WO2005028747A1 - Method for making a layered paper or board web - Google Patents

Method for making a layered paper or board web Download PDF

Info

Publication number
WO2005028747A1
WO2005028747A1 PCT/FI2004/000549 FI2004000549W WO2005028747A1 WO 2005028747 A1 WO2005028747 A1 WO 2005028747A1 FI 2004000549 W FI2004000549 W FI 2004000549W WO 2005028747 A1 WO2005028747 A1 WO 2005028747A1
Authority
WO
WIPO (PCT)
Prior art keywords
stock
fraction
paper
water
layer
Prior art date
Application number
PCT/FI2004/000549
Other languages
Finnish (fi)
French (fr)
Inventor
Matti Hietaniemi
Kari Kokkonen
Original Assignee
Metso Paper, Inc.
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Metso Paper, Inc. filed Critical Metso Paper, Inc.
Priority to US10/572,977 priority Critical patent/US20080121360A1/en
Priority to DE112004001766T priority patent/DE112004001766T5/en
Publication of WO2005028747A1 publication Critical patent/WO2005028747A1/en

Links

Classifications

    • 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
    • D21F11/06Processes for making continuous lengths of paper, or of cardboard, or of wet web for fibre board production, on paper-making machines of the cylinder type
    • D21F11/08Processes for making continuous lengths of paper, or of cardboard, or of wet web for fibre board production, on paper-making machines of the cylinder type paper or board consisting of two or more layers
    • 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

Definitions

  • the invention relates to a method for making a layered paper or board web, in which method thick stock delivered to a paper machine is diluted with tail water and the diluted stock is fractionated to produce two different stock fractions of which, the first stock fraction, containing on an average finer material than the second stock fraction, is conducted into the surface layer or layers of the paper or board web, and the second stock fraction, containing on an average coarser material than the first stock fraction, is conducted into the middle layer or layers of the paper or board web.
  • a stock feed system for a multi-layer headbox is disclosed in the US patent No. 5,746,889, in which different stock concepts are produced out of the same fresh stock to be fed into different layers of the multi-layer headbox.
  • the stock feed system contains at least one screen for transferring long fibers out of the stock that is destined to form the surface layer of the paper into the stock that is destined to form a layer placed in the interior of the paper.
  • the system may also contain another screen for transferring short fibers out of the stock that is destined to form the layer placed in the interior of the paper into the stock that is destined to form the surface layer of the paper.
  • accept fibers separated during the fractionating of the stock are on an average shorter, thinner and more pliable, and the accept contains more fines and filler than the reject.
  • the accept from fractionation will be referred to as the fine stock fraction and the reject from fractionation will be referred to as the coarse stock fraction.
  • the object of the invention is to provide an improved method for manufacturing a web from a stock by layering the different fractions thereof. Especially, the object is to maintain the different properties of the stock fractions produced by fractionating, whereupon the objectives set for ' the layering of the stock are easier to reach.
  • the coarse stock fraction is diluted with water that contains less solids originating from the stock than normal tail water, the different properties of the stock fractions used for different layers of the paper or board web can be maintained better than before, which improves the result of layering in paper or board manufacturing.
  • Tail water is a filtrate removed from the web being formed on the wire section, which water is collected into a wire pit or the like and which contains fines and filler originating from the paper stock. A major part of the solids contained in the primary tail water is returned into the process by using tail water for diluting the thick stock in the short circulation of the paper machine.
  • Water suitable for diluting the coarse stock fraction is characterized by the fact that the consistency of the water is substantially lower than the consistency of the tail water used for diluting the thick stock before fractionating.
  • the consistency of the diluting water is less than 60 % of the consistency of the primary tail water.
  • Examples of possible water fractions suitable for diluting the reject are cloudy and clear filtrate from the recovery of fibers, water coming from suction flatboxes, separately collected paper machine spray water, water coming from the press section and tail water fractioned by clarification or some other method.
  • One option is to dilute tail water with a substantially cleaner water fraction such that the consistency of water used for diluting the coarse stock fraction is substantially lower than the original consistency of the tail water.
  • Figure 1 shows a schematic view of manufacturing of layered paper using fractionating of the stock and a multi-layer headbox.
  • Figure 2 shows manufacture of a multi-layer web using fractionating of the stock and two different web-forming units.
  • thick stock M is delivered into the paper machine via a wire pit 10, where it is diluted with tail water originating from the wire section.
  • the diluted stock Mi is conducted with a pump Pi into a first centrifugal cleaning step 11 of a centrifugal cleaner equipment, where the stock is fractionated into two stock fractions A and B. Fractionating is performed so, that the first stock fraction will contain fibers that on an average are thinner, shorter and more pliable and also more fines and filler than the second stock fraction B. Because of this, the stock fractions are in the following referred to as the fine stock fraction A and the coarse stock fraction B.
  • the fine stock fraction A from fractionation is conducted as two component flows Ai and A through pumps P AI and P A and machine screens 13 AI and 13 A2 into two layers 14 A I and 14 A of a multi-layer headbox 15 that are used to form the top and bottom layers of the manufactured paper or board web.
  • the coarse stock fraction B from fractionation is diluted and the diluted stock flow Bi is conducted through a pump P 2 into a second centrifugal cleaning step 12 of the centrifugal cleaner equipment, where impurities are extracted from the stock.
  • the accept B 2 from the centrifugal cleaning step 12 is conducted through a pump PB and a machine screen 13 B into a layer 14 B of the multi-layer headbox that is used for forming the middle layer of the paper and board web.
  • tail water Di taken from the wire pit 10 containing substantial amount of fibers, fines and filler, is used for dilution.
  • a water flow D 0 whose consistency is lower than the consistency of the tail water Di taken from the wire pit 10, is conducted into diluting the coarse stock fraction B.
  • This water can, for example, be taken from fiber recovery screen, spray water recovery or from suction flatboxes.
  • water from the wire pit 10 can be used as dilution water, provided that enough solids have been extracted from it in a separate process stage (not shown). Dilution water, which is substantially cleaner than the tail water, can also be obtained by diluting water from the wire pit with a cleaner water fraction.
  • FIG. 2 illustrates another solution according to the invention.
  • the diluted stock Mi is fractioned in the first centrifugal cleaning step 11 of the centrifugal cleaner equipment into two stock fractions A and B.
  • the fine stock fraction A from fractionation is conducted into a headbox 16, which feeds the stock on a fourdrinier wire 18 for forming a first web Wi.
  • the coarse stock fraction B from fractionation is diluted with a water flow Do, whose consistency is lower than that of the tail water Di from the wire pit 10, and it is conducted into a second centrifugal cleaning step 12 of the centrifugal cleaner equipment.
  • the cleaned stock B is conducted through a pump P B and a machine screen 13 B into a headbox 17, which feeds the stock on a second fourdrinier wire 19 for forming a second web W 2 .
  • the second web W 2 is carried by the wire 19 on top of the first web Wi on the wire 18 and the webs Wi and W 2 are joined together to form a two-layered board web.
  • the web forming units may comprise besides a fourdrinier wire also a gap former.
  • fractionation can also be carried out in a manner known per se by using pressure screens.
  • fractionating techniques and the reject ratio By adapting the fractionating techniques and the reject ratio, different types of properties can be obtained for the different layers of the web. There can naturally be more than one fractionating stage.

Landscapes

  • Paper (AREA)

Abstract

A method for manufacturing a layered paper or board web, in which method thick stock (M) delivered to the paper machine is diluted with tail water and the diluted stock (M1) is fractioned in order to produce two different stock fractions (A,B). The first stock fraction (A), which contains on an average finer material than the second stock fraction (B), is conducted into the surface layer or layers of the paper or board web, and the second stock fraction (B), which contains on an average coarser material than the first stock fraction (A), is conducted into the middle layer or layers of the paper or board web. Before feeding into a headbox (15), the coarse stock fraction (B) from fractionation is diluted with water whose consistency is substantially lower than the consistency of the water added into the thick stock (M) before fractionating. When water, which contains less solids from the stock than the normal tail water, is used to dilute the coarse stock fraction, the stock fractions used for different layers of the paper or board web can, better than before, maintain their different properties, which improves the result of layering in paper or board manufacturing.

Description

Method for Making a Layered Paper or Board Web
The invention relates to a method for making a layered paper or board web, in which method thick stock delivered to a paper machine is diluted with tail water and the diluted stock is fractionated to produce two different stock fractions of which, the first stock fraction, containing on an average finer material than the second stock fraction, is conducted into the surface layer or layers of the paper or board web, and the second stock fraction, containing on an average coarser material than the first stock fraction, is conducted into the middle layer or layers of the paper or board web.
A stock feed system for a multi-layer headbox is disclosed in the US patent No. 5,746,889, in which different stock concepts are produced out of the same fresh stock to be fed into different layers of the multi-layer headbox. The stock feed system contains at least one screen for transferring long fibers out of the stock that is destined to form the surface layer of the paper into the stock that is destined to form a layer placed in the interior of the paper. The system may also contain another screen for transferring short fibers out of the stock that is destined to form the layer placed in the interior of the paper into the stock that is destined to form the surface layer of the paper.
Fractionating methods that apply centrifugal cleaning are disclosed in WO published applications Nos. 0 129 311 Al and 0 222 947 Al, in which accept from the first centrifugal cleaning step is transferred into the surface layers of the web to be formed, and the accept from a second or lower step is transferred into the middle layers of the web to be formed. By fractionating the stock, lower fines contents and higher average fiber length can be achieved in the middle layers of the web than in the surface layers of the web. On the other hand, higher fines and filler contents can be achieved in the surface layers of the web than in the middle layers, which, among other things, improves the printing properties of the paper.
The accept fibers separated during the fractionating of the stock are on an average shorter, thinner and more pliable, and the accept contains more fines and filler than the reject. For simplicity's sake, the accept from fractionation will be referred to as the fine stock fraction and the reject from fractionation will be referred to as the coarse stock fraction.
It is typical for fractionating that the consistency of the accept is decreased and the consistency of the reject is increased compared to the consistency of the feed. Because of this, the reject often has to be diluted before it can be conducted into the headbox of the paper machine. In WO 0 222 947, the rejects from the fractionating stages are diluted with tail water taken from a wire pit before they are transferred into the next stage. In WO 0 129 311, the same tail water is being used for diluting both the accept and the reject before they are fed into the different layers of the multi -layer headbox. When the coarse stock fraction intended for the middle layers of the web is diluted with "impure" tail water, i.e. containing plenty of fines and filler, at least some of the advantages obtained with fractionating are lost. Because of the tail water, the drainability of the reject can go down almost to the level of the accept and the filler content can go up to near the filler content of the accept.
The object of the invention is to provide an improved method for manufacturing a web from a stock by layering the different fractions thereof. Especially, the object is to maintain the different properties of the stock fractions produced by fractionating, whereupon the objectives set for' the layering of the stock are easier to reach.
In order to obtain these and other objects that will become evident later, the method according to the invention is characterized by what is defined in the characterizing part of claim 1.
When the coarse stock fraction is diluted with water that contains less solids originating from the stock than normal tail water, the different properties of the stock fractions used for different layers of the paper or board web can be maintained better than before, which improves the result of layering in paper or board manufacturing.
Tail water is a filtrate removed from the web being formed on the wire section, which water is collected into a wire pit or the like and which contains fines and filler originating from the paper stock. A major part of the solids contained in the primary tail water is returned into the process by using tail water for diluting the thick stock in the short circulation of the paper machine.
Water suitable for diluting the coarse stock fraction is characterized by the fact that the consistency of the water is substantially lower than the consistency of the tail water used for diluting the thick stock before fractionating. Preferably, the consistency of the diluting water is less than 60 % of the consistency of the primary tail water.
Examples of possible water fractions suitable for diluting the reject are cloudy and clear filtrate from the recovery of fibers, water coming from suction flatboxes, separately collected paper machine spray water, water coming from the press section and tail water fractioned by clarification or some other method. One option is to dilute tail water with a substantially cleaner water fraction such that the consistency of water used for diluting the coarse stock fraction is substantially lower than the original consistency of the tail water.
In the following, the invention will be described with reference to the examples in the appended figures, but the intention is not to limit the invention to these only. Figure 1 shows a schematic view of manufacturing of layered paper using fractionating of the stock and a multi-layer headbox.
Figure 2 shows manufacture of a multi-layer web using fractionating of the stock and two different web-forming units.
According to figure 1, thick stock M is delivered into the paper machine via a wire pit 10, where it is diluted with tail water originating from the wire section. The diluted stock Mi is conducted with a pump Pi into a first centrifugal cleaning step 11 of a centrifugal cleaner equipment, where the stock is fractionated into two stock fractions A and B. Fractionating is performed so, that the first stock fraction will contain fibers that on an average are thinner, shorter and more pliable and also more fines and filler than the second stock fraction B. Because of this, the stock fractions are in the following referred to as the fine stock fraction A and the coarse stock fraction B.
The fine stock fraction A from fractionation is conducted as two component flows Ai and A through pumps PAI and PA and machine screens 13AI and 13A2 into two layers 14A I and 14A of a multi-layer headbox 15 that are used to form the top and bottom layers of the manufactured paper or board web.
The coarse stock fraction B from fractionation is diluted and the diluted stock flow Bi is conducted through a pump P2 into a second centrifugal cleaning step 12 of the centrifugal cleaner equipment, where impurities are extracted from the stock. The accept B2 from the centrifugal cleaning step 12 is conducted through a pump PB and a machine screen 13B into a layer 14B of the multi-layer headbox that is used for forming the middle layer of the paper and board web.
As the fractionating increases the consistency of the coarse stock fraction B, the stock B must be diluted before conducting it into the headbox 15. Conventionally, tail water Di taken from the wire pit 10, containing substantial amount of fibers, fines and filler, is used for dilution. In the solution according to the invention, a water flow D0, whose consistency is lower than the consistency of the tail water Di taken from the wire pit 10, is conducted into diluting the coarse stock fraction B. This water can, for example, be taken from fiber recovery screen, spray water recovery or from suction flatboxes. Also water from the wire pit 10 can be used as dilution water, provided that enough solids have been extracted from it in a separate process stage (not shown). Dilution water, which is substantially cleaner than the tail water, can also be obtained by diluting water from the wire pit with a cleaner water fraction.
Figure 2 illustrates another solution according to the invention. There, the diluted stock Mi is fractioned in the first centrifugal cleaning step 11 of the centrifugal cleaner equipment into two stock fractions A and B. The fine stock fraction A from fractionation is conducted into a headbox 16, which feeds the stock on a fourdrinier wire 18 for forming a first web Wi. The coarse stock fraction B from fractionation is diluted with a water flow Do, whose consistency is lower than that of the tail water Di from the wire pit 10, and it is conducted into a second centrifugal cleaning step 12 of the centrifugal cleaner equipment. The cleaned stock B is conducted through a pump PB and a machine screen 13B into a headbox 17, which feeds the stock on a second fourdrinier wire 19 for forming a second web W2. The second web W2 is carried by the wire 19 on top of the first web Wi on the wire 18 and the webs Wi and W2 are joined together to form a two-layered board web.
When manufacturing multi-layer web, there naturally can be more than two separate web forming units and the web forming units may comprise besides a fourdrinier wire also a gap former.
Instead of the above-described centrifugal cleaning device, fractionation can also be carried out in a manner known per se by using pressure screens. By adapting the fractionating techniques and the reject ratio, different types of properties can be obtained for the different layers of the web. There can naturally be more than one fractionating stage.
In the following the patent claims will be given, and the details of the invention may show variation within the scope of the inventive idea defined in said claims and differ from the details given above for the sake of example only.

Claims

Claims
1. A method for manufacturing a layered paper or board web, in which method thick stock (M) delivered to a paper machine is diluted with tail water and the diluted stock (Mi) is fractionated to produce two different stock fractions (A, B), of which the first stock fraction (A), containing on an average finer material than the second stock fraction (B), is conducted into the surface layer or layers of the paper or board web, and the second stock fraction (B), containing on an average coarser material than the first stock fraction (A), is conducted into the middle layer or layers of the paper or board web, characterized in that the coarse stock fraction (B) is, before being fed into a headbox (15; 17), diluted with water having a consistency that is substantially lower than the consistency of the tail water added into thick stock (M) before fractionating.
2. A method according to claim 1, characterized in that the coarse stock fraction (B) from fractionation is diluted with water, whose consistency is at the most 60 % of the consistency of the tail water used for diluting the stock before fractionating.
3. A method according to any of the preceding claims, characterized in that water from fiber recovery, suction flatboxes and/or press section and/or separately collected fabric conditioning water and/or cleaned tail water is/are used for diluting the coarse stock fraction (B) from fractionation.
4. A method according to any of the preceding claims, characterized in that tail water that has been diluted with a water type substantially cleaner than the tail water itself is used for diluting the coarse stock fraction (B) from fractionation.
5. A method according to any of the preceding claims, characterized in that the coarse stock fraction (B) from fractionation is conducted into the headbox (15; 17) through a cleaning device (12) and that the stock fraction (B) in question is diluted before it is fed into said cleaning device (12).
6. A method according to any of the preceding claims, characterized in that fractionating is carried out by centrifugal cleaners (11).
7. A method according to any of the preceding claims, characterized in that fractionating is carried out by screens.
8. A method according to any of the preceding claims, characterized in that fractionating is carried out by in two or more stages.
9. A method according to any of the preceding claims, characterized in that the fine stock fraction (A) from fractionation is conducted into at least one layer (14AI, 14A2) of the multi-layer headbox (15) used for forming a suiface layer of the paper or board web, and the coarse stock fraction (B) from fractionation is conducted into at least one other layer (14B) of the same multi-layer headbox (15) used for forming a middle layer of the paper or board web.
10. A method according to any one of claims 1 to 8, characterized in that the fine stock fraction (A) from fractionation is conducted into at least one headbox (16) used for forming a surface layer of the multi-layer web, and the coarse stock fraction (B) from fractionation is conducted into at least one other headbox (17) used for forming a middle layer of the multi-layer web.
PCT/FI2004/000549 2003-09-24 2004-09-20 Method for making a layered paper or board web WO2005028747A1 (en)

Priority Applications (2)

Application Number Priority Date Filing Date Title
US10/572,977 US20080121360A1 (en) 2003-09-24 2004-09-20 Method For Making A Layered Paper Or Board Web
DE112004001766T DE112004001766T5 (en) 2003-09-24 2004-09-20 Process for producing a layered paper or board web

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
FI20031376A FI115234B (en) 2003-09-24 2003-09-24 A process for making a laminated paper or board web
FI20031376 2003-09-24

Publications (1)

Publication Number Publication Date
WO2005028747A1 true WO2005028747A1 (en) 2005-03-31

Family

ID=27839038

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/FI2004/000549 WO2005028747A1 (en) 2003-09-24 2004-09-20 Method for making a layered paper or board web

Country Status (5)

Country Link
US (1) US20080121360A1 (en)
CN (1) CN1856617A (en)
DE (1) DE112004001766T5 (en)
FI (1) FI115234B (en)
WO (1) WO2005028747A1 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104213455A (en) * 2014-08-18 2014-12-17 湖北欧华达纤维科技有限公司 Automatic environment-friendly regenerated fiber board production system

Families Citing this family (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
ITMI20060698A1 (en) * 2006-04-07 2007-10-08 Gruppo Cordenons Spa PAPER SAFETY MATERIAL IN PARTICULAR FOR LABELING AND PACKAGING AND ITS PROCESS OF MANUFACTURING
US8871059B2 (en) * 2012-02-16 2014-10-28 International Paper Company Methods and apparatus for forming fluff pulp sheets
CN103015267B (en) * 2012-12-17 2016-03-02 金红叶纸业集团有限公司 The using method of paper grade (stock) softener
CN107460764B (en) * 2017-09-13 2020-10-27 临泉鹏成机电技术有限公司 High-quality paper web papermaking process
EP3502348B1 (en) * 2017-12-21 2020-06-24 BillerudKorsnäs AB Fibre fractionation
WO2019136254A1 (en) * 2018-01-05 2019-07-11 International Paper Company Paper products having increased bending stiffness and cross-direction strength and methods for making the same

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6210529B1 (en) * 1998-06-10 2001-04-03 Valmet Corporation Method for regulating the surface level and consistency in a tank for metering component stock
US6267845B1 (en) * 1998-06-10 2001-07-31 Valmet Corporation Process arrangement for the short circulation in a paper or board machine
WO2002086233A1 (en) * 2001-04-23 2002-10-31 Metso Paper, Inc. Method and process arrangement in the short circulation of a paper machine

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE4401761C2 (en) * 1994-01-22 1997-04-24 Voith Gmbh J M Method and device for improving the paper quality of multilayer and multilayer papers
US6210535B1 (en) * 1995-06-01 2001-04-03 Valmet Corporation Stock feed system for a multi-layer headbox and method in the operation of a multi-layer headbox

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6210529B1 (en) * 1998-06-10 2001-04-03 Valmet Corporation Method for regulating the surface level and consistency in a tank for metering component stock
US6267845B1 (en) * 1998-06-10 2001-07-31 Valmet Corporation Process arrangement for the short circulation in a paper or board machine
WO2002086233A1 (en) * 2001-04-23 2002-10-31 Metso Paper, Inc. Method and process arrangement in the short circulation of a paper machine

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104213455A (en) * 2014-08-18 2014-12-17 湖北欧华达纤维科技有限公司 Automatic environment-friendly regenerated fiber board production system

Also Published As

Publication number Publication date
FI115234B (en) 2005-03-31
FI20031376A0 (en) 2003-09-24
US20080121360A1 (en) 2008-05-29
CN1856617A (en) 2006-11-01
DE112004001766T5 (en) 2006-08-03

Similar Documents

Publication Publication Date Title
US5746889A (en) Stock feed system for a multi-layer headbox and method in the operation of a multi-layer headbox
CN101321910A (en) Method for manufacturing paper
SE513596C2 (en) Method for making paper or cardboard
CN1305549A (en) Process arrangement for short circulation in paper or board machine
US20080121360A1 (en) Method For Making A Layered Paper Or Board Web
CN101802298B (en) Apparatus and method for manufacturing fibre mass suspension
FI81397C (en) Method and apparatus for removing light material from a fiber's suspension
CA2085306C (en) Method and apparatus for treating white water
FI109712B (en) Method and apparatus for fractionation of pulp in a paper or board machine
DE19526205C2 (en) Process and plant for producing a multilayer paper or cardboard web
EP0211840B1 (en) Method for manufacturing multilayer board
AU747347B2 (en) Base webs for printed circuit board production using the foam process and aramid fibers
WO2003104548A1 (en) Fractionation apparatus and method in fractionation of stock in a paper machine or equivalent
WO2001029311A1 (en) A method for the manufacture of layered paper or board
WO2004109010A1 (en) Method for the manufacture of a multilayer web
WO2004067838A1 (en) Method and device for handling filler-containing broke in a paper machine and a board machine
DE102008010447A1 (en) Fibrous material suspension treating and utilizing method for manufacturing paper, involves forming fine fraction and coarse fraction by fractioning function, where coarse fraction is predominantly used for layer of paper
JP4060917B2 (en) Corrugated cardboard exterior liner and method for manufacturing surface layer manufacturing paper fee thereof
US6585901B2 (en) Method of draining water from low-consistency water-fiber suspensions
AU750899B2 (en) Screening of fibrous suspensions
US5643413A (en) Multi-ply paper product and method of making the same
US6497788B1 (en) Backwater cycle and process for the water circulation of a paper machine

Legal Events

Date Code Title Description
WWE Wipo information: entry into national phase

Ref document number: 200480027667.5

Country of ref document: CN

AK Designated states

Kind code of ref document: A1

Designated state(s): AE AG AL AM AT AU AZ BA BB BG BW BY BZ CA CH CN CO CR CU CZ DK DM DZ EC EE EG ES FI GB GD GE GM HR HU ID IL IN IS JP KE KG KP KZ LC LK LR LS LT LU LV MA MD MK MN MW MX MZ NA NI NO NZ PG PH PL PT RO RU SC SD SE SG SK SY TJ TM TN TR TT TZ UA UG US UZ VN YU ZA ZM

AL Designated countries for regional patents

Kind code of ref document: A1

Designated state(s): GM KE LS MW MZ NA SD SZ TZ UG ZM ZW AM AZ BY KG MD RU TJ TM AT BE BG CH CY DE DK EE ES FI FR GB GR HU IE IT MC NL PL PT RO SE SI SK TR BF CF CG CI CM GA GN GQ GW ML MR SN TD TG

121 Ep: the epo has been informed by wipo that ep was designated in this application
WWE Wipo information: entry into national phase

Ref document number: 1120040017661

Country of ref document: DE

ENP Entry into the national phase

Ref document number: 93202004

Country of ref document: AT

Kind code of ref document: A

WWE Wipo information: entry into national phase

Ref document number: A9320/2004

Country of ref document: AT

WWE Wipo information: entry into national phase

Ref document number: 10572977

Country of ref document: US

122 Ep: pct application non-entry in european phase
WWP Wipo information: published in national office

Ref document number: 10572977

Country of ref document: US