US20040149412A1 - Polymer and use thereof in the production of paper and board - Google Patents

Polymer and use thereof in the production of paper and board Download PDF

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Publication number
US20040149412A1
US20040149412A1 US10/478,138 US47813803A US2004149412A1 US 20040149412 A1 US20040149412 A1 US 20040149412A1 US 47813803 A US47813803 A US 47813803A US 2004149412 A1 US2004149412 A1 US 2004149412A1
Authority
US
United States
Prior art keywords
paper
strength
cationic
starch
web
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.)
Abandoned
Application number
US10/478,138
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English (en)
Inventor
Anna-Liisa Tammi
Kari Nurmi
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 Performance Products LLC
Original Assignee
Raisio Chemicals Oy
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 Raisio Chemicals Oy filed Critical Raisio Chemicals Oy
Assigned to RAISIO CHEMICALS LTD. reassignment RAISIO CHEMICALS LTD. ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: NURMI, KARI, TAMMI, ANNA-LIISA
Publication of US20040149412A1 publication Critical patent/US20040149412A1/en
Assigned to CIBA SPECIALTY CHEMICALS OY reassignment CIBA SPECIALTY CHEMICALS OY CHANGE OF NAME (SEE DOCUMENT FOR DETAILS). Assignors: RAISIO CHEMICALS OY AND RAISIO CHEMICALS LTD.
Assigned to CIBA SPECIALTY CHEMICALS OY reassignment CIBA SPECIALTY CHEMICALS OY CHANGE OF NAME (SEE DOCUMENT FOR DETAILS). Assignors: RAISIO CHEMICALS LTD., RAISIO CHEMICALS OY
Assigned to CIBA SPECIALTY CHEMICALS CORP. reassignment CIBA SPECIALTY CHEMICALS CORP. ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: CIBA SPECIALTY CHEMICALS OY
Assigned to CIBA SPECIALTY CHEMICALS CORP. reassignment CIBA SPECIALTY CHEMICALS CORP. CORRECTIVE ASSIGNMENT TO CORRECT THE COVER PAGE AND PAGES 1,2 & 3 OF NOTICE OF RECORDATION OF ASSIGNMENT DOCUMENT, DATED 2-1-06. THE ASSIGNEE'S NAME WAS MISSPELLED AND THE HIGHLIGHTED APPLICATION NOS. AND PATENT NOS. WERE LISTED INCORRECTLY BY THE CLERK OF THE PATENT OFFICE. THE ASSIGNMENT WAS RECORDED ON REEL 017105 FRAME 0005. Assignors: CIBA SPECIALTY CHEMICALS OY
Abandoned legal-status Critical Current

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Classifications

    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21HPULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
    • D21H17/00Non-fibrous material added to the pulp, characterised by its constitution; Paper-impregnating material characterised by its constitution
    • D21H17/20Macromolecular organic compounds
    • D21H17/21Macromolecular organic compounds of natural origin; Derivatives thereof
    • D21H17/24Polysaccharides
    • D21H17/28Starch
    • D21H17/29Starch cationic

Definitions

  • the invention relates to the chemistry of additives for paper making.
  • the invention relates to a polymer stabilized with a polysaccharide and being generally used as an additive in the production of paper.
  • Various paper making additives are used to improve the properties of paper.
  • Water soluble additives such as polyamides, polyamide-epichlorohydrin resins, melamin resins, urea-formaldehyde resins, polyacrylamides as well as preferably starch together with its derivatives are used to improve the strength properties.
  • Starch is an advantageous and preferred raw material of natural origin. The amount of starch required to improve the strength properties is relatively large.
  • starch As wood fiber is anionic in character, native starch has a quite low affinity thereto. Therefore, starch has been chemically modified into the cationic direction. Starch is cationized by attaching substituents having an ionic nitrogen group, such as primary, secondary, tertiary or quaternary ammonium groups, to the carbohydrate backbone. As a measure of the cationic character, the relative ratio of substituted to unsubstituted glucose units, i.e. a degree of substitution, is used. The cationic character can also be expressed as a percentage amount of ionic nitrogen based on the weight of the substituted starch.
  • substituents having an ionic nitrogen group such as primary, secondary, tertiary or quaternary ammonium groups
  • the dry strength properties of paper are usually improved by adding hydrogen bonds to OH groups of the fiber.
  • the paper strengthening additives of this kind include hydrophilic, water-soluble polymers such as starch, carboxymethylcellulose or synthetic polymers. These include polyacrylamides of which anionic, cationic and amphoteric are used. Their use is limited by a relative high price.
  • wet strength is usually meant the strength of a finished paper when it becomes wet, which strength is obtained by the formation of covalent bonds between the fibers. This property is of importance when making paper e.g. for filter paper or kitchen paper, and it can be be obtained through reactions between fibers and additives at a high temperature of the drying section of a paper machine.
  • Another wet strength the strength of a wet web during the production of paper is of great importance for the runnability of the machine, especially when proceeding to a drying section, because the web has been fully supported up to that point. It has been tried to improve this property mainly by increasing the dry solids content of the web in the press section.
  • starch In order to combine the properties of polyacrylamides and starches to improve the wet strength of paper, products have been prepared in which acrylamide or metacrylamide and an unsaturated organic acid are polymerized in the presence of starch. In this manner starch is formed to which polymerized side chains have been bound.
  • the starch is preferably cationic, having typically a degree of substitution of 0.01-0.70.
  • Japanese patent application JP 2-26944 discloses a polymer of an acrylamide or metacrylamide and methacrylamide acid, prepared in an aqueous solution containing a cationic polysaccharide.
  • a product is prepared by polymnerizing 50-95 mol-% of (meth)acrylamide and 5-50 mol-% of an ⁇ , ⁇ -unsaturated carboxylic acid in an aqueous solution containing 40-90 parts per weight of a cationic polysaccharide.
  • a vinylic component to be polymerized is entirely in the form of amide, and after the polymerization, part of the amide groups is hydrolyzed to carboxylic groups.
  • the number of the formed side chains of the starch is large in relation to the number of the cationic groups, because low cationic starch was used.
  • additives are used in the production of paper to improve the complex of fiber and a binder.
  • the runnability of paper in a machine can be improved by web wet strength improving agents.
  • the present invention relates particularly to the wet strength of a web, i.e. to the strength of a paper or paperboard web during the production with a dry solids content of about 20-60%.
  • copolymer stabilized by a cationic polysaccharide to be an advantageous additive in the production of paper and paperboard, in which copolymer acrylamide or metacrylamide, vinylic carboxylic acid and optionally other vinylic monomers, e.g. alkylaminoacrylate or metacrylate, are used as monomers.
  • a polysaccharide having a strong cationic character is used, which in an aqueous solution is ready for use, and no time-consuming cooking is needed.
  • the degree of substitution of the cationic polysaccharide is about 0.02-0.50.
  • the polysaccharide used is preferably degraded starch.
  • the starch may be any known starch, e.g. potato, corn, waxy maize, barley, wheat or tapioca starch.
  • other useful polysaccharides are e.g. dextrine, amylopectin, amylose and mannose.
  • vinylic monomers are used in the product according to this invention.
  • the proportion of the monomers calculated on the dry solids content of the starting materials is not more than about 30%, preferably below 20%.
  • at least about 95% of the molar amount of the monomer component is amide.
  • polymerization initiators and pH adjusting agents are used as known in the art.
  • Suitable initiators are e.g. cerium salts, persulfates, hydroperoxides alone or together with a reducing metal salt, or azo compounds.
  • the cationic starch has a degree of substitution of 0.20; the cationization has been carried out by using a quaternary ammonium compound.
  • the cationic starch and water are mixed together in a reactor.
  • the pH of the solution is adjusted to 7 by using acetic acid, and 20% of both the tert-butyl hydroperoxide and the sodium metabisulfite aqueous solutions are added.
  • the temperature is raised to 60° C., and a nitrogen atmosphere is arranged in the reactor for the duration of the reaction.
  • the reaction is continued for 120 minutes at 60° C. under agitation.
  • the reaction can be initiated by various initiators, as in the above example by an oxidation-reduction-reagent pair, which includes i.a. a copper sulfate-hydrogen peroxide-pair, or e.g. by a cerium salt.
  • the catalyst may also be a persulfate or another catalyst commonly used in emulsion polymerization.
  • a paper strip was drawn by a measuring device at constant speed (50 mm/min) and the tensile force required to cause fracturing of the paper was registered.
  • test product according to the invention improves the wet tensile strength of the sheets while the cationic starch alone does not.
  • Laboratory sheets are prepared from a pulp consisting of 80% mechanical pulp and 20% chemical pulp. The additions of the additives are given in kg/t.
  • the tested sheets were prepared using a fiber orientating sheeting mould in which the machine direction (MD) and the cross direction (CD) can be distinguished.
  • MD machine direction
  • CD cross direction
  • Example 1
  • the product according to the invention significantly improves the wet web strength both in the machine direction and in the cross direction.
  • Laboratory sheets are prepared from a pulp consisting of 15% chemical pulp, 20% reject and 55% mechanical pulp, and as filler kaolin, so that the ash level will be 20%.
  • the additions of the additives are given in kg/t of the dry solids of the pulp.
  • the sheets were prepared to a basis weight of 70 g/m 2 .
  • the IGT surface resistance was measured on these sheets, and a slight improvement could also be observed compared to the zero point as well as to the use of the pulp starch alone.
  • the IGT picking indicates how the surface of a paper, which has been printed with a printing ink, is able to resist abrasion before the surface becomes flocked and the fibers can be seen on the surface.
  • a product according to the invention may be used in paper and cardboard production, for example for stabilizing hydrophobic size dispersions.
  • sizes are e.g. AKD (alkyl ketene dimer) and ASA (alkenyl succinic anhydride).
  • AKD alkyl ketene dimer
  • ASA alkenyl succinic anhydride

Landscapes

  • Paper (AREA)
  • Polysaccharides And Polysaccharide Derivatives (AREA)
  • Extrusion Of Metal (AREA)
  • Graft Or Block Polymers (AREA)
US10/478,138 2001-05-23 2002-05-20 Polymer and use thereof in the production of paper and board Abandoned US20040149412A1 (en)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
FI20011085 2001-05-23
FI20011085A FI113968B (fi) 2001-05-23 2001-05-23 Kationisella polysakkaridilla stabiloitu liuospolymeeri
PCT/FI2002/000428 WO2002095128A1 (fr) 2001-05-23 2002-05-20 Polymere et son utilisation dans la production de papier et de carton

Publications (1)

Publication Number Publication Date
US20040149412A1 true US20040149412A1 (en) 2004-08-05

Family

ID=8561260

Family Applications (1)

Application Number Title Priority Date Filing Date
US10/478,138 Abandoned US20040149412A1 (en) 2001-05-23 2002-05-20 Polymer and use thereof in the production of paper and board

Country Status (9)

Country Link
US (1) US20040149412A1 (fr)
EP (1) EP1392919B1 (fr)
AT (1) ATE459752T1 (fr)
CA (1) CA2448113A1 (fr)
DE (1) DE60235539D1 (fr)
ES (1) ES2340840T3 (fr)
FI (1) FI113968B (fr)
PT (1) PT1392919E (fr)
WO (1) WO2002095128A1 (fr)

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2007078537A1 (fr) 2005-12-15 2007-07-12 Dow Global Technologies Inc. Articles ameliores en cellulose contenant une composition d’additif
US20080076844A1 (en) * 2006-09-22 2008-03-27 The Dow Chemical Company Fibrillated polyolefin foam
US20100255207A1 (en) * 2007-09-28 2010-10-07 Dow Global Technologies Inc. Dispersions of higher crystallinity olefins
US8709555B2 (en) 2011-04-28 2014-04-29 Hewlett-Packard Development Company, L.P. Media used in digital high speed inkjet web press printing
US8916640B2 (en) 2006-07-06 2014-12-23 Dow Global Technologies Llc Blended polyolefin dispersions
WO2017149200A1 (fr) * 2016-03-01 2017-09-08 Kemira Oyj Composition de polymère, son utilisation et produit d'encollage de surface
JP2019065406A (ja) * 2017-09-28 2019-04-25 荒川化学工業株式会社 紙力増強剤及び紙
CN109749012A (zh) * 2019-01-24 2019-05-14 湖北中之天科技股份有限公司 一种环保型无氯聚丙烯酰胺湿强剂的生产方法及在造纸中的应用

Citations (20)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3006806A (en) * 1957-02-15 1961-10-31 Olin Mathieson Sized paper and process therefor
US4376177A (en) * 1979-12-26 1983-03-08 Kao Soap Co., Ltd. Sizing composition
US4381367A (en) * 1980-12-12 1983-04-26 Bayer Aktiengesellschaft Sizing agents for paper and a process for the production thereof
US4470877A (en) * 1981-05-13 1984-09-11 United States Gypsum Company Paper having calcium sulfate mineral filler for use in the production of gypsum wallboard
US4684708A (en) * 1985-03-11 1987-08-04 Akzo N.V. Cationic grafted starch copolymers
US4835212A (en) * 1987-01-30 1989-05-30 Basf Aktiengesellschaft Sizing agents for paper based on finely divided aqueous dispersions
US4866151A (en) * 1987-03-25 1989-09-12 National Starch And Chemical Corporation Polysaccharide graft polymers containing acetal groups and their conversion to aldehyde groups
US4954220A (en) * 1988-09-16 1990-09-04 E. I. Du Pont De Nemours And Company Polysilicate microgels as retention/drainage aids in papermaking
US4960876A (en) * 1987-12-29 1990-10-02 Fratelli Lamberti S.P.A. Modified galactomannans and process for their preparation
US5049634A (en) * 1989-09-22 1991-09-17 National Starch And Chemical Investment Holding Corporation Derivatized and/or crosslinked products from acetal- and aldehyde-containing polysaccharide graft polymers
US5122231A (en) * 1990-06-08 1992-06-16 Cargill, Incorporated Cationic cross-linked starch for wet-end use in papermaking
US5338406A (en) * 1988-10-03 1994-08-16 Hercules Incorporated Dry strength additive for paper
US5578678A (en) * 1991-08-22 1996-11-26 Basf Aktiengesellschaft Graft polymers of natural substances containing saccharide structures or derivatives thereof and ethylenically unsaturated compounds and their use
US5695609A (en) * 1992-01-20 1997-12-09 Kemira Oy Process for producing paper
US6034181A (en) * 1995-08-25 2000-03-07 Cytec Technology Corp. Paper or board treating composition of carboxylated surface size and polyacrylamide
US6048929A (en) * 1997-10-30 2000-04-11 E. I. Du Pont De Nemours And Company Modified starch composition for removing particles from aqueous dispersions
US6159339A (en) * 1996-03-21 2000-12-12 Betzdearborn Inc. Paper size and paper sizing process
US20010003760A1 (en) * 1998-07-10 2001-06-14 Raisio Chemicals Ltd. Additive composition for paper making
US6290765B1 (en) * 1996-11-30 2001-09-18 Raisio Chemicals Limited Uk Rosin emulsion including starch derivative for paper sizing
US6451170B1 (en) * 2000-08-10 2002-09-17 Cargill, Incorporated Starch compositions and methods for use in papermaking

Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2622965B2 (ja) * 1987-03-02 1997-06-25 星光化学工業株式会社 製紙用添加剤
JP2620806B2 (ja) * 1988-07-11 1997-06-18 星光化学工業株式会社 製紙用添加剤と製紙方法
JP2928785B2 (ja) * 1993-10-08 1999-08-03 星光化学工業株式会社 製紙用添加剤
JP3876522B2 (ja) * 1998-02-20 2007-01-31 星光Pmc株式会社 製紙用紙力増強剤及び強力紙の製造法

Patent Citations (20)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3006806A (en) * 1957-02-15 1961-10-31 Olin Mathieson Sized paper and process therefor
US4376177A (en) * 1979-12-26 1983-03-08 Kao Soap Co., Ltd. Sizing composition
US4381367A (en) * 1980-12-12 1983-04-26 Bayer Aktiengesellschaft Sizing agents for paper and a process for the production thereof
US4470877A (en) * 1981-05-13 1984-09-11 United States Gypsum Company Paper having calcium sulfate mineral filler for use in the production of gypsum wallboard
US4684708A (en) * 1985-03-11 1987-08-04 Akzo N.V. Cationic grafted starch copolymers
US4835212A (en) * 1987-01-30 1989-05-30 Basf Aktiengesellschaft Sizing agents for paper based on finely divided aqueous dispersions
US4866151A (en) * 1987-03-25 1989-09-12 National Starch And Chemical Corporation Polysaccharide graft polymers containing acetal groups and their conversion to aldehyde groups
US4960876A (en) * 1987-12-29 1990-10-02 Fratelli Lamberti S.P.A. Modified galactomannans and process for their preparation
US4954220A (en) * 1988-09-16 1990-09-04 E. I. Du Pont De Nemours And Company Polysilicate microgels as retention/drainage aids in papermaking
US5338406A (en) * 1988-10-03 1994-08-16 Hercules Incorporated Dry strength additive for paper
US5049634A (en) * 1989-09-22 1991-09-17 National Starch And Chemical Investment Holding Corporation Derivatized and/or crosslinked products from acetal- and aldehyde-containing polysaccharide graft polymers
US5122231A (en) * 1990-06-08 1992-06-16 Cargill, Incorporated Cationic cross-linked starch for wet-end use in papermaking
US5578678A (en) * 1991-08-22 1996-11-26 Basf Aktiengesellschaft Graft polymers of natural substances containing saccharide structures or derivatives thereof and ethylenically unsaturated compounds and their use
US5695609A (en) * 1992-01-20 1997-12-09 Kemira Oy Process for producing paper
US6034181A (en) * 1995-08-25 2000-03-07 Cytec Technology Corp. Paper or board treating composition of carboxylated surface size and polyacrylamide
US6159339A (en) * 1996-03-21 2000-12-12 Betzdearborn Inc. Paper size and paper sizing process
US6290765B1 (en) * 1996-11-30 2001-09-18 Raisio Chemicals Limited Uk Rosin emulsion including starch derivative for paper sizing
US6048929A (en) * 1997-10-30 2000-04-11 E. I. Du Pont De Nemours And Company Modified starch composition for removing particles from aqueous dispersions
US20010003760A1 (en) * 1998-07-10 2001-06-14 Raisio Chemicals Ltd. Additive composition for paper making
US6451170B1 (en) * 2000-08-10 2002-09-17 Cargill, Incorporated Starch compositions and methods for use in papermaking

Cited By (21)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2007078537A1 (fr) 2005-12-15 2007-07-12 Dow Global Technologies Inc. Articles ameliores en cellulose contenant une composition d’additif
US20080295985A1 (en) * 2005-12-15 2008-12-04 Moncla Brad M Cellulose Articles Containing an Additve Composition
US8029646B2 (en) 2005-12-15 2011-10-04 Dow Global Technologies Llc Cellulose articles containing an additive composition
US8177939B2 (en) 2005-12-15 2012-05-15 Dow Global Technologies Llc Cellulose articles containing an additive composition
US8916640B2 (en) 2006-07-06 2014-12-23 Dow Global Technologies Llc Blended polyolefin dispersions
US20080076844A1 (en) * 2006-09-22 2008-03-27 The Dow Chemical Company Fibrillated polyolefin foam
US8476326B2 (en) 2006-09-22 2013-07-02 Dow Global Technologies Llc Fibrillated polyolefin foam
EP2543691A2 (fr) 2007-09-28 2013-01-09 Dow Global Technologies LLC Méthode pour faire un concentré de fibres longues avec dispersion d'oléfine de cristallinité supérieure
US20100255207A1 (en) * 2007-09-28 2010-10-07 Dow Global Technologies Inc. Dispersions of higher crystallinity olefins
EP2543393A2 (fr) 2007-09-28 2013-01-09 Dow Global Technologies LLC Mousse produite à partir d'une dispersion d'oléfines de cristallinité supérieure
EP2543690A2 (fr) 2007-09-28 2013-01-09 Dow Global Technologies LLC Fibre revêtu d'une dispersion d'oléfine de cristallinité supérieure
EP2543763A2 (fr) 2007-09-28 2013-01-09 Dow Global Technologies LLC Structure fibreuse imprégniée avec dispersion d'oléfine de cristallinité supérieure
US8318257B2 (en) 2007-09-28 2012-11-27 Dow Global Technologies Llc Dispersions of higher crystallinity olefins
EP2543764A2 (fr) 2007-09-28 2013-01-09 Dow Global Technologies LLC Article à base de cellulose avec dispersion d'oléfine de cristallinité supérieure
US8709555B2 (en) 2011-04-28 2014-04-29 Hewlett-Packard Development Company, L.P. Media used in digital high speed inkjet web press printing
WO2017149200A1 (fr) * 2016-03-01 2017-09-08 Kemira Oyj Composition de polymère, son utilisation et produit d'encollage de surface
CN108699195A (zh) * 2016-03-01 2018-10-23 凯米罗总公司 聚合物组合物、其用途和表面施胶剂
US11447618B2 (en) 2016-03-01 2022-09-20 Kemira Oyj Polymer composition, its use and a surface size
JP2019065406A (ja) * 2017-09-28 2019-04-25 荒川化学工業株式会社 紙力増強剤及び紙
JP7047310B2 (ja) 2017-09-28 2022-04-05 荒川化学工業株式会社 紙力増強剤及び紙
CN109749012A (zh) * 2019-01-24 2019-05-14 湖北中之天科技股份有限公司 一种环保型无氯聚丙烯酰胺湿强剂的生产方法及在造纸中的应用

Also Published As

Publication number Publication date
EP1392919B1 (fr) 2010-03-03
ATE459752T1 (de) 2010-03-15
WO2002095128A9 (fr) 2003-01-23
FI113968B (fi) 2004-07-15
ES2340840T3 (es) 2010-06-10
EP1392919A1 (fr) 2004-03-03
FI20011085A (fi) 2002-11-24
FI20011085A0 (fi) 2001-05-23
PT1392919E (pt) 2010-03-26
DE60235539D1 (de) 2010-04-15
CA2448113A1 (fr) 2002-11-28
WO2002095128A1 (fr) 2002-11-28

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