EP3540118B1 - Machine à bande fibreuse et procédé de formation d'une bande multicouche - Google Patents

Machine à bande fibreuse et procédé de formation d'une bande multicouche Download PDF

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Publication number
EP3540118B1
EP3540118B1 EP18161992.5A EP18161992A EP3540118B1 EP 3540118 B1 EP3540118 B1 EP 3540118B1 EP 18161992 A EP18161992 A EP 18161992A EP 3540118 B1 EP3540118 B1 EP 3540118B1
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EP
European Patent Office
Prior art keywords
web
water
wire
headbox
layer
Prior art date
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Application number
EP18161992.5A
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German (de)
English (en)
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EP3540118A1 (fr
Inventor
Hannu Turpeinen
Juha KOVANEN
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.)
Valmet Technologies Oy
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Valmet Technologies Oy
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Priority to EP18161992.5A priority Critical patent/EP3540118B1/fr
Priority to CN201910187365.2A priority patent/CN110273316B/zh
Publication of EP3540118A1 publication Critical patent/EP3540118A1/fr
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    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21FPAPER-MAKING MACHINES; METHODS OF PRODUCING PAPER THEREON
    • D21F1/00Wet end of machines for making continuous webs of paper
    • D21F1/02Head boxes of Fourdrinier machines
    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21FPAPER-MAKING MACHINES; METHODS OF PRODUCING PAPER THEREON
    • D21F1/00Wet end of machines for making continuous webs of paper
    • D21F1/04Head boxes of cylinder machines
    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21FPAPER-MAKING MACHINES; METHODS OF PRODUCING PAPER THEREON
    • D21F11/00Processes for making continuous lengths of paper, or of cardboard, or of wet web for fibre board production, on paper-making machines
    • D21F11/02Processes for making continuous lengths of paper, or of cardboard, or of wet web for fibre board production, on paper-making machines of the Fourdrinier type
    • D21F11/04Processes for making continuous lengths of paper, or of cardboard, or of wet web for fibre board production, on paper-making machines of the Fourdrinier type paper or board consisting on two or more layers
    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21FPAPER-MAKING MACHINES; METHODS OF PRODUCING PAPER THEREON
    • D21F9/00Complete machines for making continuous webs of paper
    • D21F9/003Complete machines for making continuous webs of paper of the twin-wire type
    • D21F9/006Complete machines for making continuous webs of paper of the twin-wire type paper or board consisting of two or more layers

Definitions

  • the invention pertains to a fiber web machine and to a method of forming a multiply web.
  • Document WO 99 / 40 256 A1 discloses an arrangement of three forming sections each of which having a wire guided about rolls in a closed loop and a multi-layer headbox.
  • the closed loops of the wire are guided such that liquid layers ejected on and conveyed by the wires are dewatered to form plies and then are merged such that the at least three plies occurring from the liquid layers ejected by the multi-layer headbox are sandwiched between the at least two other plies.
  • document WO 99 / 40 256 A1 discloses a web forming method using the above-described arrangement.
  • Document EP 2 784 213 B1 discloses a multi-layer headbox structure for a fiber web machine which serves to supply mainly liquid substances such as water and/or a pulp suspension liquid in a layered manner onto a wire of a forming section.
  • Additives such as refined fibers, fillers, cationic polymers such as cationic starch, etc. are added to the water and/or pulp suspension liquid.
  • These liquid substances are fed to the headbox by means of a water supply or feed water supply.
  • a central diffuser of the headbox is connected with feeding means feeding fresh water, dilution water, and/or white water into the central diffuser
  • the substances applied onto a forming wire are then dewatered to form a web. This is then further transferred to a press section for additional dewatering and a dryer section in which the formed web is dried to form a paper or board web. Further treatment depends on the respective requirements of the product.
  • Fig. 1 shows an example of such a headbox structure.
  • a fiber web machine comprises at least three forming sections. Each of these forming sections has a wire guided about rolls in a closed loop, and a headbox adapted to eject at least one layer of liquid onto the respective wire. At least one of the headboxes is a multi-layer headbox adapted to eject at least three liquid layers onto the respective wire. A center diffuser of the multi-layer headbox is connected with feeding means for feeding fresh water, dilution water and/or white water.
  • the closed loops of the wire are guided such that liquid layers ejected on and conveyed by the wires are dewatered to form plies and then are merged such that the at least three plies occurring from the liquid layers ejected by the multi-layer headbox are sandwiched between the at least two other plies.
  • the feeding means supplying the center diffuser of the multi-layer headbox can be additionally connected with a starch storage in order to supply starch with the fresh water, dilution water and/or white water.
  • the middle layer plies can be optimized in order to maximize the bulk of the web.
  • the middle layer can be divided in two separate stock layers separated by the water layer.
  • brightness levels of the layers can be individually adapted. Thus, for example when applying higher brightness to the ply next to the top ply, less bleaching is required.
  • increase of the bulk is possible. For instance, the increase of the bulk can be in a range of about 15% to 30%.
  • the fiber web machine can be used for manufacturing Folding Boxboard.
  • a method of forming a multi-ply web in a fiber web machine comprises the steps:
  • a web can be formed which has middle plies the properties of which can be advantageously adapted as desired by means of one multi-layer headbox, while the web is completed by separately formed top and back plies, respectively.
  • starch can be added to the fresh water, dilution water, and/or white water guided through the central diffuser of the multi-layer headbox.
  • middle layer's stocks By adapting the starch level, properties of the middle layer's stocks can be advantageously optimized with regard to the bulk.
  • the middle layer plies can be optimized in order to maximize the bulk of the web.
  • the middle layer can be divided in two separate stock layers separated by the water layer.
  • coarser fibers can be used in the middle layer. Accordingly, less refining is required for the fibers and the bulk can be increased. It is even possible to use different refining rates between the top and back ply sides. Also, brightness levels of the layers can be individually adapted. Thus, for example when applying higher brightness to the ply next to the top ply, less bleaching is required. Thus, increase of the bulk is possible.
  • the starch can be preferably added with an amount of 1 to 20 kg per ton of water, and most preferably with an amount of 2 to 10 kg per ton of water.
  • the bulk of the middle layer(s) can be maximized.
  • the pulp suspension comprise BCTMP (Bleached Chemi Thermo Mechanical Pulp), CTMP (Chemi Thermo Mechanical Pulp), TMP (Thermo Mechanical Pulp), PGW (Pressurized Ground Wood) and/or GW (Ground Wood), wherein the pulp suspensions guided to the one or more of the adjacent diffusers of the multi-layer headbox have a different composition.
  • broke can be added to the pulp suspensions fed to one or more of the adjacent diffusers of the multi-layer headbox, wherein the amount of broke preferably differs in the individual pulp suspensions.
  • a brightness of one of the plies of the web is higher than a brightness of the other one of the plies of the web.
  • the middle layer can be divided into two layers, both of these layers can be given different properties, e.g. by using different refining rates for the added fibers. Thereby, coarser fibers can be used which advantageously leads to a higher bulk. Also, different brightness levels can be assigned to the middle layers, leading to that less bleaching is required which is also advantageous with regard to the bulk.
  • the manufacturing cost of such kinds of multiply products is achieved by dividing the middle ply stock in two layers, and feeding chemicals to between these two layers by means of the aqua layer. Then it is possible to use coarser fibers in the middle ply (which means less refining and therewith smaller energy consumption) and to also reduce bleaching chemicals consumption (the bottom side stock of the middle layer can have a smaller brightness than the top side stock). Mainly this is achieved by feeding starch between to these two layers and starch feeding happens by this central diffuser by water (fresh water, white water, or dilution water).
  • the invention can be preferably used in FBB (folding box board) production.
  • FBB folding box board
  • FBB folding box board
  • Fig. 1 schematically shows an example of a multi-layer headbox 1 as is for example disclosed in document EP 2 784 213 B1 .
  • a multi-layer headbox 1 as is for example disclosed in document EP 2 784 213 B1 .
  • the features of such a headbox it is referred to this document, the contents of which is herewith incorporated in its entirety. Merely the features necessary for understanding the invention will be now described.
  • the multi-layer headbox 1 has plural diffusers, one of them being a central diffuser 13 connected with feeding means 7 feeding fresh water, dilution water, and/or white water into the central diffuser 13.
  • the adjacent diffusers are connected with stock header feeding means 3, 5.
  • Additional dilution water can be supplied from a dilution water feeding means 9 connectable via dilution water valves 11 with a pipe feeding stock header from stock header feeding means 5 to the diffuser being arranged above the central diffuser 13 in Fig. 1 for controlling the cross machine direction basis weight profile.
  • the dilution water valves 11 are arranged in 30mm to 150 mm intervals in the headbox cross machine direction.
  • the multi-layer headbox 1 is capable of ejecting stock layers in a layered manner onto a web of a forming section.
  • Fig. 2 is a schematic view of a fiber web machine according to the invention.
  • the fiber web machine has three forming sections 21, 25 and 29.
  • a first forming section 21 of these three forming sections 21, 25 and 29 is provided with the multi-layer headbox 1 shown in Fig. 1 .
  • the forming section 21 (also referred to as first forming section) comprises a wire guided in a closed loop via guiding rollers 210, 211 and 213.
  • Other well-known forming means such as suction boxes, suction rolls, etc. are provided with the forming section 21.
  • this merging section the web formed in this first forming section 21 is merged with another web referred to a top web.
  • the top web is formed in a second forming section 25 which basically comprises a headbox 23 (also referred to as top ply headbox) and a wire guided in a closed loop about guiding rollers 250, 251, 253 and 255.
  • the headbox 23 is a single layer headbox and, thus, ejects a single stock layer onto the wire.
  • the stock layer is also dewatered by means of well-known forming means to form the top web.
  • a merging section provided between the guiding rollers 251 and 253
  • the wire is guided in a manner contacting the wire of the first forming section 21 such that the web formed in the first forming section 21 is merged with the top web.
  • the web merged with the top web is then guided further by the wire of the second forming section 25 to a second merging section defined between guiding rollers 253 and 255.
  • the web merged with the top web is merged with a third web formed in a third forming section 29.
  • the third web is also referred to as back web.
  • the back web is formed in the third forming section which basically comprises a headbox 27 (also referred to as back ply headbox) and a wire guided in a closed loop about guiding rollers 291, 293, and 290.
  • the headbox 27 is also a single layer headbox ejecting a single stock layer onto the wire of the third forming section 29.
  • the stock layer is also dewatered by well-known means to form the back web.
  • the wire of the third forming section 29 is guided such that it approaches the wire of the second forming section 25 and contacts the same in the section between the guiding rollers 253 and 255, thereby merging the back web with the web on a side opposite of the top web.
  • the web merged with the top and back webs is then guided further and handed over at a take-over roller 31 to a wire 33 of a press section for further treatment.
  • an enhanced web can be produced in which middle plies of the web (also referred to as filler ply (plies)) are then covered from both sides by a top ply occurring from the top web and a back ply occurring from the back web.
  • middle plies of the web also referred to as filler ply (plies)
  • top ply headbox and the back ply headbox are each described as single layer headboxes, one or both of them can be embodied as multi-layer headboxes.
  • Figs. 3a to 3c schematically show a section view of the filler plies, top ply and back ply, respectively.
  • the filler plies comprise two layers 51 and 53 which are connected via a starch layer 55.
  • the starch layer occurs from the central water layer having starch added.
  • the top ply is referred to by 57 and the back ply is referred to by 59.
  • the starch is added into water forming a water layer arranged between the stock layers.
  • An amount of the starch added is in a range from 1 to 20 kg/t and preferably in a range from 2 to 10 kg/t.
  • Fig. 5 is a diagram showing the effect of the added starch amount with respect to the Scott Bond (J/m 2 ).
  • the _Huygen Scott Bond test is the most commonly used test method for quantifying the delamination resistance of paper and board.
  • coarser fibers and an increased amount of broke can be supplied to the stock layers forming the filler plies.
  • the pulp suspension comprise BCTMP, CTMP, TMP, PGW and/or GW. It is also noted that the pulp suspensions guided to the one or more of the adjacent diffusers of the multi-layer headbox preferably have a different composition.
  • the individual plies can be provided with different properties.
  • the filler ply 51 arranged directly adjacent to the top ply 57 can have a higher brightness than the other filler ply 53.

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  • Paper (AREA)

Claims (10)

  1. Machine à bandes de fibres comprenant
    au moins trois sections de formation (21, 25, 29), chacune d'entre elles ayant une toile guidée autour de rouleaux en boucle fermée, et
    une caisse d'arrivée (1, 23, 27) conçue pour éjecter au moins une couche de liquide sur la toile respective, dans laquelle
    au moins une des caisses d'arrivée (1) est une caisse d'arrivée multicouche conçue pour éjecter au moins trois couches de liquide sur la toile respective, et
    les boucles fermées de la toile sont guidées de telle sorte que des couches de liquide éjectées sur et transportées par les toiles soient déshydratées pour former des jets et soient ensuite fusionnées de telle sorte que les au moins trois jets (51, 53, 55) provenant des couches de liquide éjectées par la caisse d'arrivée multicouche soient pris en sandwich entre les au moins deux autres jets
    caractérisée en ce que
    un diffuseur central (13) de la caisse d'arrivée multicouche (1) est relié à des moyens d'alimentation (7) pour l'alimentation en eau fraîche, en eau de dilution et/ou en eaux collées.
  2. Machine à bandes de fibres selon la revendication 1, dans laquelle
    les moyens d'alimentation (27) alimentant le diffuseur central de la caisse d'arrivée multicouche sont en outre reliés à un stockage d'amidon afin de fournir de l'amidon à l'eau fraîche, à l'eau de dilution et/ou aux eaux collées.
  3. Machine à bandes de fibres selon la revendication 2, dans laquelle
    la machine à bandes de fibres est utilisée pour la fabrication de carton pour boîtes pliantes.
  4. Procédé de formation d'une bande multijet dans une machine à bandes de fibres, comprenant
    l'introduction d'eau douce, d'eau de dilution et/ou d'eaux collées dans un diffuseur central (13) d'une caisse d'arrivée multicouche (1),
    l'introduction de suspensions de pâte dans des diffuseurs adjacents respectifs du diffuseur central (13),
    le guidage de l'eau douce, de l'eau de dilution et/ou des eaux collées et des différentes suspensions de pâte à travers le diffuseur central (13) pour les éjecter sur une toile d'une section de formation (21), la toile formant une boucle fermée,
    la déshydratation des substances liquides pour former une bande,
    la fusion de la bande avec une deuxième bande formée au niveau d'une deuxième caisse d'arrivée (23) éjectant la suspension de pâte sur une toile d'une deuxième section de formation (25), et
    la fusion de la bande avec une troisième bande formée au niveau d'une troisième caisse d'arrivée (27) éjectant la suspension de pâte sur une toile d'une troisième section de formation (29), dans lequel la troisième bande est agencée sur un côté de la bande opposé à celui où est agencée la deuxième bande.
  5. Procédé selon la revendication 4, dans lequel
    l'amidon est ajouté à l'eau fraîche, à l'eau de dilution et/ou aux eaux collées guidées à travers le diffuseur central (13) de la caisse d'arrivée multicouche (1).
  6. Procédé selon la revendication 5, dans lequel
    l'amidon est de préférence ajouté avec une quantité de 1 à 20 kg par tonne d'eau, et plus préférablement avec une quantité de 2 à 10 kg par tonne d'eau.
  7. Procédé selon l'une quelconque des revendications 4 à 6, dans lequel
    des fibres grossières sont ajoutées aux suspensions de pâte introduites dans un ou plusieurs des diffuseurs adjacents de la caisse d'arrivée multicouche.
  8. Procédé selon l'une quelconque des revendications 4 à 7, dans lequel
    la suspension de pâte comprend de la pâte chimico-thermo-mécanique blanchie (BCTMP), de la pâte chimico-thermo-mécanique (CTMP), de la pâte thermo-mécanique (TMP), de la pâte mécanique de défibreur sous haute pression (PGW) et/ou de la pâte mécanique de défibreur (GW), dans lequel les suspensions de pâte guidées vers les un ou plusieurs diffuseurs adjacents de la caisse d'arrivée multicouche (1) ont une composition différente.
  9. Procédé selon l'une quelconque des revendications 4 à 8, dans lequel un cassé de fabrication est ajouté aux suspensions de pâte introduites dans un ou plusieurs des diffuseurs adjacents de la caisse d'arrivée multicouche, dans lequel la quantité de cassé de fabrication diffère de préférence dans les suspensions de pâte individuelles.
  10. Procédé selon l'une quelconque des revendications 4 à 9, dans lequel une luminosité de l'un des jets de la bande est supérieure à une luminosité de l'autre des jets de la bande.
EP18161992.5A 2018-03-15 2018-03-15 Machine à bande fibreuse et procédé de formation d'une bande multicouche Active EP3540118B1 (fr)

Priority Applications (2)

Application Number Priority Date Filing Date Title
EP18161992.5A EP3540118B1 (fr) 2018-03-15 2018-03-15 Machine à bande fibreuse et procédé de formation d'une bande multicouche
CN201910187365.2A CN110273316B (zh) 2018-03-15 2019-03-13 纤维幅材机和形成多铺层幅材的方法

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
EP18161992.5A EP3540118B1 (fr) 2018-03-15 2018-03-15 Machine à bande fibreuse et procédé de formation d'une bande multicouche

Publications (2)

Publication Number Publication Date
EP3540118A1 EP3540118A1 (fr) 2019-09-18
EP3540118B1 true EP3540118B1 (fr) 2022-11-23

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EP18161992.5A Active EP3540118B1 (fr) 2018-03-15 2018-03-15 Machine à bande fibreuse et procédé de formation d'une bande multicouche

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CN (1) CN110273316B (fr)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US11866884B2 (en) * 2020-03-31 2024-01-09 Kimberly-Clark Worldwide, Inc. Method and apparatus for producing a zoned and/or layered substrate

Family Cites Families (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FI78133C (fi) * 1980-03-14 1989-06-12 Valmet Oy Foerfarande vid viradelen foer en pappersmaskin samt dubbelviraformare.
FI896202A (fi) * 1989-12-22 1991-06-23 Ahlstroem Valmet Metod och anordning vid inloppslaodan av en pappers-, kartong- eller torkmaskin.
FI103211B1 (fi) * 1998-02-09 1999-05-14 Valmet Corp Lisäaineen kerrostus kartonkikoneen rainanmuodostusyksiköllä
DE102008000778A1 (de) * 2008-03-20 2009-09-24 Voith Patent Gmbh Stoffauflauf für eine Papier- oder Kartonmaschine
DE102010029617A1 (de) * 2010-06-02 2011-12-08 Voith Patent Gmbh Verfahren zur Herstellung einer gestrichenen, mehrlagigen Faserstoffbahn
FI126656B (fi) * 2012-09-03 2017-03-31 Valmet Technologies Inc Järjestely kerrostetun rainan muodostamiseksi kuiturainakoneessa, monikerroskuiturainakone ja menetelmä kerrostetun rainan muodostamiseksi kuiturainakoneella
EP2784213B1 (fr) 2013-03-28 2016-05-18 Valmet Technologies, Inc. Caisse de tête pour une machine de production d'une bande de matière fibreuse
CN203904770U (zh) * 2014-06-11 2014-10-29 维美德技术有限公司 纸板机

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Publication number Publication date
CN110273316A (zh) 2019-09-24
EP3540118A1 (fr) 2019-09-18
CN110273316B (zh) 2021-08-31

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