EP1799905A1 - Procede de production de papier ou de carton et produit resultant - Google Patents

Procede de production de papier ou de carton et produit resultant

Info

Publication number
EP1799905A1
EP1799905A1 EP05792428A EP05792428A EP1799905A1 EP 1799905 A1 EP1799905 A1 EP 1799905A1 EP 05792428 A EP05792428 A EP 05792428A EP 05792428 A EP05792428 A EP 05792428A EP 1799905 A1 EP1799905 A1 EP 1799905A1
Authority
EP
European Patent Office
Prior art keywords
furnish
polymer
paper
board
added
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
EP05792428A
Other languages
German (de)
English (en)
Other versions
EP1799905B1 (fr
EP1799905A4 (fr
Inventor
Mats Fredlund
Lars WÅGBERG
Hans Hallgren
Hans HÖGLUND
Gunilla Pettersson
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.)
Stora Enso AB
Original Assignee
Stora Enso AB
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=36148578&utm_source=google_patent&utm_medium=platform_link&utm_campaign=public_patent_search&patent=EP1799905(A1) "Global patent litigation dataset” by Darts-ip is licensed under a Creative Commons Attribution 4.0 International License.
Application filed by Stora Enso AB filed Critical Stora Enso AB
Publication of EP1799905A1 publication Critical patent/EP1799905A1/fr
Publication of EP1799905A4 publication Critical patent/EP1799905A4/fr
Application granted granted Critical
Publication of EP1799905B1 publication Critical patent/EP1799905B1/fr
Revoked legal-status Critical Current
Anticipated expiration legal-status Critical

Links

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
    • D21H11/00Pulp or paper, comprising cellulose or lignocellulose fibres of natural origin only
    • D21H11/16Pulp or paper, comprising cellulose or lignocellulose fibres of natural origin only modified by a particular after-treatment
    • D21H11/20Chemically or biochemically modified fibres
    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21CPRODUCTION OF CELLULOSE BY REMOVING NON-CELLULOSE SUBSTANCES FROM CELLULOSE-CONTAINING MATERIALS; REGENERATION OF PULPING LIQUORS; APPARATUS THEREFOR
    • D21C9/00After-treatment of cellulose pulp, e.g. of wood pulp, or cotton linters ; Treatment of dilute or dewatered pulp or process improvement taking place after obtaining the raw cellulosic material and not provided for elsewhere
    • D21C9/001Modification of pulp properties
    • D21C9/002Modification of pulp properties by chemical means; preparation of dewatered pulp, e.g. in sheet or bulk form, containing special additives
    • 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
    • D21H17/25Cellulose
    • D21H17/26Ethers thereof
    • 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
    • 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
    • D21H23/00Processes or apparatus for adding material to the pulp or to the paper
    • D21H23/02Processes or apparatus for adding material to the pulp or to the paper characterised by the manner in which substances are added
    • D21H23/04Addition to the pulp; After-treatment of added substances in the pulp

Definitions

  • the present invention relates to a process for producing a paper or board product wherein the furnish used is partially treated with polymers in steps.
  • Paper and board products having high bulk require a smaller amount of fibers, which is desirable especially for economical reasons.
  • Bulky board products with low fiber content have better bending stiffness.
  • Paper and board products are typically produced by dewatering furnish on a wire. The furnish often contains a mixture of different pulps, including both chemical pulps and mechanical pulps. In order to produce a bulkier sheet with higher structural stiffness the interest in using mechanical pulps with high freeness has increased. To obtain the best result the mechanical pulp should contain long, intact fibers and as little fine material as possible. However, pulps that are rich in stiff, long fibers unfortunately show poor ability to produce sufficient fiber bonding of the paper or board. The bulk and strength properties of the resulting paper or board will therefore be a compromise between the ability of the pulp to increase the bulk and its ability to increase the fiber bonding properties of the paper or board.
  • the fiber bonding properties of mechanical pulp may also be improved by treatment with chemical additives.
  • the predominant treatment for improving strength, particularly dry strength, of paper or board has so far been to add cationic starch to the pulp fiber slurry prior to the sheet forming operation. It is however difficult to adsorb large amounts of starch to the fibers, especially when the fines amount is small.
  • the cationic starch molecules added to the pulp slurries can adhere to the naturally anionic pulp fibers by electrostatic attraction and thus be retained in the wet fiber mat and remain in the final paper or board.
  • the first is that the cationic starch molecules can overwhelm the anionic charge on the cellulose fibers, thus setting a limit on the amount of cationic starch which can be added to the slurry. If an excess of cationic starch is added, only a portion of the starch which is added will be retained in the sheet and the rest will circulate in the paper or board machine white water system.
  • a second problems is that fibers which have been made cationic by excessive cationic starch addition, will not be able to adsorb other cationic additives which are commonly added the to the pulp slurry, such as sizing agents.
  • Another method to enhance the strength properties of paper is to treat the fibers with polymers.
  • Such a method is described in WO 0032702 Al, in which particles, such as fibers, are provided with a multilayer coating of interacting polymers. The particles are treated in consecutive steps with solutions of the interacting polymers. Before each subsequent treatment step unabsorbed excess of the polymer of the previous step must be removed, unless the polymer amount added in each step is carefully controlled, such that substantially all polymer is absorbed to the particle surface and no excess remains.
  • the object of the invention is to provide a method of producing paper or board, which has an improved strength, without adversely affecting the bulk.
  • the present invention concerns a process for producing a paper or board product, which process comprises providing a furnish comprising fibers; subjecting a first portion (1) of the furnish to polymer treatment, in which polymers are added to the furnish in at least two steps; blending said polymer treated first portion with an untreated second portion (2) of the furnish; and dewatering the furnish on a wire to form a fiber web.
  • Said first furnish portion preferably comprises 20-80% by weight of the total furnish weight.
  • said first furnish portion comprises the longest fibers present in the furnish.
  • the polymer treatment is preferably performed on a first furnish portion which comprises sulphate or sulfite pulp from soft wood fibers.
  • the furnish may comprise fillers and optionally other paper making additives, which fillers and additives may be added subsequent to the polymer treatment of said first furnish portion. Alternatively, fillers and additives may instead be added prior to the polymer treatment of said first furnish portion.
  • the polymer used in each of the consecutive polymer treatment steps is preferably interacting with the polymer used in the subsequent step.
  • the polymer treatment preferably includes one step in which cationic polymer is added, and at least one step in which anionic polymer is added.
  • the cationic polymer is preferably cationic starch and the anionic polymer is preferably CMC.
  • the polymer treatment comprises two to seven steps.
  • the polymer treatment preferably comprises three to seven consecutive steps.
  • the invention also relates to a paper or board product produced according to the process of the present invention.
  • Figure 1 is a schematic view of one embodiment of the process of the present invention.
  • Figure 2 is a diagram which shows a comparison of density and strength of paper produced according to the present invention and produced according to the prior art process.
  • the invention relates to a process for producing paper or board from a furnish, of which a portion has been treated with polymers in at least two steps.
  • the invention also relates to a paper or board product produced according to the process of the present invention.
  • the present process for producing a paper or board product comprises providing a furnish comprising fibers; subjecting a first portion (1) of the furnish to polymer treatment, in which polymers are added to the furnish in at least two steps; blending said polymer treated first portion with an untreated second portion (2) of the furnish; and dewatering the furnish on a wire to form a fiber web.
  • Said first furnish portion comprises 20-80% by weight of the total furnish weight, preferably 20- 50% of the total furnish weight. The percentage of the first portion is adjusted in order to achieve the desired strength and density of the product while keeping the amount of polymers added as low as possible.
  • the appropriate amount of the first portion also depends on the properties of the furnish of the first portion as well as of the second portion.
  • the furnish typically contains a mixture of different kinds of pulp, for example chemical pulp (hardwood pulp, softwood pulp, sulphate pulp or sulfite pulp) or mechanical pulp (CTMP or TMP).
  • said first furnish portion comprises the longest fibers present in the furnish.
  • the polymer treatment is preferably performed on a first furnish portion which comprises sulphate or sulfite pulp, since these pulps comprise long fibers as compared to other pulps. Treatment of a furnish portion comprising sulphate or sulfite pulp is therefore a convenient way of selecting a long fiber portion of the final blended furnish.
  • first furnish portion which is subjected to polymer treatment can comprise any part of the furnish.
  • the furnish may also comprise fillers and optionally other paper making additives, which fillers and additives may be added subsequent to the polymer treatment of said first furnish portion.
  • fillers and additives may instead be added prior to the polymer treatment of said first furnish portion.
  • Some paper and board qualities contain filler or other additives which improves the surface properties of the paper.
  • the filler particles also affect the strength of the paper in a negative way.
  • One theory is that when a furnish containing filler and additives is treated with polymers according to the invention, filler particles and additives bond stronger to other particles or to the fibers, and consequently a high filler content does not affect the strength of the paper to the same extent.
  • the polymer used in each of the consecutive polymer treatment steps is preferably interacting with the polymer used in the subsequent step, thereby enabling a larger amount of polymers to be attached to the fibers and thus results in increased strength of the final paper or board product.
  • the polymer treatment preferably includes one step in which anionic polymer is added, and at least one step in which cationic polymer is added. By alternating anionic and cationic polymer coatings interacting polymer layers may be obtained.
  • the anionic polymer may be one or more chosen from the group consisting of: carboxy methyl cellulose (CMC), polyvinyl sulphate, anionic galactoglucomannan, anionic starch, polyphosphoric acid, alginate and polymethacrylic acid.
  • the anionic polymer is preferably CMC, since it interact well with cationic polymers as well as it is economically beneficial, due to its low cost.
  • the cationic polymer may be one or more chosen from the group consisting of: cationic starch, polyvinyl amine, chitosan, primary and secondary amines, polyethylene imines, polyvinyl pyrrolidone and modified poly aery 1 amides.
  • the cationic polymer is preferably cationic starch, which is advantageous because it results in a board or paper having enhanced strength properties and is economically beneficial, due to its low price and easy availability.
  • the polymer treatment preferably comprises two to seven consecutive steps.
  • the optimal number of steps depends on what properties of the paper or board that are desired and on the properties of the furnish being treated. The more steps the treatment consists of, the bigger amount polymers are added and thus retained in the paper or board. Often it is a balance between the cost and the desired properties, for example strength of the paper or board. There is usually a limit when it is not longer cost effective to add more polymers seeing to the improvement of the desired properties, for example increase of strength of the paper or board manufactured. It is preferred to add cationic polymer in the first step of the polymer treatment and to add anionic polymer in the subsequent and to continue with alternate addition of cationic and anionic polymers until the desired amount of polymers have been added in a desired number of steps.
  • the furnish need not be washed between the polymer treatment steps. Any unabsorbed excess of polymer added in the preceding step can remain in the furnish and need not be rinsed away. Washing between the polymer treatment steps has not been shown to enhance the properties of the resulting product. It is thus advantageous to subject the first furnish portion to each of the polymer treatment steps without any intermediate washing. Thereby an unnecessary step may be avoided and a faster process will be achieved, having lower water consumption.
  • After each polymer treatment step there should be sufficient time and mixing for the polymer to be absorbed to the fibers of the first furnish portion. A time period of at least 5 seconds between each polymer treatment step is suitable. The optimal time depends on the capacity of the mixing of the equipment.
  • the polymer of each polymer treatment step can be added to the furnish in a pulp vessel, such as a pulp chest, or in-line in a furnish transport pipe, or a combination thereof. Where to add the polymer depends on the equipment available and where it is possible to make the addition practically.
  • a pulp vessel such as a pulp chest
  • in-line in a furnish transport pipe or a combination thereof.
  • the pipe is long enough to allow both thorough blending of polymer and pulp, and to allow enough time between the addition step for the polymer to be absorbed or an in-line mixer can be used to ensure good mixing in the pipe.
  • the amount of polymer to be added varies depending of the properties of the pulp.
  • the amount of cationic starch added in each step is typically between 5-25 kg/ton and the amount of CMC added in each step is typically between 0.25-3 kg/ton.
  • the amount polymers added to the furnish may be controlled by measuring the z ⁇ potential or cationic demand measurement of the pulp. Even if an excess amount of added polymer is not detrimental to the final result, it is of course advantageous to add an amount of polymer that is close to what can be absorbed by the pulp, both for economical and environmental reasons.
  • FIG. 1 is a schematic description of the process according to one embodiment of the invention.
  • furnish for production of paper or board is transferred to pulp chest 1, 2 respectively.
  • the furnish transferred and contained to the first pulp chest 1 is designated the first furnish portion
  • the furnish transferred and contained in the second pulp chest 2 is designated the second furnish portion.
  • the first furnish portion is subjected to polymer treatment in three steps.
  • the second portion of furnish is not subjected to any polymer treatment.
  • a cationic polymer such as cationic starch
  • an anionic polymer is added to the furnish in the first pulp chest 1.
  • the second polymer treatment step 5 is initiated at least 5 seconds after the first polymer addition.
  • the pulp chest is equipped with an agitator, making sure that the furnish is sufficiently blended with the added polymer.
  • the furnish is conducted from pulp chest 1 to a headbox 3.
  • the third polymer treatment step is carried out by the addition of a cationic polymer (e.g. cationic starch) 6 in-line through an in-line mixer 7 in the conducting furnish pipe, which in-line mixer is placed downstream the conducting pipe but upstream the headbox.
  • a cationic polymer e.g. cationic starch
  • the polymer treated first portion of the furnish is blended with the second furnish portion, which is provided from pulp chest 2 at a point between the valve and the headbox.
  • the furnish is then conducted from the headbox onto a wire where it is dewatered and further treated in a manner known in the art in order to produce paper or board.
  • Samples 2, 4 and 6 were subjected as a whole to the polymer treatment in their entirety.
  • Samples 8, 10 and 12 were divided into a first portion, which comprised only sulphate pulp and a second portion, which comprised only CTMP.
  • the first portion of each sample (sulphate pulp) was subjected to polymer treatment, whereas the second portion of each sample (CTMP) remained untreated.
  • the first and second portions were then blended with each other.
  • Samples 1, 3, 5, 7, 9, and 11 were not subjected to any polymer treatment.
  • Sheets were then prepared by dewatering the furnish and density (STFI density) and Scott-Bond were determined for all sheets. Scott-Bond is a measure of the strength in the z-direction of the sheet. The results are shown in Table I and in the diagram in Figure 2.
  • Table I shows the increase of Scott-Bond and density in percent comparing the untreated sample with the sample that has been treated with polymers in three steps.
  • the density has increased with 14% and the Scott-Bond value with 58%.
  • the density has only increased with 3,5% and the strength with 45%. Consequently, even though only 20% of the furnish is treated with polymers, the Scott-Bond value still has increased with 45%, compared to 58% when the whole furnish has been treated, and the bulk has only increased with 3,5%, compared to 14%. .
  • Figure 2 shows the Scott-Bond values of sheets made from the furnish samples. Lines have been drawn between the value for each untreated sample and its equivalent corresponding polymer-treated sample. Solid lines in the diagram depict samples where the entire furnish was subjected to polymer treatment. Dashed lines depict samples where only the sulphate portion of the furnish was subjected to polymer treatment. A steeper inclination of the lines indicates a higher strength increase at a lower density increase.
  • the dashed lines have a steeper inclination than the solid lines. Subjecting only the sulphate portion of the furnish to polymer treatment thus results in a substantial strength increase while the density remains almost constant. As shown with solid lines, when the entire furnish is subjected to polymer treatment the increase in strength is greater than that observed after partial treatment, however the density of the sheets formed with the entirely treated furnish also increases to a larger extent than observed after partial treatment.
  • a board consisting of three layers was manufactured.
  • the furnish forming the top and bottom layers of the board consisted of 50% hardwood pulp and 50% softwood pulp with a SR number of approximately 27.
  • the furnish forming the center ply of the board consisted of 55% CTMP and 45% of a mixture, hereinafter referred to as mixture portion, which mixture portion consisted of approximately 55% bleached softwood pulp, 15 % bleached hardwood pulp and 30% CTMP.
  • a board consisting of CTMP and said mixture portion in the center ply represents a typical liquid packaging board.
  • the amount of polymer added in each step was determined by measuring the z- potential. First, small additions of cationic starch were added and the z-potential was continuously measured, when the z-potential was stabilized it indicated that it would be a suitable addition amount. Thereafter, anionic CMC was added in the same way, and when the z-potential was close to zero it indicated that that addition amount would be suitable. The amount of polymers added in the following step was determined in the same way. No wash of the furnish were performed between the polymer additions.
  • Diagram 1 Scott Bond of the board compared to the added amount of starch. It is shown in Diagram 1 that the strength of the board, when only the mixture part of the furnish has been treated with polymers in three steps, is even higher than the board where the entire furnish has been treated with polymers in three steps, even though the amount of starch added is less.
  • Diagram 2 shows the results of the measured Scott-Bond values compared to the density.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Wood Science & Technology (AREA)
  • Biochemistry (AREA)
  • Paper (AREA)
EP05792428A 2004-10-15 2005-10-13 Procede de production de papier ou de carton et produit resultant Revoked EP1799905B1 (fr)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US61937004P 2004-10-15 2004-10-15
PCT/SE2005/001520 WO2006041401A1 (fr) 2004-10-15 2005-10-13 Procede de production de papier ou de carton et produit resultant

Publications (3)

Publication Number Publication Date
EP1799905A1 true EP1799905A1 (fr) 2007-06-27
EP1799905A4 EP1799905A4 (fr) 2010-06-16
EP1799905B1 EP1799905B1 (fr) 2011-12-14

Family

ID=36148578

Family Applications (1)

Application Number Title Priority Date Filing Date
EP05792428A Revoked EP1799905B1 (fr) 2004-10-15 2005-10-13 Procede de production de papier ou de carton et produit resultant

Country Status (12)

Country Link
US (1) US20080023164A1 (fr)
EP (1) EP1799905B1 (fr)
JP (1) JP4976300B2 (fr)
CN (1) CN101040083B (fr)
AT (1) ATE537298T1 (fr)
BR (1) BRPI0516078A (fr)
CA (1) CA2581361A1 (fr)
DK (1) DK1799905T3 (fr)
ES (1) ES2377754T3 (fr)
NZ (1) NZ554090A (fr)
RU (1) RU2367739C2 (fr)
WO (1) WO2006041401A1 (fr)

Families Citing this family (32)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
ES2358529T3 (es) * 2005-05-11 2011-05-11 Stora Enso Ab Procedimiento para la producción de un papel y papel producido según ese procedimiento.
JP2007277795A (ja) * 2006-03-14 2007-10-25 Nippon Paper Industries Co Ltd 抄紙方法および紙
JP2008088582A (ja) * 2006-09-29 2008-04-17 Mitsubishi Paper Mills Ltd 低密度印刷用紙
EP1936032A1 (fr) 2006-12-18 2008-06-25 Akzo Nobel N.V. Procédé de production d'un produit en papier
JP5448853B2 (ja) 2007-03-15 2014-03-19 データレース リミテッド レゾルシニルトリアジン誘導体を主成分とする感熱性コーティング組成物
JP2008248398A (ja) * 2007-03-29 2008-10-16 Nippon Paper Industries Co Ltd 紙の製造方法および紙
KR20100077149A (ko) 2007-08-22 2010-07-07 바스프 에스이 레이저-감응성 코팅 조성물
EP2207933B1 (fr) * 2007-11-07 2014-05-21 DataLase Ltd Nouveaux produits fibreux
WO2010049281A1 (fr) 2008-10-27 2010-05-06 Basf Se Composition aqueuse sensible au laser pour marquer des substrats
PL3617400T3 (pl) 2009-03-30 2023-01-02 Fiberlean Technologies Limited Zastosowanie zawiesin nanofibrylarnej celulozy
SI2236545T1 (sl) 2009-03-30 2014-12-31 Omya International Ag Postopek za proizvodnjo gelov iz nanofibrilirane celuloze
FI121999B (fi) * 2009-10-06 2011-07-15 Upm Kymmene Corp Menetelmä rainan valmistamiseksi ja raina
PT2386682E (pt) 2010-04-27 2014-05-27 Omya Int Ag Processo para fabricar materiais estruturados, usando géis de celulose nanofibrilares
ES2464733T3 (es) 2010-04-27 2014-06-03 Omya International Ag Proceso para la producción de materiales compuestos a base de gel
JP5489914B2 (ja) * 2010-08-19 2014-05-14 花王株式会社 水解紙の製造方法及び水解性清浄物品の製造方法
SE1050985A1 (sv) * 2010-09-22 2012-03-23 Stora Enso Oyj En pappers eller kartongprodukt och en process förtillverkning av en pappers eller en kartongprodukt
US8801899B1 (en) * 2013-09-06 2014-08-12 International Paper Company Paperboards having improved bending stiffness and method for making same
BR112016007763B1 (pt) 2013-09-13 2021-12-07 Stora Enso Oyj Papelão em multicamada
PL3044371T3 (pl) 2013-09-13 2022-01-10 Stora Enso Oyj Tektura wielowarstwowa
WO2015087293A1 (fr) 2013-12-13 2015-06-18 Stora Enso Oyj Carton multicouche
SE539914C2 (sv) 2014-04-29 2018-01-09 Stora Enso Oyj Process för framställning av åtminstone ett skikt hos ett papper eller en kartong samt ett papper eller en kartong som framställts enligt processen
SE539344E (en) 2015-03-02 2020-02-11 Billerudkorsnaes Ab Pulp mixture for production of a paper product with high strength in z-direction
ES2741514T3 (es) 2015-10-14 2020-02-11 Fiberlean Tech Ltd Material laminado conformable en 3D
ES2857512T3 (es) 2016-04-05 2021-09-29 Fiberlean Tech Ltd Productos de papel y cartón
US11846072B2 (en) 2016-04-05 2023-12-19 Fiberlean Technologies Limited Process of making paper and paperboard products
SE540115C2 (en) * 2016-09-21 2018-04-03 A paper or paperboard product comprising at least one ply containing high yield pulp and its production method
WO2018171913A1 (fr) * 2017-03-24 2018-09-27 Tetra Laval Holdings & Finance S.A. Procédé de fabrication d'un matériau fibreux cellulosique moussé, feuille brute et matériau d'emballage stratifié comprenant le matériau fibreux cellulosique
WO2019035022A1 (fr) * 2017-08-16 2019-02-21 Anavo Technologies, Llc Articles en papier de soie et leurs procédés de fabrication et d'utilisation
BE1026476B1 (nl) * 2018-07-17 2020-02-19 Anheuser Busch Inbev Sa Proces voor het produceren van papier of bordpapier, meer specifiek etiketpapier of -bordpapier dat kan worden gebruikt als verpakkingsmateriaal voor drankcontainers
CN111485444B (zh) * 2019-01-29 2021-12-07 金华盛纸业(苏州工业园区)有限公司 改性纸浆制备方法、地图原纸的制备方法及地图原纸
CN111910457B (zh) * 2020-08-03 2023-03-24 湖南广信科技股份有限公司 纸板及其制作方法和应用
DE102021005047A1 (de) * 2021-10-08 2023-04-13 Factum Consult Gmbh Polyelektrolytsystem, Zusammensetzung mit einem Polyelektrolytsystem und Verfahren zur Herstellung

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4210490A (en) * 1976-07-14 1980-07-01 English Clays Lovering Pochin & Company, Limited Method of manufacturing paper or cardboard products
US5185062A (en) * 1991-01-25 1993-02-09 Nalco Chemical Company Papermaking process with improved retention and drainage
EP0790351A2 (fr) * 1996-02-14 1997-08-20 Nalco Chemical Company Procédé de fabrication de papier à l'aide d'un agent de rétention et d'égouttage multipolymère
EP0835957A2 (fr) * 1996-10-11 1998-04-15 Fort James Corporation Procédé de fabrication d'une bande de papier

Family Cites Families (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US139500A (en) * 1873-06-03 Improvement in heel-plates
US3998690A (en) * 1972-10-02 1976-12-21 The Procter & Gamble Company Fibrous assemblies from cationically and anionically charged fibers
SE8306739L (sv) * 1983-12-06 1985-06-07 Svenska Traeforskningsinst Sett att framstella papper med hog fyllmedelshalt
US5061346A (en) * 1988-09-02 1991-10-29 Betz Paperchem, Inc. Papermaking using cationic starch and carboxymethyl cellulose or its additionally substituted derivatives
JPH0441788A (ja) * 1990-05-31 1992-02-12 Kanzaki Paper Mfg Co Ltd 紙の製造方法
US5098520A (en) * 1991-01-25 1992-03-24 Nalco Chemcial Company Papermaking process with improved retention and drainage
EP0515750A3 (en) * 1991-05-29 1993-06-16 Borden, Inc. Polyamide-epichlorohydrin resin
US5318669A (en) * 1991-12-23 1994-06-07 Hercules Incorporated Enhancement of paper dry strength by anionic and cationic polymer combination
US5830320A (en) * 1996-09-18 1998-11-03 Weyerhaeuser Company Method of enhancing strength of paper products and the resulting products
JPH11107188A (ja) * 1997-10-01 1999-04-20 Seiko Kagaku Kogyo Co Ltd 強力紙の製造方法
SE521591C2 (sv) * 1998-11-30 2003-11-18 Sca Res Ab Metod att framställa en partikel uppvisande beläggning av med varandra växelverkande polymerer och pappers -eller nonwovenprodukt innehållande partiklarna
SE0001268L (sv) * 2000-04-06 2001-10-07 Sca Hygiene Prod Ab Förfarande för adsorption av på varandra följande tunna skikt av katjoniska och anjoniska polymerer på ytan hos partiklar eller grupper av partiklar, och pappers- eller nonwovenprodukt innehållande s ådana partiklar eller grupper av partiklar
US6582560B2 (en) * 2001-03-07 2003-06-24 Kimberly-Clark Worldwide, Inc. Method for using water insoluble chemical additives with pulp and products made by said method

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4210490A (en) * 1976-07-14 1980-07-01 English Clays Lovering Pochin & Company, Limited Method of manufacturing paper or cardboard products
US5185062A (en) * 1991-01-25 1993-02-09 Nalco Chemical Company Papermaking process with improved retention and drainage
EP0790351A2 (fr) * 1996-02-14 1997-08-20 Nalco Chemical Company Procédé de fabrication de papier à l'aide d'un agent de rétention et d'égouttage multipolymère
EP0835957A2 (fr) * 1996-10-11 1998-04-15 Fort James Corporation Procédé de fabrication d'une bande de papier

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
See also references of WO2006041401A1 *

Also Published As

Publication number Publication date
CA2581361A1 (fr) 2006-04-20
EP1799905B1 (fr) 2011-12-14
CN101040083A (zh) 2007-09-19
JP4976300B2 (ja) 2012-07-18
CN101040083B (zh) 2010-08-11
RU2367739C2 (ru) 2009-09-20
DK1799905T3 (da) 2012-02-13
JP2008517174A (ja) 2008-05-22
ATE537298T1 (de) 2011-12-15
BRPI0516078A (pt) 2008-08-19
EP1799905A4 (fr) 2010-06-16
WO2006041401A1 (fr) 2006-04-20
RU2007117910A (ru) 2008-11-20
NZ554090A (en) 2009-07-31
ES2377754T3 (es) 2012-03-30
US20080023164A1 (en) 2008-01-31

Similar Documents

Publication Publication Date Title
EP1799905B1 (fr) Procede de production de papier ou de carton et produit resultant
CA2607332C (fr) Procede de fabrication d'un papier et papier fabrique selon ce procede
CA1186857A (fr) Methode de fabrication du papier
WO2012039668A1 (fr) Produit de papier ou de carton et procédé de fabrication de produit de papier ou de carton
RU2208079C2 (ru) Крафт-бумага и способ ее изготовления
US20120241114A1 (en) Process for production of a paper or paperboard product
JP2000504790A (ja) 充填紙及びこれに使用するための組成物の製造
WO2007041380A1 (fr) Resine resistante temporairement a l’etat humide pour applications papier
US10145068B2 (en) Process for producing at least one ply of a paper or board and a paper or board produced according to the process
Gärdlund et al. The use of polyelectrolyte complexes (PEC) as strength additives for different pulps used for production of fine paper
US20240026606A1 (en) Method for separating cellulosic particulates out of fiber suspensions and/or filtrates
JP7459751B2 (ja) 板紙の製造方法
JP4091940B2 (ja) 新規な製紙用炭酸カルシウム填料及び該填料を使用した紙及びその製造方法
EP4202119A1 (fr) Papier recyclable à haute résistance à l'état humide
EP4453313A1 (fr) Papier recyclable à haute résistance à l'humidité

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: 20070411

AK Designated contracting states

Kind code of ref document: A1

Designated state(s): AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HU IE IS IT LI LT LU LV MC NL PL PT RO SE SI SK TR

DAX Request for extension of the european patent (deleted)
A4 Supplementary search report drawn up and despatched

Effective date: 20100518

RIC1 Information provided on ipc code assigned before grant

Ipc: D21H 11/20 20060101AFI20110331BHEP

Ipc: D21H 23/06 20060101ALI20110331BHEP

Ipc: D21H 17/29 20060101ALI20110331BHEP

Ipc: D21H 17/26 20060101ALI20110331BHEP

GRAP Despatch of communication of intention to grant a patent

Free format text: ORIGINAL CODE: EPIDOSNIGR1

GRAS Grant fee paid

Free format text: ORIGINAL CODE: EPIDOSNIGR3

GRAA (expected) grant

Free format text: ORIGINAL CODE: 0009210

AK Designated contracting states

Kind code of ref document: B1

Designated state(s): AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HU IE IS IT LI LT LU LV MC NL PL PT RO SE SI SK TR

REG Reference to a national code

Ref country code: GB

Ref legal event code: FG4D

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

REG Reference to a national code

Ref country code: DK

Ref legal event code: T3

REG Reference to a national code

Ref country code: NL

Ref legal event code: T3

REG Reference to a national code

Ref country code: DE

Ref legal event code: R096

Ref document number: 602005031682

Country of ref document: DE

Effective date: 20120223

REG Reference to a national code

Ref country code: SE

Ref legal event code: TRGR

REG Reference to a national code

Ref country code: ES

Ref legal event code: FG2A

Ref document number: 2377754

Country of ref document: ES

Kind code of ref document: T3

Effective date: 20120330

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

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: 20111214

LTIE Lt: invalidation of european patent or patent extension

Effective date: 20111214

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

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: 20120315

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: 20111214

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: 20111214

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 FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20111214

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: 20111214

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

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: 20120414

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: 20120314

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: 20111214

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: 20111214

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: 20111214

REG Reference to a national code

Ref country code: DE

Ref legal event code: R061

Ref document number: 602005031682

Country of ref document: DE

PLBR Kind of request for revocation recorded

Free format text: ORIGINAL CODE: EPIDOSNRVR2

PLBT Request for revocation filed by patent holder

Free format text: ORIGINAL CODE: EPIDOSNRVR1

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

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: 20120416

Ref country code: PL

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: 20111214

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: 20111214

PLDH Decision on request for revocation

Free format text: ORIGINAL CODE: EPIDOSNRVR3

RDAA Patent revoked on request of proprietor

Free format text: ORIGINAL CODE: 0009220

PLBU Request for revocation filed by patent holder

Free format text: ORIGINAL CODE: EPIDOSNRVR6

PLBI Opposition filed

Free format text: ORIGINAL CODE: 0009260

REG Reference to a national code

Ref country code: DE

Ref legal event code: R103

Ref document number: 602005031682

Country of ref document: DE

Ref country code: DE

Ref legal event code: R064

Ref document number: 602005031682

Country of ref document: DE

PLAN Information deleted related to communication of a notice of opposition and request to file observations + time limit

Free format text: ORIGINAL CODE: EPIDOSDOBS2

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

Free format text: ORIGINAL CODE: EPIDOSNOBS2

PLAZ Examination of admissibility of opposition: despatch of communication + time limit

Free format text: ORIGINAL CODE: EPIDOSNOPE2

26 Opposition filed

Opponent name: SCA HYGIENE PRODUCTS AB

Effective date: 20120912

REG Reference to a national code

Ref country code: DE

Ref legal event code: R026

Ref document number: 602005031682

Country of ref document: DE

Effective date: 20120912

PLCX Information related to decision on request for revocation modified

Free format text: ORIGINAL CODE: 0009299RVR3

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

Free format text: STATUS: PATENT REVOKED BY PROPRIETOR

RVDA Request for revocation filed during opposition period found admissible

Filing date: 20120828

Effective date: 20121010

REG Reference to a national code

Ref country code: CH

Ref legal event code: PL

PLBJ Opposition found inadmissible

Free format text: ORIGINAL CODE: 0009275

REG Reference to a national code

Ref country code: NL

Ref legal event code: V1

Effective date: 20130501

26U Opposition found inadmissible

Opponent name: SCA HYGIENE PRODUCTS AB

Effective date: 20130417

GBPC Gb: european patent ceased through non-payment of renewal fee

Effective date: 20121013

REG Reference to a national code

Ref country code: FR

Ref legal event code: ST

Effective date: 20130628

REG Reference to a national code

Ref country code: AT

Ref legal event code: MM01

Ref document number: 537298

Country of ref document: AT

Kind code of ref document: T

Effective date: 20121031

REG Reference to a national code

Ref country code: ES

Ref legal event code: FD2A

Effective date: 20140611

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

Free format text: ORIGINAL CODE: 0009299OPPO

R26U Opposition found inadmissible (corrected)

Opponent name: ESSITY HYGIENE AND HEALTH AKTIEBOLAG

Effective date: 20130417