EP3088604A1 - Verfahren und system zum optimieren der eigenschaften einer mehrschichtigen faserstoffbahn in der faserbahnherstellung - Google Patents

Verfahren und system zum optimieren der eigenschaften einer mehrschichtigen faserstoffbahn in der faserbahnherstellung Download PDF

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Publication number
EP3088604A1
EP3088604A1 EP16167211.8A EP16167211A EP3088604A1 EP 3088604 A1 EP3088604 A1 EP 3088604A1 EP 16167211 A EP16167211 A EP 16167211A EP 3088604 A1 EP3088604 A1 EP 3088604A1
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EP
European Patent Office
Prior art keywords
fiber web
dilution
basis weight
stock
zones
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
EP16167211.8A
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English (en)
French (fr)
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EP3088604B1 (de
Inventor
Teuvo Virkkunen
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Valmet Technologies Oy
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Valmet Technologies Oy
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Publication of EP3088604A1 publication Critical patent/EP3088604A1/de
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    • 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
    • D21F1/00—Wet end of machines for making continuous webs of paper
    • D21F1/08—Regulating consistency
    • 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
    • D21F1/022—Means for injecting material into flow within the headbox
    • D—TEXTILES; PAPER
    • D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21G—CALENDERS; ACCESSORIES FOR PAPER-MAKING MACHINES
    • D21G9/00—Other accessories for paper-making machines
    • D21G9/0009—Paper-making control systems
    • D21G9/0027—Paper-making control systems controlling the forming section

Definitions

  • the present invention relates to a method for the optimization of the properties of a multilayer fiber web in the manufacture of a fiber web, in which method the multilayer fiber web is formed by feeding at least two stock suspensions that form a layer of the fiber web to a forming section from two or more headboxes divided into parallel feed zones, where those properties of the stock suspensions that affect the strength of the finished fiber web differ from each other, and the basis weight profile of the stock suspensions is adjusted in two or more headboxes by feeding dilution water in zones in the cross direction of the fiber web machine into each stock suspension.
  • the present invention also relates to a corresponding system.
  • the cross-directional strength properties of the fiber web are critical in terms of the quality of the product.
  • the objective is to minimize the variation of the cross-directional strength properties of the fiber web in the cross direction of the fiber web.
  • the uneven contraction of the fiber web in the dryer section leads to a deterioration of the cross-directional strength properties on the edges of the fiber web, since there is more contraction on the edges of the fiber web than in the center. Poorer cross-directional strength on the edges of the fiber web may even cause the rejection of edge rolls in quality control, if the edge rolls do not fulfill the strength requirements of the order.
  • the strength problem can be solved by increasing the basis weight of the fiber web on the edges, but in this case expensive raw material is lost when the required basis weight is exceeded in the edge rolls.
  • the headbox of the fiber web machine is divided into several parallel feed zones, and at least two different stock suspensions are fed into each of these feed zones.
  • the different stock suspensions contain fractions with different fiber lengths, advantageously the first stock suspension contains short-fiber fraction and the second stock suspension contains long-fiber fraction.
  • An object of the present invention is to accomplish a method that is more cost effective than the prior art methods for the optimization of the properties of a multilayer fiber web.
  • the characteristic features of the present invention will be more fully understood from claim 1.
  • Another object of the present invention is to accomplish a system for the optimization of the properties of a multilayer fiber web, which system is more advantageous to use than prior art systems.
  • the characteristic features of the present invention will be more fully understood from claim 8.
  • This object can be achieved by means of a method for the optimization of the properties of a multilayer fiber web in the manufacture of a fiber web, in which method the multilayer fiber web is formed by feeding at least two stock suspensions that form a layer of the fiber web to a forming section from two or more headboxes divided into parallel feed zones, where those properties of the stock suspensions that affect the strength of the finished fiber web differ from each other.
  • the basis weight profile of the stock suspensions is adjusted in two or more headboxes by feeding dilution water in zones in the cross direction of the fiber web machine into each stock suspension.
  • the cross-directional basis weight profile and strength of the formed fiber web are adjusted in the cross direction of the fiber web machine by adjusting the amount of dilution water in zones separately in each stock suspension fed.
  • the dilution of two different stock suspensions it is possible to adjust the ratio between two different layers in the basis weight profile of a finished fiber web, and in this way the cross-directional basis weight profile and cross-directional strength properties of the finished fiber web can be made essentially even over the entire width of the fiber web.
  • the cross-directional strength of the fiber web can refer to the cross-directional compression strength or flat crush resistance. In the case of a multilayer fiber web, these strengths are usually more important strength indicators than tensile strength, which is naturally high in a product like this.
  • One of the two layers in the fiber web is advantageously a core layer and the other layer is a surface layer with better strength properties than in the core layer.
  • the strength properties of the layers of the fiber web differ from each other, which enables a change in the strength properties in the fiber web by changing the mutual ratio of the layers.
  • the dilution of the stock suspensions fed can be adjusted independently of each other, in other words the dilution equipment used for the dilutions is not in an adjustment relation with respect to each other.
  • the adjustment of dilution is restricted by a goal to a certain desired basis weight in the fiber web.
  • the basis weight profile of the fiber web is adjusted advantageously to an essentially even profile over the width of the fiber web by means of the dilution of the stock suspension that forms the core layer.
  • the basis weight profile of the fiber web is adjusted advantageously to an essentially even profile over the width of the fiber web by means of the dilution of the stock suspension that forms the core layer.
  • the dilution of the stock suspension that forms the thicker core layer also gives a greater adjustment response than the adjustment of the stock suspension that forms the thinner surface layer.
  • the strength profile of the fiber web is adjusted advantageously to an essentially even profile over the width of the fiber web by means of the dilution of the stock suspension that forms the surface layer.
  • the dilution of the surface layer it is possible to dilute the stock suspension that comes to the center of the fiber web more than the stock suspension that comes to the edges, and in this way savings can be achieved in the raw material costs.
  • an essentially even basis weight profile means that the variation of basis weight in the cross direction of the fiber web is less than ⁇ 1 g/m 2 .
  • Essentially even strength properties mean that the cross-directional strength properties of the fiber web vary no more than ⁇ 2 %.
  • the basis weight profile of the fiber web is measured as an online measurement, and on the basis of the measurement result the dilution of the stock suspension that forms the core layer is adjusted in individual feed zones.
  • the adjustment works as a feedback control circuit, and the basis weight profile can be adjusted easily in order to change the basis weight of the finished fiber web when shifting over from one grade to another.
  • the stock suspension fed to the core layer is diluted more in those feed zones of the headbox that form the edge area of the core layer of the fiber web than in those feed zones that form the center part of the fiber web.
  • a greater part of the total basis weight of the fiber web on the edges can be composed of a surface layer that has better strength properties than the core layer, which surface layer produces the effect that improves the strength properties of the edges of the fiber web.
  • two headboxes are used, each adapted to feed one stock suspension.
  • the use of separate headboxes enables a conventional design of the fiber web machine, where the different layers of a finished multilayer fiber web are formed initially on their own forming sections and are combined later into a uniform fiber web on the forming section.
  • the object of the system according to the present invention can be accomplished by means of a system for the optimization of the properties of a multilayer fiber web in the manufacture of a fiber web, where the system includes two or more headboxes for the feeding of at least two different stock suspensions to form at least two layers, the strength properties of which differ from each other, to a fiber web to be formed on the forming section, and dilution equipment divided into feed zones in the cross direction of the fiber web machine, adapted in connection with two or more headboxes for the dilution of the stock suspensions in zones in the cross direction of the fiber web machine in at least some of the feed zones for the optimization of the properties of the fiber web.
  • the dilution equipment is adapted to adjust separately in zones the amount of dilution water in each stock suspension fed for the adjustment of the cross-directional basis weight profile and strength of the formed fiber web in the cross direction of the fiber web machine.
  • the system according to the invention is very advantageous to implement, because the system can be implemented without a complex headbox design and control system.
  • the system includes two headboxes, each for feeding one stock suspension, in which system the dilution equipment is adapted in connection with both headboxes.
  • the dilution equipment of the different stock suspensions is advantageously independent of each other.
  • the dilution of the stock suspensions can be adjusted independently of each other, in other words the dilution equipment used for the dilutions is not in an adjustment relation with respect to each other.
  • the adjustment of dilution is restricted by a goal to a certain desired basis weight in the fiber web.
  • a characteristic feature of the method according to the invention is that the cross-directional basis weight profile and strength of the formed fiber web in the cross direction of the fiber web machine are adjusted in the method by adjusting the amount of dilution water in zones separately in each stock suspension fed.
  • a characteristic feature of the system according to the invention is that the dilution equipment is adapted to adjust separately in zones the amount of dilution water in each stock suspension fed for the adjustment of the cross-directional basis weight profile and strength of the formed fiber web in the cross direction of the fiber web machine.
  • the advantage to be achieved with the method and system according to the invention is an essentially straight basis weight profile in the cross direction of the fiber web and an essentially straight strength profile in the cross direction.
  • a system 100 includes at least two headboxes 12 for the feeding of at least two different stock suspensions onto a forming section 50 of a fiber web machine 200 to form a fiber web 10.
  • two or more separate headboxes 12 each have dilution adjustment for one stock suspension.
  • there can be dilution adjustments in more numerous feeds of stock suspensions fed but in its simplest configuration the invention can be implemented by means of two dilution adjustments. So that the dilution adjustment gives the desired outcome, in other words even basis weight profile and strength profile in the cross direction of the fiber web, the dilution adjustments must be in stock suspensions where the properties of the stock suspensions differ from each other.
  • the core layer that forms the core of the fiber web in a multilayer fiber web contains a cheaper raw material than the surface layer, which cheaper raw material contains more short fiber than the surface layer and which has a poorer strength than the surface layer.
  • the surface layer is composed of a more expensive raw material than the core layer, in which more expensive raw material the proportion of long fibers is greater than in the core layer, and consequently also the strength of the layer of the fiber web formed is better than in the core layer.
  • Figure 1 shows the first embodiment of the system according to the invention, in which first embodiment two separate headboxes 12 are used, each equipped with dilution adjustment.
  • the dilution adjustment is implemented by means of dilution equipment 32 placed in connection with the headboxes 12.
  • the dilution equipment 32 can be, in accordance with Figure 4 , feed lines coming to the headbox 12, which feed lines feed into the headbox water or a stock suspension with a considerably higher water content than in the stock suspension fed on the headbox for the dilution of the fed stock suspension in zones in the cross direction of the fiber web.
  • each layer of the finished fiber web is formed on its own wire 42 and 44, which combine the layers into a finished fiber web 10 in a later stage.
  • the fiber web machine can also include a separate top wire cycle 40 in accordance with Figure 1 .
  • reference number 46 refers to the press section of the fiber web machine.
  • Figure 2 shows the second embodiment of the system 100 according to the invention, in which embodiment the multilayer fiber web produced consists of three separate layers.
  • the system has three headboxes 12, and there is dilution equipment in connection with at least two of these headboxes.
  • the left-hand side headbox 12 feeds the stock suspension of the core layer
  • the middle headbox 12 feeds the stock suspension of the intermediate layer
  • the right-hand side headbox 12 feeds the stock suspension of the surface layer.
  • the dilution equipment is advantageously in the headboxes that form the core and surface layers and the intermediate layer can be without dilution, because the cross-directional adjustment of the basis weight profile and strength profile according to the invention can be done by means of two dilution adjustments.
  • each headbox 12 used in the system according to the invention is divided into several feed zones 18 in the cross-direction of the fiber web.
  • the width of an individual feed zone is 40 - 120 mm, in which case the headbox is divided into dozens, even to more than one hundred feed zones, each of which can be adjusted for dilution independently of each other.
  • each headbox equipped with dilution adjustment includes dozens, even hundreds of control valves 66 and their control devices (not shown in the figures) for adjusting the dilutions.
  • At least two different stock suspensions are fed from two or more headboxes 12 for the forming of a multilayer fiber web 10.
  • a certain basis weight such as 100 g/m 2 , has been specified for the produced multilayer fiber web in the order, which basis weight is the minimum basis weight of the fiber web in all reels.
  • the objective is that the basis weight of the fiber web produced comes as close to the target as possible; however, so that the basis weight of the entire fiber web is above the minimum basis weight specified in the order.
  • the feed ratio of the stock suspensions is defined initially and the flows are adapted so that the total basis weight of the layers that form the fiber web exceeds the target.
  • the basis weight of the core layer can be 75 g/m 2 and the basis weight of the surface layer can be 25 g/m 2 , in which case the basis weight of the two-layer fiber web is 100 g/m 2 .
  • the fiber web is formed using rough settings, and the strengths and basis weight of the finished fiber web are measured.
  • the measurement of basis weight can be carried out as an online measurement 24 shown in Figures 1 and 2 , but the strengths must be calculated from samples taken from the fiber web using a laboratory analysis.
  • the measurement instrument used for the online measurement of basis weight can be a basis weight scanner of the type known from prior art.
  • the basis weight of the surface layer is advantageously at least 25 g/m 2 so that a surface layer essential for the appearance and printability of the fiber web is formed on the fiber web.
  • the system advantageously includes programmatic equipment for controlling dilution.
  • the programmatic equipment can be a part of a computer or a part integrated into or connected to the control system of the fiber web machine, by means of which programmatic equipment the functioning of the dilution equipment can be controlled.
  • the dilution equipment can include valves for restricting the flow of dilution water or corresponding medium, and valve control equipment, which can advantageously be controlled via a field bus by means of the programmatic equipment.
  • the valve control equipment is advantageously electric actuators.
  • the programmatic equipment can be automatic equipment, which controls, on the basis of pre-set criteria, the valves of the dilution equipment to adjust the dilution flows.
  • the selected criteria can include the difference between the strength measured on the basis of individual feed zones of the headbox and the target, the difference between the measured basis weight and the target, or some other corresponding criterion. In dilution, it is also possible to use the filtrates of wires or other corresponding waters that do not contain much fibers.
  • the measurement results of the basis weight and strengths of the fiber web are advantageously fed to the programmatic equipment, which studies how close to the target the evenness of the cross-directional basis weight profile and strength profile of the fiber web are.
  • the programmatic equipment can be adapted to adjust the basis weight profile on the basis of the measured difference by only adjusting the dilution equipment of the stock suspension that forms the core layer.
  • the basis weight profile is adjusted by increasing or decreasing the dilution of the core layer with respect to the target.
  • the dilution of the core layer can be adjusted by individual feed zones using the feed zones of the headbox, until an even/straight basis weight profile is achieved in the cross direction of the fiber web.
  • the goal is to achieve the set strength target by using the programmatic equipment.
  • a new strength measurement is carried out in terms of the fiber web that has a straight cross-sectional basis weight profile.
  • the dilution of the stock suspension coming to the surface layer is decreased on the basis of the differences in the strengths at different points in those zones where the strength of the fiber web is too low.
  • the decrease in dilution increases the amount of fiber coming to the surface layer in this feed zone of the headbox and increases the basis weight. Dilution can be added by means of the programmatic equipment to compensate for this change in those feed zones of the headbox that form the core layer and that correspond to the adjustable feed zones of the surface layer.
  • the stock suspension fed to the core layer 20 is generally diluted more in those feed zones of the headbox that form the edge area 26 of the core layer 20 of the fiber web 10 than in those feed zones 18, shown in Figure 4 , that form the center part 28 of the fiber web 10.
  • more long-fiber fiber fraction of the surface layer 22 can be brought to the edge areas 26, which long-fiber fiber fraction reinforces the edge areas, which become naturally weaker during the drying of the fiber web.
  • the mutual relationship of the basis weights of the layers 16 varies in the cross direction of the fiber web 10.
  • the cross-directional optimization of the basis weight profile and strength profile of the fiber web can be carried out by means of the method according to the invention by using separate headboxes equipped with dilution adjustment.
  • the dilutions of the stock suspensions fed, forming the various layers, can be adjusted independently of each other.
  • the multilayer fiber web manufactured by means of the method and system according to the invention is board used in exterior packaging, where the core layer of the board is formed from a raw material which results in a layer that has a poorer strength and cheaper costs than the surface layer, and the surface layer, in turn, is more expensive and stronger than the core layer.
  • the invention relates to a method for the optimization of the properties of a multilayer fiber web (10) in the manufacture of a fiber web (10), in which method the multilayer fiber web (10) is formed by feeding at least two stock suspensions that form a layer (16) of the fiber web (10) to a forming section (50) from two or more headboxes (12) divided into parallel feed zones (18), where those properties of said stock suspensions that affect the strength of the finished fiber web differ from each other, and the basis weight profile of said stock suspensions is adjusted in two or more headboxes (12) by feeding dilution water in zones in the cross direction of the fiber web machine into each stock suspension.
  • the cross-directional basis weight profile and strength of the formed fiber web (10) are adjusted in the cross direction of the fiber web machine by adjusting the amount of dilution water in zones separately in each stock suspension fed.
  • the invention also relates to a corresponding system.

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EP16167211.8A 2015-04-28 2016-04-27 Verfahren und system zum optimieren der eigenschaften einer mehrschichtigen faserstoffbahn in der faserbahnherstellung Active EP3088604B1 (de)

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FI20155312 2015-04-28

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EP3088604A1 true EP3088604A1 (de) 2016-11-02
EP3088604B1 EP3088604B1 (de) 2020-03-25

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Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN115298370B (zh) * 2020-03-31 2023-05-02 金伯利-克拉克环球有限公司 用于生产分区和/或分层基材的方法和设备

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE19514236A1 (de) * 1995-04-15 1996-10-17 Voith Sulzer Papiermasch Gmbh Stoffauflauf für eine Papiermaschine zum Erzeugen einer mehrlagigen oder mehrschichtigen Papierbahn
US6284100B1 (en) * 1997-01-24 2001-09-04 Valmet Corporation Method and apparatus for controlling a headbox in a paper machine
WO2004109010A1 (en) * 2003-06-05 2004-12-16 Metso Paper, Inc. Method for the manufacture of a multilayer web
DE102009028135A1 (de) * 2008-08-12 2010-03-11 Metso Paper, Inc. Verfahren und System zur Optimierung von Eigenschaften einer Faserbahn

Family Cites Families (7)

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Publication number Priority date Publication date Assignee Title
DE19634993A1 (de) * 1996-08-30 1998-03-05 Voith Sulzer Papiermasch Gmbh Verfahren und Vorrichtung zum Einstellen des Stoffdichte- und Faserorientierungsprofils in einem Stoffauflauf
FI100345B (fi) * 1997-01-24 1997-11-14 Valmet Corp Menetelmä ja laite paperikoneen perälaatikon säädössä
US6375799B1 (en) * 1999-01-28 2002-04-23 Voith Sulzer Papiertechnik Patent Gmbh Process and apparatus for producing a fibrous material web
FI116688B (fi) * 2004-02-13 2006-01-31 Metso Paper Inc Monikerrosrainan muodostusosa
CN101012629B (zh) * 2006-05-31 2011-04-27 华南理工大学 流浆箱的稀释水添加装置
FI20085782L (fi) * 2008-08-22 2010-02-23 Metso Paper Inc Kartonkikone
DE102009014268B3 (de) * 2009-03-20 2010-04-08 Andritz Küsters Gmbh Anordnung an Papiermaschinen zur Einstellung eines Flächengewichts-Querprofils

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE19514236A1 (de) * 1995-04-15 1996-10-17 Voith Sulzer Papiermasch Gmbh Stoffauflauf für eine Papiermaschine zum Erzeugen einer mehrlagigen oder mehrschichtigen Papierbahn
US6284100B1 (en) * 1997-01-24 2001-09-04 Valmet Corporation Method and apparatus for controlling a headbox in a paper machine
WO2004109010A1 (en) * 2003-06-05 2004-12-16 Metso Paper, Inc. Method for the manufacture of a multilayer web
DE102009028135A1 (de) * 2008-08-12 2010-03-11 Metso Paper, Inc. Verfahren und System zur Optimierung von Eigenschaften einer Faserbahn
FI121888B (fi) 2008-08-12 2011-05-31 Metso Paper Inc Menetelmä kuiturainan ominaisuuksien optimoimiseksi

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Publication number Publication date
CN106087519B (zh) 2019-01-11
CN106087519A (zh) 2016-11-09
EP3088604B1 (de) 2020-03-25

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