EP0100370A1 - Procédé de production de papier ou de tissu non-tissé - Google Patents

Procédé de production de papier ou de tissu non-tissé Download PDF

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Publication number
EP0100370A1
EP0100370A1 EP19820106937 EP82106937A EP0100370A1 EP 0100370 A1 EP0100370 A1 EP 0100370A1 EP 19820106937 EP19820106937 EP 19820106937 EP 82106937 A EP82106937 A EP 82106937A EP 0100370 A1 EP0100370 A1 EP 0100370A1
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EP
European Patent Office
Prior art keywords
paper
woven fabric
slurry
fiber
pulp
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.)
Withdrawn
Application number
EP19820106937
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German (de)
English (en)
Inventor
Tadashi Hirakawa
Makoto Yoshida
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Teijin Ltd
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Teijin Ltd
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 Teijin Ltd filed Critical Teijin Ltd
Priority to EP19820106937 priority Critical patent/EP0100370A1/fr
Publication of EP0100370A1 publication Critical patent/EP0100370A1/fr
Withdrawn legal-status Critical Current

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    • 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
    • D21H17/53—Polyethers; Polyesters
    • 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
    • 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
    • D21H17/36—Polyalkenyalcohols; Polyalkenylethers; Polyalkenylesters
    • 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
    • D21H17/44—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
    • D21H17/55—Polyamides; Polyaminoamides; Polyester-amides

Definitions

  • the invention relates to a process for producing paper or wet non-woven fabric. More particularly, the invention relates to a process for producing, by a wet papermaking technique, paper or wet non-woven fabric having an excellent strength, water resistance, and bulkiness.
  • Fibrous binders and synthetic resin emulsions have generally been employed as an internal binder in the production of paper or non-woven fabric by a wet papermaking process of fiber or pulp.
  • the fibrous binders there have broadly been employed hot water-soluble or low melting point resins such as polyvinyl alcohol, polyethylene, ethylene-vinyl acetate copolymer and copolyesters in the form of fiber.
  • hot water-soluble or low melting point resins such as polyvinyl alcohol, polyethylene, ethylene-vinyl acetate copolymer and copolyesters in the form of fiber.
  • paper or non-woven fabric obtained by using polyvinyl alcohol fiber as the fibrous binder has a poor water resistance, thermal resistance, softness, and strength.
  • the emulsions are demulsified with a salt of a polyvalent metal to form the aggregate of the synthetic resin, which is then deposited on the fibers in a fiber slurry.
  • a salt of a polyvalent metal to form the aggregate of the synthetic resin, which is then deposited on the fibers in a fiber slurry.
  • the fibers themselves aggregate due to the aggregating action of the polyvalent metal salt, the aggregate of the resin has a poor durability, the stoppage of a forming wire occurs, foaming occurs due to the emulsifier, and the resultant paper or non-woven fabric has a poor surface texture.
  • the present invention therefore provides a process for producing paper or wet non-woven fabric, which process comprises mixing an aqueous anionic polymer solution with an aqueous cationic polymer solution, adding the mixture to a slurry of fiber or pulp, converting the slurry into paper or non-woven fabric by a wet papermaking technique, and drying the paper or non-woven fabric.
  • the anionic polymer generally acts as a binder
  • the cationic polymer generally acts to aggregate the anionic polymer, to fix the thus formed aggregate to the fiber or pulp, and optionally to cross-link the anionic polymer.
  • the "aqueous anionic polymer solution” or “aqueous cationic polymer solution” as used herein refers to an aqueous liquid in which the anionic polymer or cationic polymer is dissolved in water or dispersed in water without the assistance of any emulsifying or dispersing agents.
  • the anionic polymer usable for the present invention may include water-soluble polymers having on the backbone, ends, or side chains thereof one or more acid groups, such as carboxyl (-COOH), sulfino (-SOOH), sulfo (-S0 2 0H), sulfoamino (-NHS0 2 0H), aci-nitro (-NOOH), hydroxyamino (-NHOH), hydroxyimino (-NOH), or sodiosulfo (-SO 2 ONa) or salts thereof.
  • acid groups such as carboxyl (-COOH), sulfino (-SOOH), sulfo (-S0 2 0H), sulfoamino (-NHS0 2 0H), aci-nitro (-NOOH), hydroxyamino (-NHOH), hydroxyimino (-NOH), or sodiosulfo (-SO 2 ONa) or salts thereof.
  • anionic polymer are (1) carboxy-modified polyvinyl alcohol, (2) cellulose ethers such as carboxymethylcellulose, carboxyethyl- cellulose, and sodium salts thereof and sulfoethylcellulose ether, (3) oxidized starch, (4) polymers of acrylic acid and methacrylic acid and sodium salts or copolymers thereof, (5) anionically modified polyacrylamide, and (6) water--soluble polyesters such as copolyesters having polyethylene glycol units as at least a part of the diol component and having one or more sodiosulfo groups bound to the aromatic nucleus (see, for example, Japanese Examined Patent Publication No. 47-40873).
  • the cationic polymer usable for the present invention nay include water-soluble polymers having on the backbone, ends, or side chains thereof one or more primary, secondary, or tertiary groups or salts thereof or quaternary ammonium groups.
  • Preferred examples of the water-soluble cationic polymer are (1) polyalkylene polyamines and their derivatives, such as polyethylene-imine, polyamide epichlorohydrin, polyamide-polyamine epichlorohydrin (PPE) (see, for example, U.S.
  • Patent 2,926,116 polyvinyl imidazoline, and polyvinyl imidazoline salts, (2) cationically modified polyacrylamide, (3) cyclic polymers of diallylammonium halides (see, for example, U.S. Patent 3,288,770), (4) polyvinyl pyridine, (5) polymers of dialkylaminoethyl acrylate or methacrylate, (6) cationically modified urea--formaldehyde resin, and (7) cationically modified melamine--formaldehyde resin.
  • the aqueous anionic polymer solution is mixed with the aqueous cationic polymer solution to form a binder slurry containing solid aggregate particles.
  • a binder slurry may advantageously be employed for the production of paper or non-woven fabric based on synthetic fibers.
  • the concentrations of the solutions and the stirring conditions upon mixing of the solutions may vary depending upon the nature of the anionic polymer and the cationic polymer to be employed. However, in general, if both the solutions each having a concentration of 0.1% to 5% by weight are slowly brought into contact, a stable binder slurry containing solid aggregate particles of a uniform particle size can be obtained.
  • the solid aggregate particles may preferably have a positive i-potential in a slurry of fiber or pulp after the binder slurry is added to the fiber or pulp slurry in order to make easy fixation of the aggregate particles to the fiber or pulp since the fiber or pulp usually has a negative ç-potential.
  • the aggregate particles should preferably have a negative ç-potential if the fiber or pulp has a positive ç-potential, i.e., if the slurry is a slurry of polyamide fiber or animal fiber, such as wool or silk, having a low pH value or a slurry of asbestos fiber.
  • the pH of the fiber or pulp slurry may be controlled or an anionic or cationic thickner may be added to the fiber or pulp slurry.
  • the aqueous anionic polymer solution is mixed with the aqueous cationic polymer solution to form a binder liuquid.
  • a binder liquid may advantageously be employed for the production of paper or non-woven fabric based on natural pulp.
  • the binder liquid preferably contains liquid aggregate of the anionic polymer and the cationic polymer.
  • the binder liquid preferably contains no liquid aggregate and has a pH value of not higher than 7.
  • the polymers can be deposited onto the fiber or pulp almost completely without employing a fixing- agent.
  • These preferred liquids can be obtained by controlling conditions such as the concentrations and temperatures of the polymer solutions and the stirring conditions upon mixing of the solutions, which conditions may vary depending upon the nature of the polymers.
  • a 1% aqueous solution of a sodium carboxylate-modified polyvinyl alcohol ("Gosenal T-330", manufactured by Japan Synthetic Chemicals Corp.; polymerization degree, 1800; molar fraction of sodium carboxylate, not more than 2%) is employed as the aqueous anionic polymer solution
  • a 15% aqueous solution of PPE (“Polyfix 105”, manufactured by Showa High Polymer Co. Ltd.) is employed as the aqueous cationic polymer solution, and both solutions are mixed at a temperature of 15°C while being stirred, the preferred amount of PPE being 0.01 to 0.1 l per A of the modified polyvinyl alcohol solution.
  • the binder liquid has a pH value of not more than 7. Since the fiber or pulp usually has a negative s-potential, the polymers can easily be fixed onto the fiber or pulp if the cationic polymer exists in an excessive amount. Also, in this case, it'will be appreciated that the binder liquid should preferably have a pH value of not less than 7 in the case where the fiber or pulp has a positive ç-potential.
  • wood fibers such as groundwood pulp, kraft pulp, semi-chemical pulp, sulfite pulp, and soda pulp
  • vegetable fibers such as cotton, Manila hemp, jute, paper mulberry, mitsumata, and gampi
  • synthetic fibers or synthetic pulps of polyester polyacrylonitrile, polyolefins, polyvinyl chloride, polyamides and polyvinyl alcohol
  • regenerated cellulose fibers such as viscose rayon and acetate fiber
  • inorganic fibers such as glass fiber, asbestos fiber and ceramic fiber, and mixtures of two or more thereof.
  • the slurry of fiber or pulp having the binder slurry or liquid mixed therewith is converted into paper or non-woven fabric by a conventional wet papermaking technique and the paper or non-woven fabric is then dried in a usual manner.
  • the paper or non-woven fabric thus obtained generally has a fairly high strength and water resistance.
  • known reactions concerning cellulose, polyvinyl alcohol, starch, acrylic or methacrylic acid polymers, polyesters, and the like can be utilized.
  • cellulose may be converted into an acetal or subjected to cyanoethylation or may be cross-linked by means of dimethylolethylene urea, dimethylol urea, or epichlorohydrin.
  • Polyvinyl alcohol may be converted into an acetal or formal or may be subjected to esterification, etherification, or cross-linking by an aldehyde, an N--methylol compound, a dicarboxylic acid, a dicarboxylic acid chloride, a bis-halogen compound, a bis-epoxide, a bis-aziridine, epichlorohydrin, ethylene glycol diglycidyl ether, or the like.
  • Acrylic or methacrylic acid polymers may be cross-linked by an oxide of a divalent or polyvalent metal or an organic acid salt or by a diamine, diol, or bis-epoxide.
  • The-insolubilizing treatment or cross-linking treatment may be carried out at a separate stage with respect to the paper or non-woven fabric obtained by a wet papermaking technique.
  • a cationic polymer being reactive to the anionic polymer may be employed as the cationic polymer to be mixed with the anionic polymer to also act as an insolubilizing agent or cross-linking agent.
  • a cationic polymer there may preferably be employed a cationic polymer having on at least a part of the ends or side chains thereof one or more reactive groups such as epoxy, N-methylol, or isocyanate.
  • Typical examples of the polymer may include cationically modified urea-formaldehyde resin, PPE, and polyamide-polyamine-polyester-polyether epichlorohydrin.
  • the cationic polymers may be appropriately selected depending upon the reacivity thereof regarding the employed anionic polymer. However, the combination of an anionic polymer selected from the hereinbefore-mentioned carboxy-modified polyvinyl alcohol and water-soluble polyester and a cationic polymer selected from the hereinbefore-mentioned cationically modified melamine-formaldehyde resin and PPE is particularly preferred as being able to produce paper or non-woven fabric having an excellent strength, water resistance, and hot-water resistance.
  • Japanese Unexamined Patent Publication No. 55-62298 there is described the production of paper or non-woven fabric having an excellent hot-water resistance by using of polyvinyl alcohol and polyamide-l-halogen-2,3-epoxy resin.
  • this reference does not describe any liquid containing carboxy-modified polyvinyl alcohol and polyamide--l-halogen-2,3-epoxy resin or the incorporation of such a liquid into a fiber or pulp slurry.
  • a melamine-acidified colloidal solution may be added to the fiber or pulp slurry or to the binder slurry or liquid for insolubilizing or cross-linking of the anionic polymer.
  • the melamine-acidified colloidal solution may be fixed onto the fiber or pulp or onto the anionic polymer to cross-link and insolubilize the anionic polymer.
  • the present invention there can stably be obtained paper or non-woven fabric excellent in strength, water resistance, and thermal resistance by a simple operation, and, thus, the present invention may broadly be applied to the production of paper or non--woven fabric using wood fibers, vegetable fibers, animal fibers, semi-synthetic fibers, synthetic fibers, and inorganic fibers.
  • a sample was immersed for 30 minutes in water having a temperature of 20°C and thereafter the above-mentioned measurement for standard strength was carried out.
  • polyester fibers (“TM04", manufactured by Teijin Ltd.; fineness, 1.5 deniers; length, 5 mm) was dispersed in 2l of water to form a fiber slurry.
  • a total of 40 cc of the above-mentioned binder slurry was added to the fiber slurry, and then 200 cc of a 0.01% aqueous solution of an anionic polyacrylamide ("Meipam", manufactured by Meisei Chemical Works Co. Ltd.) was added as a thickner.
  • the slurry was then formed into a wet sheet on a laboratory papermaking machine, and the sheet was dried on a drum dryer at 120°C to form a paper of 25 cm x 25 cm.
  • the paper was immersed in a 1% to 4% aqueous solution of trimethylolmelamine ("Sumitex Resin M-3", manufactured by Sumitomo Chemical Co. Ltd.) containing "Sumitex Accelerator AC” (manufactured by Sumitomo Chemical Co. Ltd.) as a catalyst in an amount equal to 1/10 of the amount of the trimethylolmelamine. Then the paper was dried and cured.
  • trimethylolmelamine "Sumitex Resin M-3", manufactured by Sumitomo Chemical Co. Ltd.) containing "Sumitex Accelerator AC” (manufactured by Sumitomo Chemical Co. Ltd.) as a catalyst in an amount equal to 1/10 of the amount of the trimethylolmelamine.
  • the physical properties of the obtained paper are shown in Table 1 below.
  • the paper had a strength sufficient to form a paper layer after sheet formation and drying but the strength was not sufficient enough for the paper to be practically used.
  • the paper had a high standard strength and a high wet strength.
  • 150 cc of an aqueous solution (having the concentration shown in Table 2) of PPE ("Polyfix 105", manufactured by Showa High Polymer Co. Ltd.) was gradually added to 150 cc of a 0.267% aqueous solution of a copolyester (having the composition shown in Table 2) while being stirred. The mixture was stirred for 10 minutes more to prepare a binder liquid or slurry. Where the concentration of PPE was low, a white turbid liquid was formed. Where the concentration of PPE was high, solid particles started to form. The higher the concentration of PPE was, the larger the particle size was, so that particles of a size of 50 to 100 ⁇ m were formed at an appropriate concentration. Where the concentration of PPE was too high, solid particles of too large a size formed , and where the concentration was further increased, solid particles were not formed.
  • 300 cc of the thus obtained liquid or slurry was added to 2 £ of a slurry of polyester fibers (polyethylene terephthalate staple fibers having a fineness of 0.5 deniers and a length of 5 mm) having a concentration of 1 g/£ and then 200 cc of a 0.01% aqueous solution of an anionic polyacrylamide ("Meipam", manufactured by Meisei Chemical Works Co. Ltd.) was added as a thickner.
  • the fiber slurry was then formed into a wet sheet on a laboratory papermaking machine, and the sheet was dried at 120°C and heat treated at 160°C for 5 minutes to obtain a paper having a weight of 40 g/m .
  • Polyester fibers as used in Example 1 or polyvinyl alcohol fibers ("UPB 103", manufactured by Kuraray Co.; fineness, 1 denier; length, 5 mm) were slurried as described in Example 1, and to 2 t of the fiber slurry 200 cc of the above-mentioned binder slurry was added.
  • the mixed slurry was slowly stirred for about 10 minutes and then 200 cc of an aqueous solution of an anionic polyacrylamide ("Meipam”, manufactured by Meisei Chemical Works Co. Ltd.) having a concentration of 2 g/l was added as a thickner.
  • the slurry was formed into a wet sheet and dried as described in Example 1.
  • the resultant fabric had a weight of 40 gfm 2 .
  • the slurry had a pH value of 8.1 before papermaking was carried out.
  • the resultant non-woven fabric was then heat treated at 180°C for 5 minutes.
  • the strength of the fabric is shown in Table 3 below.
  • Unbleached kraft pulp having a concentration of 2% was beaten on a disc refiner (manufactured by Kumagai Machinery Co.) to obtain a pulp of 0.15% having a freeness number of 400 cc.
  • a disc refiner manufactured by Kumagai Machinery Co.
  • the stock was then formed into a wet sheet on a laboratory papermaking machine, and the sheet was dried on a cylinder dryer at 120°C to obtain a paper having a weight of 50 gjm 2 .
  • the wet strength of the paper increased as the amount of PPE was increased and, in particular, the paper sheets of Run Nos. 4, 5, and 6 where the binder liquid was white turbid were excellent in both standard strength and wet strength.
  • 150 cc of a 2% (solid) aqueous solution of PPE (“Polyfix 105", manufactured by Showa High Polymer Co. Ltd.) was gradually added to 150 cc of a 2% aqueous solution of carboxymethylcellulose ("Cellogen WS-C", manufactured by Daiichi Kogyo Seiyaku Co. Ltd.) while being stirred.
  • the obtained liquid was cloudy and contained liquid aggregate.
  • Example 2 30 cc of the liquid was added to 2 t of a polyester fiber slurry (2 g/2 l) as used in Example 1. The slurry was then formed into a wet sheet on a laboratory hand papermaking device and the sheet was dried. The weight of the obtained paper was 40 g/m 2 , and the standard strength and wet strength were 2.5 kg/15 mm and 1.5 kg/15 mm, respectively.

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  • Chemical Kinetics & Catalysis (AREA)
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EP19820106937 1982-07-31 1982-07-31 Procédé de production de papier ou de tissu non-tissé Withdrawn EP0100370A1 (fr)

Priority Applications (1)

Application Number Priority Date Filing Date Title
EP19820106937 EP0100370A1 (fr) 1982-07-31 1982-07-31 Procédé de production de papier ou de tissu non-tissé

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Application Number Priority Date Filing Date Title
EP19820106937 EP0100370A1 (fr) 1982-07-31 1982-07-31 Procédé de production de papier ou de tissu non-tissé

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EP0100370A1 true EP0100370A1 (fr) 1984-02-15

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Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4925530A (en) * 1985-12-21 1990-05-15 The Wiggins Teape Group Limited Loaded paper
US6828014B2 (en) 2001-03-22 2004-12-07 Kimberly-Clark Worldwide, Inc. Water-dispersible, cationic polymers, a method of making same and items using same
US6897168B2 (en) 2001-03-22 2005-05-24 Kimberly-Clark Worldwide, Inc. Water-dispersible, cationic polymers, a method of making same and items using same
US6908966B2 (en) 2001-03-22 2005-06-21 Kimberly-Clark Worldwide, Inc. Water-dispersible, cationic polymers, a method of making same and items using same
US7070854B2 (en) 2001-03-22 2006-07-04 Kimberly-Clark Worldwide, Inc. Water-dispersible, cationic polymers, a method of making same and items using same

Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
NL6402888A (fr) * 1964-03-18 1965-09-20
UST881008I4 (en) * 1970-05-13 1970-12-01 Defensive publication
FR2041667A5 (fr) * 1969-05-30 1971-01-29 Protex
US3677888A (en) * 1966-04-29 1972-07-18 American Cyanamid Co Manufacture of paper using amphoteric strengthening agents
US3902958A (en) * 1974-01-30 1975-09-02 Nalco Chemical Co Method of making improved paper and paper products
US4210489A (en) * 1978-06-21 1980-07-01 W. R. Grace & Co. Method of imparting wet strength to paper products
US4218286A (en) * 1976-06-25 1980-08-19 C. H. Dexter Limited Paper having good absorbency and alkali resistance and method of making said paper
FR2459817A1 (fr) * 1979-06-27 1981-01-16 Du Pont Produits d'interaction alcool polyvinylique/resine melamine-formaldehyde
WO1982001020A1 (fr) * 1980-09-19 1982-04-01 O Sunden Procede de fabrication du papier utilisant une structure muqueuse amphotere comme liant

Patent Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
NL6402888A (fr) * 1964-03-18 1965-09-20
US3677888A (en) * 1966-04-29 1972-07-18 American Cyanamid Co Manufacture of paper using amphoteric strengthening agents
FR2041667A5 (fr) * 1969-05-30 1971-01-29 Protex
UST881008I4 (en) * 1970-05-13 1970-12-01 Defensive publication
US3902958A (en) * 1974-01-30 1975-09-02 Nalco Chemical Co Method of making improved paper and paper products
US4218286A (en) * 1976-06-25 1980-08-19 C. H. Dexter Limited Paper having good absorbency and alkali resistance and method of making said paper
US4210489A (en) * 1978-06-21 1980-07-01 W. R. Grace & Co. Method of imparting wet strength to paper products
FR2459817A1 (fr) * 1979-06-27 1981-01-16 Du Pont Produits d'interaction alcool polyvinylique/resine melamine-formaldehyde
WO1982001020A1 (fr) * 1980-09-19 1982-04-01 O Sunden Procede de fabrication du papier utilisant une structure muqueuse amphotere comme liant

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4925530A (en) * 1985-12-21 1990-05-15 The Wiggins Teape Group Limited Loaded paper
US6828014B2 (en) 2001-03-22 2004-12-07 Kimberly-Clark Worldwide, Inc. Water-dispersible, cationic polymers, a method of making same and items using same
US6897168B2 (en) 2001-03-22 2005-05-24 Kimberly-Clark Worldwide, Inc. Water-dispersible, cationic polymers, a method of making same and items using same
US6908966B2 (en) 2001-03-22 2005-06-21 Kimberly-Clark Worldwide, Inc. Water-dispersible, cationic polymers, a method of making same and items using same
US7070854B2 (en) 2001-03-22 2006-07-04 Kimberly-Clark Worldwide, Inc. Water-dispersible, cationic polymers, a method of making same and items using same

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