EP1999314A1 - Procédé de fabrication de papier et de carton présentant une grande résistance à sec - Google Patents

Procédé de fabrication de papier et de carton présentant une grande résistance à sec

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Publication number
EP1999314A1
EP1999314A1 EP07712497A EP07712497A EP1999314A1 EP 1999314 A1 EP1999314 A1 EP 1999314A1 EP 07712497 A EP07712497 A EP 07712497A EP 07712497 A EP07712497 A EP 07712497A EP 1999314 A1 EP1999314 A1 EP 1999314A1
Authority
EP
European Patent Office
Prior art keywords
polymer
acid
pulp
paper
units
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
EP07712497A
Other languages
German (de)
English (en)
Other versions
EP1999314B1 (fr
Inventor
Martin Rübenacker
Norbert Schall
Ellen KRÜGER
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
Application filed by BASF SE filed Critical BASF SE
Priority to EP07712497.2A priority Critical patent/EP1999314B1/fr
Publication of EP1999314A1 publication Critical patent/EP1999314A1/fr
Application granted granted Critical
Publication of EP1999314B1 publication Critical patent/EP1999314B1/fr
Not-in-force 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
    • D21H17/21—Macromolecular organic compounds of natural origin; Derivatives thereof
    • D21H17/23—Lignins
    • 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
    • D21H17/42—Synthetic macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds containing ionic groups anionic
    • 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
    • D21H17/42—Synthetic macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds containing ionic groups anionic
    • D21H17/43—Carboxyl groups or derivatives thereof

Definitions

  • the invention relates to a process for the production of paper, paperboard and cardboard with high dry strength by separately adding a polymer containing vinylamine units and a polymeric anionic compound to a pulp, dewatering the pulp and drying the paper products.
  • a process for the production of paper with high dry strength is known in which the paper stock is first a water-soluble cationic polymer, eg. As polyethyleneimine, and then adding a water-soluble anionic polymer, eg. As a hydrolyzed polyacrylamide, added and dehydrated the pulp on the paper machine with sheet formation.
  • the anionic polymers contain up to 30 mol% of copolymerized acrylic acid.
  • a process for the production of paper with high dry strength in which one adds to the paper stock first a water-soluble cationic polymer and then a water-soluble anionic polymer sat.
  • 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-crosslinked condensation products of adipic acid and diethylenetriamine.
  • the use of partially hydrolyzed homo- and copolymers of N-vinylformamide has also been considered.
  • the hydrolysis The degree of segregation of the N-vinylformamide polymers is at least 30 mol% and is preferably from 50 to 100 mol%.
  • 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 from 25 to 100%, is added in combination with an anionic polyacrylamide, the pulp is then dewatered and dried.
  • WO 03/052206 discloses a paper product with improved strength properties which can be obtained 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 Alde - Hydro functions such as aldehyde-containing polysaccharides applies. Not only does the paper improve its dry and wet strength, it also observes a sizing effect of the treating agents.
  • WO 04/061235 a process for the production of paper, in particular tissue, with particularly high wet and / or dry strengths is known, in which one adds to the paper material first a water-soluble cationic polymer, the at least 1, 5meq / g polymer of primary amino functionalities contains and has 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.
  • the advantage of this method is mainly the variability of the two-component systems described in terms of various paper properties, including wet and dry strength, exposed.
  • EP-A 438 744 is the use of copolymers of, for example, N-vinylformamide and acrylic acid, methacrylic acid and / or maleic acid having a K value of 8 to 50 (determined by H. Fikentscher in 1% aqueous solution at pH 7 and 25 ° C.) and the polymers obtainable therefrom by partial or complete removal of formyl groups from the copolymerized vinylformamide to form vinylamine units as coating inhibitors in water-carrying systems such as boilers or pipes.
  • copolymers obtained by copolymerizing N-vinylcarboxamides, monoethylenically unsaturated carboxylic acids and optionally other ethylenically unsaturated monomers and subsequent hydrolysis of the vinylcarboxylic acid units contained in the copolymers to the corresponding the amine or ammonium units are available, can be used in papermaking as an additive to the paper stock to increase the rate of dewatering and retention and the dry and wet strength of the paper, see. EP-B 672 212.
  • a process for the production of paper, paperboard and cardboard with high dry strength is known by separate addition of a polymer containing vinylamine units and a polymeric anionic compound to a pulp, dewatering of the pulp and drying of the paper products ,
  • the polymeric anionic compound used is at least one copolymer obtainable by copolymerizing
  • R 1 , R 2 H or C 1 to C 6 alkyl
  • lignosulfonic acid and lignosulfonates as dispersants in cement and gypsum mortars, as flotation agents, as an additive in feed pelting, as molding sand binders and as agglomerating agents in ore smelting, cf. Römpp, 9th edition, Georg Thieme Verlag Stuttgart, 1990, page 251 1.
  • the present invention has for its object to provide a further process for the production of paper with high dry strength and lowest possible wet strength available.
  • the dry strength in particular in packaging papers (for example, wave from waste paper, Fluting) should be further improved compared to the previously known methods.
  • the object is achieved according to the invention by a process for the production of paper, paperboard and cardboard with high dry strength by separately adding a polymer comprising vinylamine units and a polymeric anionic compound to a paper stock, draining the paper stock and drying the paper stock. when used as a polymeric anionic compound lignosulfonic acid and / or a lignosulfonate.
  • a polymer comprising vinylamine units is added to the paper stock as the polymeric cationic component.
  • These compounds are preferably used as the sole cationic component. However, they may optionally be replaced by other cationic polymers, such as cationic poly (meth) acrylamides, polydiallyldimethylammonium chlorides, condensates of dimethylamine and epichlorohydrin or polydialkyl (meth) acrylamides, up to a proportion of 50% by weight.
  • Suitable polymers containing vinylamine units are all polymers which are specified, for example, in WO 04/061235, page 12, line 28 to page 13, line 21 and in FIG. 1 cited in the prior art.
  • the molar mass M w of the polymers containing vinylamine units is, for example, 1000 to 5 million and is usually in the range from 5 000 to 500 000, preferably 40 000 D to 400 000 D.
  • Polymers containing vinylamine units are obtainable, for example, by polymerizing at least one monomer of the formula
  • R 1 , R 2 H or C 1 - to C 6 -alkyl
  • the indication of vinylamine units comprises the sum of vinylamine and amidine units in the polymer.
  • a polymer containing at least 1 mol% of N-vinylformamide homopolymer is used as the polymer containing vinylamine units.
  • Polyvinylamine and / or at least 50 mol% of hydrolyzed homopolymers of N-vinylformamide are preferably used in the inventive method as a cationic component.
  • amphoteric copolymers which contain vinylamine units and which have at least at least 10 mol% more cationic than anionic groups.
  • amphoteric polymers are obtainable, for example, by copolymerization
  • R 1 , R 2 H or C 1 to C 6 alkyl
  • This group of polymers which are amphoteric and which have a total of more cationic than anionic groups contains, for example, up to a maximum of 35 mol%, preferably up to a maximum of 10 mol% of at least one acid group-containing monomer of group (b) in copolymerized form.
  • lignosulfonic acid and / or a lignosulfonate into consideration. Further details of these products can be found, for example, in the abovementioned reference Römpp, 9th edition, G. Thieme Verlag Stuttgart, 1990, page 251 1 and in Ullmann 's Encyclopedia of Industrial Chemistry, 5th Completely Revised Edition, Volume A15, Pages 31 1 to 314.
  • Lignosulphonic acid is produced in cellulose production by sulfite digestion of wood, whereby lignin reacts with sulphurous acid. It is sulfonated here on the C3 side chains of the phenylpropane units.
  • lignin sulphonic acid or lignin sulphonates are formed, for example, the sodium, potassium, ammonium, magnesium or calcium salts of lignosulphonic acid.
  • Lignosulfonic acid and the salts of lignosulfonic acid mentioned are soluble in water.
  • the molecular weight of the lignosulfonic acid is, for example 10,000 to 200,000 g / mol.
  • Lignosulfonates are z. B. obtained from the sulfite waste liquors (black liquor) of cellulose production.
  • Lignosulfonic acid and / or lignin sulfonate are used, for example, in an amount of from 0.1 to 10% by weight, preferably from 0.2 to 5% by weight and in particular from 0.5 to 2% by weight, based on dry paper stock.
  • lignosulfonate for example, the water-soluble sodium, potassium, ammonium, calcium, magnesium salts or mixtures thereof are used.
  • the sodium, ammonium and calcium salts are used.
  • Vinylamine-containing polymer and lignosulfonic acid and / or Ligninsulfo- are used in the inventive method, for example in a weight ratio of 5: 1 to 1: 5, preferably in a weight ratio of 2: 1 to 1: 2.
  • lignin sulfonic acid and / or lignin sulfonate are used together with an anionic copolymer of an N-vinylcarboxamide.
  • the dosage of these two components can be done separately or as a mixture.
  • it is used as a polymeric anionic compound
  • R 1 , R 2 H or C 1 - to C 6 -alkyl
  • B at least one acid group-containing monoethylenically unsaturated monomer and / or their alkali metal, alkaline earth metal or ammonium salts and optionally
  • polymeric anionic compound (ii) is a copolymer obtainable by copolymerizing
  • the polymeric anionic compound (ii) contains, for example
  • These compounds may be modified so that they additionally contain at least one compound having at least two ethylenically unsaturated double bonds in copolymerized form in the molecule.
  • branched copolymers are obtained.
  • the proportions and reaction conditions are to be selected so that water-soluble polymers are still obtained.
  • polymerization regulators Use can be made of all known regulators, e.g. Thiols, sec. Alcohols, sulfites, phosphites, hypophosphites, thioacids, aldehydes, etc. (further details can be found, for example, in EP-A 438 744, page 5, lines 7-12).
  • the branched copolymers contain, for example
  • Examples of monomers of group (a) are N-vinylformamide, N-vinyl-N-methylformamide, N-vinylacetamide, N-vinyl-N-methylacetamide, N-vinyl-N-ethylacetamide, N-vinyl-N-methylpropionamide and N -Vinylpropionamid.
  • the monomers of group (a) can be used alone or in a mixture in the copolymerization with the monomers of the other groups.
  • Suitable monomers of group (b) are, in particular, monoethylenically unsaturated carboxylic acids having 3 to 8 carbon atoms and the water-soluble salts of these carboxylic acids.
  • This group of monomers includes, for example, 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 of group (b) are monomers containing sulfo groups, such as vinylsulfonic acid, acrylamido-2-methylpropanesulfonic acid and styrenesulfonic acid and 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.
  • the monomers of group (b) are preferably used in the copolymerization in partially neutralized form.
  • the copolymers may optionally contain monomers of group (c) in copolymerized form for modification, e.g. Esters of ethylenically unsaturated C3 to C8 carboxylic acids such as methyl acrylate, ethyl acrylate, n-butyl acrylate, isobutyl acrylate, isobutyl methacrylate, methyl methacrylate, ethyl methacrylate and vinyl esters e.g. Vinyl acetate or vinyl propionate, or other monomers such as N-vinylpyrrolidone, N-vinylimidazole, acrylamide and / or methacrylamide.
  • group (c) in copolymerized form for modification, e.g. Esters of ethylenically unsaturated C3 to C8 carboxylic acids such as methyl acrylate, ethyl acrylate, n-butyl acrylate, isobutyl acrylate, iso
  • a further modification of the copolymers is possible by using in the copolymerization monomers (d) which contain at least two double bonds in the molecule, for.
  • monomers (d) which contain at least two double bonds in the molecule
  • methylenebisacrylamide glycol diacrylate, Glykoldimethacrylat, Gylcerintriacrylat, triallylamine, 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.
  • the amounts used are up to 2 mol%, z. B. 0.001 to 1 mol%.
  • copolymerization of the monomers takes place in a known manner in the presence of free-radical polymerization initiators and optionally in the presence of polymerization regulators, cf. EP-B 672 212, page 4, lines 13-37 or EP-A 438 744, page 2, line 26 to page 8, line 18.
  • Suitable polymeric anionic compounds (ii) are also amphoteric copolymers obtainable by copolymerizing
  • R 1 , R 2 H or C 1 - to C 6 -alkyl
  • amphoteric compounds having a total anionic charge include, for example
  • the hydrolysis of the anionic 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
  • polymeric anionic compound (ii) is preferably used a copolymer which
  • the average molecular weights Mw of the anionic or amphoteric polymers (ii) are, for example, 30,000 D to 10 million D, preferably 100,000 D to 1 million D.
  • These polymers have, for example, K values (determined according to H. Fikentscher in 5% iger aqueous saline solution at pH 7, a polymer concentration of 0.5% by weight and a temperature of 25 ° C) in the range of 20 to 250, preferably 50 to 150.
  • the invention further provides the use of lignosulfonic acid and / or at least one lignosulfonate as additive to the paper stock in the production of paper, paperboard and cardboard in the presence of at least one vinylamine units containing cationic polymers to increase the dry strength.
  • lignosulfonic acid and / or lingosulfonate are first metered into the paper stock, then the polymer containing vinylamine units is added and the paper stock is subsequently dehydrated.
  • An embodiment of the process according to the invention is particularly preferred in which, after addition of lignin sulphonic acid and / or lignin sulphonate and at least one polymer containing vinylamine units to the paper stock, an anionic vinyl chloride is also added.
  • copolymer containing carboxylic acid amide units which is obtainable by copolymerizing
  • R 1 , R 2 H or C 1 to C 6 alkyl
  • Wood pulp includes, for example, groundwood, thermomechanical pulp (TMP), chemo-thermo-mechanical pulp (CTMP), pressure groundwood, semi-pulp, high yield pulp, and refiner mechanical pulp (RMP).
  • TMP thermomechanical pulp
  • CMP chemo-thermo-mechanical 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, or a waste paper pulp.
  • Suitable annual plants for the production of pulps are, for example, rice, wheat, sugar cane and kenaf.
  • waste paper is usually used, which is used either alone or in admixture with other fibers or it is based on fiber blends of a primary material and recycled coated Committee, z. Bleached pine sulfate in admixture with recycled coated broke.
  • the dewatering of the stock usually takes place on the wire of a paper machine.
  • the method according to the invention has particular significance for the production of paper and board from waste paper, because it significantly increases the strength properties of the recycled fibers.
  • 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 polymers comprising vinylamine units, ie the cationic component of the polymers to be metered into the paper stock, are added to the process according to the invention, for example to thick stock or preferably to a thin stock.
  • the point of addition is preferably in front of the screens, but may also be between a shearing stage and a screen or afterwards.
  • the anionic component is preferably dosed to the thin.
  • a vinylamine-containing polymer as the sole cationic component
  • an anionic polymer of vinylformamide it is also possible first to add the cationic component (vinylamine units-containing polymer as the sole cationic component) to the paper stock and to meter the anionic component simultaneously but separately from the cationic component to the paper stock.
  • the vinylamine units-containing polymer is used, for example, in an amount of 0.05 to 2.0 wt .-%, preferably 0.1 to 1 wt .-%, based on dry pulp.
  • the ratio of cationic component (polymer containing vinylamine units) to polymeric anionic component (ligninsulfonic acid and / or ligninsulfonate or combination of ligninsulfonic acid and / or ligninsulfonate with at least one anionic polymer of vinylformamide) is for example 5: 1 to 1: 5 and is preferably in the range of 2: 1 to 1: 2.
  • the process according to the invention gives paper products which, compared with the processes of the prior art, have a higher level of dry strength with simultaneously low wet strength.
  • these papers have a high CMT value compared with known paper products.
  • the parts given in the following examples are parts by weight, the percentages are based on the weight of the substances.
  • the K value of the polymers was determined according to H. Fikentscher, Cellulose-Chemie, Vol. 13, 58-64 and 71-74 (1932) at a temperature of 20 ° C. in 5% strength by weight aqueous sodium chloride solutions at a pH of 7 and a polymer concentration of 0.5%.
  • K k * 1000.
  • the lignosulfonate used was a commercially available 54.69% strength aqueous solution of the calcium salt of lignosulfonic acid.
  • PVAm 1 The cationic polymer used was a 50% hydrolysed homopolymer of N-vinylformamide in the form of a 13% strength aqueous solution. The polymer had a molecular weight M w of 400,000.
  • Anionic polymer 1 copolymer of 70% N-vinylformamide and 30% sodium methacrylate having a molecular weight M w of 400,000.

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  • Paper (AREA)

Abstract

L'invention concerne un procédé de fabrication de papier et de carton présentant une grande résistance à sec, par addition séparée d'un polymère contenant des unités vinylamine et d'acide sulfonique de lignine et/ou d'un sulfonate de lignine à une pâte à papier, déshydratation de la pâte à papier et séchage des produits de papier.
EP07712497.2A 2006-03-16 2007-03-09 Procédé de fabrication de papier et de carton présentant une grande résistance à sec Not-in-force EP1999314B1 (fr)

Priority Applications (1)

Application Number Priority Date Filing Date Title
EP07712497.2A EP1999314B1 (fr) 2006-03-16 2007-03-09 Procédé de fabrication de papier et de carton présentant une grande résistance à sec

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
EP06111267 2006-03-16
EP07712497.2A EP1999314B1 (fr) 2006-03-16 2007-03-09 Procédé de fabrication de papier et de carton présentant une grande résistance à sec
PCT/EP2007/052238 WO2007104716A1 (fr) 2006-03-16 2007-03-09 Procédé de fabrication de papier et de carton présentant une grande résistance à sec

Publications (2)

Publication Number Publication Date
EP1999314A1 true EP1999314A1 (fr) 2008-12-10
EP1999314B1 EP1999314B1 (fr) 2017-02-22

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Family Applications (1)

Application Number Title Priority Date Filing Date
EP07712497.2A Not-in-force EP1999314B1 (fr) 2006-03-16 2007-03-09 Procédé de fabrication de papier et de carton présentant une grande résistance à sec

Country Status (8)

Country Link
US (1) US7922867B2 (fr)
EP (1) EP1999314B1 (fr)
JP (1) JP5156650B2 (fr)
CN (1) CN101405457B (fr)
CA (1) CA2644348C (fr)
ES (1) ES2625622T3 (fr)
PT (1) PT1999314T (fr)
WO (1) WO2007104716A1 (fr)

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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
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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
JP6999162B2 (ja) * 2017-12-22 2022-02-10 国立研究開発法人産業技術総合研究所 リグニンスルホン酸とカチオン性高分子を成分とするイオン複合材料
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JP2009530504A (ja) 2009-08-27
US20100108279A1 (en) 2010-05-06
ES2625622T3 (es) 2017-07-20
CA2644348C (fr) 2014-06-10
EP1999314B1 (fr) 2017-02-22
CN101405457A (zh) 2009-04-08
US7922867B2 (en) 2011-04-12
CA2644348A1 (fr) 2007-09-20
WO2007104716A1 (fr) 2007-09-20
PT1999314T (pt) 2017-05-26
JP5156650B2 (ja) 2013-03-06
CN101405457B (zh) 2011-08-17

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