EP2443284A1 - Procédé permettant d'augmenter la résistance à l'état sec du papier, du carton souple et du carton - Google Patents

Procédé permettant d'augmenter la résistance à l'état sec du papier, du carton souple et du carton

Info

Publication number
EP2443284A1
EP2443284A1 EP10724788A EP10724788A EP2443284A1 EP 2443284 A1 EP2443284 A1 EP 2443284A1 EP 10724788 A EP10724788 A EP 10724788A EP 10724788 A EP10724788 A EP 10724788A EP 2443284 A1 EP2443284 A1 EP 2443284A1
Authority
EP
European Patent Office
Prior art keywords
polymers
water
units
monomers
polymer
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
EP10724788A
Other languages
German (de)
English (en)
Other versions
EP2443284B2 (fr
EP2443284B1 (fr
Inventor
Christian Jehn-Rendu
Ellen KRÜGER
Hans-Joachim HÄHNLE
Martin Rübenacker
Norbert Schall
Thomas MÜHLENBERND
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
BASF SE
Original Assignee
BASF SE
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Family has litigation
First worldwide family litigation filed litigation Critical https://patents.darts-ip.com/?family=42647475&utm_source=google_patent&utm_medium=platform_link&utm_campaign=public_patent_search&patent=EP2443284(A1) "Global patent litigation dataset” by Darts-ip is licensed under a Creative Commons Attribution 4.0 International License.
Application filed by BASF SE filed Critical BASF SE
Priority to PL10724788T priority Critical patent/PL2443284T5/pl
Priority to EP10724788.4A priority patent/EP2443284B2/fr
Publication of EP2443284A1 publication Critical patent/EP2443284A1/fr
Application granted granted Critical
Publication of EP2443284B1 publication Critical patent/EP2443284B1/fr
Publication of EP2443284B2 publication Critical patent/EP2443284B2/fr
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • D—TEXTILES; PAPER
    • D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
    • D21H21/00—Non-fibrous material added to the pulp, characterised by its function, form or properties; Paper-impregnating or coating material, characterised by its function, form or properties
    • D21H21/14—Non-fibrous material added to the pulp, characterised by its function, form or properties; Paper-impregnating or coating material, characterised by its function, form or properties characterised by function or properties in or on the paper
    • D21H21/18—Reinforcing agents
    • D—TEXTILES; PAPER
    • D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
    • D21H17/00—Non-fibrous material added to the pulp, characterised by its constitution; Paper-impregnating material characterised by its constitution
    • D21H17/20—Macromolecular organic compounds
    • D21H17/33—Synthetic macromolecular compounds
    • D21H17/34—Synthetic macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds
    • D21H17/37—Polymers of unsaturated acids or derivatives thereof, e.g. polyacrylates
    • D—TEXTILES; PAPER
    • D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
    • D21H17/00—Non-fibrous material added to the pulp, characterised by its constitution; Paper-impregnating material characterised by its constitution
    • D21H17/20—Macromolecular organic compounds
    • D21H17/33—Synthetic macromolecular compounds
    • D21H17/34—Synthetic macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds
    • D21H17/41—Synthetic macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds containing ionic groups
    • D21H17/44—Synthetic macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds containing ionic groups cationic
    • D—TEXTILES; PAPER
    • D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
    • D21H17/00—Non-fibrous material added to the pulp, characterised by its constitution; Paper-impregnating material characterised by its constitution
    • D21H17/20—Macromolecular organic compounds
    • D21H17/33—Synthetic macromolecular compounds
    • D21H17/46—Synthetic macromolecular compounds obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds
    • D21H17/54—Synthetic 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
    • D21H17/56—Polyamines; Polyimines; Polyester-imides
    • D—TEXTILES; PAPER
    • D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
    • D21H17/00—Non-fibrous material added to the pulp, characterised by its constitution; Paper-impregnating material characterised by its constitution
    • D21H17/63—Inorganic compounds
    • D21H17/66—Salts, e.g. alums
    • D—TEXTILES; PAPER
    • D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
    • D21H17/00—Non-fibrous material added to the pulp, characterised by its constitution; Paper-impregnating material characterised by its constitution
    • D21H17/71—Mixtures of material ; Pulp or paper comprising several different materials not incorporated by special processes
    • D21H17/74—Mixtures of material ; Pulp or paper comprising several different materials not incorporated by special processes of organic and inorganic material

Definitions

  • the invention relates to a process for the production of paper, paperboard and cardboard with high dry strength by adding (a) at least one trivalent cation, (b) at least one water-soluble cationic polymer selected from the group consisting of (i) vinylamine units polymers and (ii) Ethyleniminiseren and (c) at least one water-soluble amphoteric polymer to a pulp, dewatering the stock to form sheets, and drying the resulting paper product.
  • a process for the production of paper with high dry strength in which initially an aluminum sulphate solution is added to the paper stock. Thereafter, a water-soluble amphoteric polymer is added. Subsequently, the paper stock is dewatered on the paper machine to form sheets, and the paper products are dried.
  • Suitable amphoteric polymers are, for example, copolymers of acrylamide, acrylic acid and dimethylaminoethyl (meth) acrylate.
  • DE 35 06 832 A1 discloses a process for the production of paper with high dry strength, in which first a water-soluble cationic polymer and then a water-soluble anionic polymer are added to the paper stock.
  • Suitable anionic polymers are, for example, homopolymers or copolymers of ethylenically unsaturated C 3 -C 8 -carboxylic acids.
  • the copolymers contain at least 35% by weight of an ethylenically unsaturated C 3 -C 5 -carboxylic acid (for example acrylic acid) in copolymerized form.
  • the cationic polymers described in the examples are polyethyleneimine, polyvinylamine, polydiallyldimethylammonium chloride and epichlorohydrin-reacted condensation products of adipic acid and diethylenetriamine.
  • the use of partially hydrolyzed homo- and copolymers of N-vinylformamide has also been considered.
  • JP 02-1 12498 relates to a process for the production of corrugated cardboard, wherein dosing alum, a polyallylamine and an anionic or amphoteric polymer to a fiber suspension.
  • the combination produces papers with a high strength.
  • JP 05-272092 a process for the production of paper with high dry strength is described, in which one first admits to the pulp an aluminum sulfate solution, and then a water-soluble amphoteric polymer with high molecular weight dosed, then drained the paper stock on the paper machine with sheet formation and the paper products dried.
  • amphoteric polymers include copolymers of acrylamide, acrylic acid, dimethylaminoethyl (meth) acrylate, (meth) acrylamide and sodium (meth) allylsulfonate. These amphoteric polymers are characterized by very high molecular weights and low solution viscosities.
  • JP 08-269891 A variant of the method described in JP 05-272092 is disclosed in JP 08-269891.
  • an aluminum sulfate solution is also added to the paper stock first, followed by metering in a high molecular weight water-soluble amphoteric polymer, followed by dewatering of the paper stock on the paper machine and drying of the paper products.
  • Copolymers of acrylamide, acrylic acid, dimethylaminoethyl methacrylates, (meth) acrylamide, sodium (meth) allylsulfonate and a crosslinker such as methylenebisacrylamide or triallylamine are used as amphoteric polymers, for example.
  • These amphoteric polymers have a very high molecular weight and a further reduced solution viscosity compared to JP 05-272092.
  • EP 0 659 780 A1 describes a process for the preparation of polymers having a weight-average molecular weight of 1,500,000 to 10,000,000 (a) and a weight-average root mean square radius of 30 to 150 nm (b), the ratio (b) / (a) ⁇ 0.00004, and their use as solidifying agents.
  • WO 98/06898 A1 describes a papermaking process in which a cationic starch or a cationic wet strength agent and a water-soluble amphoteric polymer are added to the stock.
  • This amphoteric polymer is composed of the nonionic monomers acrylamide and methacrylamide, an anionic monomer, a cationic monomer and a crosslinker, the amount of anionic and cationic monomer not exceeding 9% by weight of the total monomers used in the amphoteric polymer.
  • 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 by Hydrolysis of polyvinylformamide with a degree of hydrolysis of 25 to 100% is available, in combination with an anionic polyacrylamide admits, the pulp then dewatered with sheet formation and the paper dries.
  • EP 0 919 578 A1 relates to amphoteric polymers (type B) prepared by a two-stage polymerization.
  • a polymer (type A) is prepared by the copolymerization of methallylsulfonic acid with others Vinyl monomers, then in the presence of the type A polyamor there is a further polymerization of vinyl monomers to the B-type polymer wherein the type A polymers have a molecular weight of from 1,000 to 5,000,000 and the type B polymers have a molecular weight of from 100,000 to 10,000,000 exhibit.
  • this document comprises the use of the polymers of type B as solidifying agents for papermaking and the papers produced therewith, whereby the possibility of a combination with alum and anionic polyacrylamides is also described. Finally, the possibility of modifying the type B polymers by Hofmann degradation is also mentioned.
  • JP 2001-279595 relates to a process for producing high-strength paper wherein a mixture of a cationic, anionic or amphoteric polyacrylamide with a water-soluble aluminum compound is added to the fibers. This is followed by a metered addition of another polyacrylamide. This not only increases the strength, but also improves drainage at the same time.
  • a paper product with improved strength properties is known, which is 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 with Aldehyde functions such as aldehyde group-containing polysaccharides applies.
  • a polyvinylamine and a polymeric anionic compound which can form a polyelectrolyte complex with polyvinylamine, or a polymeric compound with Aldehyde functions such as aldehyde group-containing polysaccharides applies.
  • the paper improve its dry and wet strength, it also observes a sizing effect of the treating agents.
  • JP 2005-023434 describes a process for producing high-strength paper obtained by metering two polymers.
  • the first polymer is a branched amphoteric polyacrylamide.
  • the second polymer is a copolymer of a cationic vinyl monomer as the main monomer into consideration.
  • DE 10 2004 056 551 A1 discloses another method for improving the dry strength of paper.
  • a separate addition of a VinylamineinRIC polymers and a polymeric anionic compound to a pulp, dewatering of the pulp and drying of the paper products takes place, being used as the polymeric anionic compound at least one copolymerisate obtainable by copolymerizing (a) at least one N-vinylcarboxamide of the formula
  • R 1 , R 2 H or C 1 - to C 6 -alkyl
  • WO 2006/120235 A1 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 is carried out alternately with cationic and anionic polymers and comprises at least three steps.
  • WO 2006/090076 A1 also relates to a process for producing paper and paperboard having a high dry strength, wherein three components are added to the paper stock: (a) a polymer having primary amino groups and a charge density of
  • EP 1 849 803 A1 also discloses a paper additive for strengthening which is obtained as a water-soluble polymer by polymerizing (meth) acrylamide, an ⁇ , ⁇ -unsaturated mono- or dicarboxylic acid or salts thereof, a cationic monomer and a crosslinking monomer. In a second stage, the remaining residual monomer is polymerized with further persulfate catalyst.
  • the objects are achieved by a method for producing paper, cardboard and cardboard with high dry strength, by adding
  • the water-soluble cationic polymer (b) is selected from the group of (i) vinylamine units-containing polymers and (ii) polymers containing ethyleneimine units.
  • the said components of the solidification system may be added to the stock in any order or else as a mixture of two or more components.
  • trivalent metal or semimetallic cations are suitable as trivalent cations in the process according to the invention.
  • Preferred metal cations are Al 3+ , Zr 3+ and Fe 3+ . Most preferred is Al 3+ .
  • the metal and semimetal cations are used in the form of their salts.
  • Al 3+ this can be used, for example, in the form of aluminum sulfate, polyaluminum chloride or aluminum lactate.
  • Metal cations are used, but preferably only a trivalent metal cation is used in the process according to the invention.
  • different salts of this metal cation can be used in any mixtures.
  • a trivalent metal cation in one of the described salt forms is used.
  • the trivalent cations are usually added to the stock in amounts of between 3 and 100 moles per ton of dry paper, preferably in the range of 10 to 30 moles per ton of dry paper.
  • the water-soluble cationic polymer (b) is selected from the group of polymers containing (i) vinylamine units and (ii) polymers containing ethyleneimine units.
  • the cationic polymers (b) are water-soluble.
  • the solubility in water under normal conditions (20 ° C., 1013 mbar) and pH 7.0 is, for example, at least 5% by weight, preferably at least 10% by weight.
  • the charge density of the cationic polymers (without counterion) is for example at least 1.0 meq / g and is preferably in the range from 4 to 10 meq / g.
  • the water-soluble cationic polymers (b) usually have average molecular weights in the range of 10,000 to 10,000,000 daltons, preferably in the range of 20,000 to 5,000,000 daltons, more preferably in the range of 40,000 to 3,000,000 daltons.
  • Vinylamine-containing polymers (i) are known, cf. the DE 35 06 832 A1 and DE 10 2004 056 551 A1 referred to in the prior art.
  • polymers which contain (i) vinylamine units are reaction products which are obtainable
  • R 1 , R 2 H or C 1 - to C 6 -alkyl
  • polymers containing (i) vinylamine units are, for example, the reaction products obtainable by polymerizing
  • R 1 , R 2 H or C 1 - to C 6 -alkyl
  • the polymers which are preferably used as (i) vinylamine units are the reaction products obtainable by polymerizing N-vinylformamide and subsequent cleavage of formyl groups from the vinylformamide units copolymerized in the polymer to form amino groups, or the reaction products are used. by copolymerizing
  • the vinylamine units containing polymers can 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%, above the content of anionic groups.
  • Such polymers are obtainable, for example, by polymerizing
  • R 1 , R 2 H or C 1 - to C 6 -alkyl
  • polymers containing amphoteric vinylamine units which carry a total cationic charge and which are obtained, for example, by copolymerizing
  • 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 (a) may be used alone or in admixture in the copolymerization with the monomers of the other groups.
  • Preferably used monomer of this group is N-vinylformamide.
  • Examples of monomers of group (2) are esters of ⁇ , ß-ethylenically unsaturated mono- and dicarboxylic acids with Ci-C3o-alkanols, C2-C3o-alkanediols and C2-C30-amino alcohols, amides of ⁇ , ß-ethylenically unsaturated monocarboxylic acids and their N-alkyl and N, N-dialkyl derivatives, nitriles of ⁇ , ß-ethylenically unsaturated mono- and dicarboxylic acids, esters of vinyl alcohol and allyl alcohol with C1-C30 monocarboxylic acids, N-vinyl lactams, nitrogen-containing heterocycles with ⁇ , ß-ethylenic unsaturated double bonds, vinyl aromatics, vinyl halides, vinylidene halides, C 2 -C 8 monoolefins, and mixtures thereof.
  • Suitable representatives are e.g. Methyl (meth) acrylate (in which (meth) acrylate in the sense of the present invention means both acrylate and methacrylate), methyl acrylate, ethyl (meth) acrylate, ethyl ethacrylate, n-butyl (meth) acrylate, isobutyl (meth) acrylate, tert-butyl (meth) acrylate, tert-butyl ethacrylate, n-octyl (meth) acrylate, 1,1,3,3-tetramethylbutyl (meth) acrylate, ethylhexyl (meth) acrylate and mixtures thereof.
  • Methyl (meth) acrylate in which (meth) acrylate in the sense of the present invention means both acrylate and methacrylate
  • methyl acrylate ethyl (meth) acrylate, ethyl
  • Suitable additional monomers of the group (2) are also the esters of ⁇ , ß-ethylenically unsaturated mono- and dicarboxylic acids with amino alcohols, preferably C2-Ci2-amino alcohols. These may be d-Cs-monoalkylated or dialkylated on the amine nitrogen.
  • the acid component of these esters e.g. Acrylic, methacrylic, fumaric, maleic, itaconic, crotonic, maleic, monobutyl, and mixtures thereof. 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.
  • Such monomers of group (2) 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 additional monomers of group (2) are furthermore acrylamide, methacrylamide, N-methyl (meth) acrylamide, N-ethyl (meth) acrylamide, n-
  • monomers of group (2) 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. e.g. EP 0 528 409 A1 or DE 43 28 975 A1.
  • aminin units are formed 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 means the sum of vinylamine and amidine units.
  • Suitable monomers of the group (2.) are furthermore N-vinyllactams and their derivatives, which are e.g. may have one or more d-C ⁇ -alkyl substituents (as defined above).
  • 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 N-vinylimidazoles and alkylvinylimidazoles, in particular methylvinylimidazoles such as, for example, 1-vinyl-2-methylimidazole, 3-vinylimidazoleN-oxide, 2- and 4-vinylpyridine N-oxides and also betaine derivatives and quaternization products these monomers as well as ethylene, propylene, isobutylene, butadiene, styrene, ⁇ -methylstyrene, vinyl acetate, vinyl propionate, vinyl chloride, vinylidene chloride, vinyl fluoride, vinylidene fluoride and mixtures thereof.
  • 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 (2.) and anionic monomers into consideration, which are referred to above as monomers (2.1). If appropriate, they may be copolymerized with the above-described neutral and / or cationic monomers (2.2). However, the amount of anionic monomers (2.1) is at most
  • anionic monomers of group (2.1) are ethylenically unsaturated C3- to C6-carboxylic acids such as acrylic acid, methacrylic acid, dimethacrylic acid, ethacrylic acid, maleic acid, fumaric acid, itaconic acid, mesaconic acid, citraconic acid, methylenemalonic acid, allylacetic acid, vinylacetic acid and crotonic acid.
  • monomers containing sulfonic groups such as vinylsulfonic acid, acrylamido-2-methylpropanesulfonic acid and styrenesulfonic acid, and monomers containing phosphonic 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 tetraethylene pentamine.
  • 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, e.g. Triallylamine, methylenebisacrylamide, glycol diacrylate, glycol dimethacrylate, glycerol triacrylate, pentaerythritol triallyl ether, polyalkylene glycols esterified at least twice with acrylic acid and / or methacrylic acid, or polyols such as pentaerythritol, soudite or glucose. These are so-called crosslinkers. If at least one monomer of the above group is used in the polymerization, the amounts used are up to 2 mol%, e.g. 0.001 to 1 mole%.
  • regulators typically, from 0.001 to 5 mole percent is used. All regulators known from the literature, for example sulfur compounds such as mercaptoethanol, 2-ethylhexyl thioglycolate, thiourea, can be used. oglycolic acid and dodecyl mercaptan and sodium hypophosphite, formic acid or Tribromchlormethan and terpinolene.
  • the polymers (i) 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 can be obtained 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 described above 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 vinylcarboxamide copolymers is described in detail in EP 0 438 744 A1, page 8, line 20 to page 10, line 3.
  • 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 preparation of the homo- and copolymers (i) 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.
  • aqueous media are water and mixtures of water and at least one water-miscible solvent, e.g. an alcohol such as methanol, ethanol, n-propanol or isopropanol.
  • vinylamine units also include the reaction products obtained by Hofmann degradation of homo- or copolymers of acrylamide or methacrylamide in an aqueous medium in the presence of sodium hydroxide and sodium hypochlorite and subsequent decarboxylation of the carbamate groups of the reaction products in the presence of a Acid are available.
  • Such polymers are known, for example, from EP 0 377 313 and WO 2006/0751 15 A1.
  • the preparation of polymers containing vinylamine groups is discussed in detail in WO 2006/0751 15 A1, page 4, line 25 to page 10, line 22 and in the examples on pages 13 and 14, for example.
  • 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.
  • comonomers are dimethyldiallylammonium salts, acrylamidopropyltrimethylammonium chloride and / or methacrylamidopropyltrimethylammonium chloride, N-vinylformamide, N-vinylacetamide, N-vinylpyrrolidone, vinyl acetate and acrylic and methacrylic acid esters.
  • anionic monomers such as acrylic acid, methacrylic acid, maleic anhydride, maleic acid, itaconic acid, acrylamidomethylpropanesulphonic acid, methallylsulphonic acid and vinylsulphonic acid and the alkali metal, alkaline earth metal and ammonium salts of the abovementioned acidic monomers, where not more than 5 molar % 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, e.g. ethylenically unsaturated monomers which contain at least two double bonds in the molecule, such as triallylamine, methylenebisacrylamide, ethylene glycol diacrylate, ethylene glycol dimethacrylate, polyethylene glycol dimethacrylate and trimethylol trimethacrylate.
  • crosslinker e.g. ethylenically unsaturated monomers which contain at least two double bonds in the molecule, such as triallylamine, methylenebisacrylamide, ethylene glycol diacrylate, ethylene glycol dimethacrylate, polyethylene glycol dimethacrylate and trimethylol trimethacrylate.
  • the amounts used are, for example, 5 to 5000 ppm.
  • the polymerization of the monomers can be carried out by any known method, e.g. by free-radical initiated solution, precipitation or suspension polymerization. If appropriate, it is possible to work in the presence of customary polymer
  • 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 alkali metal hydroxide to alkali metal hypochlorite is for example 2 to 6, preferably 2 to 5.
  • For a certain amine group content in the degraded polymer is calculated for the degradation of the polymer required amount of alkali metal hydroxide.
  • the Hofmann degradation of the polymer takes place for example in the temperature range from 0 to 45 0 C, preferably 10 to prevent the starting polymer to 20 0 C in the presence of quaternary ammonium salts as a stabilizer to amide groups, a side reaction of the resulting amino groups with the A-.
  • 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 unit containing vinylamine units Product is set to a value of 2 to 7.
  • the concentration of the degradation product 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 (ii) 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 US 3,203,910. If desired, these polymers can subsequently be subjected to crosslinking.
  • crosslinkers come e.g. all multifunctional compounds containing groups reactive with primary amino groups, e.g.
  • multifunctional epoxides such as bisglycidyl ethers of oligo- or polyethylene oxides 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.
  • Further crosslinkers are described in WO 97/25367 A1, pages 8 to 16.
  • Polymers containing ethyleneimine units are known, for example, from EP 0 41 1 400 A1, DE 24 34 816 A1 and US Pat. No. 4,066,494.
  • Polymers containing (ii) ethyleneimine units are e.g. in the process according to the invention at least one water-soluble cationic polymer from the group of
  • Carboxylic acids, phosphonomethylated polyethyleneimines, - carboxylated polyethyleneimines and alkoxylated polyethyleneimines 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 subsequently crosslinking the reaction products with one of the abovementioned compounds belong to the ethylenimine units which are preferably suitable Links.
  • a process for preparing such compounds is described, for example, in DE 24 34 816 A1, where ⁇ , ⁇ -chlorohydrin ethers of oligo- or polyethylene oxides are used as crosslinkers.
  • Reaction products of polyethyleneimines with monobasic carboxylic acids to amidated polyethyleneimines are known from WO 94/12560 A1.
  • Michael addition products of polyethyleneimines to ethylenically unsaturated acids, salts, esters, amides or nitriles of monoethylenically unsaturated carboxylic acids are the subject of WO 94/14873 A1.
  • Phosphonomethylated polyethyleneimines are described in detail in WO 97/25367 A1.
  • Carboxylated polyethyleneimines are obtainable, for example, by means of a stretching 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 water-soluble cationic polymer (b) used may be, in each case, the polymers containing (i) vinylamine units or polymers containing (ii) ethyleneimine units.
  • the polymers containing (i) vinylamine units or polymers containing (ii) ethyleneimine units may be, in each case, the polymers containing (i) vinylamine units or polymers containing (ii) ethyleneimine units.
  • any mixture of (i) polymer containing vinylamine units and (ii) polymer containing ethylene-mine units can also be used.
  • the weight ratio of (i) polymers containing vinylamine units to (ii) polymers containing ethyleneimine units is, for example, 10: 1 to 1:10, preferably in the range of 5: 1 to 1: 5, and more preferably in the range of 2: 1 to 1: 2.
  • the at least one water-soluble cationic polymer (b) is particularly preferred in the process according to the invention for producing paper, for example in an amount of 0.01 to 2.0% by weight, preferably 0.03 to 1.0% by weight 0.1 to 0.5 wt .-%, each based on dry pulp, used.
  • the amphoteric polymers (c) are water-soluble.
  • the solubility in water under normal conditions (20 ° C., 1013 mbar) and pH 7.0 is for example at least 5% by weight, preferably at least 10% by weight.
  • the water-soluble amphoteric polymers (c) which can be used in the process according to the invention are composed of at least three structural units:
  • water-soluble amphoteric polymers (c) may also contain crosslinkers and / or regulators.
  • crosslinkers and regulators are also those already used in the water-soluble cationic polymers (b).
  • Examples of monomers whose polymers contain structural units (A) are esters of ⁇ , ⁇ -ethylenically unsaturated mono- and dicarboxylic acids with C 2 -C 30 -aminoalcohols, amides of ⁇ , ⁇ -ethylenically unsaturated monocarboxylic acids and their N-alkyl and N, N-dialkyl derivatives, nitrogen-containing heterocycles having ⁇ , ⁇ -ethylenically unsaturated double bonds and mixtures thereof.
  • Suitable monomers of this group are the esters of ⁇ , ß-ethylenically unsaturated mono- and dicarboxylic acids with amino alcohols, preferably C2-Ci2-amino alcohols. These may be C 1 -C 12 monoalkylated or dialkylated on the amine nitrogen.
  • the acid component of these esters e.g. Acrylic, methacrylic, fumaric, maleic, itaconic, crotonic, maleic, monobutyl, and mixtures thereof. 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.
  • N-vinylimidazoles and alkylvinylimidazoles in particular methylvinylimidazoles such as, for example, 1-vinyl-2-methylimidazole, 3-vinylimidazole N-oxide, 2- and 4-vinylpyridine N-oxides and also betaine derivatives and quaternization products of these monomers and mixtures from that.
  • the respective quaternary compounds are also suitable.
  • the quaternary compounds of the monomers are obtained by reacting the monomers with known quaternizing agents, e.g. with methyl chloride, benzyl chloride, ethyl chloride, butyl bromide, dimethyl sulfate and diethyl sulfate or Alkylepoxiden.
  • Examples of monomers whose polymers contain structural units (B) are those which carry an acid function. These are selected from monoethylenically unsaturated sulfonic acids, monoethylenically unsaturated phosphonic acids and monoethylenically unsaturated carboxylic acids having 3 to 8 C atoms in the molecule and / or their alkali metal, alkaline earth metal or ammonium salts.
  • Examples of such monomers of this group are ethylenically unsaturated C3 to Cs carboxylic acids such as acrylic acid, methacrylic acid, dimethacrylic acid, ethacrylic acid, maleic acid, fumaric acid, itaconic acid, mesaconic acid, citraconic acid, methylenemalonic acid, allylacetic acid, vinylacetic acid and crotonic acid.
  • monomers containing sulfonic groups such as vinylsulfonic acid, acrylamido-2-methylpropanesulfonic acid and styrenesulfonic acid, and monomers containing phosphonic groups, such as vinylphosphonic acid.
  • Sulfonic group-containing monomers are, in particular, those of the formula (II) and salts thereof
  • R 1 H or a Ci-C4-alkyl group and n is an integer in the range of 1 to 8 is, preferably.
  • 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 this are caustic soda, Potassium hydroxide, soda, potash, sodium bicarbonate, magnesium oxide, calcium hydroxide, calcium oxide, triethanolamine, ethanolamine, morpholine, diethylenetriamine or tetraethylenepentamine.
  • Monomers whose polymers contain structural units (C) are monomers of formula (I), esters of ⁇ , ß-ethylenically unsaturated mono- and dicarboxylic acids with C1-C30 alkanols and C2-C3o-alkanediols, (meth) acrylamides, nitriles of ⁇ , ß-ethylenically unsaturated mono- and dicarboxylic acids, esters of vinyl alcohol and allyl alcohol with d-C3o monocarboxylic acids, N-vinyl lactams and mixtures thereof.
  • Monomers of the formula (I) are, for example, 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.
  • These monomers can be used alone or in admixture in the copolymerization with the monomers of the other groups.
  • Preferably used monomer of this group is N-vinylformamide.
  • Suitable representatives of this monomer group are e.g. 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-butyl octyl (meth) acrylate,
  • Suitable monomers of this group 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 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.
  • nitriles of ⁇ , ß-ethylenically unsaturated mono- and dicarboxylic acids such as acrylonitrile and methacrylonitrile are suitable.
  • Suitable monomers of this group are furthermore N-vinyllactams and derivatives thereof, which may have, for example, one or more C 1 -C 6 -alkyl substituents (as defined above).
  • 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.
  • the proportion of monomers whose polymers contain the structural units (C) in the water-soluble amphoteric polymer is at least 50% by weight, based on the total weight of the monomers used to prepare the water-soluble polymer (c).
  • the proportion of monomers whose polymers contain the structural units (C) is preferably at least 60% by weight, particularly preferably at least 75% by weight and especially preferably at least 85% by weight, but not more than 98% by weight. , in each case based on the total weight of the monomers, which are used for the preparation of the water-soluble Polymweren (c).
  • the molar ratio of the monomers whose polymers contain the structural units (A) to those whose polymers contain the structural units (B) is usually in the range of 5: 1 to 1: 5, preferably 2: 1 to 1: 2 and more preferably 1: 1.
  • amphoteric polymers (c) are known in the literature, as well as their preparation.
  • the amphoteric polymers can be prepared by radical polymerization of the aforementioned monomers in solution, as gel polymerization, precipitation polymerization, water-in-water polymerization, water-in-oil polymerization or by spray polymerization.
  • the water-soluble amphoteric polymers (c) used are preferably those as described in EP 0 659 780 A1, EP 0 919 578 A1, EP 1 849 803 A1, JP 08-269891, JP 2005-023434 and JP 2001-1279595 disclosed.
  • the at least one water-soluble amphoteric polymer (c) is used in the process according to the invention for the production of paper, for example in an amount of from 0.01 to 2.0% by weight, preferably from 0.03 to 1.0% by weight, particularly preferably 0.1 to 0.5 wt .-%, each based on dry paper stock used.
  • the present invention also provides the papers produced by the process described above, as well as cardboard and paperboard.
  • suitable fibrous materials for the production of the pulps are all qualities customary for this purpose, eg wood pulp, bleached and unbleached pulp and pulps from all annual plants.
  • Wood pulp includes, for example, groundwood, thermo-mechanical pulp (TMP), chemo-thermo-mechanical pulp (CTMP), pressure groundwood, semi-pulp, high yield pulp and refiner mechanical pulp (RMP).
  • TMP thermo-mechanical pulp
  • CMP chemo-thermo-mechanical pulp
  • RMP refiner mechanical pulp
  • pulp for example, sulphate, sulfate Fit and soda pulps into consideration.
  • unbleached pulp also referred to as unbleached kraft pulp
  • Suitable annual plants for the production of paper materials are for example rice, wheat, sugarcane and kenaf.
  • the inventive method is particularly suitable for the production of dry-proof papers from waste paper (including deinked waste paper), which is used either alone or in admixture with other fibers. It is also possible to start with fiber blends of primary and recycled coated broke, e.g. bleached pine sulfate in admixture with reclaimed 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, usually 6 to 7.5.
  • an acid such as sulfuric acid or aluminum sulphate.
  • the order of addition of the components (a), (b) and (c) is arbitrary, wherein the components can be added to the fiber suspension individually or in each mixture.
  • the cationic components namely the (a) trivalent cations in the form of a salt and (b) water-soluble cationic polymers, are metered into the pulp.
  • the addition of the cationic components (a) and (b) may be carried out separately or in admixture with the thick material (fiber concentration> 15 g / l, for example in the range of 25 to 40 g / l up to 60 g / l) or preferably in the Thin material (fiber concentration ⁇ 15 g / l, eg 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 metering of the cationic components (a) and (b) to the paper stock can be carried out successively, simultaneously or as a mixture of (a) and (b) as described above.
  • the water-soluble amphoteric polymer (c) is usually added only after the addition of the cationic components (a) and (b) to the pulp, but can also be added to the pulp simultaneously and also in admixture with (a) and (b). Furthermore, it is also possible first to add the water-soluble amphoteric polymer (c) and subsequently the cationic components (a) and (b) or first to meter one of the cationic components (a) or (b) to the stock, then the water-soluble amphoteric polymer (c) and then adding the other cationic component (a) or (b).
  • the addition of a mixture of the (a) trivalent cation in the form of a salt and the (c) water-soluble amphoteric polymer to the paper stock is first carried out. Subsequently, the (b) water-soluble cationic polymer is added.
  • the process chemicals commonly used in papermaking can be used in the usual amounts, e.g. Retention aids, dehydrating agents, other dry strength agents such as, for example, 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 compared to known methods.
  • the percentages in the examples are by weight unless otherwise specified.
  • sheets were produced in laboratory tests in a Rapid-Köthen laboratory sheet former. The leaves were stored for 24 hours at 23 0 C and a humidity of 50%. Thereafter, the following strength tests were carried out:
  • Alum technical aluminum sulphate powder [Ab (SO 4 ) S-14 HbO]
  • Polymer K3 Cationic polyvinylamine, Hofmann degradation product, molecular weight about 25,000 daltons, solids content 8% by weight (RSL HF 70D from SNF SAS)
  • Polymer A2 Amphoteric polyacrylamide, solids content 20 wt .-% (Polystron ® PS GE 200 R Arakawa)
  • Anionic polyacrylamide molecular weight about 600,000 daltons, solid content 16 wt .-% (Luredur ® PR 8284 of BASF SE)
  • Polymer V3 polyallylamine, molecular weight approx. 15,000 daltons, solids content 93% by weight (PAA-HCl-3S from Nittobo)
  • the trivalent cations and polymers shown in the Tables were added successively to the stock described above with stirring.
  • the polymer concentration of the aqueous solutions of cationic and anionic polymers was 1% each, and that of the trivalent cation in aqueous solution was 1% each.
  • 0.27% of a commercial defoamer SLO Afranil ® from BASF SE
  • the amounts of the trivalent cations and polymers used in each case are given in percent by weight, based on the solids content of the paper stock.
  • Examples 1 to 10 according to the invention show in particular the surprisingly good effect of the system consisting of three components on the dry strength and at the same time on the dewatering.
  • Comparison 1 Comparison according to DE 10 2004 056 551 A1
  • Comparison 2 Comparison analogous to DE 10 2004 056 551 A1 and additionally predosing a trivalent cation
  • Example 1 Dosing order: Cation 1, Polymer K1, Polymer A1
  • Example 2 Dosing order: Cation 2, Polymer K1, Polymer A1
  • Example 3 Dosing order: Polymer K1, Cation 1, Polymer A1
  • Example 4 Dosing order: Mixture of cation 1 and polymer K1, polymer A1 10
  • Example 5 Dosing order: cation 1, polymer A1, polymer K1
  • Comparison 4 Comparison according to DE 10 2004 056 551 A1
  • Comparison 5 Comparison according to DE 10 2004 056 551 A1 and additionally pre-dosage of a trivalent cation
  • Comparison 7 Comparison according to JP 54-030913 A1
  • Comparison 8 Comparison according to JP 54-030913 A1
  • Comparison 10 Comparison analogous to JP 02-1 12498 A1
  • Examples 6 to 10 Dosing order in each case: trivalent cation, cationic polymer, amphoteric polymer

Landscapes

  • Paper (AREA)
  • Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
  • Macromolecular Compounds Obtained By Forming Nitrogen-Containing Linkages In General (AREA)

Abstract

L'invention concerne un procédé de fabrication de papier, carton-pâte et carton présentant une haute résistance à l'état sec, comprenant les étapes suivantes: ajouter à une pâte à papier (a) au moins un cation trivalent sous forme d'un sel, (b) au moins un polymère cationique soluble dans l'eau et (c) au moins un polymère amphotère soluble dans l'eau; égoutter la pâte à papier de manière à former des feuilles puis sécher les produits papier, le polymère cationique (b) soluble dans l'eau étant choisi dans le groupe des (i) polymères contenant des unités vinylamine et des (ii) polymères contenant des unités éthylène-imine.
EP10724788.4A 2009-06-16 2010-06-07 Procédé de fabrication pour augmenter la résistance à sec de papier et de carton présentant Active EP2443284B2 (fr)

Priority Applications (2)

Application Number Priority Date Filing Date Title
PL10724788T PL2443284T5 (pl) 2009-06-16 2010-06-07 Sposób zwiększania wytrzymałości na sucho papieru, tektury i kartonu
EP10724788.4A EP2443284B2 (fr) 2009-06-16 2010-06-07 Procédé de fabrication pour augmenter la résistance à sec de papier et de carton présentant

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
EP09007861 2009-06-16
PCT/EP2010/057890 WO2010145956A1 (fr) 2009-06-16 2010-06-07 Procédé permettant d'augmenter la résistance à l'état sec du papier, du carton souple et du carton
EP10724788.4A EP2443284B2 (fr) 2009-06-16 2010-06-07 Procédé de fabrication pour augmenter la résistance à sec de papier et de carton présentant

Publications (3)

Publication Number Publication Date
EP2443284A1 true EP2443284A1 (fr) 2012-04-25
EP2443284B1 EP2443284B1 (fr) 2018-01-17
EP2443284B2 EP2443284B2 (fr) 2020-11-18

Family

ID=42647475

Family Applications (1)

Application Number Title Priority Date Filing Date
EP10724788.4A Active EP2443284B2 (fr) 2009-06-16 2010-06-07 Procédé de fabrication pour augmenter la résistance à sec de papier et de carton présentant

Country Status (8)

Country Link
US (1) US8926797B2 (fr)
EP (1) EP2443284B2 (fr)
JP (1) JP5832426B2 (fr)
CN (2) CN104532674A (fr)
CA (1) CA2763508C (fr)
ES (1) ES2663702T5 (fr)
PL (1) PL2443284T5 (fr)
WO (1) WO2010145956A1 (fr)

Families Citing this family (33)

* 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
CN104947509B (zh) 2009-08-05 2017-11-03 国际纸业公司 干燥绒毛浆片材添加剂
WO2011017532A2 (fr) 2009-08-05 2011-02-10 International Paper Company Processus pour appliquer une composition contenant un métal trivalent cationique et un agent tensio-actif délieur, et réalisation d'une feuille de pâte défibrée
MY162376A (en) 2009-08-05 2017-06-15 Shell Int Research Method for monitoring a well
US8454799B2 (en) 2010-05-05 2013-06-04 Basf Se Pulp composition for paper and solid board production
CN103003489B (zh) 2010-07-20 2016-01-20 国际纸业公司 包含多价阳离子型金属和含胺抗静电剂的组合物及制造和使用方法
CN103003488B (zh) 2010-07-22 2015-04-15 国际纸业公司 使用阳离子型染料和解胶剂型表面活性剂制造绒毛浆片材的方法和由该方法制得的绒毛浆片材
GB201107885D0 (en) 2011-05-12 2011-06-22 Reckitt Benckiser Nv Improved composition
US9103071B2 (en) * 2011-06-20 2015-08-11 Basf Se Manufacture of paper and paperboard
WO2013081955A1 (fr) 2011-12-01 2013-06-06 Buckman Laboratories International, Inc. Procédé et système de production de pâte commercialisée et produits associés
ES2720487T3 (es) * 2012-02-01 2019-07-22 Basf Se Proceso para la fabricación de papel y cartón
US9051687B2 (en) 2012-08-22 2015-06-09 Basf Se Production of paper, card and board
SI2897922T1 (sl) 2012-09-24 2017-01-31 Basf Se Sistem in postopek za izdelavo pene na kraju samem
FI126216B (en) 2013-03-26 2016-08-31 Kemira Oyj Procedure for the manufacture of cardboard
CN104452463B (zh) 2013-09-12 2017-01-04 艺康美国股份有限公司 造纸方法以及组合物
CN104452455B (zh) 2013-09-12 2019-04-05 艺康美国股份有限公司 造纸助剂组合物以及增加成纸灰分保留的方法
US8894817B1 (en) 2014-01-16 2014-11-25 Ecolab Usa Inc. Wet end chemicals for dry end strength
US9567708B2 (en) 2014-01-16 2017-02-14 Ecolab Usa Inc. Wet end chemicals for dry end strength in paper
CN103866630B (zh) * 2014-02-25 2016-10-12 苏州恒康新材料有限公司 一种黄原胶湿强剂及其制备方法
WO2015144428A1 (fr) * 2014-03-28 2015-10-01 Basf Se Procédé de fabrication de carton ondulé
US9702086B2 (en) 2014-10-06 2017-07-11 Ecolab Usa Inc. Method of increasing paper strength using an amine containing polymer composition
US9920482B2 (en) 2014-10-06 2018-03-20 Ecolab Usa Inc. Method of increasing paper strength
WO2016058730A1 (fr) * 2014-10-13 2016-04-21 Basf Se Composition de durcissement pour papier et carton
CA3001757C (fr) 2015-10-20 2023-10-17 Basf Se Systeme et procede pour la fabrication d'une mousse in situ
CN106930142B (zh) * 2015-12-31 2020-03-24 艺康美国股份有限公司 干强剂组合物以及提高纸张干强度的方法
FR3048436B1 (fr) 2016-03-03 2018-03-23 S.P.C.M. Sa Procede de fabrication de papier et de carton
EP3455404B1 (fr) 2016-05-13 2024-05-15 Ecolab USA Inc. Réduction de poussière de mouchoir en papier
CN107447582B (zh) * 2016-06-01 2022-04-12 艺康美国股份有限公司 用于在高电荷需求系统中造纸的高效强度方案
EP3775087B1 (fr) * 2018-04-04 2023-05-24 Solenis Technologies, L.P. Application assistée par moussage d'additifs de résistance à des produits de papier
KR20210030923A (ko) 2018-07-12 2021-03-18 케미라 오와이제이 다층 섬유성 웹을 제조하는 방법, 및 다층 섬유성 웹
EP3850020A1 (fr) * 2018-09-14 2021-07-21 Solenis Technologies Cayman, L.P. Procédé de production de papier ou de carton
CN109264875B (zh) * 2018-10-12 2021-09-28 山东理工大学 Per-pamam和pesa无磷复合阻垢剂
US11028538B2 (en) 2019-02-28 2021-06-08 Solenis Technologies, L.P. Composition and method for increasing wet and dry paper strength

Family Cites Families (46)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5430913A (en) 1977-08-12 1979-03-07 Arakawa Rinsan Kagaku Kogyo Paper strength enhancing agent
DE3506832A1 (de) 1985-02-27 1986-08-28 Basf Ag, 6700 Ludwigshafen Verfahren zur herstellung von papier mit hoher trockenfestigkeit
DE3534273A1 (de) * 1985-09-26 1987-04-02 Basf Ag Verfahren zur herstellung von vinylamin-einheiten enthaltenden wasserloeslichen copolymerisaten und deren verwendung als nass- und trockenverfestigungsmittel fuer papier
JP2731920B2 (ja) 1988-10-14 1998-03-25 ハリマ化成株式会社 製紙方法
JPH03167392A (ja) * 1989-08-09 1991-07-19 Kanzaki Paper Mfg Co Ltd 紙の製造方法
JP3075589B2 (ja) * 1990-06-28 2000-08-14 三井化学株式会社 紙の抄造方法および製紙用添加剤
JP3186139B2 (ja) 1991-09-25 2001-07-11 日本ピー・エム・シー株式会社 紙の製造法
JP3173113B2 (ja) 1992-03-17 2001-06-04 荒川化学工業株式会社 製紙用添加剤の製造法
DE4241117A1 (de) * 1992-12-07 1994-06-09 Basf Ag Verwendung von hydrolysierten Copolymerisaten aus N-Vinylcarbonsäureamiden und monoethylenisch ungesättigten Carbonsäuren bei der Papierherstellung
JP3487059B2 (ja) 1995-02-01 2004-01-13 荒川化学工業株式会社 製紙用添加剤
JP3273534B2 (ja) * 1995-09-14 2002-04-08 星光化学工業株式会社 製紙用添加剤及び製紙方法
ES2140954T3 (es) * 1996-01-08 2000-03-01 Basf Ag Procedimiento para la obtencion de condensados y productos de adicion hidrosolubles, que contienen grupos amino, y su empleo.
DE19607674A1 (de) * 1996-02-29 1997-09-04 Basf Ag Verwendung von hydrolysierten Polymerisaten von N-Vinylcarbonsäureamiden als Mittel zur Erhöhung der Trockenfestigkeit von Papier, Pappe und Karton
DE19627553A1 (de) 1996-07-09 1998-01-15 Basf Ag Verfahren zur Herstellung von Papier und Karton
AU3913197A (en) 1996-08-15 1998-03-06 Hercules Incorporated Amphoteric polyacrylamides as dry strength additives for paper
DE19713755A1 (de) 1997-04-04 1998-10-08 Basf Ag Verfahren zur Herstellung von Papier, Pappe und Karton mit hoher Trockenfestigkeit
JP3151427B2 (ja) 1997-11-06 2001-04-03 株式会社トキワ 段ボール原紙の製造方法
JP2000022092A (ja) † 1998-07-03 2000-01-21 Nippon Telegr & Teleph Corp <Ntt> 単電子メモリ素子
JP4238945B2 (ja) 1999-01-27 2009-03-18 荒川化学工業株式会社 製紙用添加剤および紙の製造方法
JP2001279595A (ja) * 2000-03-30 2001-10-10 Harima Chem Inc 製紙方法
JP2003055454A (ja) * 2001-08-10 2003-02-26 Hymo Corp ポリアルキレンイミン変性物。
JP2003181466A (ja) 2001-12-21 2003-07-02 Hymo Corp 製紙排水処理方法
JP4465646B2 (ja) 2003-06-30 2010-05-19 荒川化学工業株式会社 製紙用添加剤および当該製紙用添加剤を用いた紙
JP4517662B2 (ja) 2004-02-10 2010-08-04 栗田工業株式会社 紙及び板紙の製造方法
JP4770121B2 (ja) 2004-03-30 2011-09-14 栗田工業株式会社 紙及び板紙の製造方法
DE102004056551A1 (de) 2004-11-23 2006-05-24 Basf Ag Verfahren zur Herstellung von Papier, Pappe und Karton mit hoher Trockenfestigkeit
US8308902B2 (en) * 2004-12-29 2012-11-13 Hercules Incorporated Retention and drainage in the manufacture of paper
US20060142431A1 (en) 2004-12-29 2006-06-29 Sutman Frank J Retention and drainage in the manufacture of paper
CN101133211A (zh) * 2004-12-29 2008-02-27 赫尔克里士公司 造纸中留着和滤水的改进
US20060142432A1 (en) * 2004-12-29 2006-06-29 Harrington John C Retention and drainage in the manufacture of paper
FR2880901B1 (fr) * 2005-01-17 2008-06-20 Snf Sas Soc Par Actions Simpli Procede de fabrication de papier et carton de grande resistance a sec et papiers et cartons ainsi obtenus
JP4891601B2 (ja) * 2005-12-02 2012-03-07 ハリマ化成株式会社 板紙の製造方法
CN101405457B (zh) 2006-03-16 2011-08-17 巴斯夫欧洲公司 生产具有高干强度的纸、纸板和卡纸板的方法
US7981250B2 (en) * 2006-09-14 2011-07-19 Kemira Oyj Method for paper processing
CN101086148A (zh) * 2007-06-28 2007-12-12 上海东升新材料有限公司 纸用乳液干强剂及其制备方法
CA2692303C (fr) 2007-07-05 2017-02-07 Basf Se Procede pour preparer des suspensions aqueuses de charges en fines particules et leur utilisation pour produire des papiers a teneur en charges et a resistance a sec elevees
WO2009004078A1 (fr) 2007-07-05 2009-01-08 Basf Se Suspensions aqueuses de charges en fines particules, leur procédé de préparation et leur utilisation pour produire des papiers à teneur en charges et à résistance à sec élevées
ES2378425T5 (es) 2007-07-05 2017-05-16 Omya International Ag. Suspensiones acuosas de materiales de relleno finamente divididos, procedimiento para su preparación y su uso para la fabricación de papeles con alto contenido en materiales de relleno y alta resistencia en seco
JP2010532404A (ja) 2007-07-05 2010-10-07 ビーエーエスエフ ソシエタス・ヨーロピア 微細充填剤の水性スラリーの製造方法及び高い充填剤含量及び高い乾燥強度を有する紙を製造するための前記水性スラリーの使用
EP2205660B1 (fr) 2007-10-04 2012-06-13 Basf Se Aminoalkyl vinylethers contenant des unites ethyleneimine, leur procede de preparation et leur utilisation
WO2009080613A1 (fr) 2007-12-20 2009-07-02 Basf Se Polymères greffés contenant des chaînes latérales oligoalkylène-imine, leur procédé de fabrication et leur utilisation
CA2722237A1 (fr) 2008-05-15 2009-11-19 Basf Se Procede de production de papier, de carton-pate, et de carton presentant une resistance a sec elevee
EP2304106B1 (fr) 2008-06-24 2018-09-12 Basf Se Production de papier
EP2315875B1 (fr) * 2008-08-18 2014-03-05 Basf Se Procédé pour améliorer la résistance à sec du papier, du carton-pâte et du carton
WO2011090672A1 (fr) * 2009-12-29 2011-07-28 Hercules Incorporated Procédé pour améliorer la résistance à l'état sec du papier, par traitement par des polymères contenant de la vinylamine et des polymères contenant de l'acrylamide
US8454799B2 (en) 2010-05-05 2013-06-04 Basf Se Pulp composition for paper and solid board production

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
See references of WO2010145956A1 *

Also Published As

Publication number Publication date
US8926797B2 (en) 2015-01-06
US20120073773A1 (en) 2012-03-29
PL2443284T5 (pl) 2021-04-19
EP2443284B2 (fr) 2020-11-18
JP5832426B2 (ja) 2015-12-16
ES2663702T5 (es) 2021-12-16
WO2010145956A1 (fr) 2010-12-23
JP2012530196A (ja) 2012-11-29
EP2443284B1 (fr) 2018-01-17
CN102459760A (zh) 2012-05-16
ES2663702T3 (es) 2018-04-16
CA2763508C (fr) 2018-07-17
CA2763508A1 (fr) 2010-12-23
CN104532674A (zh) 2015-04-22
PL2443284T3 (pl) 2018-07-31

Similar Documents

Publication Publication Date Title
EP2443284B1 (fr) Procédé de fabrication pour augmenter la résistance à sec de papier et de carton présentant
EP2315875B1 (fr) Procédé pour améliorer la résistance à sec du papier, du carton-pâte et du carton
EP1819877B1 (fr) Procede pour produire du papier, du carton, du carton blanchi presentant une resistance elevee a sec
EP2491177B1 (fr) Procédé de fabrication de papier, carton souple et carton avec une grande résistance à sec
EP2288750B1 (fr) Procédé de production de papier, de carton-pâte, et de carton présentant une résistance à sec élevée
EP0416427B1 (fr) Produit d&#39;encollage neutre pour masses de papier brut utilisant des dispersions polymères cationiques
EP1999314B1 (fr) Procédé de fabrication de papier et de carton présentant une grande résistance à sec
EP2304106B1 (fr) Production de papier
EP2393982B1 (fr) Procédé de fabrication de papier, de carton-pâte et de carton présentant une grande résistance à sec
DE69408485T2 (de) Verfahren zur Herstellung von Papier mit erhöhter Festigkeit im nassen und trockenen Zustand
DE3706525A1 (de) Verfahren zur herstellung von papier, pappe und karton mit hoher trockenfestigkeit
WO2010145990A1 (fr) Procédé de réduction de dépôts dans la partie sèche lors de la fabrication de papier et carton
EP3332063B1 (fr) Procédé de fabrication de papier
EP2723943B1 (fr) Procédé de fabrication de papier, de papier-carton et de carton compact
EP3234259A1 (fr) Procédé de fabrication de papier et de carton
EP2888404B1 (fr) Procédé de fabrication de papier, de carton-pâte et de carton
EP3122937B1 (fr) Procédé de fabrication de carton ondulé
WO2016058730A1 (fr) Composition de durcissement pour papier et carton
WO2006136556A2 (fr) Procede de fabrication de papier et de carton

Legal Events

Date Code Title Description
PUAI Public reference made under article 153(3) epc to a published international application that has entered the european phase

Free format text: ORIGINAL CODE: 0009012

17P Request for examination filed

Effective date: 20120116

AK Designated contracting states

Kind code of ref document: A1

Designated state(s): AL AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HR HU IE IS IT LI LT LU LV MC MK MT NL NO PL PT RO SE SI SK SM TR

DAX Request for extension of the european patent (deleted)
REG Reference to a national code

Ref country code: DE

Ref legal event code: R079

Ref document number: 502010014574

Country of ref document: DE

Free format text: PREVIOUS MAIN CLASS: D21H0021180000

Ipc: D21H0017370000

GRAP Despatch of communication of intention to grant a patent

Free format text: ORIGINAL CODE: EPIDOSNIGR1

STAA Information on the status of an ep patent application or granted ep patent

Free format text: STATUS: GRANT OF PATENT IS INTENDED

RIC1 Information provided on ipc code assigned before grant

Ipc: D21H 17/66 20060101ALI20170725BHEP

Ipc: D21H 17/44 20060101ALI20170725BHEP

Ipc: D21H 17/56 20060101ALI20170725BHEP

Ipc: D21H 17/37 20060101AFI20170725BHEP

Ipc: D21H 17/00 20060101ALI20170725BHEP

Ipc: D21H 21/18 20060101ALI20170725BHEP

INTG Intention to grant announced

Effective date: 20170810

GRAS Grant fee paid

Free format text: ORIGINAL CODE: EPIDOSNIGR3

GRAA (expected) grant

Free format text: ORIGINAL CODE: 0009210

STAA Information on the status of an ep patent application or granted ep patent

Free format text: STATUS: THE PATENT HAS BEEN GRANTED

AK Designated contracting states

Kind code of ref document: B1

Designated state(s): AL AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HR HU IE IS IT LI LT LU LV MC MK MT NL NO PL PT RO SE SI SK SM TR

REG Reference to a national code

Ref country code: GB

Ref legal event code: FG4D

Free format text: NOT ENGLISH

REG Reference to a national code

Ref country code: CH

Ref legal event code: EP

REG Reference to a national code

Ref country code: IE

Ref legal event code: FG4D

Free format text: LANGUAGE OF EP DOCUMENT: GERMAN

REG Reference to a national code

Ref country code: AT

Ref legal event code: REF

Ref document number: 964512

Country of ref document: AT

Kind code of ref document: T

Effective date: 20180215

REG Reference to a national code

Ref country code: DE

Ref legal event code: R096

Ref document number: 502010014574

Country of ref document: DE

REG Reference to a national code

Ref country code: ES

Ref legal event code: FG2A

Ref document number: 2663702

Country of ref document: ES

Kind code of ref document: T3

Effective date: 20180416

REG Reference to a national code

Ref country code: SE

Ref legal event code: TRGR

REG Reference to a national code

Ref country code: LT

Ref legal event code: MG4D

REG Reference to a national code

Ref country code: FR

Ref legal event code: PLFP

Year of fee payment: 9

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: CY

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20180117

Ref country code: LT

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20180117

Ref country code: HR

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20180117

Ref country code: NO

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20180417

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: BG

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20180417

Ref country code: GR

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20180418

Ref country code: LV

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20180117

Ref country code: IS

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20180517

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: MT

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20180117

REG Reference to a national code

Ref country code: DE

Ref legal event code: R026

Ref document number: 502010014574

Country of ref document: DE

PLBI Opposition filed

Free format text: ORIGINAL CODE: 0009260

PLAX Notice of opposition and request to file observation + time limit sent

Free format text: ORIGINAL CODE: EPIDOSNOBS2

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: EE

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20180117

Ref country code: AL

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20180117

Ref country code: RO

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20180117

Ref country code: IT

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20180117

26 Opposition filed

Opponent name: KEMIRA OYJ

Effective date: 20181017

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: CZ

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20180117

Ref country code: DK

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20180117

Ref country code: SM

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20180117

Ref country code: SK

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20180117

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: SI

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20180117

REG Reference to a national code

Ref country code: BE

Ref legal event code: MM

Effective date: 20180630

PLBB Reply of patent proprietor to notice(s) of opposition received

Free format text: ORIGINAL CODE: EPIDOSNOBS3

REG Reference to a national code

Ref country code: IE

Ref legal event code: MM4A

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: LU

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20180607

Ref country code: MC

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20180117

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: IE

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20180607

REG Reference to a national code

Ref country code: GB

Ref legal event code: 732E

Free format text: REGISTERED BETWEEN 20190503 AND 20190508

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: BE

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20180630

REG Reference to a national code

Ref country code: DE

Ref legal event code: R081

Ref document number: 502010014574

Country of ref document: DE

Owner name: SOLENIS TECHNOLOGIES CAYMAN, L.P., GEORGE TOWN, KY

Free format text: FORMER OWNER: BASF SE, 67063 LUDWIGSHAFEN, DE

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: IT

Payment date: 20190620

Year of fee payment: 12

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: SE

Payment date: 20190627

Year of fee payment: 10

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: AT

Payment date: 20190521

Year of fee payment: 10

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: CH

Payment date: 20190702

Year of fee payment: 10

PLAB Opposition data, opponent's data or that of the opponent's representative modified

Free format text: ORIGINAL CODE: 0009299OPPO

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: TR

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20180117

R26 Opposition filed (corrected)

Opponent name: KEMIRA OYJ

Effective date: 20181017

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: HU

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT; INVALID AB INITIO

Effective date: 20100607

Ref country code: PT

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20180117

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: MK

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20180117

PUAH Patent maintained in amended form

Free format text: ORIGINAL CODE: 0009272

STAA Information on the status of an ep patent application or granted ep patent

Free format text: STATUS: PATENT MAINTAINED AS AMENDED

REG Reference to a national code

Ref country code: CH

Ref legal event code: AELC

27A Patent maintained in amended form

Effective date: 20201118

AK Designated contracting states

Kind code of ref document: B2

Designated state(s): AL AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HR HU IE IS IT LI LT LU LV MC MK MT NL NO PL PT RO SE SI SK SM TR

REG Reference to a national code

Ref country code: DE

Ref legal event code: R102

Ref document number: 502010014574

Country of ref document: DE

REG Reference to a national code

Ref country code: CH

Ref legal event code: PL

REG Reference to a national code

Ref country code: NL

Ref legal event code: MM

Effective date: 20200701

REG Reference to a national code

Ref country code: AT

Ref legal event code: MM01

Ref document number: 964512

Country of ref document: AT

Kind code of ref document: T

Effective date: 20200607

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: NL

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20200701

Ref country code: LI

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20200630

Ref country code: CH

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20200630

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: AT

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20200607

Ref country code: SE

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20200608

REG Reference to a national code

Ref country code: SE

Ref legal event code: EUG

REG Reference to a national code

Ref country code: ES

Ref legal event code: DC2A

Ref document number: 2663702

Country of ref document: ES

Kind code of ref document: T5

Effective date: 20211216

P01 Opt-out of the competence of the unified patent court (upc) registered

Effective date: 20230510

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: ES

Payment date: 20230703

Year of fee payment: 14

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: GB

Payment date: 20240627

Year of fee payment: 15

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: DE

Payment date: 20240627

Year of fee payment: 15

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: FR

Payment date: 20240625

Year of fee payment: 15

Ref country code: FI

Payment date: 20240625

Year of fee payment: 15

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: PL

Payment date: 20240521

Year of fee payment: 15