• 专利附录
  • 专利说明
  • 权利要求
  • 类似技术
  • 同族专利
  • 引用文献
  • 法律状态
  • 优先权
    • 专利摘要:
    Method and apparatus for applying starch to a running fiber web, in particular to a testliner or a corrugated paper web, wherein first starch is applied either on one side or on both sides of the fibrous web and then the fiber web through one of a first roller and a second roller formed treatment press nip (Nip), characterized in that at least one of the first or the second roll, preferably both rolls, a hardness of 15 P & J (Pusey & Jones) or less.
    公开号:AT519598A2
    申请号:T50040/2018
    申请日:2018-01-19
    公开日:2018-08-15
    发明作者:
    申请人:Voith Patent Gmbh；
    IPC主号:
    专利说明:

    Summary
    Method and device for applying starch on a running fiber web, in particular on a testliner or a corrugated paper web, starch being applied either to one side or to both sides of the fiber web and then the fiber web by one of a first roller and a second roller formed treatment press nip (nip), characterized in that at least one of the first or the second roller, preferably both rollers, have a hardness of 15 P&J (Pusey & Jones) or less.
    (Figure 1) / 16
    Method and device for applying starch
    The invention relates to a method and an apparatus for treating a fibrous web. The invention is particularly directed to a method for applying starch according to the preamble of claim 1 and to a device for applying starch according to the preamble of claim 6.
    The production of paper, cardboard and packaging webs is experiencing an increasing use of waste paper due to the associated economic and environmental advantages. Waste paper is usually used as the sole source of fiber, especially for types such as testliner (TL) or corrugated medium (CM). Due to the increased number of recycling cycles, there has been a deterioration in the quality of the waste paper used for the types mentioned above. The accumulation of fillers and a reduction in the fiber quality due to mechanical and chemical fiber damage lead to a deterioration in various strength properties in the cartons and packaging papers produced.
    The addition of fillers such as mineral pigments (e.g. CaCOs, TiO2, sand ...) reduces the wet strength of the paper web. This causes an increased number of web breaks in production.
    The deteriorated fiber quality, for example the reduced fiber length, can be partially compensated for by treating the fibers with synthetic binders such as polymer latex. Alternatively, the fibrous web can be treated with natural binders such as starch. Since the use of polymer latex is usually expensive, the use of starch is often preferred.
    The use of starch has long been a standard practice. Starch can be fed directly into the fiber or sprayed onto a wet web in the forming section of a paper machine. However, starch is also applied more efficiently after the press section and a pre-dryer section. The starch can also be sprayed onto the fiber web here, but is usually sprayed with a / 16
    Film press or a size press applied. For example, the use of a size press is described in DE 10 2011 076718 in the case of an inferior secondary fiber in testliner production.
    Due to the mentioned deterioration in the quality of the fiber material and also due to the higher production speed for most types of paper including TL and CM, there is a need in the industry for an efficient procedure for further increasing the strength properties of the fiber web.
    The aim of the invention is therefore to provide a technologically and economically efficient procedure for increasing the strength of the fiber web. Another object of the invention is to provide an efficient method of applying starch to a running paper web.
    Another object of the invention is to provide a method for the stable production of testliner (TL) and corrugated paper (CM) even with a low quality of the raw material.
    The aforementioned objectives and those that will become clearer in the following were completely achieved by a method according to the features of claim 1 and by a device according to the features of claim 6.
    In terms of the method, the goal is achieved by a method for applying starch to a running fiber web, in particular to a testliner or a corrugated paper web, starch being applied either to one side or to both sides of the fiber web and then the fiber web by one of a first Roll and a second roller formed treatment press nip (nip), characterized in that at least one of these rollers, preferably both rollers, have a hardness of 15 P&J (Pusey & Jones) or less.
    P&J hardness is a common measure for rollers. It can be determined using commercially available devices, such as the P&J hardness tester Zwick 3108, which meets the requirements of ASTM D531-89.
    / 16
    Unless otherwise stated, the term hardness of a roller is understood to mean the hardness of the outer layer or the outer cover of the corresponding roller, even if the inner layers, i.e. H. the layers without contact with the fiber web may have a different hardness.
    The inventors surprisingly discovered that when one or two rollers with relatively high hardness are used in a treatment press nip, the starch can be transferred to the fiber web far more efficiently. The rolls in standard size presses or film presses today have a hardness of 20 P&J or more, which means that today's rolls are much softer than in the present invention. It has been shown that this harder roller improves the transfer of starch to the fiber web.
    The starch can be applied in all technically known application means, including but not limited to the following:
    The starch can be applied to only one side of the fiber web or to both sides at the same time.
    The starch can be applied directly to the fiber web, for example using spray technology or using sump technology.
    Alternatively, the starch can be applied indirectly. Starch can be applied to one roller or to both rollers, for example metered or sprayed on, and then transferred to the fiber web in the press nip between the rollers.
    Advantageous features of the inventive method are described in the subclaims.
    It may be beneficial to use even harder rollers. In some applications, at least one of the first or second rollers, preferably both rollers, has a hardness of 5 P&J (Pusey & Jones) or less, preferably 1 P&J or less.
    / 16
    In an advantageous variant, the treatment press nip can be formed from two hard rolls which have a hardness of 15 P&J and less. This combination can further improve the transfer of starch to the fiber web.
    In another advantageous variant, the treatment press nip can be formed from a hard roll with a hardness of 15 P&J and less and a softer roll. The softer roller can have a hardness of over 15 P&J, in particular over 20 P&J.
    The fibrous web according to the present invention can be a single-ply or a multi-ply web. The layers of the multilayer fibrous web can be formed in two, three or more forming sections and then joined together, usually before the inventive starch application. Such multilayer webs are common for TL and CM applications.
    As described above, the fibrous web can be made from a fibrous material which is produced from waste paper. The strength-generating effect of the invention is particularly useful here.
    To further improve the starch transfer, the line pressing force of the treatment press nip can be selected between 30 kN / m and 140 kN / m, preferably between 60 kN / m and 100 kN / m.
    The production speed for TL and CM on modern machines is very high, at least over 800 m / min. The standard speed is over 1000 m / min and goes up to 1500 m / min or even reaches 1900 m / min. At such high speeds, efficient starch transfer is particularly important since the machines are usually operated at the upper strength limit of the web and the lack of strength of the fibrous web is probably a limit for the further increase in speed here.
    In some applications it may be useful to adjust the properties of the starch used accordingly. A solids content of the starch can be chosen between 6% and 25%, preferably between 8% and 18%.
    / 16
    A viscosity between 5 mPas and 60 mPas, preferably between 10 mPas and 40 mPas of strength, can be selected.
    The combination of the above-mentioned solids contents and viscosity has proven to be particularly advantageous.
    Unless otherwise stated, viscosity values in this application are always Brookfield viscosities, measured at 50 ° C. and 100 min -1 .
    The starch can be applied at a temperature between 50 ° C and 80 ° C.
    After applying the starch and drying it further, the fiber web is wound on a roll. In some preferred applications, e.g. B. for TL and CM, the grammage of the fiber web on the reel can be between 60 g / m 2 and 250 g / m 2 , more often between 90 g / m2 and 170 g / m2.
    In a preferred embodiment of the method, the starch application is set in the inventive method step so that the starch content of the fiber web on the roller apparatus is between 2.5% and 6% of the grammage. The amount of starch is usually sufficient to achieve the desired increase in strength properties.
    In another preferred embodiment, the crowning of the rolls can be adapted in such a way that a homogeneous gap length to the treatment press gap is generated across the transverse direction (width) of the rolls.
    Device-wise, the goal is achieved by a device for applying starch to a running fibrous web, comprising: a first roller and a second roller positioned to form a treatment press nip for the fibrous web, and means for direct or indirect application of Starch on the fibrous web, characterized in that at least one of the first or the second roller, preferably both rollers, has a hardness of 15 P&J (Pusey & Jones) or less.
    Advantageous features are again described in the subclaims.
    / 16
    It may be beneficial to use even harder rollers. In some applications, at least one of the first or second rollers, preferably both rollers, has a hardness of 5 P&J (Pusey & Jones) or less, preferably 1 P&J or less.
    In an advantageous embodiment, the treatment press nip can be formed from a hard roll with a hardness of 15 P&J and less and a softer roll. The softer roller can have a hardness of over 15 P&J, in particular over 20 P&J. This combination can further improve the transfer of starch to the fiber web.
    In preferred embodiments of the application device, the diameters of the first roller and the second roller are the same or differ by less than 10%.
    Depending on the fiber web and also on the production speeds, such a relative hard nip can cause undesired vibrations for the glue application. If the two rollers are of the same size or approximately the same size, this tendency to oscillate can be reduced, which improves the running stability of the machine.
    It is usually advantageous if the diameters of the first roller and / or the second roller are between 0.25 m and 2 m, in particular between 0.7 m and 1.8 m.
    In another preferred embodiment of the device, the first roller has a cover, which comprises a metal or a ceramic with a layer thickness between 50 μm and 150 μm, and / or the second roller has a cover, which is either a rubber, a polyurethane or a composite material with a layer thickness between 10 mm and 20 mm.
    Various aspects have to be considered when selecting the layers. The hardness desired according to the invention must first be achieved. In addition, a higher layer thickness can increase the potential runtime of the roller. In the case of rolls with a thicker outer layer, for example, the probability is higher that / 16
    Ί unwanted vibrations occur. The values given above represent an optimal compromise for many applications.
    It should be noted that basically any type of roller customary in the industry can be used in the device. In some embodiments, for example, it can be advantageous if at least one of the rollers is a shoe roller or a deflection-controlled roller.
    The positioning of the rollers can be chosen freely. The first and the second roller can be arranged laterally next to one another with a fiber web running vertically through the press nip.
    Alternatively, they can be arranged one above the other with a horizontally continuous path. But an inclined positioning is also possible. If the first and second rollers have different hardnesses, regardless of their general positioning, it may be preferable to take the softer roller to the higher position.
    In another preferred embodiment, at least one of the first and second rolls has sensor means for measuring the pressing force in the roll gap. In a more preferred embodiment, these sensor means are measuring means for determining a cross profile of the pressing force. These means can include fiber-optic sensors, one or more sensors based on piezo elements or film sensors.
    If the first and second rollers are of different hardness, it may be advantageous to position the sensor means on or in the softer roller. In a more preferred embodiment, these sensor means are also able to determine the length of the treatment press gap (for example the length in the machine direction), in particular over the entire transverse direction (width) of the treatment press gap.
    On the basis of the measurements of these sensor means it is possible, for example, to adjust the crowning of a roll and / or the pressing force acting in the roll gap to / 16 in order to adjust the conditions in the treatment press gap depending on the properties of the product produced, such as sheet thickness, grammage or quality of the used fiber material, adjust and optimize the transfer of starch to the web.
    The invention is described in more detail below with reference to the accompanying drawings:
    FIG. 1 shows a schematic view of a device according to one aspect of the invention.
    Figure 2 shows a schematic view of a device according to another aspect of the invention.
    FIG. 3 shows a schematic view of a device according to another aspect of the invention.
    Figures 4a and 4b show different embodiments of a roller with sensor means according to another aspect of the invention.
    According to one aspect of the invention, the device in FIG. 1 comprises a first roller 1 and a second roller 2, which form a treatment press nip 6. The fibrous web 5, which can be, for example, a test liner web (TL) or a corrugated paper web (CM) 5, runs through the press nip 6. Since the rollers are positioned in an oblique position, the web 5 also runs in an oblique direction, preferably in one Angle of about 45 ° to the horizontal.
    Here the starch is applied to the surface of the rollers 1, 2 by two metering devices 3 and from there transferred to the web 5 in the press nip. In order to achieve a better transfer of the starch to the web, one roller 1,2 or both rollers 1,2 have a hardness of 15 P&J (Pusey & Jones) or less. In particular, at least one roller can have a hardness of less than 5 P&J or even less than 1 P&J.
    In the example of FIG. 1, the diameter of the rollers 1, 2 is selected to be the same size in the range between 0.7 m and 1.8 m, but can also be larger or smaller depending on the application.
    / 16
    The starch used can have a solids content of between 6% and 25%, preferably between 8% and 18%.
    In addition, a viscosity between 5 mPas and 60 mPas, preferably between 10 mPas and 40 mPas of strength, can be selected.
    The pressing force of the press nip 6 can be set in the range between 30 kN / m and 140 kN / m, preferably between 60 kN / m and 100 kN / m. For example, one roller 1, 2 can be selected so that it comprises a layer of ceramic or metal, while the other roller comprises a layer of rubber, polyurethane or a composite material.
    The typical amount of starch transferred with a device according to the invention is usually between 2.5% and 6% of the grammage.
    Figure 2 shows an embodiment of another aspect of the invention.
    While the device according to FIG. 2 can have rollers 1, 2 similar to the device in FIG. 1, these are arranged side by side and the fiber web 5 runs vertically through the press nip. In this embodiment, the starch is applied to the rollers 1, 2 via spray devices 3a.
    It should be noted that in a similar embodiment, the starch could be sprayed directly onto the running web from the spray devices 3a instead of onto the rollers 1, 2 before the web enters the press nip.
    All features mentioned for the embodiment of FIG. 1, which relate to the roll size, roll hardness or roll composition, the pressing force and the starch properties, also apply to the embodiment of FIG. 2.
    The embodiment of Figure 3 is very similar to the embodiment of Figure 2. It differs only in the way the starch is applied to the fiber web 5. The embodiments of FIGS. 1 and 2 show an indirect application, at which thickness is first applied to the first and second rollers 1, 2 and transferred to the web 5 in the treatment press nip 6. In contrast, FIG. 3 shows an embodiment with direct application. Here the thickness of spray devices 3a is sprayed onto the web 5 at the same time before it passes through the treatment press nip 6.
    / 16
    Devices such as the embodiments shown in the figures can be used to carry out methods according to the invention.
    FIGS. 4a and 4b show how a first or a second roller 1, 2 comprises a set of sensor means 4 for measuring the line force in the press nip. The sensor means 4 in these examples are connected by a signal carrier 10. The signal carrier can carry electrical or optical signals, depending on the nature of the measuring equipment.
    In Figure 4a, all measuring means are arranged along a line in the transverse direction. In the embodiment in FIG. 4b, the sensor means are arranged spirally around the circumference of the roller 1, 2.
    The sensor means 4 can, for example, be contained in the outer layer 6 or in the cover of the roller 1, 2 or be positioned between the outer layer and the next layer.
    / 16
    权利要求:
    Claims (11)
    [1]
    Expectations
    1. A method for applying starch on a running fibrous web (5), in particular on a test liner (5) or a corrugated paper web (5), starch being applied either to one side or to both sides of the fibrous web (5) and the The fiber web (5) is then passed through a treatment press nip (6) formed from a first roller (1) and a second roller (1), characterized in that at least one of the first or the second roller (1, 2), preferably both rollers (1, 2), have a hardness of 15 P&J (Pusey & Jones) or less, preferably 5 P&J or less, most preferably 1 P&J or less.
    [2]
    2. The method according to claim 1, characterized in that the first roller (1) and the second roller (2) have a hardness of 15 P&J or less, preferably 5 P&J or less, most preferably 1 P&J or less.
    [3]
    3. The method according to any one of the preceding claims, characterized in that the pressing force of the treatment press nip (6) is set between 30 kN / m and 140 kN / m, preferably between 60 kN / m and 100 kN / m.
    [4]
    4. The method according to any one of the preceding claims, characterized in that the fibrous web (5) passes through the press nip at a speed of over 800 m / min, preferably between 1000 m / min and 1900 m / min.
    [5]
    5. The method according to any one of the preceding claims, characterized in that the starch with a solids content between 6% and 25%, preferably between 8% and 18%, and / or with a viscosity between 5 mPas and 60 mPas, preferably between 10 mPas and 40 mPas.
    [6]
    6. The method according to any one of the preceding claims, characterized in that the starch content of the fiber web (5) on the reel is between 2.5% and 6% of the grammage.
    [7]
    A device for applying starch to a running fiber web (5), comprising: a first roller (1) and a second roller (2) positioned in this way
    12/16
    - 12 are that they form a treatment press nip (6) for the fiber web (5) and means (3, 3a) for the direct or indirect application of starch to the fiber web (5), characterized in that at least one of the first roller ( 1) or the second roller (2), preferably both rollers (1, 2), have a hardness of 15 P&J (Pusey & Jones) or less, preferably 5 P&J or less, most preferably 1 P&J or less.
    [8]
    8. The device according to claim 7, characterized in that the diameters of the first roller (1) and the second roller (2) are the same or differ from one another by less than 10%.
    [9]
    9. Device according to one of claims 7 or 8, characterized in that the diameter of the first roller (1) and / or the second roller (2) between 0.25 m and 2 m, in particular between 0.7 m and 1, 8 m.
    [10]
    10. Device according to one of claims 7 to 9, characterized in that the first roller (1) has a cover (6) which comprises a metal or a ceramic with a layer thickness between 50 microns and 150 microns, and / or the second Roller has a cover (6) which comprises either a rubber, a polyurethane or a composite material with a layer thickness between 10 mm and 20 mm.
    [11]
    11. Device according to one of claims 7 to 10, characterized in that at least one of the first roller (1) or the second roller (2) comprises sensor means (11) for measuring the pressing force.
    13/16
    1.3
    类似技术:
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    同族专利:
    公开号 | 公开日
    DE102018100924A1|2018-08-02|
    AT519598A3|2019-08-15|
    FI127948B|2019-05-31|
    FI20170013L|2018-08-02|
    AT519598B1|2019-12-15|
    引用文献:
    公开号 | 申请日 | 公开日 | 申请人 | 专利标题
    SE427805B|1978-12-20|1983-05-09|Inventing Ab|SET AND ESTABLISHMENT FOR OPTIONAL TREATMENT, SUCH AS SINGLE OR DOUBLE COATING, IMPREGNATION OR SURFACE OF A CURRENT COAT.|
    US20110003079A1|2008-03-21|2011-01-06|Takehiro Yoshimatsu|Processes for preparing coated papers|
    CN102076911B|2008-06-20|2013-03-13|国际纸业公司|Composition and recording sheet with improved optical properties|
    FI124591B|2010-12-01|2014-10-31|Valmet Technologies Inc|METHOD AND EQUIPMENT FOR THE MANUFACTURE OF PAPER OR PAPERBOARD|
    FI20115400A|2011-04-26|2012-10-27|Metso Paper Inc|Roll coating and process for making it|
    DE102011076718A1|2011-05-30|2012-12-06|Metso Paper, Inc.|Producing coated paper or cardboard useful for flexographic printing, comprises providing paper or cardboard with pigment coating comprising porous layer|
    JP5682460B2|2011-06-07|2015-03-11|王子ホールディングス株式会社|Method for producing coated paper for printing|
    FI126292B|2015-08-20|2016-09-15|Valmet Technologies Oy|DEVICE FOR PROCESSING FIBERS|EP3875684A1|2018-08-30|2021-09-08|Valmet Technologies Oy|Method of treating a fiber web and a treatment system for treatment of a fiber web|
    EP3842591A1|2019-12-23|2021-06-30|Andritz Küsters GmbH|Device for applying an applied medium|
    DE102020117953A1|2020-07-08|2022-01-13|Voith Patent Gmbh|Coating installation and method for coating|
    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    FI20170013A|FI127948B|2017-02-01|2017-02-01|Method and device for starch application|
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