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 PDFInfo
- 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
- Authority
- EP
- European Patent Office
- Prior art keywords
- web
- water
- wire
- headbox
- layer
- 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.)
- Active
Links
- 239000000835 fiber Substances 0.000 title claims description 31
- 238000000034 method Methods 0.000 title claims description 20
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 48
- 229920002472 Starch Polymers 0.000 claims description 24
- 239000008107 starch Substances 0.000 claims description 24
- 235000019698 starch Nutrition 0.000 claims description 24
- 239000000725 suspension Substances 0.000 claims description 21
- 239000007788 liquid Substances 0.000 claims description 18
- 239000012895 dilution Substances 0.000 claims description 17
- 238000010790 dilution Methods 0.000 claims description 17
- 239000013505 freshwater Substances 0.000 claims description 13
- 239000000126 substance Substances 0.000 claims description 9
- 238000004519 manufacturing process Methods 0.000 claims description 6
- 239000011087 paperboard Substances 0.000 claims description 4
- 239000000203 mixture Substances 0.000 claims description 3
- 102100031260 Acyl-coenzyme A thioesterase THEM4 Human genes 0.000 claims 1
- 101000638510 Homo sapiens Acyl-coenzyme A thioesterase THEM4 Proteins 0.000 claims 1
- 239000010410 layer Substances 0.000 description 74
- 239000000945 filler Substances 0.000 description 10
- 238000007670 refining Methods 0.000 description 9
- 229920001131 Pulp (paper) Polymers 0.000 description 5
- 238000004061 bleaching Methods 0.000 description 4
- 230000007423 decrease Effects 0.000 description 3
- 239000000123 paper Substances 0.000 description 3
- 239000002356 single layer Substances 0.000 description 3
- 238000010586 diagram Methods 0.000 description 2
- 239000002023 wood Substances 0.000 description 2
- HLYCTXRRGDDBOW-UHFFFAOYSA-N 2-methylpiperazine-1-carbodithioic acid Chemical compound CC1CNCCN1C(S)=S HLYCTXRRGDDBOW-UHFFFAOYSA-N 0.000 description 1
- 241000274582 Pycnanthus angolensis Species 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 238000013459 approach Methods 0.000 description 1
- 239000007844 bleaching agent Substances 0.000 description 1
- 125000002091 cationic group Chemical group 0.000 description 1
- 229920006317 cationic polymer Polymers 0.000 description 1
- 230000032798 delamination Effects 0.000 description 1
- 230000001419 dependent effect Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 238000010998 test method Methods 0.000 description 1
Images
Classifications
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21F—PAPER-MAKING MACHINES; METHODS OF PRODUCING PAPER THEREON
- D21F1/00—Wet end of machines for making continuous webs of paper
- D21F1/02—Head boxes of Fourdrinier machines
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21F—PAPER-MAKING MACHINES; METHODS OF PRODUCING PAPER THEREON
- D21F1/00—Wet end of machines for making continuous webs of paper
- D21F1/04—Head boxes of cylinder machines
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21F—PAPER-MAKING MACHINES; METHODS OF PRODUCING PAPER THEREON
- D21F11/00—Processes for making continuous lengths of paper, or of cardboard, or of wet web for fibre board production, on paper-making machines
- D21F11/02—Processes 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
- D21F11/04—Processes 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
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21F—PAPER-MAKING MACHINES; METHODS OF PRODUCING PAPER THEREON
- D21F9/00—Complete machines for making continuous webs of paper
- D21F9/003—Complete machines for making continuous webs of paper of the twin-wire type
- D21F9/006—Complete 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.
Landscapes
- Paper (AREA)
Claims (10)
- Machine à bandes de fibres comprenantau moins trois sections de formation (21, 25, 29), chacune d'entre elles ayant une toile guidée autour de rouleaux en boucle fermée, etune caisse d'arrivée (1, 23, 27) conçue pour éjecter au moins une couche de liquide sur la toile respective, dans laquelleau 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, etles 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 jetscaractérisée en ce queun 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.
- 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. - 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. - Procédé de formation d'une bande multijet dans une machine à bandes de fibres, comprenantl'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), etla 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.
- 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). - 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. - 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. - 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. - 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.
- 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.
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 |
Family
ID=61683654
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP18161992.5A Active EP3540118B1 (fr) | 2018-03-15 | 2018-03-15 | Machine à bande fibreuse et procédé de formation d'une bande multicouche |
Country Status (2)
Country | Link |
---|---|
EP (1) | EP3540118B1 (fr) |
CN (1) | CN110273316B (fr) |
Families Citing this family (1)
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)
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 |
-
2018
- 2018-03-15 EP EP18161992.5A patent/EP3540118B1/fr active Active
-
2019
- 2019-03-13 CN CN201910187365.2A patent/CN110273316B/zh active Active
Also Published As
Publication number | Publication date |
---|---|
CN110273316A (zh) | 2019-09-24 |
EP3540118A1 (fr) | 2019-09-18 |
CN110273316B (zh) | 2021-08-31 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
FI75200B (fi) | Foerfarande vid pappersframstaellningsprocess foer foerbaettring av egenskaper hos papperet, saerskilt dess retention. | |
CN102131981B (zh) | 纸板机 | |
US6712931B1 (en) | Method for manufacturing a paper or board web and a paper or board machine | |
US20120219816A1 (en) | Process for the production of a paper or board product and a paper or board produced according to the process | |
CN112585317B (zh) | 用于制造多层纤维料幅的方法和机器 | |
US2098733A (en) | Plyboard | |
US5609726A (en) | Headbox and method for producing multilayer and multi-ply paper webs | |
CN108691235B (zh) | 多叠纤维幅材的成形部段和多叠纤维幅材的成形方法 | |
US20230019391A1 (en) | Light weight linerboard for corrugated board | |
CN106715797B (zh) | 用于生产纸或纸板的至少一个层的方法以及根据该方法生产的纸或纸板 | |
EP3540118B1 (fr) | Machine à bande fibreuse et procédé de formation d'une bande multicouche | |
US20020060003A1 (en) | Machine for the manufacture of a fibrous plasterboard web | |
US4961824A (en) | Method for manufacturing multilayer board | |
US6423181B1 (en) | Gravure paper and manufacturing process for this paper | |
FI104002B (fi) | Monikerrosrainaus yksinkertaista perusmassasysteemiä käyttäen | |
US11512431B2 (en) | Method of forming a three-layer board web and a forming section of forming a three-layer board web | |
EP0233058B1 (fr) | Procédé et appareil pour la fabrication d'un carton multicouche | |
EP3540119B1 (fr) | Machine à bande fibreuse et procédé de formation d'une bande multicouche | |
US6540873B2 (en) | Board machine and method of manufacturing a multilayer cardboard web | |
CN111684128B (zh) | 用于制造多层式的纤维料幅的方法和装置 | |
CN112567094A (zh) | 用于制造瓦楞纸板原纸幅的机器和方法 | |
US4957778A (en) | Method of producing chemically self-copying or self-containing paper | |
WO2023186562A1 (fr) | Bande de matériau fibreux multicouche | |
US6932886B2 (en) | Multi-ply fibrous plasterboard web | |
FI20227069A1 (en) | Fiber web machine for producing a multilayer fiber web |
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 |
|
STAA | Information on the status of an ep patent application or granted ep patent |
Free format text: STATUS: THE APPLICATION HAS BEEN PUBLISHED |
|
AK | Designated contracting states |
Kind code of ref document: A1 Designated state(s): AL AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HR HU IE IS IT LI LT LU LV MC MK MT NL NO PL PT RO RS SE SI SK SM TR |
|
AX | Request for extension of the european patent |
Extension state: BA ME |
|
STAA | Information on the status of an ep patent application or granted ep patent |
Free format text: STATUS: REQUEST FOR EXAMINATION WAS MADE |
|
17P | Request for examination filed |
Effective date: 20200318 |
|
RBV | Designated contracting states (corrected) |
Designated state(s): AL AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HR HU IE IS IT LI LT LU LV MC MK MT NL NO PL PT RO RS SE SI SK SM TR |
|
GRAP | Despatch of communication of intention to grant a patent |
Free format text: ORIGINAL CODE: EPIDOSNIGR1 |
|
STAA | Information on the status of an ep patent application or granted ep patent |
Free format text: STATUS: GRANT OF PATENT IS INTENDED |
|
INTG | Intention to grant announced |
Effective date: 20220609 |
|
GRAS | Grant fee paid |
Free format text: ORIGINAL CODE: EPIDOSNIGR3 |
|
GRAA | (expected) grant |
Free format text: ORIGINAL CODE: 0009210 |
|
STAA | Information on the status of an ep patent application or granted ep patent |
Free format text: STATUS: THE PATENT HAS BEEN GRANTED |
|
AK | Designated contracting states |
Kind code of ref document: B1 Designated state(s): AL AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HR HU IE IS IT LI LT LU LV MC MK MT NL NO PL PT RO RS SE SI SK SM 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: AT Ref legal event code: REF Ref document number: 1533209 Country of ref document: AT Kind code of ref document: T Effective date: 20221215 Ref country code: DE Ref legal event code: R096 Ref document number: 602018043279 Country of ref document: DE |
|
REG | Reference to a national code |
Ref country code: IE Ref legal event code: FG4D |
|
REG | Reference to a national code |
Ref country code: LT Ref legal event code: MG9D |
|
REG | Reference to a national code |
Ref country code: NL Ref legal event code: MP Effective date: 20221123 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: SE 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: 20221123 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: 20230323 Ref country code: NO 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: 20230223 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: 20221123 Ref country code: FI 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: 20221123 Ref country code: ES 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: 20221123 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: RS 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: 20221123 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: 20221123 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: 20221123 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: 20230323 Ref country code: HR 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: 20221123 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: 20230224 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: NL 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: 20221123 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: SM 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: 20221123 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: 20221123 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: 20221123 Ref country code: DK 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: 20221123 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: 20221123 |
|
REG | Reference to a national code |
Ref country code: DE Ref legal event code: R097 Ref document number: 602018043279 Country of ref document: DE |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
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: 20221123 Ref country code: AL 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: 20221123 |
|
PLBE | No opposition filed within time limit |
Free format text: ORIGINAL CODE: 0009261 |
|
STAA | Information on the status of an ep patent application or granted ep patent |
Free format text: STATUS: NO OPPOSITION FILED WITHIN TIME LIMIT |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: MC 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: 20221123 |
|
REG | Reference to a national code |
Ref country code: CH Ref legal event code: PL |
|
26N | No opposition filed |
Effective date: 20230824 |
|
GBPC | Gb: european patent ceased through non-payment of renewal fee |
Effective date: 20230315 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
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: 20221123 |
|
REG | Reference to a national code |
Ref country code: BE Ref legal event code: MM Effective date: 20230331 |
|
REG | Reference to a national code |
Ref country code: AT Ref legal event code: UEP Ref document number: 1533209 Country of ref document: AT Kind code of ref document: T Effective date: 20221123 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: LU Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20230315 |
|
REG | Reference to a national code |
Ref country code: IE Ref legal event code: MM4A |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: GB Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20230315 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: LI Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20230331 Ref country code: IE Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20230315 Ref country code: GB Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20230315 Ref country code: FR Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20230331 Ref country code: CH Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20230331 |
|
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 NON-PAYMENT OF DUE FEES Effective date: 20230331 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: AT Payment date: 20240321 Year of fee payment: 7 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: DE Payment date: 20240320 Year of fee payment: 7 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: IT 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: 20221123 |