EP0995834A1 - Method and device for improving the cross-machine shrinkage profile in a paper machine - Google Patents

Abstract

To maintain the lateral profile of a running paper or cardboard web, the lateral shrinkage profile is adjusted during the formation process. The variations are through alterations in the fiber suspension composition locally to affect sections across the web width, using different proportions of suspension components with different shrinkage behaviors. <??>The shrinkage is increased at a section zone by a raised feed of fibers and/or other matter with a high shrinkage, or replacing fibers with fibers which shrink more strongly. The shrinkage is reduced by increasing the fiber feed of fibers with a low shrinkage character and/or other matter which shrinks less or replacing the fibers with the suspension containing fibers with lower shrinkage. The composition of the fiber suspension is adjusted at the stock inlet and/or the wet web section of the machine. Two flows of fiber suspension are prepared, to be mixed together at sections of the stock inlet to set the lateral shrinkage, while the lateral weight profile of the web is modified by the controlled flow of diluting water in sections across the web width. The fibers with a high shrinking tendency are long fibers and vice versa, very open fibers and vice versa, highly chopped or ground fibers and vice versa. The added matter to increase shrinkage is carboxymethyl cellulose (CMC) and/or other matter. The added matter to reduce shrinkage is a synthetic resin and/or wet strength agents and/or the like. The lateral weight profile of the web is measured, and the control values are determined to match the web weight in sections (N) across the web width together with a nominal profile for the operation of actuators (7). The shrinkage is computed by on-line mapping of the lateral weight profile, and the control values to set the shrinkage in sections (M) across the machine width using the nominal profile, and operate the actuators accordingly. The shrinkage with corrected values is measured, and the lateral shrinkage profile is computed by correlation between the measured values and the shrinkage. The control values are computed for sections (M) across the machine width, and the actuators are operated as appropriate. The on-line lateral weight mapping and the measurement of shrinkage with corrected values can be done together. The calculation for the lateral shrinkage profile is through correlation between the measured values and the shrinkage, and the weighted lateral shrinkage profile is registered from the measured and the computed lateral shrinkage profile to give the control values for the operation of the actuators. The profile control algorithm separates the lateral weight and shrinkage profiles. The measured values of the polish and/or strength are correlated with the shrinkage. An Independent claim is included for a paper or cardboard web prodn. machine with a constant section at the stock inlet with two zones for different fiber suspensions of fiber mixtures of different shrinkage characteristics, to be fed to the stock inlet. The stock inlet has a number of mixing points, by sections, where the different fiber suspensions are fed into the flow.

Description

The invention relates to a method for equalization the property cross profile of a running material web Paper or cardboard according to the preamble of claim 1.

Furthermore, the invention relates to a for carrying out the Above method suitable paper machine according to the General term of the first device claim.

A method is disclosed in DE 37 15 551 A1 to reduce the flutter of the web edges Paper web, as well as a paper machine for performing this Procedure known. According to this disclosure proposed in the edge region of the paper web to be produced a stock suspension with higher strength potential than in to use the remaining web width range. Regarding the Paper machine is proposed in the headbox additional lines are provided which are of higher quality Stock suspension in the side areas of the headbox respectively.

Despite this lateral feeding of different Suspensions or different additives for Material suspension results for the resulting material web a different shrinkage across the width of the Material web. As a rule, the edges shrink as a result further processing in the paper machine more than the middle areas of the material web. However, it can also by drying at different speeds or by different processing across the entire web a different shrinkage behavior over the entire Width of the material web arise. So the problem is the uneven shrinkage not only on the edges of the Paper web limited.

It is an object of the invention a method in the Production of a running material web from paper or To represent cardboard, which is an equalization of the Shrinkage behavior of the material web over the entire Width causes.

Another object of the invention is a paper machine to carry out this method according to the invention To make available.

The inventors have recognized that due to the different shrinkage behavior of the paper web the width also others, essential for a good one Paper quality necessary quality criteria, for example the surface roughness or the strength values etc., change across the width depending on the shrinkage cross profile. It is said to be by equalizing the Shrinkage behavior of the paper web not only that Shrinkage behavior itself, but also with it correlated property parameters of the paper via the entire web width can be evened out.

Accordingly, it is proposed the method of manufacture to improve a paper or cardboard web in that the shrinkage cross profile of the web of material during its Creation process through sectional across the width Influencing the local composition of the Stock suspension with components with different Shrinkage behavior is evened out. Is this achieved, there is inevitably a reduction in the Differences in the properties of the material web over the entire width, in particular on its surface, for Example of roughness.

According to a particularly advantageous embodiment of the The procedure is proposed to strengthen the Shrinkage of a sectional area due to increased Feeding fibers and / or other substances with increased Cause shrinkage tendency, or in another Embodiment in the "normal" mixture of the stock suspension Fibers and / or other substances with less Tendency to shrink due to fibers and / or fabrics with increased Tendency to replace shrinkage.

Will decrease the shrinkage of a particular one desired sectional area, this can be done according to a another advantageous embodiment of the invention happen that more fibers and / or other substances with reduced shrinkage tendency in this section be, or that the "normal" fiber mixture through replaced a fiber mixture with reduced tendency to shrink becomes. The same applies in the opposite sense to a Increase in shrinkage.

The desired fibers are advantageously added and / or other shrinkage influencing substances in the Headbox. Regarding the possibilities of dosing or admixtures of material suspensions with different Fiber properties are based on earlier patent applications Applicant DE 37 41 603 A1, DE 40 19 593 A1, DE 44 22 907 A1, DE 42 37 304 A1 and DE 42 11 291 A1 referenced and their Disclosure content in full in the disclosure content this registration. In particular, regarding the cited prior art indicated that possible changes in basis weight caused by the metering of special fibers etc., could arise through a control mechanism in the known sectioned Headboxes with different material suspensions Concentration fed and controlled sectionally, can be compensated. Likewise, this is cited State of the art details how the feed from stock suspension of different properties to Casserole carried out and the basis weight cross-section the material web can be kept even.

According to a particularly advantageous development of the Procedure is used to achieve or obtain a desired cross section suggested that in the constant part the paper machine or board machine at least two Stock suspension flows with fibers with different Shrinkage behavior and / or with other shrinkage influencing substances are provided and in the area of the headbox by sectional mixing of at least two stock suspension streams with fibers different tendency to shrink, the shrinkage of the Material web is compensated across the machine width, while the basis weight cross profile and / or that Cross section of fiber orientation through sectional addition of White water flows are influenced so that the desired basis weight profiles are retained, or can be achieved.

A special embodiment of the method set out above is that as fibers with increased Shrinkage behavior long fibers and as fibers with reduced shrinkage behavior, short fibers are used become.

Another or also feasible variant is that as fibers with elevated Shrinkage behavior of highly digested fibers and as Low shrinkage fibers disrupted fibers are used.

In addition or as an alternative, there is the option of To use fibers whose shrinkage behavior due to a higher grinding is increased, or their Shrinkage behavior due to less grinding is lowered. Other substances can also be added, which influence the shrinkage, for example promote (CMC = Carboxymethyl cellulose) or inhibit (synthetic resins, Wet strength agent). Also the use of fibers respectively Fiber mixtures, the starting material of which is not wood - how for example plastic fibers - represents a possible one Variant.

According to the second task, the inventors propose one Paper machine with a constant part, a headbox with at least one stock suspension feed from the Constant part, a wet section, a press section and to design a dryer section in such a way that the Constant part has at least two areas different material suspensions with fiber mixtures provide different shrinkage behavior that Stock suspension feeds from the constant part to the Headbox at least two strands for the at least two have different substance suspensions and in the range the headbox has a large number of sectional mixing points are provided, which the substance suspensions with different shrink properties. As already explained above, the different Fiber mixtures are made by either Fiber material with longer or shorter fibers is used and / or more or less disrupted fibers and / or more or less ground fibers and / or the Shrinkage influencing substances for the substance suspension be used. According to their processing and / or Structure and / or their starting material produce this Fibers a different shrinkage behavior, which can ultimately be used over the entire Web width a uniform shrinkage behavior of the To generate material web.

• Berechnung des Schrumpfungsquerprofils durch On-Line-Mapping des Flächengewichtsquerprofils,
• Bestimmung der Regelgrößen zur Beeinflussung der Schrumpfung in M Sektionen über die Maschinenbreite an Hand eines Soll-Profils für die Schrumpfung und
• Betätigung von Aktuatoren zur Anpassung des Schrumpfungsquerprofils.

According to the concept of the invention, a method for controlling the shrinkage cross profile of a running material web made of paper or cardboard can also be used. In addition to the known process steps for controlling the basis weight with the process steps according to the preamble of claim 12, the following process steps are proposed:

• Calculation of the shrinkage cross profile by online mapping of the basis weight cross profile,
• Determination of the controlled variables for influencing the shrinkage in M sections across the machine width using a target profile for the shrinkage and
• Actuation of actuators to adjust the shrinking cross profile.

Regarding the online mapping known per se, reference is made to the Article "Requirements for a successful installation" in "Das Papier", 6/1998, 344-354, in particular chapter 6, pointed out and in particular its disclosure content at On-line mapping included in this content.

• Messung einer mit der Schrumpfung korrelierenden Größe,
• Berechnung des Schrumpfungsquerprofils durch Korrelation zwischen der gemessenen Größe und der Schrumpfung,
• Bestimmung der Regelgrößen zur Beeinflussung der Schrumpfung in M Sektionen über die Maschinenbreite an Hand eines Soll-Profils für die Schrumpfung und
• Betätigung von Aktuatoren zur Anpassung des Schrumpfungsquerprofils.

As an alternative to the mathematical determination of the shrinkage profile, the following process steps are proposed:

• Measurement of a quantity correlating with the shrinkage,
• Calculation of the shrinkage cross profile by correlation between the measured size and the shrinkage,
• Determination of the controlled variables for influencing the shrinkage in M sections across the machine width using a target profile for the shrinkage and
• Actuation of actuators to adjust the shrinking cross profile.

• Berechnung des Schrumpfungsquerprofils durch On-Line-Mapping des Flächengewichtsquerprofils, und zusätzlich
• Messung einer mit der Schrumpfung korrelierenden Größe und
• Berechnung des Schrumpfungsquerprofils durch Korrelation zwischen der gemessenen Größe und der Schrumpfung,
• Bestimmung eines gewichteten Schrumpfungsquerprofils aus dem gemessenen und dem berechneten Schrumpfungsquerprofil,
• Bestimmung der Regelgrößen zur Beeinflussung der Schrumpfung in M Sektionen über die Maschinenbreite an Hand eines Soll-Profils für die Schrumpfung und
• Betätigung von Aktuatoren zur Anpassung des Schrumpfungsquerprofils.

In addition, there is also the possibility of combining the above-mentioned processes and accordingly carrying out the following process steps:

• Calculation of the shrinkage cross profile by online mapping of the basis weight cross profile, and in addition
• Measurement of a size and correlating with shrinkage
• Calculation of the shrinkage cross profile by correlation between the measured size and the shrinkage,
• Determination of a weighted shrinkage cross profile from the measured and calculated shrinkage cross profile,
• Determination of the controlled variables for influencing the shrinkage in M sections across the machine width using a target profile for the shrinkage and
• Actuation of actuators to adjust the shrinking cross profile.

It should be noted that the above procedure both with a headbox with dilution water control, and can also be carried out with an adjustable aperture. At a dilution water controlled headbox exist Actuators for basis weight cross profile control mostly Valves to control the dilution flows. At aperture-controlled headboxes provide the adjustment spindles the headbox cover these actuators for the Basis weight cross section control.

In a particularly advantageous embodiment of the Control method shown can be in the profile control algorithm a decoupling between the basis weight cross section and Shrinkage cross profile are performed so that the mutual influences of the cross section regulations at least be avoided in the first order.

As a quantity to be measured, which correlates with the shrinkage and via which the shrinkage transverse profile is measured indirectly or is determined, are particularly suitable Smoothness and / or the strength of the paper web produced. However, others that are accessible for measurement can also be used Property sizes of the paper web can be used.

Further refinements of the inventions are in the Subclaims to the first procedural claim, or the first device claim and in the shown following figure descriptions.

It is understood that the above and Features of the invention not yet to be explained below only in the specified combination, but also in other combinations or used alone, without leaving the scope of the invention.

Further features and advantages of the invention result from the following description more preferred Embodiments with reference to the drawings.

Figur 1:

Typisches Schrumpfungsquerprofil einer Papierbahn;

Figur 2:

Schrumpfungsquerprofil nach erfindungsgemäßer Beeinflussung des sektionalen Schrumpfungsverhaltens durch sektionale Zusammensetzungsänderung des Stoffsuspension;

Figur 3:

Stoffauflauf nach dem Verdünnungswasserprinzip für die Anwendung des erfindungsgemäßen Verfahrens;

Figur 4:

Anfangsbereich einer Papiermaschine mit primären und sekundärem Stoffauflauf;

Figur 4a:

Ansicht A aus Figur 4;

Figur 5:

Anfangsbereich einer Papiermaschine mit Spritzrohr zu Auftragen von schrumpfungsbeeinflussenden Mitteln;

Figur 6:

Regelung des Schrumpfungsquerprofils.

The invention will be explained in more detail below with reference to the drawings. They represent:

Figure 1:

Typical shrink cross profile of a paper web;

Figure 2:

Shrinkage cross profile after influencing the sectional shrinkage behavior according to the invention by sectional compositional change of the stock suspension;

Figure 3:

Headbox according to the dilution water principle for the application of the method according to the invention;

Figure 4:

Initial area of a paper machine with primary and secondary headbox;

Figure 4a:

View A from Figure 4;

Figure 5:

Initial area of a paper machine with a spray tube for applying shrinkage-influencing agents;

Figure 6:

Regulation of the shrinkage cross profile.

Figure 1 shows a typical shrink cross profile of paper webs. The edge areas B ₁ and B ₃ are characterized by high shrinkage gradients and high absolute values of the shrinkage ε ₂ . In the central area B ₂ , the shrinkage is at a relatively low level and is almost straight and horizontal. This course of shrinkage is typical for many types of paper, but there are also many other forms of cross-section shrinkage. These depend on many parameters, such as the type of paper and the design of the process steps in paper production - for example the drying process. For example, cross-sectional shrinkage profiles with an asymmetrical course or with a non-linear course can also occur in the central region B _{2 of} the paper web.

FIG. 2 shows a shrinkage cross profile 1 after the proportion of fibers with a smaller tendency to shrink has been increased in the edge regions B ₁ and B _{3 of} the paper web - or - the proportion of fibers with a greater tendency to shrink has been reduced, while the composition of the stock suspension in the central region B ₂ the paper web has remained unchanged. In order to achieve the most linear possible shrinkage, it may also be necessary to section the edge areas across the width and to influence the shrinkage in the sections to different extents.

Figure 3 shows an example of a headbox according to the dilution water principle for the application of the method according to the invention, as described for example in the above-mentioned DE 40 19 593. In addition to the high and low consistency partial streams Q _H and Q _L , the suspension Q _{F is} fed in front of the turbulence generator at several feed points 7, distributed over the headbox width. This suspension Q _F contains fibers which differ in their shrinkage behavior from the fibers which are contained in the suspension Q _H. For example, if the fibers in Q _{F have} a lower tendency to shrink than those in Q _H , the cross-sectional shrinkage profile 1 shown in FIG. 1 can be improved by increasing the sectional volume flow Q _F at the edges.

The feed points 7 for Q _F can be distributed uniformly or non-uniformly - for example only at the edges - over the width of the headbox. The geometry of the feed for Q _F can preferably be designed such that the sectional total volume flow at the outlet of the nozzle remains constant despite the variation of Q _F. Such a design of a headbox is described in detail in DE 42 11 291. Cross distribution pipes or central distributors can be used to distribute the suspensions over the headbox width.

FIG. 4 shows the initial area of a paper machine with a primary headbox 2, which applies stock suspension to a sieve 11. The screen 11 is deflected via rollers 12 and the dewatering of the stock suspension takes place in a known manner via dewatering elements 13, consisting of suction boxes and dewatering strips. Subsequent to the primary headbox 2, a secondary headbox 2.1 is provided, by means of which the stock suspension Q _{F can be applied in} sections metered over the machine width to the already existing stock suspension layer.

FIG. 4a shows view A from FIG. 4, in which the secondary headbox 2.1 is shown. The secondary headbox has a transverse distributor 3.1, via which the stock suspension Q _{F is} fed machine-wide to the first chamber 8.1 of the headbox. A plurality of valves 6 are interposed between the distributor 3.1 and the first chamber 8.1 of the headbox 2.1, which enables a metered supply of the suspension Q _F which is sectioned over the machine width. Following the first chamber 8.1 of the headbox, a turbulence generator 9.1 and a subsequent nozzle 10.1 are shown in a known manner.

FIG. 5 shows in a spatial representation the beginning of a four-wire paper machine with a headbox 2, to which the high and low consistent stock suspension streams Q _H and Q _{L are} fed. The headbox 2 distributes the stock suspension evenly over the screen 11. The screen 11 is deflected over a plurality of rollers 12 and then on the headbox 2 dewatering elements 13 are provided which dewater the fibrous layer lying on the screen 11. When viewed in the machine direction, behind the headbox 2 there is a spray pipe 17 running across the machine width. The spray tube 17 is supplied with the shrinkage-influencing material suspension Q _F , which according to the invention contains a fibrous mixture which differs in terms of its tendency to shrink from the fibrous mixture of the material suspension Q _H , or can also directly shrinkage-influencing substances, such as (CMC = carboxymethyl cellulose), via this spray tube 17. , Wet strength agents or the like can be supplied. The spray pipe 17 has a plurality of spray nozzles 15 and 16, which are arranged here by way of example only to the edges of the paper web and thus only the edges of the paper web with the suspension Q _F spray. The use of fibers or fiber mixtures, the starting material of which is not wood, such as plastic fibers, is also within the scope of the invention.

With the method described above and in the figures shown devices, it is now possible in the Production of a running material web from paper or Cardboard an equalization of the shrinkage behavior of the Effect material web over the entire web width.

FIG. 6 shows an exemplary shrinkage cross profile control on a paper machine. On the left is the manufacturing process of the paper web is shown very schematically, which shrink in the course of the manufacturing process experienced and ultimately led to the trolley. The Headbox 2 is an example here with one Known dilution water control to adjust the atro basis weight cross profile fitted. This points before the Trolley onto a machine-wide scanner that does the job atro / basis weight cross profile measures, a profile control algorithm feeds and the actuators, here N valves 7 of Dilution water supply with N sections, operated.

According to the invention, this regulation is expanded by the actual profile the shrinkage (shrinkage cross profile) over a known online mapping is calculated and with a Target profile for the shrinkage is compared. The The profile rule algorithm then determines the necessary ones Corrections and influenced via the actuator positioner the actuators for influencing shrinkage, which are shown here in Form of control valves 7 in the M sections of the feed lines for the liquid that affects shrinkage are.

The number of N sections of the dilution control and the M Sections of the shrinkage control are in the present Example the same, but can also be different fail. In particular, it can be advantageous to Sections for shrinkage regulation in the edge area are too fine subdivide than in the middle area of the paper web.

By changes in the addition of suspensions that affect shrinkage also change inevitably the basis weight profile. This one Changes in both their section and their Size can be predetermined, compensation can be made of the expected basis weight error already in Carry out anticipation procedure. The same principle is also reversely applicable. In the figure this is Possibility of compensation through the decoupling circuit between the two profile control loops. In this way you get a large degree of independence between the Basis weight control and shrinkage control.

In addition, one possibility is shown in dashed lines in FIG the indirect measurement of the shrinkage cross profile Measuring a size shown with the shrinkage correlated. For example, the Smoothness / surface roughness and / or the strength of the Paper web can be used. In the control process, this can measured profile now directly and alone or in combination can be used with the calculated shrinkage profile. If both profiles are used for regulation, then by a corresponding direction an optimization of the Control mechanism to be performed.

Reference list

1

shrinkage

2nd

primary headbox

2.1

secondary headbox

3rd

Distributor

3.1

Cross distributor

4th

container

5

Connecting line

6

Valves

7

Feed points / valves

8th

first chamber in the headbox

8.1

first chamber in the headbox

9

Turbulence generator

9.1

Turbulence generator

10th

jet

10.1

jet

11

scree

12th

Rollers

13

Drainage elements

14

Feed points

15, 16

Spray nozzles

17th

Spray tube

18th

hydration-influencing fluid intake

19th

Dilution water supply

20th

Stock suspension feed

Q _L

low-consistent stock suspension

Q _H

highly consistent stock suspension

Q _F

shrinkage influencing stock suspension

Claims (18)

Method for equalizing the property profile of a running material web made of paper or cardboard with at least the following process steps: 1.1 Create at least one machine-wide fabric suspension layer on a sieve (11) or between two sieves and 1.2 dewatering, pressing and drying of the material web resulting from the fabric suspension layer,
characterized in that 1.3 the shrinkage cross profile (1) of the material web during its creation process is made more uniform by influencing the local composition of the stock suspension across the width by changing the proportions of the components with different shrinkage behavior. A method according to claim 1, characterized in that an increase in the shrinkage of a sectional area is brought about by increased supply of fibers and / or other substances with an increased tendency to shrink. A method according to claim 1, characterized in that an increase in the shrinkage of a sectional area is brought about by the replacement of fibers with reduced tendency to shrink by fibers and / or other substances with increased tendency to shrink. Method according to one or more of claims 1-3, characterized in that a reduction in the shrinkage of a sectional area is brought about by an increased supply of fibers and / or other substances with a reduced tendency to shrink. Method according to one or more of claims 1-3, characterized in that the shrinkage of a sectional area is reduced by the replacement of fibers with an increased tendency to shrink by fibers and / or other substances with a reduced tendency to shrink. Method according to one or more of claims 1-5, characterized in that the desired fibers and / or other substances are added in the headbox and / or in the wet part. Method according to one or more of claims 1-6, characterized in that at least two stock suspension streams with fibers and / or other materials with different shrinkage behavior are provided in the constant part of the paper or board machine and in the area of the headbox by sectional mixing of at least two stock suspension streams with fibers and / or other materials with different tendencies to shrink, the shrinkage of the material web is compensated for over the machine width, while the basis weight cross profile and / or the fiber orientation cross profile is influenced by sectional metering of dilution water. Method according to one or more of claims 1-7, characterized in that long fibers and vice versa are used as fibers with an increased tendency to shrink. Method according to one or more of claims 1-8, characterized in that highly disintegrated fibers and vice versa are used as fibers with an increased tendency to shrink. Method according to one or more of claims 1-9, characterized in that the fibers which are ground higher as fibers with an increased tendency to shrink and vice versa are used. Process according to one or more of claims 1-10, characterized in that carboxymethyl cellulose (CMC) and / or other substances are used as agents for increasing the shrinkage and synthetic resins and / or wet strength agents and / or other substances are used for inhibiting shrinkage. Process for controlling the shrinkage cross profile of a running material web made of paper or cardboard with at least the following process steps: 12.1 measurement of the basis weight cross profile of the material web, 12.2 Determination of the controlled variables for adapting the basis weight in N sections across the machine width using a target profile for the basis weight and 12.3 actuation of actuators (7) to adapt the basis weight cross-section,
characterized by the following process steps: 12.4 Calculation of the shrinkage cross profile by online mapping of the basis weight cross profile, 12.5 Determination of the controlled variables for influencing the shrinkage in M sections across the machine width using a target profile for the shrinkage and 12.3 Actuation of actuators to adjust the shrinkage cross profile. Method according to the preamble of claim 12, characterized by the following method steps: 13.1 measurement of a quantity correlating with the shrinkage, 13.2 calculation of the shrinkage cross profile by correlation between the measured size and the shrinkage, 13.3 Determination of the controlled variables for influencing the shrinkage in M sections across the machine width using a target profile for the shrinkage and 13.4 Actuation of actuators to adjust the shrinking cross profile. Method according to the preamble of claim 12, characterized by the following method steps: 14.1 Calculation of the shrinkage cross profile by online mapping of the basis weight cross profile, and additionally 14.2 Measuring a size and correlating with shrinkage 14.3 calculation of the shrinkage cross profile by correlation between the measured size and the shrinkage, 14.4 determination of a weighted shrinkage cross profile from the measured and calculated shrinkage cross profile, 14.5 Determination of the controlled variables for influencing the shrinkage in M sections across the machine width using a target profile for the shrinkage and 14.6 Actuation of actuators to adjust the shrinkage cross profile. Method according to one of claims 12 - 14, characterized in that a decoupling between the basis weight cross profile and the shrinkage cross profile is carried out in the profile control algorithm. Method according to one of claims 12-15, characterized in that the adjustment of the shrinkage cross profile takes place by a method according to one of claims 1-11. Method according to one of claims 13 - 16, characterized in that the smoothness and / or the strength is used as the quantity to be measured, which correlates with the shrinkage. Paper or board machine with a constant part, a headbox and at least one stock suspension feed from the constant part, a wet section, a press section and a dryer section, whereby 18.1 in the area of the headbox, a large number of sectional feeds of material flows of different properties and their mixture is provided,
characterized in that 18.2 the constant part has at least two areas which provide different material suspensions with fiber mixtures with different shrinkage behavior, 18.3 the stock suspension feeds from the constant part to the headbox have at least two strands for the at least two different stock suspensions and 18.4 a plurality of sectional mixing points are provided in the area of the headbox, which bring the stock suspensions together with different shrinkage behavior.

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