in which R 1 , R 2 = H or C 1 - to C 6 -alkyl,
  • (ii, a) at least one monoethylenically unsaturated sulfonic acid, one monoethylenically unsaturated phosphonic acid, one monoethylenically unsaturated carboxylic acid having 3 to 8 C atoms in the molecule and / or their alkali metal, alkaline earth metal or ammonium salts and optionally
  • (ii, b) at least one other neutral and / or cationic monomer and optionally
  • (Iii) at least one crosslinking monomer having at least two double bonds in the molecule
and subsequent partial or complete cleavage of groups -CO-R 1 from the copolymerized in the polymer monomers of formula I to form amino groups, wherein the content of amino groups in the copolymer at least 5 mol% above the content of copolymerized acid groups of the monomers (ii , a) is.

Vorzugsweise setzt man als (a) Vinylamineinheiten enthaltende Polymere die Reaktionsprodukte ein, die durch Polymerisieren von N-Vinylformamid und anschließende Abspaltung von Formylgruppen aus den in das Polymerisat einpolymerisierten Vinylformamideinheiten unter Bildung von Aminogruppen erhältlich sind oder man verwendet die Reaktionsprodukte, die durch Copolymerisieren von

  1. (i) N-Vinylformamid und
  2. (ii) Acrylnitril
und anschließende Abspaltung von Formylgruppen aus den in das Copolymerisat einpolymerisierten Vinylformamideinheiten unter Bildung von Aminogruppen erhältlich sind.Preferably used as (a) vinylamine units containing the reaction products, which are obtainable by polymerizing N-vinylformamide and subsequent cleavage of formyl groups from the copolymerized in the polymer vinylformamide units to form amino groups or one uses the reaction products by copolymerizing
  1. (i) N-vinylformamide and
  2. (ii) acrylonitrile
and subsequent cleavage of formyl groups from the copolymerized in the copolymer vinylformamide units to form amino groups are available.

Von Interesse sind außerdem amphotere Vinylamineinheiten enthaltende Poly-mere, die eine kationische Gesamtladung tragen und die beispielsweise durch Copolymerisieren von

  • (i) N-Vinylformamid,
  • (ii,a) Acrylsäure, Methacrylsäure und/oder deren Alkalimetall-, Erdalkalimetall- oder Ammoniumsalzen und gegebenenfalls
  • (ii,b) Acrylnitril und/oder Methacrylnitril
und anschließende teilweise oder vollständige Abspaltung von Formylgruppen aus dem in das Polymerisat einpolymerisierten N-Vinylformamid unter Bildung von Aminogruppen erhältlich sind, wobei der Gehalt an Aminogruppen im Copolymerisat mindestens 5 Mol-% über dem Gehalt an einpolymerisierten Säuregruppen der Monomere (ii,a) beträgt.Also of interest are amphoteric Vinylamineinheiten containing polymers that carry a total cationic charge and, for example, by copolymerizing
  • (i) N-vinylformamide,
  • (ii, a) acrylic acid, methacrylic acid and / or their alkali metal, alkaline earth metal or ammonium salts and optionally
  • (ii, b) acrylonitrile and / or methacrylonitrile
and subsequent partial or complete cleavage of formyl groups from the N-vinylformamide polymerized into the polymer to form amino groups are obtainable, wherein the content of amino groups in the copolymer at least 5 mol% above the content of copolymerized acid groups of the monomers (ii, a) ,

Beispiele für Monomere der Formel I sind N-Vinylformamid, N-Vinyl-N-methylformamid, N-Vinylacetamid, N-Vinyl-N-methylacetamid, N-Vinyl-N-ethylacetamid, N-Vinylpropionamid und N-Vinyl-N-methylpropionamid und N-Vinylbutyramid. Die Monomeren der Gruppe (i) können allein oder in Mischung bei der Copolymerisation mit den Monomeren der anderen Gruppen eingesetzt werden. Bevorzugt eingesetztes Monomer dieser Gruppe ist N-Vinylformamid.Examples of monomers of the formula I are N-vinylformamide, N-vinyl-N-methylformamide, N-vinylacetamide, N-vinyl-N-methylacetamide, N-vinyl-N-ethylacetamide, N-vinylpropionamide and N-vinyl-N-methylpropionamide and N-vinylbutyramide. The monomers of group (i) can be used alone or mixed in the copolymerization with the monomers of the other groups. Preferably used monomer of this group is N-vinylformamide.

Diese Polymere können gegebenenfalls modifiziert sein, indem die N-Vinylcarbonsäureamide (i) zusammen mit (ii) mindestens einem anderen monoethylenisch ungesättigten Monomeren copolymerisiert und die Copolymerisate anschließend unter Bildung von Aminogruppen hydrolysiert werden. Falls bei der Copolymerisation anionische Monomere eingesetzt werden, so wird die Hydrolyse der einpolymerisierten Vinylcarbonsäureamideinheiten so weit geführt, dass der molare Überschuß an Amineinheiten gegenüber den anionischen Einheiten im Polymerisat mindestens 5 Mol-% beträgt.These polymers may optionally be modified by copolymerizing the N-vinylcarboxamides (i) together with (ii) at least one other monoethylenically unsaturated monomer and then hydrolyzing the copolymers to form amino groups. If anionic monomers are used in the copolymerization, the hydrolysis of the copolymerized vinylcarboxamide units is carried out so far that the molar excess of amine units compared to the anionic units in the polymer is at least 5 mol%.

Beispiele für Monomere der Gruppe (ii) sind Ester von α,β-ethylenisch ungesättigten Mono- und Dicarbonsäuren mit C1-C30-Alkanolen, C2-C30-Alkandiolen und C2-C30-Aminoalkoholen, Amide von α,β-ethylenisch ungesättigten Monocarbonsäuren und deren N-Alkyl- und N,N-Dialkylderivate, Nitrile von α,β-ethylenisch ungesättigten Mono-und Dicarbonsäuren, Ester von Vinylalkohol und Allylalkohol mit C1-C30-Monocarbonsäuren, N-Vinyllactame, stickstoffhaltige Heterocyclen mit α,β-ethylenisch ungesättigten Doppelbindungen, Vinylaromaten, Vinylhalogenide, Vinylidenhalogenide, C2-C8-Monoolefine und Mischungen davon.Examples of monomers of group (ii) are esters of α, β-ethylenically unsaturated mono- and dicarboxylic acids with C 1 -C 30 -alkanols, C 2 -C 30 -alkanediols and C 2 -C 30 -aminoalcohols, amides of α, β-ethylenically unsaturated monocarboxylic acids and their N-alkyl and N, N-dialkyl derivatives, nitriles of α, β-ethylenically unsaturated mono- and dicarboxylic acids, esters of vinyl alcohol and allyl alcohol with C 1 -C 30 monocarboxylic acids, N-vinyl lactams, nitrogen-containing Heterocycles with α, β-ethylenically unsaturated double bonds, vinyl aromatics, vinyl halides, vinylidene halides, C 2 -C 8 monoolefins and mixtures thereof.

Geeignete Vertreter sind z.B. Methyl(meth)acrylat (diese Schreibweise symbolisiert hier wie auch im folgenden Text sowohl "Acrylate" als auch "Methacrylate"), Methylethacrylat, Ethyl(meth)acrylat, Ethylethacrylat, n-Butyl(meth)acrylat, Isobutyl(meth)acrylat, tert.-Butyl(meth)acrylat, tert.-Butylethacrylat, n-Ocytl(meth)acrylat, 1,1,3,3-Tetramethylbutyl(meth)acrylat, Ethylhexyl(meth)acrylat und Mischungen davon. Geeignete zusätzliche Monomere der Guppe (ii) sind weiterhin die Ester von α,β-ethylenisch ungesättigten Mono- und Dicarbonsäuren mit Aminoalkoholen, vorzugsweise C2-C12-Aminoalkoholen. Diese können am Aminstickstoff C1-C8-monoalkyliert oder -dialkyliert sein. Als Säurekomponente dieser Ester eignen sich z. B. Acrylsäure, Methacrylsäure, Fumarsäure, Maleinsäure, Itaconsäure, Crotonsäure, Maleinsäureanhydrid, Monobutylmaleat und Gemische davon. Bevorzugt werden Acrylsäure, Methacrylsäure und deren Gemische eingesetzt. Dazu zählen beispielsweise N-Methylaminomethyl(meth)acrylat, N-Methylaminoethyl(meth)acrylat, N,N-Dimethylaminomethyl(meth)acrylat, N,N-Dimethylaminoethyl(meth)acrylat, N,N-Diethylaminoethyl(meth)acrylat, N,N-Dimethylaminopropyl(meth)acrylat, N,N-Diethylaminopropyl(meth)acrylat und N,N-Dimethylaminocyclohexyl(meth)acrylat.Suitable representatives are, for example, methyl (meth) acrylate (this notation symbolizes both "acrylates" and "methacrylates" here as well as in the following text), methyl methacrylate, Ethyl (meth) acrylate, ethyl ethacrylate, n-butyl (meth) acrylate, isobutyl (meth) acrylate, tert-butyl (meth) acrylate, tert-butyl methacrylate, n-o-cytriethyl (meth) acrylate, 1,1,3, 3-Tetramethylbutyl (meth) acrylate, ethylhexyl (meth) acrylate and mixtures thereof. Suitable additional monomers of group (ii) are furthermore the esters of α, β-ethylenically unsaturated mono- and dicarboxylic acids with aminoalcohols, preferably C 2 -C 12 -aminoalcohols. These may be C 1 -C 8 -monoalkylated or -dialkylated on the amine nitrogen. As the acid component of these esters are z. For example, acrylic acid, methacrylic acid, fumaric acid, maleic acid, itaconic acid, crotonic acid, maleic anhydride, monobutyl maleate and mixtures thereof. Preference is given to using acrylic acid, methacrylic acid and mixtures thereof. These include, for example, N-methylaminomethyl (meth) acrylate, N-methylaminoethyl (meth) acrylate, N, N-dimethylaminomethyl (meth) acrylate, N, N-dimethylaminoethyl (meth) acrylate, N, N-diethylaminoethyl (meth) acrylate, N , N-dimethylaminopropyl (meth) acrylate, N, N-diethylaminopropyl (meth) acrylate and N, N-dimethylaminocyclohexyl (meth) acrylate.

Weiterhin sind als Monomere der Gruppe (ii) geeignet 2-Hydroxyethyl(meth)acrylat, 2-Hydroxyethylethacrylat, 2-Hydroxypropyl(meth)acrylat, 3-Hydroxypropyl(meth)acrylat, 3-Hydroxybutyl(meth)acrylat, 4-Hydroxybutyl(meth)acrylat, 6-Hydroxyhexyl(meth)acrylat und Mischungen davon.Further suitable monomers of group (ii) are 2-hydroxyethyl (meth) acrylate, 2-hydroxyethyl methacrylate, 2-hydroxypropyl (meth) acrylate, 3-hydroxypropyl (meth) acrylate, 3-hydroxybutyl (meth) acrylate, 4-hydroxybutyl ( meth) acrylate, 6-hydroxyhexyl (meth) acrylate and mixtures thereof.

Geeignete zusätzliche Monomere der Gruppe (ii) sind weiterhin Acrylsäureamid, Methacrylsäureamid, N-Methyl(meth)acrylamid, N-Ethyl(meth)acrylamid, n-Propyl(meth)acrylamid, N-(n-Butyl)(meth)acrylamid, tert.-Butyl(meth)acrylamid, n-Octyl(meth)acrylamid, 1,1,3,3-Tetramethylbutyl(meth)acrylamid, Ethylhexyl(meth)acrylamid und Mischungen davon.Further suitable monomers of group (ii) are acrylamide, methacrylamide, N-methyl (meth) acrylamide, N-ethyl (meth) acrylamide, n-propyl (meth) acrylamide, N- (n-butyl) (meth) acrylamide, tert-butyl (meth) acrylamide, n-octyl (meth) acrylamide, 1,1,3,3-tetramethylbutyl (meth) acrylamide, ethylhexyl (meth) acrylamide and mixtures thereof.

Darüber hinaus sind als weitere Monomere der Gruppe (ii) N-[2-(Dimethylamino)ethyl]acrylamid, N-[2-(Dimethylamino)ethyl]methacrylamid, N-[3-(Dimethylamino)propyl]acrylamid, N-[3-(Dimethylamino)propyl]methacrylamid, N-[4-(Dimethylamino)butyl]acrylamid, N-[4-(Dimethylamino)butyl]methacrylamid, N-[2-(Diethylamino)ethyl]acrylamid, N-[2-(Diethylamino)ethyl]methacrylamid und Mischungen davon geeignet.In addition, as further monomers of group (ii) N- [2- (dimethylamino) ethyl] acrylamide, N- [2- (dimethylamino) ethyl] methacrylamide, N- [3- (dimethylamino) propyl] acrylamide, N- [ 3- (dimethylamino) propyl] methacrylamide, N- [4- (dimethylamino) butyl] acrylamide, N- [4- (dimethylamino) butyl] methacrylamide, N- [2- (diethylamino) ethyl] acrylamide, N- [2-] (Diethylamino) ethyl] methacrylamide and mixtures thereof.

Weitere Beispiele für Monomere der Gruppe (ii) sind Nitrile von α,β-ethylenisch ungesättigten Mono- und Dicarbonsäuren wie beispielsweise Acrylnitril und Methacrylnitril. Die Anwesenheit von Einheiten dieser Monomeren im Copolymerisat führt während bzw. nach der Hydrolyse zu Produkten, die Amidineinheiten aufweisen, vgl. z.B. EP-A 0 528 409 oder DE-A 43 28 975 . Bei der Hydrolyse von N-Vinylcarbonsäureamidpolymer-en entstehen nämlich in einer sekundären Reaktion Amidineinheiten, indem Vinylami-neinheiten mit einer benachbarten Vinylformamideinheit oder - sofern eine Nitrilgruppe als benachbarte Gruppe im Polymerisat vorhanden ist - damit reagieren. Im Folgenden bedeutet die Angabe von Vinylamineinheiten in den amphoteren Copolymerisaten oder in nicht modifizierten Homo- bzw. Copolymerisaten immer die Summe aus Vinylamin- und Amidineinheiten.Further examples of monomers of group (ii) are nitriles of α, β-ethylenically unsaturated mono- and dicarboxylic acids such as, for example, acrylonitrile and methacrylonitrile. The presence of units of these monomers in the copolymer leads during or after the hydrolysis to products which have amidine units, cf. eg EP-A 0 528 409 or DE-A 43 28 975 , Namely, in the hydrolysis of N-vinylcarboxylic acid amide polymers, amidine units are formed in a secondary reaction by reacting vinylamine units with an adjacent vinylformamide unit or, if a nitrile group is present as an adjacent group in the polymer. In the following means the indication of vinylamine units in the amphoteric Copolymers or in unmodified homo- or copolymers always the sum of vinylamine and amidine units.

Geeignete Monomere der Gruppe (ii) sind weiterhin N-Vinyllactame und deren Derivate, die z. B. einen oder mehrere C1-C6-Alkylsubstituenten (wie oben definiert) aufweisen können. Dazu zählen N-Vinylpyrrolidon, N-Vinylpiperidon, N-Vinylcaprolactam, N-Vinyl-5-methyl-2-pyrrolidon, N-Vinyl-5-ethyl-2-pyrrolidon, N-Vinyl-6-methyl-2-piperidon, N-Vinyl-6-ethyl-2-piperidon, N-Vinyl-7-methyl-2-caprolactam, N-Vinyl-7-ethyl-2-caprolactam und deren Mischungen.Suitable monomers of group (ii) are furthermore N-vinyllactams and derivatives thereof which, for. B. one or more C 1 -C 6 alkyl substituents (as defined above) may have. These include N-vinylpyrrolidone, N-vinylpiperidone, N-vinylcaprolactam, N-vinyl-5-methyl-2-pyrrolidone, N-vinyl-5-ethyl-2-pyrrolidone, N-vinyl-6-methyl-2-piperidone, N-vinyl-6-ethyl-2-piperidone, N-vinyl-7-methyl-2-caprolactam, N-vinyl-7-ethyl-2-caprolactam and mixtures thereof.

Weiterhin sind als Monomere der Gruppe (ii) N-Vinylimidazole und Alkylvinylimidazole geeignet, insbesondere Methylvinylimidazole wie beispielsweise 1-Vinyl-2-methylimidazol, 3-VinylimidazolN-oxid, 2- und4-Vinylpyridin-N-oxide sowie betainische Derivate und Quaternisierungsprodukte dieser Monomere sowie Ethylen, Propylen, Isobutylen, Butadien, Styrol, α-Methylstyrol, Vinylacetat, Vinylpropionat, Vinylchlorid, Vinylidenchlorid, Vinylfluorid, Vinylidenfluorid und Mischungen davon.Further suitable monomers of group (ii) are N-vinylimidazoles and alkylvinylimidazoles, in particular methylvinylimidazoles such as 1-vinyl-2-methylimidazole, 3-vinylimidazoleN-oxide, 2- and 4-vinylpyridine N-oxides and betaine derivatives and quaternization products of these monomers and ethylene, propylene, isobutylene, butadiene, styrene, α-methylstyrene, vinyl acetate, vinyl propionate, vinyl chloride, vinylidene chloride, vinyl fluoride, vinylidene fluoride and mixtures thereof.

Die zuvor genannten Monomeren können einzeln oder in Form von beliebigen Mischungen eingesetzt werden. Typischerweise werden sie in Mengen von 1 bis 90 Mol-%, bevorzugt 10 bis 80 Mol-% und besonders bevorzugt 10 bis 60 Mol-% eingesetzt.The aforementioned monomers can be used individually or in the form of any mixtures. Typically, they are used in amounts of 1 to 90 mol%, preferably 10 to 80 mol% and particularly preferably 10 to 60 mol%.

Zur Herstellung von amphoteren Copoylmerisaten kommen als andere monoethylenisch ungesättigte Monomere der Gruppe (ii) auch anionische Monomere in Betracht, die oben als Monomere (ii,a) bezeichnet sind. Sie können gegebenenfalls mit den oben beschriebenen neutralen und/oder kationischen Monomeren (ii,b) copolymerisiert werden. Die Mengen an anionischen Monomeren (ii,a) beträgt jedoch höchstens 45 Mol%, damit das entstehende amphotere Copolymerisat insgesamt eine kationische Ladung aufweist.For the preparation of amphoteric Copoylmerisaten come as other monoethylenically unsaturated monomers of group (ii) also anionic monomers into consideration, which are referred to above as monomers (ii, a). They may optionally be copolymerized with the neutral and / or cationic monomers (ii, b) described above. However, the amounts of anionic monomers (ii, a) is at most 45 mol%, so that the resulting amphoteric copolymer has a total cationic charge.

Beispiele für anionische Monomere der Gruppe (ii,a) sind ethylenisch ungesättigte C3-bis C8-Carbonsäuren wie beispielsweise Acrylsäure, Methacrylsäure, Dimethacrylsäure, Ethacrylsäure, Maleinsäure, Fumarsäure, Itoconsäure, Mesaconsäure, Citraconsäure, Methylenmalonsäure, Allylessigsäure, Vinylessigsäure und Crotonsäure. Als Monomere dieser Gruppe eignen sich außerdem Sulfogruppen enthaltende Monomere wie Vinylsulfonsäure, Acrylamido-2-methyl-propansulfonsäure und Styrolsulfonsäure sowie Phosphongruppen enthaltende Monomere wie Vinylphosphonsäure. Die Monomeren dieser Gruppe können allein oder in Mischung miteinander, in teilweise oder in vollständig neutralisierter Form bei der Copolymerisation eingesetzt werden. Zur Neutralisation verwendet man beispielsweise Alkalimetall- oder Erdalkalimetallbasen, Ammoniak, Amine und/oder Alkanolamine. Beispiele hierfür sind Natronlauge, Kalilauge, Soda, Pottasche, Natriumhydrogencarbonat, Magnesiumoxid, Calciumhydroxid, Calciumoxid, Triethanolamin, Ethanolamin, Morpholin, Diethylentriamin oder Tetraethylenpentamin.Examples of anionic monomers of group (ii, a) are ethylenically unsaturated C 3 to C 8 carboxylic acids such as acrylic acid, methacrylic acid, dimethacrylic acid, ethacrylic acid, maleic acid, fumaric acid, itoconic acid, mesaconic acid, citraconic acid, methylenemalonic acid, allylacetic acid, vinylacetic acid and crotonic acid. Also suitable as monomers of this group are monomers containing sulfo groups, such as vinylsulfonic acid, acrylamido-2-methylpropanesulfonic acid and styrenesulfonic acid, and monomers containing phosphono groups, such as vinylphosphonic acid. The monomers of this group can be used alone or in admixture with each other, in partially or completely neutralized form in the copolymerization. For neutralization, for example, alkali metal or alkaline earth metal bases, ammonia, amines and / or alkanolamines are used. Examples of these are sodium hydroxide solution, potassium hydroxide solution, soda, potash, sodium bicarbonate, magnesium oxide, calcium hydroxide, calcium oxide, Triethanolamine, ethanolamine, morpholine, diethylenetriamine or tetraethylenepentamine.

Eine weitere Modifizierung der Copolymerisate ist dadurch möglich, dass man bei der Copolymerisation Monomere der Gruppe (iii) einsetzt, die mindestens zwei Doppelbindungen im Molekül enthalten, z. B. Triallylamin, Methylenbisacrylamid, Glykoldiacrylat, Glykoldimethacrylat, Glycerintriacrylat, Pentaerythrittriallylether, mindestens zweifach mit Acrylsäure und/oder Methacrylsäure veresterte Polyalkylenglykole oder Polyole wie Pentaerythrit, Sobit oder Glukose. Falls mindestens ein Monomer der vorstehenden Gruppe bei der Polymerisation eingesetzt wird, so betragen die angewendeten Mengen bis zu 2 Mol-%, z. B. 0,001 bis 1 Mol-%.A further modification of the copolymers is possible by using in the copolymerization monomers of group (iii) which contain at least two double bonds in the molecule, for. B. triallylamine, methylenebisacrylamide, glycol diacrylate, glycol dimethacrylate, glycerol triacrylate, pentaerythritol triallyl ether, at least two times with acrylic acid and / or methacrylic acid esterified polyalkylene glycols or polyols such as pentaerythritol, Sobit or glucose. If at least one monomer of the above group is used in the polymerization, the amounts used are up to 2 mol%, e.g. B. 0.001 to 1 mol%.

Weiterhin kann es zur Modifizierung der Polymeren sinnvoll sein, den Einsatz vorstehender Vernetzter mit dem Zusatz von Reglern zu kombinieren Eingesetzt werden typischerweise 0,001 bis 5 Mol-%. Anwendung finden können alle literturbekannten Regler, z. B. Schwefelverbindungen wie Mercaptoethanol, 2-Ethylhexylthioglycolat, Thioglycolsäure und Dodecylmercaptan sowie Natriumhypophosphit, Ameisensäure oder Tribromchlormethan.Furthermore, it may be useful for modifying the polymers to combine the use of the above crosslinked with the addition of regulators are typically used 0.001 to 5 mol%. All regulators known in the literature can be used, eg. For example, sulfur compounds such as mercaptoethanol, 2-Ethylhexylthioglycolat, thioglycolic acid and dodecyl mercaptan and sodium hypophosphite, formic acid or Tribromchlormethan.

Zu den Vinylamineinheiten enthaltenden Polymeren gehören auch hydrolysierte Pfropfpolymerisate von beispielsweise N-Vinylformamid auf Polyalkylenglykolen, Polyvinylacetat, Polyvinylalkolhol, Polyvinylformamiden, Polysacchariden wie Stärke, Oligosacchariden oder Monosacchariden. Die Pfropfpolymerisate sind dadurch erhältlich, dass man beispielsweise N-Vinylformamid in wässrigem Medium in Gegenwart mindestens einer der genannten Pfropfgrundlagen gegebenenfalls zusammen mit copolymerisierbaren anderen Monomeren radikalisch polymerisiert und die aufgepfropften Vinylformamideinheiten anschließend in bekannten Weise zu Vinylamineinheiten hydrolysiert.The polymers containing vinylamine units also include hydrolyzed graft polymers of, for example, N-vinylformamide on polyalkylene glycols, polyvinyl acetate, polyvinyl alcohol, polyvinylformamides, polysaccharides such as starch, oligosaccharides or monosaccharides. The graft polymers are obtainable by free-radically polymerizing, for example, N-vinylformamide in aqueous medium in the presence of at least one of the stated grafting bases together with copolymerizable other monomers and then hydrolyzing the grafted vinylformamide units in a known manner to give vinylamine units.

Die Hydrolyse der Copolymerisate kann in Gegenwart von Säuren oder Basen oder auch enzymatisch durchgeführt werden. Bei der Hydrolyse mit Säuren liegen die aus den Vinylcarbonsäureamideinheiten entstehenden Vinylamingruppen in Salzform vor. Die Hydrolyse von Vinylcarbonsäureamidcopolymerisaten ist in der EP-A 0 438 744 , Seite 8, Zeile 20 bis Seite 10, Zeile 3, ausführlich beschrieben. Die dort gemachten Ausführungen gelten entsprechend für die Herstellung der erfindungsgemäß einzusetzenden Vinylamineinheiten enthaltenden rein kationischen und/oder amphoteren Polymeren mit einer kationischen Gesamtladung. Die Vinylamineinheiten enthaltenden Polymeren können auch in Form der freien Basen bei dem erfindungsgemäßen Verfahren eingesetzt werden. Solche Polymere fallen beispielsweise bei der Hydrolyse von Vinylcarbonsäureeinheiten enthaltenden Polymeren mit Basen an.The hydrolysis of the copolymers can be carried out in the presence of acids or bases or else enzymatically. In the case of hydrolysis with acids, the vinylamine groups formed from the vinylcarboxamide units are present in salt form. The hydrolysis of vinylcarboxylic acid amide copolymers is described in U.S. Pat EP-A 0 438 744 , Page 8, line 20 to page 10, line 3, described in detail. The explanations made there apply correspondingly to the preparation of the cationic and / or amphoteric polymers containing vinylamine units to be used according to the invention and having a total cationic charge. The polymers containing vinylamine units can also be used in the form of the free bases in the process according to the invention. Such polymers are useful, for example, in the hydrolysis of polymers containing vinylcarboxylic acid units with bases.

Die Vinylamineinheiten enthaltenden Polymeren haben beispielsweise K-Werte (bestimmt nach H. Fikentscher in 5 %iger wässriger Kochsalzlösung bei pH 7, einer Polymerkonzentration von 0,5 Gew.-% und einer Temperatur von 25°C) in dem Bereich von 20 bis 250, vorzugsweise 50 bis 150.The polymers containing vinylamine units have, for example, K values (determined according to H. Fikentscher in 5% strength aqueous sodium chloride solution at pH 7, a polymer concentration of 0.5% by weight and a temperature of 25 ° C.) in the range from 20 to 250 , preferably 50 to 150.

Die Herstellung der oben beschriebenen Vinylamineinheiten enthaltenden Homo- und Copolymerisate kann durch Lösungs-, Fällungs-, Suspensions- oder Emulsionspolymerisation erfolgen. Bevorzugt ist die Lösungspolymerisation in wässrigen Medien. Geeignete wässrige Medien sind Wasser und Gemische aus Wasser und mindestens einem wassermischbaren Lösungsmittel, z. B. einem Alkohol, wie Methanol, Ethanol, n-Propanol oder Isopropanol. Die kationischen Polymerisate sind wasserlöslich. Die Löslichkeit in Wasser bei einer Temperatur von 20 °C, 1013 mbar und einem pH von 7,0 beträgt beispielsweise mindestens 5 Gew.-%, vorzugsweise mindestens 10 Gew.-%.The preparation of the homopolymers and copolymers containing vinylamine units described above can be carried out by solution, precipitation, suspension or emulsion polymerization. Preference is given to solution polymerization in aqueous media. Suitable aqueous media are water and mixtures of water and at least one water-miscible solvent, e.g. As an alcohol such as methanol, ethanol, n-propanol or isopropanol. The cationic polymers are water-soluble. The solubility in water at a temperature of 20 ° C, 1013 mbar and a pH of 7.0, for example, at least 5 wt .-%, preferably at least 10 wt .-%.

Die Ladungsdichte der kationischen Polymeren (ohne Gegenionen) beträgt beispielsweise mindestens 1,0 meq/g und liegt vorzugsweise in dem Bereich von 4 bis 10 meq/g.The charge density of the cationic polymers (without counterions) is for example at least 1.0 meq / g and is preferably in the range of 4 to 10 meq / g.

Als (a) Vinylamineinheiten enthaltende Polymere kommen außerdem die Reaktionsprodukte in Betracht, die durch Hofmann-Abbau von Homo- oder Copolymerisaten des Acrylamids oder Methacrylamids in wäßrigem Medium in Gegenwart von Natronlauge und Natriumhypochlorit und anschließende Decarboxylierung der Carbamatgruppen der Umsetzungsprodukte in Gegenwart einer Säure erhältlich sind. Solche Polymere sind beispielsweise aus EP-A 0 377 313 und WO 2006/075115 bekannt. Die Herstellung von Vinylamingruppen enthaltenden Polymeren wird beispielsweise in WO 2006/075115 , Seite 4, Zeile 25 bis Seite 10, Zeile 22 sowie in den Beispielen auf den Seiten 13 und 14 ausführlich behandelt. Die dort gemachten Angaben gelten für die Charakterisierung der durch Hofmann-Abbau hergestellten Vinylamineinheiten enthaltenden Polymeren.As (a) polymers containing vinylamine units, the reaction products which are obtainable by Hofmann degradation of homopolymers or copolymers of acrylamide or methacrylamide in an aqueous medium in the presence of sodium hydroxide solution and sodium hypochlorite and subsequent decarboxylation of the carbamate groups of the reaction products in the presence of an acid are also suitable , Such polymers are for example made EP-A 0 377 313 and WO 2006/075115 known. The preparation of polymers containing vinylamine groups is described, for example, in WO 2006/075115 , Page 4, line 25 to page 10, line 22 and in the examples on pages 13 and 14 are treated in detail. The information given there applies to the characterization of the polymers containing vinylamine units prepared by Hofmann degradation.

Man geht dabei von Polymeren aus, die Acrylamid- und/oder Methacrylamideinheiten enthalten. Es handelt sich dabei um Homo- bzw. Copolymerisate von Acrylamid und Methacrylamid. Als Comonomere kommen beispielsweise Dialkylaminoalkyl(meth)acrylamide, Diallylamin, Methyldiallylamin und sowie die Salze der Amine und die quaternierten Amine in Betracht. Außerdem eignen sich als Comonomere Dimethyldiallylammonium salze, Acrylamidopropyltrimethylammoniumchlorid und/oder Methacrylamidopropyltrimethylammoniumchlorid, N-Vinylformamid, N-Vinylacetamid, N-Vinylpyrrolidon, Vinylacetat und Acrylsäure- und Methacrylsäureester. Als Comonere kommen gegebenenfalls auch anionische Monomere wie Acrylsäure, Methacrylsäure, Maleinsäureanhydrid, Maleinsäure, Itaconsäure, Acrylamidomethylpropansulfonsäure, Methallylsulfonsäure und Vinylsulfonsäure sowie die Alkalimetall-, Erdalkylimetall- und Ammoniumsalze der genannten sauren Monomeren in Betracht, wobei nicht mehr als 5 Mol-% dieser Monomeren bei der Polymerisation eingesetzt werden. Die Menge an wassserunlöslichen Monomeren wird bei der Polymerisation so gewählt, dass die entstehenden Polymeren in Wasser löslich sind.It is based on polymers containing acrylamide and / or methacrylamide units. These are homopolymers or copolymers of acrylamide and methacrylamide. Suitable comonomers are, for example, dialkylaminoalkyl (meth) acrylamides, diallylamine, methyldiallylamine and also the salts of the amines and the quaternized amines. Also suitable as comonomers Dimethyldiallylammonium salts, acrylamidopropyltrimethylammonium chloride and / or Methacrylamidopropyltrimethylammoniumchlorid, N-vinylformamide, N-vinylacetamide, N-vinylpyrrolidone, vinyl acetate and acrylic and methacrylic acid esters. As comonomers are optionally also anionic monomers such as acrylic acid, methacrylic acid, maleic anhydride, maleic acid, itaconic acid, acrylamidomethylpropanesulfonic acid, methallylsulfonic acid and vinylsulfonic acid and the alkali metal, Erdalkylimetall- and Ammonium salts of said acidic monomers into consideration, wherein not more than 5 mol% of these monomers are used in the polymerization. The amount of water-insoluble monomers is chosen in the polymerization so that the resulting polymers are soluble in water.

Als Comonomere können gegebenenfalls auch Vernetzer eingesetzt werden, z. B. ethylenisch ungesättigte Monomere, die mindestens zwei Doppelbindungen im Molekül enthalten wie Triallylamin, Methylenbisacrylamid, Ethylenglykoldiacrylat, Ethylenglykoldimethacrylat, Polyethylenglykoldimethacrylat, Triallylamin und Trimethyloltrimethacrylat. Falls ein Vernetzer angewendet wird, so betragen die eingesetzten Mengen beispielsweise 5 bis 5000 ppm. Die Polymerisation der Monomeren kann nach allen bekannten Verfahren erfolgen, z. B. durch radikalisch initiierte Lösungs-, Fällungs- oder Suspensionspolymerisation. Man kann dabei gegebenenfalls in Gegenwart üblicher Polymerisationsregler arbeiten.If appropriate, comonomers may also be used crosslinkers, for. B. ethylenically unsaturated monomers containing at least two double bonds in the molecule such as triallylamine, methylenebisacrylamide, ethylene glycol diacrylate, ethylene glycol dimethacrylate, polyethylene glycol dimethacrylate, triallylamine and trimethylol trimethacrylate. If a crosslinker is used, the amounts used are, for example, 5 to 5000 ppm. The polymerization of the monomers can be carried out by any known method, for. B. by free-radical initiated solution, precipitation or suspension polymerization. If appropriate, it is possible to work in the presence of customary polymerization regulators.

Beim Hofmann-Abbau geht man beispielsweise von 20 bis 40 gew.-%igen wässrigen Lösungen mindestens eines Acrylamid- und/oder Methacrylamideinheiten enthaltenden Polymeren aus. Das Verhältnis von Alkalimetallhypochlorit zu (Meth)acrylamideinheiten im Polymer ist maßgebend für den entstehenden Gehalt an Amingruppen im Polymer. Das molare Verhältnis von Alkylimetallhydroxid zu Alkylimetallhypochlorit beträgt beispielsweise 2 bis 6, vorzugsweise 2 bis 5. Für einen bestimmten Amingruppengehalt im abgebauten Polymer berechnet man die für den Abbau des Polymeren erforderliche Menge an Alkalimetallhydroxid.When Hofmann degradation is for example from 20 to 40 wt .-% aqueous solutions of at least one acrylamide and / or methacrylamide units containing polymers. The ratio of alkali metal hypochlorite to (meth) acrylamide units in the polymer is decisive for the resulting content of amine groups in the polymer. The molar ratio of alkyl metal hydroxide to alkyl metal hypochlorite is, for example, 2 to 6, preferably 2 to 5. For a certain amine group content in the degraded polymer, the amount of alkali metal hydroxide required for the degradation of the polymer is calculated.

Der Hofmann-Abbau des Polymeren erfolgt z. B. in dem Temperaturbereich von 0 bis 45 °C, vorzugsweise 10 bis 20 °C in Gegenwart von quaternären Ammoniumsalzen als Stabilisator, um eine Nebenreaktion der entstehenden Aminogruppen mit den Amidgruppen des Ausgangspolymeren zu verhindern. Nach Beendigung der Umsetzung mit Alkylilauge/Alkalimetallhypochlorit wird die wässrige Reaktionslösung in einen Reaktor geleitet, in dem eine Säure für die Decarboxylierung des Umsetzungsprodukts vorgelegt ist. Der pH-Wert des Vinylamineinheiten enthaltenden Reaktionsprodukts wird auf einen Wert von 2 bis 7 eingestellt. Die Konzentration des Vinylamineinheiten enthaltenden Abbauprodukts beträgt beispielsweise mehr als 3,5 Gew.-%, meistens liegt sie oberhalb von 4,5 Gew.-%. Die wässrigen Polymerlösungen können beispielsweise mit Hilfe einer Ultrafiltration aufkonzentriert werden.The Hofmann degradation of the polymer takes place z. In the temperature range of 0 to 45 ° C, preferably 10 to 20 ° C in the presence of quaternary ammonium salts as a stabilizer to prevent side reaction of the resulting amino groups with the amide groups of the starting polymer. After completion of the reaction with alkyllauge / alkali metal hypochlorite, the aqueous reaction solution is passed into a reactor in which an acid is introduced for the decarboxylation of the reaction product. The pH of the reaction product containing vinylamine units is adjusted to a value of 2 to 7. The concentration of the decomposition products containing vinylamine units is, for example, more than 3.5% by weight, in most cases above 4.5% by weight. The aqueous polymer solutions can be concentrated for example by means of ultrafiltration.

Zu den Ethylenimineinheiten enthaltenden Polymeren gehören alle Polymere, die durch Polymerisation von Ethylenimin in Gegenwart von Säuren, Lewissäuren oder Halogenalkanen erhältlich sind wie Homopolymerisate des Ethylenimins oder Pfropfpolymerisate von Ethylenimin, vgl. US 2,182,306 oder in US 3,203,910 . Diese Polymeren können gegebenenfalls nachträglich einer Vernetzung unterworfen werden. Als Vernetzer kommen z. B. alle multifunktionellen Verbindungen in Betracht, die gegenüber primären Aminogruppen reaktive Gruppen enthalten z.B. multifunktionelle Epoxide wie Bisglyciyglether von Oligo- oder Polyethylenoxiden oder anderen multifunktionellen Alkoholen wie Gylcerin oder Zuckern, mulitunktionelle Carbonsäureester, mulifunktionelle Isocyante, multifunktionelle Acrylsäure- oder Methacrylsäureester, multifunktionelle Acrylsäure - oder Methacrylsäureamide, Epichlorhydrin, multifunktionelle Säurehalogenide, multifunktionelle Nitrile, α,ω-Chlorhydrinether von Oligo- oder Polyethylenoxiden oder von anderen multifunktio-nellen Alkoholen wie Gylcerin oder Zuckern, Divinylsulfon, Maleinsäureanhydrid oder ω-Halogencarbonsäurechloride, multifunktionelle Halogenalkane insbesondere α,ω-Dichloralkane. Weitere Vernetzer sind in WO 97/25367 , Seiten 8 bis16 beschrieben.The polymers containing ethyleneimine units include all polymers obtainable by polymerization of ethyleneimine in the presence of acids, Lewis acids or haloalkanes, such as homopolymers of ethyleneimine or graft polymers of ethyleneimine, cf. US 2,182,306 or in US 3,203,910 , If desired, these polymers can subsequently be subjected to crosslinking. As crosslinkers z. B. all multifunctional compounds into consideration, the opposite For example, multifunctional epoxides such as bisglycol ethers of oligo- or polyethyleneoxides or other multifunctional alcohols such as glycerol or sugars, multifunctional carboxylic acid esters, mulifunctional isocyanates, polyfunctional acrylic or methacrylic acid esters, multifunctional acrylic or methacrylic acid amides, epichlorohydrin, multifunctional acid halides, multifunctional nitriles, α, ω-chlorohydrin ethers of oligo- or polyethylene oxides or of other multifunctional alcohols such as glycerol or sugars, divinyl sulfone, maleic anhydride or ω-halocarboxylic acid chlorides, multifunctional haloalkanes in particular α, ω-dichloroalkanes. Other crosslinkers are in WO 97/25367 , Pages 8 to 16 described.

Ethylenimineinheiten enthaltende Polymere sind beispielsweise aus EP-A- 0411400 , DE 2434816 und US 4,066,494 bekannt.For example, polymers containing ethyleneimine units are made EP-A-0411400 . DE 2434816 and US 4,066,494 known.

Als (b) Ethylenimineinheiten enthaltende Polymere verwendet man z. B. bei dem erfindungsgemäßen Verfahren mindestens ein wasserlösliches kationisches Polymer aus der Gruppe der

  • Homopolymerisate des Ethylenimins,
  • mit mindestens bifunktionellen Vernetzern umgesetzten Polyethylenimine,
  • mit Ethylenimin gepfropften Polyamidoamine, die mit mindestens bifunktionellenVernetzern umgesetzt sind,
  • Umsetzungsprodukte von Polyethyleniminen mit einbasischen Carbonsäuren zu amidierten Polyethyleniminen,
  • Michaeladditionsprodukte von Polyethyleniminenen an ethylenisch ungesättigte Säuren, Salze, Ester, Amide oder Nitrile von monoethylenisch ungesätitgten Carbonsäuren,
  • phosphonomethylierten Polyethylenimine,
  • carboxylierten Polyethylenimine und
  • alkoxylierten Polyethylenimine.
As (b) ethyleneimine units containing polymers used z. B. in the inventive method, at least one water-soluble cationic polymer from the group of
  • Homopolymers of ethyleneimine,
  • polyethyleneimines reacted with at least bifunctional crosslinkers,
  • ethyleneimine grafted polyamidoamines reacted with at least bifunctional crosslinkers,
  • Reaction products of polyethylenimines with monobasic carboxylic acids to amidated polyethylenimines,
  • Michael addition products of polyethyleneimines to ethylenically unsaturated acids, salts, esters, amides or nitriles of monoethylenically unsaturated carboxylic acids,
  • phosphonomethylated polyethyleneimines,
  • carboxylated polyethyleneimines and
  • alkoxylated polyethyleneimines.

Polymere, die dadurch erhalten werden, dass man zunächst mindestens eine Polycarbonsäure mit mindestens einem Polyamin zu Polyamidoamine kondensiert, dann mit Ethylenimin pfropft und die Umsetzungsprodukte anschließend mit einer der oben genanten Verbindungen vernetzt, gehören zu den bevorzugt in Betracht kommenden E-thylenimineinheiten enthaltenden Verbindungen. Ein Verfahren zur Herstellung sol-cher Verbindungen ist beispielsweise in DE-A-2434816 beschrieben, wobei α,ω-Chlorhydrinether von Oligo- oder Polyethylenoxiden als Vernetzer Anwendung finden.Polymers which are obtained by first condensing at least one polycarboxylic acid with at least one polyamine to form polyamidoamines, then grafting with ethyleneimine and then crosslinking the reaction products with one of the abovementioned compounds belong to the compounds preferably containing E-thylenimine units. A method for producing such compounds is, for example, in DE-A-2434816 wherein α, ω-chlorohydrin ethers of oligo- or polyethylene oxides are used as crosslinkers application.

Besonders bevorzugt sind Produkte der beiden vorstehenden Typen, die einer Ultrafiltration unterzogen und so in ihrem Molekulargewichtsverteilung optimiert wurden. Solche ultrafiltrierten Produkte werden ausführlich in WO 00/67884 und WO 97/ 25367 beschrieben.Particularly preferred are products of the two above types which have been subjected to ultrafiltration and thus optimized in their molecular weight distribution. Such ultrafiltered products are extensively in WO 00/67884 and WO 97/25367 described.

Umsetzungsprodukte von Polyethyleniminen mit einbasischen Carbonsäuren zu amidierten Polyethyleniminen sind aus der WO 94/12560 bekannt. Michaeladditionsprodukte von Polyethyleniminen an ethylenisch ungesättigte Säuren, Salze, Ester, Amide oder Nitrile von monoethylenisch ungesätitgten Carbonsäuren sind Gegenstand der WO 94/14873 . Phosphonomethylierte Polyethylenimine werden ausführlich in der WO 97/25367 beschrieben. Carboxylierten Polyethylenimine sind beispielsweise mit Hilfe einer Steckersynthese durch Umsetzung von Polyethyleniminen mit Formaldehyd und Ammoniak/Cyanwasserstoff und Hydrolyse der Umsetzungsprodukte erhältlich. Alkoxylierte Polyethylenimine sind durch Umsetzung von Polyethyleiminen mit Alkylenoxiden wie Ethylenoxid und/oder Propylenoxid herstellbar.Reaction products of polyethylenimines with monobasic carboxylic acids to amidated polyethylenimines are known from the WO 94/12560 known. Michael addition products of polyethyleneimines with ethylenically unsaturated acids, salts, esters, amides or nitriles of monoethylenically unsaturated carboxylic acids are the subject of WO 94/14873 , Phosphonomethylated polyethylenimines are described in detail in U.S. Pat WO 97/25367 described. Carboxylated polyethyleneimines are obtainable, for example, by means of a plug synthesis by reacting polyethyleneimines with formaldehyde and ammonia / hydrogen cyanide and hydrolysing the reaction products. Alkoxylated polyethyleneimines can be prepared by reacting Polyethyleiminen with alkylene oxides such as ethylene oxide and / or propylene oxide.

Die Ethylenimineinheiten enthaltenden Polymeren haben beispielsweise Molmassen von 10 000 bis 3 000 000. Die kationische Ladung der Ethylenimineinheiten enthaltenden Polymeren beträgt z.B. mindestens 4 meq/g. Sie liegt meistens in dem Bereich von 8 bis 20 meq/g.The polymers containing ethyleneimine units have, for example, molecular weights of from 10,000 to 3,000,000. The cationic charge of the polymers containing ethyleneimine units is e.g. at least 4 meq / g. It is usually in the range of 8 to 20 meq / g.

Das Gewichtsverhältnis von (a) Vinylamineinheiten enthaltenden Polymeren zu (b) Ethylenimineinheiten enthaltenden Polymeren beträgt bei dem erfindungsgemäßen Verfahren beispielsweise 10 : 1 bis 1 : 10, vorzugsweise 5 : 1 bis 1 : 5. Die Kombination aus Ethylenimineinheiten enthaltenden Polymeren und Vinylamineinheiten enthaltenden Polymeren werden bei dem erfindungsgemäßen Verfahren zur Herstellung von Papier beispielsweise in einer Menge von 0,01 bis 2,0 Gew.-%, vorzugsweise 0,1 bis 1,0 Gew.-%, bezogen auf trockenen Papierstoff eingesetzt.The weight ratio of polymers containing (a) vinylamine units to polymers containing (b) ethyleneimine units in the process of the present invention is, for example, 10: 1 to 1:10, preferably 5: 1 to 1: 5. The combination of polymers containing ethyleneimine units and polymers containing vinylamine units used in the inventive method for producing paper, for example in an amount of 0.01 to 2.0 wt .-%, preferably 0.1 to 1.0 wt .-%, based on dry pulp.

Zu den wasserlöslichen polymeren anionischen Verbindungen gehören alle Polymere, die Säuregruppen oder deren Salze tragen und eine Ladungdichte von > 0,5 meq/g besitzen. Bei den Säuregruppen kann es sich um Carboxylgruppen, Sulfonsäuregruppen und Phosphonsäuregruppen handeln. Auch Ester der Phosphorsäure gehören hierzu, wobei mindestens eine Säurefunktion der Phosphorsäure nicht verestert ist. Grundsätzlich Verwendung finden können Polymerisate, Polykondensate z.B. Polyasparaginsäure , Polyadditionsverbindungen und auch durch ringöffnende Polymerisation hergestellte Verbindungen mit einer Ladungsdichte von jeweils > 0,5 meq/g. Ebenfalls anwendbar sind Polymere, die durch polymeranaloge Reaktionen wie Strecker-Reaktion oder durch Phosphonomethylierung mit sauren Gruppen modifiziert wurden. Bevorzugt sind jedoch Polymerisate folgender Zusammensetzung:

  1. (1) wenigstens einem Monomer, das ausgewählt ist aus der Gruppe bestehend aus
    • (1.1) monoethylenisch ungesättigten Sulfonsäuren, Phosphonsäuren, Phosphorsäureestern und Derivaten davon, und
    • (1.2) monoethylenisch ungesättigten Mono- und Dicarbonsäuren, deren Salzen und Dicarbonsäureanhydriden,
  2. (2) gegebenenfalls wenigstens einem von den Komponenten (1.1) und (1.2) verschiedenen monoethylenisch ungesättigten Monomer, und
  3. (3) gegebenenfalls wenigstens eine Verbindung, die mindestens zwei ethylenisch ungesättigte Doppelbindungen im Molekül aufweist,
mit der Maßgabe, dass das Monomerengemisch mindestens ein Monomer (1) mit mindestens einer freien Säuregruppe und/oder einer Säuregruppe in Salzform enthält.The water-soluble polymeric anionic compounds include all polymers which carry acid groups or their salts and have a charge density of> 0.5 meq / g. The acid groups may be carboxyl groups, sulfonic acid groups and phosphonic acid groups. Also esters of phosphoric acid belong to this, wherein at least one acid function of the phosphoric acid is not esterified. In principle, it is possible to use polymers, polycondensates, for example polyaspartic acid, polyaddition compounds and also compounds prepared by ring-opening polymerization with a charge density of> 0.5 meq / g in each case. Also applicable are polymers which have been modified by polymer-analogous reactions such as Strecker reaction or by phosphonomethylation with acidic groups. However, preference is given to polymers of the following composition:
  1. (1) at least one monomer selected from the group consisting of
    • (1.1) monoethylenically unsaturated sulfonic acids, phosphonic acids, phosphoric acid esters and derivatives thereof, and
    • (1.2) monoethylenically unsaturated mono- and dicarboxylic acids, their salts and dicarboxylic acid anhydrides,
  2. (2) optionally at least one monoethylenically unsaturated monomer other than components (1.1) and (1.2), and
  3. (3) if appropriate, at least one compound which has at least two ethylenically unsaturated double bonds in the molecule,
with the proviso that the monomer mixture contains at least one monomer (1) with at least one free acid group and / or one acid group in salt form.

Als Monomere der Gruppe (1.1) sind Verbindungen geeignet, die einen organischen Rest mit einer polymerisierbaren, α,β-ethylenisch ungesättigten Doppelbindung und mindestens einer Sulfonsäure- oder Phosphonsäuregruppe pro Molekül aufweisen. Geeignet sind weiterhin die Salze und Ester der zuvor genannten Verbindungen. Bei den Estern der Phosphonsäuren kann es sich dabei um die Mono- oder die Diester handeln. Geeignete Monomere (1.1) sind weiterhin Ester der Phosphorsäure mit Alkoholen mit einer polymersierbaren, a,β-ethylenisch ungesättigten Doppelbindung. Dabei kann ein Proton der Phosphorsäuregruppe oder es können die beiden übrigen Protonen der Phosphorsäuregruppe durch geeignete Basen neutralisiert oder mit Alkoholen, die keine polymerisierbaren Doppelbindungen aufweisen, verestert sein.Suitable monomers of group (1.1) are compounds which have an organic radical having a polymerizable, α, β-ethylenically unsaturated double bond and at least one sulfonic acid or phosphonic acid group per molecule. Also suitable are the salts and esters of the aforementioned compounds. The esters of phosphonic acids may be mono- or diesters. Suitable monomers (1.1) are furthermore esters of phosphoric acid with alcohols having a polymerizable, α, β-ethylenically unsaturated double bond. In this case, a proton of the phosphoric acid group or the other two protons of the phosphoric acid group can be neutralized by suitable bases or esterified with alcohols which have no polymerizable double bonds.

Geeignete Basen zur teilweisen oder vollständigen Neutralisation der Säuregruppen der Monomere (1.1) sind beispielsweise Alkalimetall- oder Erdalkalimetallbasen, Ammoniak, Amine und/oder Alkanolamine. Beispiele hierfür sind Natriumhydroxid, Kaliumhydroxid, Natriumcarbonat, Kaliumcarbonat, Natriumhydrogencarbonat, Kaliumhydrogencarbonat, Magnesiumhydroxid, Magnesiumoxid, Calciumhydroxid, Calciumoxid, Triethanolamin, Ethanolamin, Morpholin, Diethylentriamin oder Tetraethylenpentamin. Geeignete Alkohole zur Veresterung der Phosphorsäure sind beispielsweise C1-C6-Alkanole, wie beispielsweise Methanol, Ethanol, n-Propanol, Isopropanol, n-Butanol, sec.-Butanol, tert.-Butanol, n-Pentanol, n-Hexanol sowie deren Isomere.Suitable bases for the partial or complete neutralization of the acid groups of the monomers (1.1) are, for example, alkali metal or alkaline earth metal bases, ammonia, amines and / or alkanolamines. Examples of these are sodium hydroxide, potassium hydroxide, sodium carbonate, potassium carbonate, sodium hydrogencarbonate, potassium hydrogencarbonate, magnesium hydroxide, magnesium oxide, calcium hydroxide, calcium oxide, triethanolamine, ethanolamine, morpholine, diethylenetriamine or tetraethylenepentamine. Suitable alcohols for the esterification of phosphoric acid are, for example, C 1 -C 6 -alkanols, such as, for example, methanol, ethanol, n-propanol, isopropanol, n-butanol, sec-butanol, tert-butanol, n-pentanol, n-hexanol and their isomers.

Zu den Monomeren (1.1) zählen beispielsweise Vinylsulfonsäure, Allylsulfonsäure, Methallylsulfonsäure, Sulfoethylacrylat, Sulfoethylmethacrylat, Sulfopropylacrylat, Sulfopropylmethacrylat, 2-Hydroxy-3-acryloxypropylsulfonsäure, 2-Hydroxy-3-methacryloxypropylsulfonsäure, Styrolsulfonsäure, Acrylamidomethylenphosphonsäure, 2-Acrylamido-2-methylpropansulfonsäure, Vinylphosphonsäure, CH2=CH-NH-CH2-PO3H, Vinylphosphonsäuremonomethylester, Vinylphosphonsäuredimethylester, Al-lylphosphonsäure, Allylphosphonsäuremonomethylester, Allylphosphonsäuredimethylester, Acrylamidomethylpropylphosphonsäure, (Meth)acrylethylenglykolphosphat und Phosphorsäuremonoallylester.The monomers (1.1) include, for example, vinylsulfonic acid, allylsulfonic acid, methallylsulfonic acid, sulfoethyl acrylate, sulfoethyl methacrylate, sulfopropyl acrylate, sulfopropyl methacrylate, 2-hydroxy-3-acryloxypropylsulfonic acid, 2-hydroxy-3-methacryloxypropylsulfonic acid, styrenesulfonic acid, acrylamidomethylenephosphonic acid, 2-acrylamido-2-methylpropanesulfonic acid, Vinylphosphonic acid, CH 2 = CH-NH-CH 2 -PO 3 H, monomethyl vinylphosphonate, dimethyl vinylphosphonate, allylphosphonic acid, monomethyl allylphosphonate, dimethyl allylphosphonate, acrylamidomethylpropylphosphonic acid, (meth) acrylethylene glycol phosphate and monoesters of phosphoric acid.

Werden als Komponente (1.1) ausschließlich Monomere eingesetzt, bei denen alle Protonen der Säuregruppen verestert sind, wie z. B. Vinylphosphonsäuredimethylester oder Allylphosphonsäuredimethylester, so wird zur Polymerisation wenigstens eine monoethylenisch ungesättigte Mono- und/oder Dicarbonsäure oder ein Salz davon eingesetzt, wie sie im Folgenden als Komponente (1.2) beschrieben werden. Somit ist sichergestellt, dass die erfindungsgemäß eingesetzten Copolymerisate anionische Gruppen aufweisen.Are used as component (1.1) exclusively monomers in which all protons of the acid groups are esterified, such as. As Vinylphosphonsäuredimethylester or Allylphosphonsäuredimethylester, so at least one monoethylenically unsaturated mono- and / or dicarboxylic acid or a salt thereof is used for the polymerization, as described below as component (1.2). This ensures that the copolymers used according to the invention have anionic groups.

Die zuvor genannten Monomere (1.1) können einzeln oder in Form von beliebigen Mischungen bei der Herstellung der anionischen Polymeren eingesetzt werden.The abovementioned monomers (1.1) can be used individually or in the form of any desired mixtures in the preparation of the anionic polymers.

Als Monomere der Gruppe (1.2) kommen monoethylenisch ungesättigte Carbonsäuren mit 3 bis 8 C-Atomen sowie die wasserlöslichen Salze wie Akalimetall-, Erdalkalimetall-oder Ammoniumsalze dieser Carbonsäuren und die monoethylenisch ungesättigten Carbonsäureanhydride in Betracht. Zu dieser Gruppe von Monomeren gehören beispielsweise Acrylsäure, Methacrylsäure, Dimethacrylsäure, Ethacrylsäure, α-Chloracrylsäure, Maleinsäure, Maleinsäureanhydrid, Fumarsäure, Itaconsäure, Mesaconsäure, Citraconsäure, Glutaconsäure, Aconitsäure, Methylenmalonsäure, Allylessigsäure, Vinylessigsäure und Crotonsäure. Die Monomeren der Gruppe (1.2) können allein oder in Mischung miteinander, in teilweise oder in vollständig neutralisierter Form bei der Homo- bzw. Copolymerisation eingesetzt werden. Zur Neutralisation geeignete Basen sind die oben bei der Komponente (1.1) genannten Verbindungen.Suitable monomers of group (1.2) are monoethylenically unsaturated carboxylic acids having 3 to 8 carbon atoms and the water-soluble salts such as alkali metal, alkaline earth metal or ammonium salts of these carboxylic acids and the monoethylenically unsaturated carboxylic acid anhydrides. This group of monomers includes, for example, acrylic acid, methacrylic acid, dimethacrylic acid, ethacrylic acid, α-chloroacrylic acid, maleic acid, maleic anhydride, fumaric acid, itaconic acid, mesaconic acid, citraconic acid, glutaconic acid, aconitic acid, methylenemalonic acid, allylacetic acid, vinylacetic acid and crotonic acid. The monomers of group (1.2) can be used alone or mixed with each other, in partially or completely neutralized form in the homo- or copolymerization. Suitable bases for neutralization are the compounds mentioned above in component (1.1).

Das wasserlösliche anionische Polymerisat enthält wenigstens ein Monomer aus der Gruppe (1), das ausgewählt ist aus den Untergruppen (1.1) und/oder (1.2). Selbstverständlich kann das wasserlösliche Copolymerisat auch Mischungen von Monomeren aus den Untergruppen (1.1) und (1.2) einpolymerisiert enthalten.The water-soluble anionic polymer contains at least one monomer from the group (1) which is selected from the subgroups (1.1) and / or (1.2). Of course, the water-soluble copolymer may also contain mixtures of monomers from subgroups (1.1) and (1.2) in copolymerized form.

Die Copolymerisate können zur Modifizierung gegebenenfalls wenigstens ein weiteres Monomer der Gruppe (2) in einpolymerisierter Form enthalten. Vorzugsweise sind diese Monomere ausgewählt unter Estern α,β-ethylenisch ungesättigter Mono- und Dicarbonsäuren mit C1-C30-Alkanolen, C2-C30-Alkandiolen und C2-C30-Aminoalkoholen, Amiden α,β-ethylenisch ungesättigter Monocarbonsäuren und deren N-Alkyl- und N,N-Dialkylderivaten, Estern von Vinylalkohol und Allylalkohol mit C1-C30-Monocarbonsäuren, N-Vinyllactamen, stickstoffhaltigen Heterocyclen mit α,β-ethylenisch ungesättigten Doppelbindungen, Vinylaromaten, Vinylhalogeniden, Vinylidenhalogeniden, C2-C8-Monoolefinen und Mischungen davon.If appropriate, the copolymers may contain at least one further monomer of group (2) in copolymerized form for modification. These monomers are preferably selected from esters of α, β-ethylenically unsaturated mono- and dicarboxylic acids with C 1 -C 30 -alkanols, C 2 -C 30 -alkanediols and C 2 -C 30 -aminoalcohols, amides of α, β-ethylenically unsaturated monocarboxylic acids and their N-alkyl and N, N-dialkyl derivatives, esters of vinyl alcohol and allyl alcohol with C 1 -C 30 monocarboxylic acids, N-vinyl lactams, nitrogen-containing heterocycles having α, β-ethylenically unsaturated double bonds, vinyl aromatics, vinyl halides, vinylidene halides, C 2 C 8 monoolefins and mixtures thereof.

Geeignete Vertreter der Gruppe (2) sind z. B. Methyl(meth)acrylat, Methylethacrylat, Ethyl(meth)acrylat, Ethylethacrylat, n-Butyl(meth)acrylat, Isobutyl(meth)acrylat, tert.-Butyl(meth)acrylat, tert.-Butylethacrylat, n-Ocytl(meth)acrylat, 1,1,3,3-Tetramethylbutyl(meth)acrylat, Ethylhexyl(meth)acrylat und Mischungen davon. Geeignete zusätzliche Monomere (2) sind weiterhin Acrylsäureamid, Methacrylsäureamid, N-Methyl(meth)acrylamid, N-Ethyl(meth)acrylamid, n-Propyl(meth)acrylamid, N-(n-Butyl)(meth)acrylamid, tert.-Butyl(meth)acrylamid, n-Octyl(meth)acrylamid, 1,1,3,3-Tetramethylbutyl(meth)acrylamid, Ethylhexyl(meth)acrylamid und Mischungen davon.Suitable representatives of group (2) are z. Methyl (meth) acrylate, methyl methacrylate, ethyl (meth) acrylate, ethyl methacrylate, n-butyl (meth) acrylate, isobutyl (meth) acrylate, tert-butyl (meth) acrylate, tert-butyl methacrylate, n-ocytl ( meth) acrylate, 1,1,3,3-tetramethylbutyl (meth) acrylate, ethylhexyl (meth) acrylate and mixtures thereof. Suitable additional monomers (2) are furthermore acrylic acid amide, methacrylamide, N-methyl (meth) acrylamide, N-ethyl (meth) acrylamide, n-propyl (meth) acrylamide, N- (n-butyl) (meth) acrylamide, tert. Butyl (meth) acrylamide, n-octyl (meth) acrylamide, 1,1,3,3-tetramethylbutyl (meth) acrylamide, ethylhexyl (meth) acrylamide and mixtures thereof.

Weiterhin sind als Monomere (2) geeignet 2-Hydroxyethyl(meth)acrylat, 2-Hydroxyethylethacrylat, 2-Hydroxypropyl(meth)acrylat, 3-Hydroxypropyl(meth)acrylat, 3-Hydroxybutyl(meth)acrylat, 4-Hydroxybutyl(meth)acrylat, 6-Hydroxyhexyl(meth)acrylat und Mischungen davon.Further, as monomers (2), 2-hydroxyethyl (meth) acrylate, 2-hydroxyethyl methacrylate, 2-hydroxypropyl (meth) acrylate, 3-hydroxypropyl (meth) acrylate, 3-hydroxybutyl (meth) acrylate, 4-hydroxybutyl (meth) are suitable. acrylate, 6-hydroxyhexyl (meth) acrylate and mixtures thereof.

Weiterhin geeignete Monomere der Gruppe (2) sind Nitrile von α,β-ethylenisch ungesättigten Mono- und Dicarbonsäuren, wie beispielsweise Acrylnitril und Methacrylnitril.Further suitable monomers of group (2) are nitriles of α, β-ethylenically unsaturated mono- and dicarboxylic acids, such as, for example, acrylonitrile and methacrylonitrile.

Geeignete Monomere der Gruppe (2) sind weiterhin N-Vinyllactame und deren Derivate, die z. B. einen oder mehrere C1-C6-Alkylsubstituenten (wie oben definiert) aufweisen können. Dazu zählen N-Vinylpyrrolidon, N-Vinylpiperidon, N-Vinylcaprolactam, N-Vinyl-5-methyl-2-pyrrolidon, N-Vinyl-5-ethyl-2-pyrrolidon, N-Vinyl-6-methyl-2-piperidon, N-Vinyl-6-ethyl-2-piperidon, N-Vinyl-7-methyl-2-caprolactam, N-Vinyl-7-ethyl-2-caprolactam und deren Mischungen.Suitable monomers of group (2) are also N-vinyl lactams and derivatives thereof, the z. B. one or more C 1 -C 6 alkyl substituents (as defined above) may have. These include N-vinylpyrrolidone, N-vinylpiperidone, N-vinylcaprolactam, N-vinyl-5-methyl-2-pyrrolidone, N-vinyl-5-ethyl-2-pyrrolidone, N-vinyl-6-methyl-2-piperidone, N-vinyl-6-ethyl-2-piperidone, N-vinyl-7-methyl-2-caprolactam, N-vinyl-7-ethyl-2-caprolactam and mixtures thereof.

Geeignete zusätzliche Monomere der Gruppe (2) sind weiterhin Ethylen, Propylen, Isobutylen, Butadien, Styrol, α-Methylstyrol, Vinylacetat, Vinylpropionat, Vinylchlorid, Vinylidenchlorid, Vinylfluorid, Vinylidenfluorid und Mischungen davon.Further suitable monomers of group (2) are ethylene, propylene, isobutylene, butadiene, styrene, α-methylstyrene, vinyl acetate, vinyl propionate, vinyl chloride, vinylidene chloride, vinyl fluoride, vinylidene fluoride and mixtures thereof.

Die zuvor genannten Monomere der Gruppe (2) können bei der Copolymerisation mit mindestens einem anionischen Monomer einzeln oder in Form von beliebigen Mischungen eingesetzt werden.The aforementioned monomers of group (2) can be used in the copolymerization with at least one anionic monomer, individually or in the form of any mixtures.

Eine weitere Modifizierung der Copolymerisate ist dadurch möglich, dass man bei der Copolymerisation Monomere der Gruppe (3) einsetzt, die mindestens zwei Doppelbindungen im Molekül enthalten, z. B. Methylenbisacrylamid, Glykoldiacrylat, Glykoldimethacrylat, Glycerintriacrylat, Pentaerythrittriallylether, mindestens zweifach mit Acrylsäure und/oder Methacrylsäure veresterte Polyalkylenglykole oder Polyole wie Pentaerythrit, Sobit oder Glukose. Falls mindestens ein Monomer der Gruppe (3) bei der Copolymerisation eingesetzt wird, so betragen die angewendeten Mengen bis zu 2 Mol-%, z. B. 0,001 bis 1 Mol-%.A further modification of the copolymers is possible by using in the copolymerization monomers of group (3) which contain at least two double bonds in the molecule, for. As methylenebisacrylamide, glycol diacrylate, glycol dimethacrylate, glycerol triacrylate, pentaerythritol triallyl ether, at least two times with acrylic acid and / or methacrylic acid esterified polyalkylene glycols or polyols such as pentaerythritol, soba or glucose. If at least one monomer of group (3) is used in the copolymerization, the amounts used are up to 2 mol%, z. B. 0.001 to 1 mol%.

Weiterhin kann es sinnvoll sein, bei der Polymerisation den Einsatz vorstehender Vernetzter mit dem Zusatz von Reglern zu kombinieren. Eingesetzt werden typischerweise 0,001 bis 5 Mol-% mindestens eines Reglers. Anwendung finden können alle literaturbekannten Regler wie Mercaptoethanol, 2-Ethylhexylthioglycolat, Thioglycolsäure, Dodecylmercaptan, Natriumhypophosphit, Ameisensäure und/oder Tribromchlormethan.Furthermore, it may be useful to combine the use of the above crosslinked with the addition of regulators in the polymerization. Typically, from 0.001 to 5 mole percent of at least one regulator is employed. All known literature can be used Regulators such as mercaptoethanol, 2-ethylhexyl thioglycolate, thioglycolic acid, dodecyl mercaptan, sodium hypophosphite, formic acid and / or tribromochloromethane.

Vorzugsweise verwendet man als anionische polymere Verbindung Homopolymerisate von ethylenisch ungesättigten C3- bis C5-Carbonsäuren, insbesondere Polyacrylsäure und Polymethacrylsäure sowie hydrolysierte Homopolymerisate von Maleinsäureanhydrid und von Itaconsäureanhydrid. Bevorzugt in Betracht kommende anionische Copolymerisate enthalten beispielsweise (1) 10 bis 99 Gew.-% mindestens einer ethylenisch ungesättigten C3- bis C5-Carbonsäure und (2) 90 bis 1 Gew.-% mindestens eines Amids, Nitrils und/oder eines Esters einer ethylenisch ungesättigten C3- bis C5-Carbonsäure in einpolymerisierter Form. Die Summe der Gewichtsprozente aus den Komponenten (1) und (2) beträgt dabei immer 100. Besonders bevorzugt sind Copolymerisate aus Acrylsäure und Acrylamid, Copoylmerisate aus Acrylsäure und Acrylnitril, Copolymerisate aus Acrylsäure und N-Vinylformamid, Copolymerisate aus Methacrylsäure und Methacrylamid, Copolymerisate aus Methacrylsäure und N-Vinylformamid, Copolymerisate aus Acrylsäure und Methacrylamid, Copolymerisate aus Acrylsäure und Methacrylnitril, Copolymerisate aus Methacrylsäure und Methacrylnitril sowie Copolymerisate aus Acrylsäure, Acrylamid und Acrylnitril.The anionic polymeric compound used is preferably homopolymers of ethylenically unsaturated C 3 - to C 5 -carboxylic acids, in particular polyacrylic acid and polymethacrylic acid, and also hydrolyzed homopolymers of maleic anhydride and of itaconic anhydride. Preferred anionic copolymers comprise, for example, (1) 10 to 99% by weight of at least one ethylenically unsaturated C 3 to C 5 carboxylic acid and (2) 90 to 1% by weight of at least one amide, nitrile and / or one Esters of an ethylenically unsaturated C 3 - to C 5 -carboxylic acid in copolymerized form. The sum of the percentages by weight of components (1) and (2) is always 100. Particularly preferred are copolymers of acrylic acid and acrylamide, Copoylmerisate of acrylic acid and acrylonitrile, copolymers of acrylic acid and N-vinylformamide, copolymers of methacrylic acid and methacrylamide, copolymers of Methacrylic acid and N-vinylformamide, copolymers of acrylic acid and methacrylamide, copolymers of acrylic acid and methacrylonitrile, copolymers of methacrylic acid and methacrylonitrile and copolymers of acrylic acid, acrylamide and acrylonitrile.

Die anionischen Polymerisate sind wasserlöslich. Sie können in Form der freien Säuren und/oder als Alkalimetall-, Erdalkalimetall- oder als Ammoniumsalz bei dem erfindungsgemäßen Verfahren eingesetzt werden. Sie haben beispielsweise einen K-Wert von 50 bis 250 (bestimmt nach H. Fikentscher in 5 gew.-%iger wässriger Kochsalzlösung bei 25 °C und pH 7).The anionic polymers are water-soluble. They can be used in the form of the free acids and / or as alkali metal, alkaline earth metal or ammonium salt in the process according to the invention. They have, for example, a K value of 50 to 250 (determined according to H. Fikentscher in 5% strength by weight aqueous sodium chloride solution at 25 ° C. and pH 7).

Das wasserlösliche anionische Polymer wird bei dem erfindungsgemäßen Verfahren in einer Menge von beispielsweise 0,01 bis 2,0 Gew.-%, vorzugsweise 0,05 bis 1,0 Gew.-%, insbesondere 0,1 bis 0,5 Gew.-%, bezogen auf trockenen Papierstoff, eingesetzt. Das Gew.-Verhältnis von kationischen Polymeren (a) Vinylamineinheiten enthaltenden Polymeren und (b) Ethylenimineinheiten enthaltenden Polymeren zu den wasserlöslichen polymeren anionischen Verbindungen beträgt beispielsweise 3 : 1 bis 1 : 3 und liegt vorzugsweise bei 1 : 1.The water-soluble anionic polymer is used in the process according to the invention in an amount of, for example, from 0.01 to 2.0% by weight, preferably from 0.05 to 1.0% by weight, in particular from 0.1 to 0.5% by weight. %, based on dry pulp, used. The weight ratio of cationic polymers (a) polymers containing vinylamine units and (b) polymers containing ethyleneimine units to the water-soluble polymeric anionic compounds is for example 3: 1 to 1: 3 and is preferably 1: 1.

Für die Papierherstellung kommen als Faserstoffe zur Herstellung der Pulpen kommen sämtliche dafür gebräuchlichen Qualitäten in Betracht, z.B. Holzstoff, gebleichter und ungebleichter Zellstoff sowie Pa-pierstoffe aus allen Einjahrespflanzen. Zu Holzstoff gehören beispielsweise Holzschliff, thermomechanischer Stoff (TMP), chemothermomechanischer Stoff (CTMP), Druck-schliff, Halbzellstoff, Hochausbeute-Zellstoff und Refiner Mechanical Pulp (RMP). Als Zellstoff kommen beispielsweise Sulfat-, Sulfit- und Natronzellstoffe in Betracht. Bei-spielsweise verwendet man ungebleichten Zellstoff, der auch als ungebleichter Kraft-zellstoff bezeichnet wird. Geeignete Einjahrespflanzen zur Herstellung von Papierstoffen sind beispielsweise Reis, Weizen, Zuckerrohr und Kenaf.For papermaking, the pulps used for producing the pulps are all grades which are customary for this purpose, for example wood pulp, bleached and unbleached pulp and paper pulp from all annual plants. Wood pulp includes, for example, groundwood, thermomechanical pulp (TMP), chemothermomechanical pulp (CTMP), pressure groundwood, semi-pulp, high yield pulp, and refiner mechanical pulp (RMP). As pulp, for example, sulphate, sulphite and soda pulps come into consideration. For example, unbleached pulp, also referred to as unbleached kraft pulp, is used. Suitable annual plants For example, rice, wheat, sugar cane and kenaf are used to make paper stocks.

Das erfindungsgemäße Verfahren eignet sich insbesondere für die Herstellung von trockenfest ausgerüsteten Papieren aus Altpapier (umfassend deinked Altpapier), das entweder allein oder in Mischung mit anderen Faserstoffen eingesetzt wird. Man kann auch von Fasermischungen aus einem Primärstoff und zurückgeführtem gestrichenem Ausschuss ausgehen, z. B. gebleichtes Kiefernsulfat in Mischung mit zurückgeführtem gestrichenem Ausschuss. Das erfindungsgemäße Verfahren ist für die Herstellung von Papier, Pappe und Karton aus Altpapier und in speziellen Fällen auch aus deinked Altpapier von technischem Interesse, weil es die Festigkeitseigenschaften der zurückgeführten Fasern deutlich erhöht. Es hat besondere Bedeutung für die Verbesserung von Festigkeitseigenschaften von graphischen Papieren und von Verpackungspapieren.The inventive method is particularly suitable for the production of dry-proof papers from waste paper (comprising deinked waste paper), which is used either alone or in admixture with other fibers. It is also possible to start with fiber blends of a primary material and recycled coated broke, e.g. B. bleached pine sulfate in admixture with recycled coated broke. The inventive method is for the production of paper, cardboard and cardboard from waste paper and in special cases from deinked waste paper of technical interest, because it significantly increases the strength properties of the recycled fibers. It is of particular importance for improving the strength properties of graphic papers and packaging papers.

Der pH-Wert der Stoffsuspension liegt beispielsweise in dem Bereich von 4,5 bis 8, meisten bei 6 bis 7,5. Zur Einstellung des pH-Wertes kann man beispielsweise eine Säure wie Schwefelsäure oder Aluminiumsulfat verwenden.The pH of the stock suspension is, for example, in the range of 4.5 to 8, most 6 to 7.5. To adjust the pH, it is possible to use, for example, an acid, such as sulfuric acid or aluminum sulphate.

Bei dem erfindungsgemäßen Verfahren werden vorzugsweise zunächst die kationischen Polymerisate, nämlich (a) Vinylamineinheiten enthaltende Polymere und (b) Ethylenimineinheiten enthaltende Polymere, zum Papierstoff dosiert. Die Zugabe der kationischen Polymeren kann dabei zum Dickstoff (Faserkonzentration >15 g/l, z.B. in dem Bereich von 25 bis 40 g/l bis zu 60 g/l) oder vorzugsweise zu einem Dünnstoff (Faserkonzentration <15 g/l, z.B. in dem Bereich von 5 bis 12 g/l) erfolgen. Die Zugabestelle liegt vorzugsweise vor den Sieben, sie kann jedoch auch zwischen einer Scherstufe und einem Screen oder danach liegen. Die Dosierung der kationischen Polymeren (a) und (b) zum Papierstoff kann beispielsweise nacheinander, gleichzeitig oder auch als Mischung von (a) und (b) erfolgen.In the process according to the invention, the cationic polymers, namely (a) polymers comprising vinylamine units and polymers containing ethyleneimine units, are preferably first metered into the pulp. The cationic polymers can be added to the thick material (fiber concentration> 15 g / l, for example in the range from 25 to 40 g / l up to 60 g / l) or preferably to a thin material (fiber concentration <15 g / l, eg in in the range of 5 to 12 g / l). The point of addition is preferably in front of the screens, but it can also be between a shearing stage and a screen or afterwards. The dosage of the cationic polymers (a) and (b) to the paper stock can be carried out, for example, successively, simultaneously or else as a mixture of (a) and (b).

Die anionische Komponente wird meistens erst nach der Zugabe der kationischen Polymeren (a) und (b) zum Papierstoff zugegeben, kann aber auch gleichzeitig, jedoch getrennt von den kationischen Polymeren zum Papierstoff dosiert werden. Weiterhin ist es auch möglich zuerst die anionische und nachfolgend die kationische Komponente zuzugeben oder zunächst eine der kationischen Komponenten (a) oder (b) zum Papierstoff zu dosieren, dann das anionische Polymer zuzugeben und anschließend die andere kationische Komponente zuzusetzen.The anionic component is usually added only after the addition of the cationic polymers (a) and (b) to the paper stock, but can also be metered simultaneously to the stock, but separately from the cationic polymers. Furthermore, it is also possible first to add the anionic and subsequently the cationic component or first to meter one of the cationic components (a) or (b) to the paper stock, then to add the anionic polymer and then to add the other cationic component.

Bei dem erfindungsgemäßen Verfahren können die üblicherweise bei der Papierherstellung verwendeten Prozeßchemikalien in den üblichen Mengen eingesetzt werden, z. B. Retentionsmittel, Entwässerungsmittel, andere Trockenverfestiger wie beispielsweise Stärke, Pigmente, Füllstoffe, optische Aufheller, Entschäumer, Biozide und Papierfarbstoffe.In the method according to the invention, the process chemicals commonly used in papermaking can be used in the usual amounts, for. As retention aids, dehydrating agents, other dry strength such as Starch, pigments, fillers, optical brighteners, defoamers, biocides and paper dyes.

Nach dem erfindungsgemäßen Verfahren erhält man trockenfest ausgerüstete Papiere, deren Trockenfestigkeit gegenüber Papieren, die nach bekannten Verfahren hergestellt werden, eine erhöhte Trockenfestigkeit aufweisen. Außerdem ist bei dem erfindungsgemäßen Verfahren die Entwässerungsgeschwindigkeit im Vergleich mit bekannten Verfahren verbessert.The process according to the invention gives dry-proof papers whose dry strength relative to papers produced by known processes has an increased dry strength. In addition, in the method according to the invention, the dewatering rate is improved in comparison with known methods.

Die Prozentangaben in den Beispielen bedeuten, falls nichts anderes angegeben ist, Gewichtsprozent. Der K-Wert der Polymerisate wurde nach Fikentscher, CelluloseChemie, Band 13, 58 - 64 und 71 - 74 (1932 ) bei einer Temperatur von 25 °C in 5 gew.-%igen wässrigen Kochsalzlösungen bei einem pH-Wert von 7 und einer Polymerkonzentration von 0,5% bestimmt.The percentages in the examples are by weight unless otherwise specified. The K value of the polymers was after Fikentscher, Cellulose Chemie, Vol. 13, 58-64 and 71-74 (1932 ) at a temperature of 25 ° C in 5 wt .-% aqueous saline solutions at a pH of 7 and a polymer concentration of 0.5%.

Für die einzelnen Tests wurden in Laborversuchen Blätter in einem Rapid-Köthen-Laborblattbildner hergestellt. Die Blätter wurden für 24 Stunden bei 23°C und einer Luftfeutchtigkeit von 50 % gelagert. Danach wurden folgende Festigkeitsprüfungen durchgeführt:

  • Berstdruck nach DIN ISO 2758 (bis 600 kPa), DIN ISO 2759 (ab 600 kPa)
  • SCT nach DIN 54518 (Bestimmung des Streifenstauchwiderstandes)
  • CMT nach DIN EN 23035 (Bestimmung des Flachstauchwiderstandes)
  • DIN EN ISO 7263 (Bestimmung des Flachstauchwiderstandes an labormäßig gewellter Wellpappe)
For the individual tests, sheets were produced in laboratory tests in a Rapid-Köthen laboratory sheet former. The leaves were stored for 24 hours at 23 ° C and a 50% Luftfeutchtigkeit. Thereafter, the following strength tests were carried out:
  • Bursting pressure according to DIN ISO 2758 (up to 600 kPa), DIN ISO 2759 (from 600 kPa)
  • SCT according to DIN 54518 (determination of the strip crush resistance)
  • CMT according to DIN EN 23035 (determination of the flat crush resistance)
  • DIN EN ISO 7263 (Determination of the flat crush resistance on laboratory-corrugated corrugated board)

BeispieleExamples

In den Beispielen und in den Vergleichsbeispielen wurden folgende Polymere verwendet:

  • Polymer KA
    Polyethylenimin (Polymin® P, BASF SE, D-67056 Ludwigshafen)
  • Polymer KB
    Verwendet wurde ein mit Ethylenimin gepropftes und mit einem Dichlorhydrinether von Polyethylenglykol vernetztes Polyamidoamin, wie in DE-A 2434816 , Beispiel 13 beschrieben.
  • Polymer KC
    Verwendet wurde ein mit Ethylenimin gepropftes und vernetztes Polyamidoamin, das zusätzlich noch einer Ultrafiltration unterworfen wurde, vgl. WO 00/67884 , Seite 23, Beispiel B1 b.
  • Polymer KD
    Verwendet wurde ein zu 30 % teilhydrolysiertes Polyvinylformamid mit einem K-Wert von 90, wie in DE-A 10 2004 056551 , Seite 9, letzter Abschnitt als PVAm 4 beschrieben.
  • Polymer KE
    Verwendet wurde ein Polymer, das durch saure Hydrolyse eines Copolymers aus 30 Mol-% N-Vinylformamid und 70 Mol-% Acrylnitril hergestellt wurde, wie in DE 4328975 als Beispiel P auf den Seiten 8 und 9 beschrieben.
  • Polymer KF
    Verwendet wurde ein handelsübliches Hofmann-Abbau Produkt der Firrma SNF mit der Bezeichnung RSL HF 70D. Das Produkt hatte einen Festgehalt von 24,2 %, eine Viskosität von 19 mPas (Brookfield, LVT, Spindel 1, 60 Upm, 20°C) und eine Ladungsdichte von 57,2 meq/100 g Produkt (Polyelektrolyttitration).
  • Polymer KG
    Das verwendete Polymer war identisch mit dem in WO 2006/075115 auf Seite 13 in der Tabelle als C8 beta 2 bezeichnete Hofmann-Abbauprodukt. Es wurde hergestellt durch Umsetzung von Polyacrylamid mit Natriumhypochlorit im Molverhältnis 1 : 1, und Natronlauge, wobei das Molverhältnis von Natriumhydroxid zu Natriumhypochlorit 2 : 1 betrug.
  • Polymer KH
    Das verwendete Polymer war identisch mit dem in WO 2006/090076 auf Seite 15, Zeile 23 als C2 bezeichneten glyoxylierten Copolymer aus 95 Mol-% Acrylamid und 5 Mol-% Diallyldimethylammoniumchlorid (DADMAC).
  • Polymer AA
    Copolymer aus 70 % N-Vinylformamid und 30 % Acrylsäure in Form des Na-Salzes mit einem K-Wert von 85, wie in DE 10 2004 056551 auf Seite 9, letzter Abschnitt als Copolymerisat 4 beschrieben.
  • Polymer AB
    Das verwendete Polymer war identisch mit dem in WO 2006/075115 auf Seite 14 in der Tabelle als A1 bezeichneten Copolymer aus 70 % Acrylamid und 30 % Acrylsäure in Form des Na-Salzes.
  • Polymer AC
    Das verwendete Polymer war identisch mit dem in WO 2006/075115 auf Seite 14 in der Tabelle als A2 bezeichneten Copolymer aus 70 Mol-% Acrylamid und 30 Mol-% Acrylsäure, vernetzt mit Methylenbisacrylamid (MBA) in Form des Na-Salzes. Das Copolymer hatte eine anionische Ladung von 3,85 meq/g.
  • Polymer AD
    Das verwendete Polymer war identisch mit dem in WO 2006/090076 auf Seite 16 in der Tabelle als A2 bezeichneten Copolymer aus 70 Mol-% Acrylamid und 30 Mol-% Acrylsäure, vernetzt mit Methylenbisacrylamid (MBA) in Form des Na-Salzes. Das Copolymer hatte eine anionische Ladung von 3,85 meq/g.
In the examples and in the comparative examples, the following polymers were used:
  • Polymer KA
    Polyethyleneimine (Polymin® P, BASF SE, D-67056 Ludwigshafen)
  • Polymer KB
    A polyamidoamine grafted with ethyleneimine and crosslinked with a dichlorohydrin ether of polyethylene glycol was used as in DE-A 2434816 Example 13.
  • Polymer KC
    A polyamidoamine grafted with ethyleneimine and cross-linked, which was additionally subjected to ultrafiltration, was used, cf. WO 00/67884 , Page 23, example B1 b.
  • Polymer KD
    A 30% partially hydrolyzed polyvinylformamide having a K value of 90 was used as in DE-A 10 2004 056551 , Page 9, last section described as PVAm 4.
  • Polymer KE
    A polymer prepared by acid hydrolysis of a copolymer of 30 mole% N-vinylformamide and 70 mole% acrylonitrile was used as in DE 4328975 described as Example P on pages 8 and 9.
  • Polymer KF
    A commercially available Hofmann degradation product of the Firrma SNF with the designation RSL HF 70D was used. The product had a solids content of 24.2%, a viscosity of 19 mPas (Brookfield, LVT, Spindle 1, 60 rpm, 20 ° C) and a charge density of 57.2 meq / 100 g product (polyelectrolyte titration).
  • Polymer KG
    The polymer used was identical to that in WO 2006/075115 on page 13 in the table referred to as C8 beta 2 Hofmann degradation product. It was prepared by reacting polyacrylamide with sodium hypochlorite in a molar ratio of 1: 1, and sodium hydroxide solution, the molar ratio of sodium hydroxide to sodium hypochlorite being 2: 1.
  • Polymer KH
    The polymer used was identical to that in WO 2006/090076 on page 15, line 23, designated C2, glyoxylated copolymer of 95 mole% acrylamide and 5 mole% diallyldimethylammonium chloride (DADMAC).
  • Polymer AA
    Copolymer of 70% N-vinylformamide and 30% acrylic acid in the form of the Na salt with a K value of 85, as in DE 10 2004 056551 on page 9, last section described as copolymer 4.
  • Polymer AB
    The polymer used was identical to that in WO 2006/075115 on page 14 in the table as A1 designated copolymer of 70% acrylamide and 30% acrylic acid in the form of the Na salt.
  • Polymer AC
    The polymer used was identical to that in WO 2006/075115 on page 14 in the table referred to as A2 copolymer of 70 mol% of acrylamide and 30 mol% of acrylic acid, crosslinked with methylenebisacrylamide (MBA) in the form of the Na salt. The copolymer had an anionic charge of 3.85 meq / g.
  • Polymer AD
    The polymer used was identical to that in WO 2006/090076 on page 16 in the table referred to as A2 copolymer of 70 mol% of acrylamide and 30 mol% of acrylic acid, crosslinked with methylenebisacrylamide (MBA) in the form of the Na salt. The copolymer had an anionic charge of 3.85 meq / g.

Herstellung des Papierstoffs für die Beispiele und VergleichsbeispielePreparation of the paper stock for the examples and comparative examples

Ein Papier aus 100 % Altpapier (Mischung der Sorten: 1.02, 1.04,4.01) wurde mit Trinkwasser bei einer Stoffdichte von 4 % in einem Laborpulper stippenfrei aufgeschlagen und in einem Laborrefiner auf einen Mahlgrad von 40 °SR gemahlen. Dieser Stoff wurde anschließend mit Trinkwasser auf eine Stoffdichte von 0,7 % verdünnt.A paper made of 100% waste paper (mixture of the grades: 1.02, 1.04,4.01) was pitched with drinking water at a consistency of 4% in a laboratory pulper without specks and ground in a laboratory refiner to a freeness of 40 ° SR. This substance was then diluted with drinking water to a consistency of 0.7%.

Entwässerungsprüfungdrainage test

In den Beispielen und Vergleichsbeispielen wurde jeweils 1 Liter des oben beschriebenen Papierstoffs verwendet und jeweils nacheinander mit den in der Tabelle jeweils angegebenen wasserlöslichen Polymeren unter Rühren versetzt und danach mit Hilfe eines Schopper-Riegler-Entwässerungsprüfers entwässert, wobei man die Zeit in Sekunden für eine Durchflussmenge (Filtrat) von 600 ml bestimmte. Die Konzentration der wasserlöslichen kationischen und anionischen Polymeren, die jeweils als Trockenverfestigungsmittel für Papier getestet wurden, betrug jeweils 1 %. Die Messergebnisse sind in der Tabelle angegeben.In the examples and comparative examples, in each case 1 liter of the paper stock described above was used and in each case successively mixed with the water-soluble polymers indicated in the table with stirring and then dewatered using a Schopper-Riegler dewatering tester, wherein the time in seconds for a flow rate (Filtrate) of 600 ml. The concentration of water-soluble cationic and anionic polymers each tested as a dry strength agent for paper was 1% each. The measurement results are given in the table.

Blattbildungsheet formation

In den Beispielen und Vergleichsbeispielen wurden dem oben beschriebenen Papierstoff unter Rühren die in der Tabelle angegebenen Polymeren nacheinander zugesetzt. Die Polymerkonzentration der wässrigen Lösungen der kationschen und der anionischen Polymeren betrug jeweils 1 %. In der Tabelle sind die jeweils eingesetzten Mengen der Polymeren in Gewichtsprozent, bezogen auf den Festgehalt des Papierstoffs angegeben. Nach der letzten Zugabe eines wasserlöslichen Polymers zum Papierstoff wurde soviel Stoff abgenommen (ca. 500 ml), um auf einem Rapid-Köthen-Blattbildner ein Blatt mit einem Flächengewicht von 120 g/m2 (3,2 g otro = ofentrocken) herzustellen. Die Blätter wurden, wie im Rapid-Köthen-Verfahren üblich, abgegautscht und 8 Minuten bei 110 °C in einem Trockenzylinder getrocknet. Die Ergebnisse sind in der Tabelle angegeben. Tabelle 1 Beispiele Kationisches Polymer 1 Dosierung [%] Kationisches Polymer 2 Dosierung [%] anionisches Polymer Dosierung [%] Entwässerungszeit für 600 ml [s] Berstdruck [kPa] SCT [kN] CMT 30 [N] Vergleich 1 ohne ohne ohne 87 291 1,37 137 Vergleich 2 Polymer KD 0,3 ohne Polymer AA 0,3 72 375 2,04 180 Vergleich 3 Polymer KG 0,3 ohne Polymer AB 0,3 79 345 1,59 163 Vergleich 4 Polymer KG 0,3 ohne Polymer AC 0,3 76 358 1,61 170 Vergleich 5 Polymer KH 0,16 Polymer KG 0,14 Polymer AD 0,3 76 359 1,6 171 Beispiel 1 Polymer KA 0,1 Polymer KD 0,2 Polymer AA 0,3 69 376 2,06 180 Beispiel 2 Polymer KB 0,1 Polymer KD 0,2 Polymer AA 0,3 56 380 2,11 181 Beispiel 3 Polymer KC 0,1 Polymer KD 0,2 Polymer AA 0,3 50 385 2,17 186 Beispiel 4 Polymer KC 0,15 Polymer KD 0,15 Polymer AA 0,3 53 379 2,1 182 Beispiel 5 Polymer KC 0,2 Polymer KD 0,1 Polymer AA 0,3 60 377 2,05 181 Beispiel 6 Polymer KC 0,1 Polymer KD 0,2 Polymer AB 0,3 51 386 2,12 182 Beispiel 7 Polymer KC 0,1 Polymer KD 0,2 Polymer AC 0,3 50 388 2,16 185 Beispiel 8 Polymer KC 0,1 Polymer KE 0,2 Polymer AA 0,3 51 386 2,14 183 Beispiel 9 Polymer KF 0,2 Polymer KA 0,1 Polymer AA 0,3 77 358 1,6 170 Beispiel 10 Polymer KF 0,2 Polymer KB 0,1 Polymer AA 0,3 73 361 1,63 174 Beispiel 11 Polymer KF 0,2 Polymer KC 0,1 Polymer AA 0,3 67 368 1,67 177 Beispiel 12 Polymer KF 0,15 Polymer KC 0,15 Polymer AA 0,3 69 362 1,63 173 Beispiel 13 Polymer KF 0,1 Polymer KC 0,2 Polymer AA 0,3 74 359 1,6 173 Beispiel 14 Polymer KF 0,2 Polymer KC 0,1 Polymer AB 0,3 66 363 1,64 174 Beispiel 15 Polymer KF 0,2 Polymer KC 0,1 Polymer AC 0,3 64 365 1,68 177 Vergleich 2 nach Beispiel 6 der DE-A-10 2004 056551
Vergleich 3 nach Beispiel 17 der WO-A-2006/075115
Vergleich 4 nach Beispiel 1 der WO-A-2006/075115
Vergleich 5 nach Beispiel 5 der WO-A-2006/090076
In the examples and comparative examples, the polymers listed in the table were added successively to the above-described paper stock with stirring. The polymer concentration of the aqueous solutions of cationic and anionic polymers was 1% each. In the table, the amounts of polymers used in each case are given in percent by weight, based on the solids content of the paper stock. After the last addition of a water-soluble polymer to the stock, as much stock was removed (approximately 500 mL) to produce a sheet having a basis weight of 120 g / m 2 (3.2 g otro = oven-dry) on a Rapid-Kothen sheet former. The leaves were, as usual in Rapid-Köthen method, abgegautscht and dried for 8 minutes at 110 ° C in a drying cylinder. The results are given in the table. Table 1 Examples Cationic Polymer 1 Dosage [%] Cationic Polymer 2 Dosage [%] anionic polymer Dosage [%] Drainage time for 600 ml [s] Burst pressure [kPa] SCT [kN] CMT 30 [N] Comparison 1 without without without 87 291 1.37 137 Comparison 2 Polymer KD 0.3 without Polymer AA 0.3 72 375 2.04 180 Comparison 3 Polymer KG 0.3 without Polymer AB 0.3 79 345 1.59 163 Comparison 4 Polymer KG 0.3 without Polymer AC 0.3 76 358 1.61 170 Comparison 5 Polymer KH 0.16 Polymer KG 0.14 Polymer AD 0.3 76 359 1.6 171 example 1 Polymer KA 0.1 Polymer KD 0.2 Polymer AA 0.3 69 376 2.06 180 Example 2 Polymer KB 0.1 Polymer KD 0.2 Polymer AA 0.3 56 380 2.11 181 Example 3 Polymer KC 0.1 Polymer KD 0.2 Polymer AA 0.3 50 385 2.17 186 Example 4 Polymer KC 0.15 Polymer KD 0.15 Polymer AA 0.3 53 379 2.1 182 Example 5 Polymer KC 0.2 Polymer KD 0.1 Polymer AA 0.3 60 377 2.05 181 Example 6 Polymer KC 0.1 Polymer KD 0.2 Polymer AB 0.3 51 386 2.12 182 Example 7 Polymer KC 0.1 Polymer KD 0.2 Polymer AC 0.3 50 388 2.16 185 Example 8 Polymer KC 0.1 Polymer KE 0.2 Polymer AA 0.3 51 386 2.14 183 Example 9 Polymer KF 0.2 Polymer KA 0.1 Polymer AA 0.3 77 358 1.6 170 Example 10 Polymer KF 0.2 Polymer KB 0.1 Polymer AA 0.3 73 361 1.63 174 Example 11 Polymer KF 0.2 Polymer KC 0.1 Polymer AA 0.3 67 368 1.67 177 Example 12 Polymer KF 0.15 Polymer KC 0.15 Polymer AA 0.3 69 362 1.63 173 Example 13 Polymer KF 0.1 Polymer KC 0.2 Polymer AA 0.3 74 359 1.6 173 Example 14 Polymer KF 0.2 Polymer KC 0.1 Polymer AB 0.3 66 363 1.64 174 Example 15 Polymer KF 0.2 Polymer KC 0.1 Polymer AC 0.3 64 365 1.68 177 Comparison 2 according to Example 6 of DE-A-10 2004 056551
Comparison 3 according to Example 17 of WO-A-2006/075115
Comparison 4 according to Example 1 of WO-A-2006/075115
Comparison 5 according to Example 5 of WO-A-2006/090076

Claims (11)

  1. A process for the production of paper, board and cardboard having high dry strength by addition of at least one water-soluble cationic polymer and at least one water-soluble polymeric anionic compound to a paper stock, draining of the paper stock with sheet formation and drying of the paper products, wherein
    (a) polymers comprising vinylamine units and
    (b) polymers comprising ethylenimine units
    are metered as water-soluble cationic polymers in any sequence or as a mixture into a paper stock and the weight ratio of (a) polymers comprising vinylamine units to (b) polymers comprising ethylenimine units being from 10 : 1 to 1 : 10 and the reaction products which are obtainable
    - by polymerization of at least one monomer of the formula
    Figure imgb0009
    in which R1, R2 are H or C1- to C6-alkyl,
    and subsequent partial or complete elimination of the groups -CO-R1 from the units of the monomers (I) incorporated in the form of polymerized units into the polymer with formation of amino groups
    and/or
    - by Hofmann degradation of polymers which have acrylamide and/or methacrylamide units
    are used as (a) polymers comprising vinylamine units.
  2. The process according to claim 1, wherein the reaction products which are obtainable by polymerization of
    (i) at least one monomer of the formula
    Figure imgb0010
    in which R1, R2 are H or C1- to C6-alkyl,
    (ii) at least one other monoethylenically unsaturated monomer and, if appropriate,
    (iii) at least one crosslinking monomer having at least two double bonds in the molecule
    and subsequent partial or complete elimination of the groups -CO-R1 from the units of the monomers (I) incorporated in the form of polymerized units into the polymer with formation of amino groups are used as (a) polymers comprising vinylamine units.
  3. The process according to claim 1 or 2, wherein the reaction products which are obtainable by polymerization of
    (i) at least one monomer of the formula
    Figure imgb0011
    in which R1, R2 are H or C1- to C6-alkyl,
    (ii,a) at least in each case one monoethylenically unsaturated sulfonic acid, one monoethylenically unsaturated phosphonic acid, one monoethylenically unsaturated carboxylic acid having 3 to 8 carbon atoms in the molecule and/or the alkali metal, alkaline earth metal or ammonium salts thereof and optionally
    (ii,b) at least one other neutral and/or one cationic monomer and optionally
    (iii) at least one crosslinking monomer having at least two double bonds in the molecule
    and subsequent partial or complete elimination of groups -CO-R1 from the monomers of the formula (I) which are incorporated in the form of polymerized units into the polymer with formation of amino groups, the content of amino groups in the copolymer being at least 5 mol% above the content of acid groups of the monomers (ii,a) which are incorporated in the form of polymerized units, are used as (a) polymers comprising vinylamine units.
  4. The process according to any of claims 1 to 3, wherein the reaction products which are obtainable by polymerization of N-vinylformamide and subsequent elimination of formyl groups from the vinylformamide units incorporated in the form of polymerized units into the polymer with formation of amino groups are used as (a) polymers comprising vinylamine units.
  5. The process according to any of claims 1 to 4, wherein the reaction products which are obtainable by copolymerization of
    (i) vinylformamide and
    (ii) acrylonitrile
    and subsequent elimination of formyl groups from the vinylformamide units incorporated in the form of polymerized units into the copolymer with formation of amino groups are used as (a) polymers comprising vinylamine units.
  6. The process according to claim 3, wherein the reaction products which are obtainable by copolymerization of
    (i) N-vinylformamide,
    (ii,a) acrylic acid, methacrylic acid and/or the alkali metal, alkaline earth metal or ammonium salts thereof and optionally
    (ii,b) acrylonitrile and/or methacrylonitrile
    and subsequent partial or complete elimination of formyl groups from the N-vinylformamide incorporated in the form of polymerized units into the polymer with formation of amino groups, the content of amino groups in the copolymer being at least 5 mol% above the content of acid groups of the monomers (ii,a) which are incorporated in the form of polymerized units, are used as (a) reaction products comprising vinylamine units.
  7. The process according to claim 1, wherein the reaction products which are obtainable by Hofmann degradation of homo- or copolymers of acrylamide or of methacrylamide in an aqueous medium in the presence of sodium hydroxide solution and sodium hypochlorite and subsequent decarboxylation of the carbamate groups of the reaction product in the presence of an acid are used as (a) polymers comprising vinylamine units.
  8. The process according to any of claims 1 to 7, wherein at least one water-soluble cationic polymer from the group consisting of the
    - homopolymers of ethylenimine,
    - polyethylenimines reacted with at least bifunctional crosslinking agents,
    - polyamidoamines which have been grafted with ethylenimine and reacted with at least bifunctional crosslinking agents,
    - reaction products of polyethylenimines with monobasic carboxylic acids to give amidated polyethylenimines,
    - Michael adducts of polyethylenimines with ethylenically unsaturated acids, salts, esters, amides or nitriles of monoethylenically unsaturated carboxylic acids,
    - phosphonomethylated polyethylenimines,
    - carboxylated polyethylenimines and
    - alkoxylated polyethylenimines
    is used as (b) polymers comprising ethylenimine units.
  9. The process according to claim 8, wherein homopolymers of ethylenimine and/or polyamidoamines grafted with ethylenimine and subsequently reacted with at least bifunctional crosslinking agents are used as (b) polymers comprising ethylenimine units.
  10. The process according to any of claims 1 to 9, wherein a water-soluble polymer having acid groups and having a charge density of >0.5 meq/g or salts thereof is or are used as the polymeric anionic compound.
  11. The process according to claim 10, wherein at least one water-soluble compound from the group consisting of polyacrylic acid, polymethacrylic acid, copolymers of acrylamide and acrylic acid, copolymers of N-vinylformamide and acrylic acid, hydrolyzed copolymers of N-vinylformamide and acrylic acid and in each case the salts thereof is used as the polymeric anionic compound.
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Families Citing this family (22)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US8088250B2 (en) 2008-11-26 2012-01-03 Nalco Company Method of increasing filler content in papermaking
CA2763508C (en) 2009-06-16 2018-07-17 Basf Se Method for increasing the dry strength of paper, paperboard, and cardboard
US8454799B2 (en) 2010-05-05 2013-06-04 Basf Se Pulp composition for paper and solid board production
CA2837149C (en) * 2011-06-20 2017-01-24 Basf Se Process of making paper or paperboard with a dual polymeric retention system
BR112014017989B1 (en) * 2012-02-01 2021-02-23 Basf Se process for making paper or cardboard
US9816233B2 (en) 2012-09-28 2017-11-14 Kimberly-Clark Worldwide, Inc. Hybrid fiber compositions and uses in containerboard packaging
US9908680B2 (en) 2012-09-28 2018-03-06 Kimberly-Clark Worldwide, Inc. Tree-free fiber compositions and uses in containerboard packaging
CN104452455B (en) 2013-09-12 2019-04-05 艺康美国股份有限公司 The method that paper making auxiliary agent composition and increase are stayed at paper ash code insurance
CN104452463B (en) 2013-09-12 2017-01-04 艺康美国股份有限公司 Papermaking process and compositions
FR3016363B1 (en) * 2014-01-15 2017-05-26 Snf Sas AQUEOUS SOLUTION OF ACRYLAMIDE-DERIVED CATIONIC COPOLYMERS, PROCESS FOR PREPARATION AND USE
US9567708B2 (en) 2014-01-16 2017-02-14 Ecolab Usa Inc. Wet end chemicals for dry end strength in paper
US8894817B1 (en) * 2014-01-16 2014-11-25 Ecolab Usa Inc. Wet end chemicals for dry end strength
CN103866633B (en) * 2014-02-25 2016-08-17 苏州恒康新材料有限公司 A kind of wet strengthening agents for papermaking and preparation method thereof
US10047480B2 (en) 2014-03-28 2018-08-14 Basf Se Method for producing corrugated cardboard
US9920482B2 (en) 2014-10-06 2018-03-20 Ecolab Usa Inc. Method of increasing paper strength
US9702086B2 (en) 2014-10-06 2017-07-11 Ecolab Usa Inc. Method of increasing paper strength using an amine containing polymer composition
WO2016058730A1 (en) * 2014-10-13 2016-04-21 Basf Se Solidifying composition for paper and cardboard
EP3234259A1 (en) * 2014-12-16 2017-10-25 Basf Se Method for producing paper and cardboard
EP3455404B1 (en) 2016-05-13 2024-05-15 Ecolab USA Inc. Tissue dust reduction
CN111511986B (en) * 2017-10-11 2022-11-11 索理思科技开曼公司 Method for producing paper or paperboard
ES2989653T3 (en) * 2017-10-18 2024-11-27 Solenis Technologies Cayman Lp Method for producing monolayer or multilayer paper
CN115477729B (en) * 2022-09-21 2023-12-26 济宁明升新材料有限公司 Cationic polyacrylamide dry strength agent with narrow molecular weight and preparation method thereof

Family Cites Families (33)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2182306A (en) 1935-05-10 1939-12-05 Ig Farbenindustrie Ag Polymerization of ethylene imines
US3203910A (en) 1962-04-13 1965-08-31 Dow Chemical Co Polymerization of alkylenimines
DE2434816C3 (en) 1974-07-19 1981-01-22 Basf Ag, 6700 Ludwigshafen Process for the production of nitrogen-containing condensation products and their use as retention aids, flocculants and dewatering accelerators in paper manufacture
DE2436386C2 (en) 1974-07-29 1982-09-23 Basf Ag, 6700 Ludwigshafen Use of nitrogen-containing condensation products
SE443818B (en) 1978-04-24 1986-03-10 Mitsubishi Chem Ind PROCEDURE FOR MAKING PAPER WITH IMPROVED DRY STRENGTH
DE3506832A1 (en) 1985-02-27 1986-08-28 Basf Ag, 6700 Ludwigshafen METHOD FOR PRODUCING PAPER WITH HIGH DRY RESISTANCE
DE3541163A1 (en) * 1985-11-21 1987-05-27 Basf Ag METHOD FOR PRODUCING PAPER AND CARDBOARD
US5039757A (en) 1988-12-28 1991-08-13 Mitsui Toatsu Chemicals, Inc. Method of manufacturing cationic acrylamide polymers, cationic acrylamide polymers, and the applications of these polymers
DE3925439A1 (en) 1989-08-01 1991-02-07 Bayer Ag BASIC CONDENSATES
DE4001808A1 (en) 1990-01-23 1991-07-25 Basf Ag Water sol co-polymer for water treatment - from unsatd. carboxylic acid and vinyl:amide deriv.
DE4105919A1 (en) * 1991-02-26 1992-08-27 Basf Ag AQUEOUS PENDINGS OF FINE-PARTIC FILLERS AND THEIR USE FOR THE PRODUCTION OF FUEL-CONTAINING PAPER
EP0528409B1 (en) 1991-08-20 1996-05-22 Mitsubishi Chemical Corporation Cationic polymer flocculating agents
JP3237228B2 (en) 1992-09-03 2001-12-10 三菱化学株式会社 Papermaking additives consisting of cationic polymers
DE4240110A1 (en) 1992-11-28 1994-06-01 Basf Ag Condensation products of polyalkylene polyamines, process for their preparation and their use in the manufacture of paper
DE4244194A1 (en) 1992-12-24 1994-06-30 Basf Ag Water-soluble condensation products from compounds containing amino groups and crosslinking agents, processes for their preparation and their use
WO1997025367A1 (en) 1996-01-08 1997-07-17 Basf Aktiengesellschaft Method of producing water-soluble condensates and addition products containing amino groups, and use of said condensates and addition products
DE19713755A1 (en) * 1997-04-04 1998-10-08 Basf Ag Process for the production of paper, cardboard and cardboard with high dry strength
DE19921507A1 (en) 1999-05-10 2000-11-16 Basf Ag Process for the fractionation of water-soluble or dispersible amino group-containing polymers with a broad molar mass distribution
JP3703067B2 (en) 1999-05-20 2005-10-05 シャープ株式会社 Manufacturing method of flex-rigid multilayer wiring board
US6695950B1 (en) * 1999-08-17 2004-02-24 National Starch And Chemical Investment Holding Corporation Aldehyde modified cellulose pulp for the preparation of high strength paper products
US6824650B2 (en) 2001-12-18 2004-11-30 Kimberly-Clark Worldwide, Inc. Fibrous materials treated with a polyvinylamine polymer
US20040118540A1 (en) 2002-12-20 2004-06-24 Kimberly-Clark Worlwide, Inc. Bicomponent strengtheninig system for paper
MXPA04003942A (en) * 2003-05-05 2007-06-29 German Vergara Lopez Retention and drainage system for the manufacturing of paper, paperboard and similar cellulosic products.
DE102004056551A1 (en) * 2004-11-23 2006-05-24 Basf Ag Process for the production of paper, cardboard and cardboard with high dry strength
DE102005022799A1 (en) * 2005-05-12 2006-11-16 Basf Ag Manufacture of paper products in presence of aqueous elutriate containing fine, coated filler materials, adds specified additional cationic and amphoteric polymers
JP5130049B2 (en) * 2004-12-17 2013-01-30 ビーエーエスエフ ソシエタス・ヨーロピア Paper with high filler content and high dry strength
FR2880901B1 (en) 2005-01-17 2008-06-20 Snf Sas Soc Par Actions Simpli METHOD FOR MANUFACTURING PAPER AND CARDBOARD OF HIGH RESISTANCE BY DRY AND PAPERS AND CARTONS THUS OBTAINED
FR2882373B1 (en) 2005-02-24 2007-04-27 Snf Sas Soc Par Actions Simpli METHOD FOR MANUFACTURING PAPER AND CARDBOARD OF HIGH RESISTANCE BY DRY AND PAPERS AND CARTONS THUS OBTAINED
ES2358529T3 (en) 2005-05-11 2011-05-11 Stora Enso Ab PROCEDURE FOR THE PRODUCTION OF A PAPER AND PAPER PRODUCED ACCORDING TO THAT PROCEDURE.
WO2009004080A2 (en) 2007-07-05 2009-01-08 Basf Se Method for producing aqueous suspensions of fine particulate fillers and use thereof for producing papers having a high filler content and a high dry strength
JP2010532404A (en) 2007-07-05 2010-10-07 ビーエーエスエフ ソシエタス・ヨーロピア Method for producing an aqueous slurry of fine filler and use of said aqueous slurry for producing paper with high filler content and high dry strength
ES2378425T5 (en) 2007-07-05 2017-05-16 Omya International Ag. Aqueous suspensions of finely divided fillers, process for their preparation and use for the manufacture of papers with high content in fillers and high dry strength
PL2164907T3 (en) 2007-07-05 2017-08-31 Basf Se Aqueous suspensions of fine particulate fillers, method for producing the same and use thereof for producing papers having a high filler content and a high dry strength

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