• 专利附录
  • 专利说明
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    • 专利摘要:
    17 ABSTRACT A ply for a paper and paperboard made from a ply substrate material,wherein the ply comprises a hybrid material, in an amount of 1-25 wt-% of theply, wherein the hybrid material is introduced into a target suspension of theshort circulation of a fibrous web forming process of a fibrous web machine, inan in-line process, wherein said target suspension forms the ply substratematerial, and the hybrid material comprises an alkaline earth carbonateprecipitated onto or into fibers or fibrils of a nanofibrillated polysaccharide. Figure elected for publication: 2
    公开号:SE1251279A1
    申请号:SE1251279
    申请日:2012-11-09
    公开日:2014-05-10
    发明作者:Olavi Imppola；Jouni Matula；Jussi Matula；Karri Tahkola；Isto Heiskanen；Matti Väkeväinen；Jari Räsänen
    申请人:
    IPC主号:
    专利说明:

    AWAPATENT AB Kontor/HandläggareLinköping/Sofia Zander Jakobsson/SZJ Vår referens SE-11013130 Ansökningsnr 1 PLY FOR A BOARD FROM AN lN-LINE PRODUCTION PROCESS Technical field The present document relates to a ply for a paper or paperboardcomprising a hybrid material, produced through a method for an inlineproduction method in a paper making process.
    BackgroundFillers are added to a papermaking pulp to fill void spaces not occupied with the fibres and thus to smoothen the surface of paper. They improve forexample paper printability, dimensional stability, formation, and gloss. Addedto this, optical paper properties like opacity, light scattering, and brightnessare usually improved, because fillers' light scattering coefficient andbrightness that are often higher than those of pulp.
    Fillers are low-priced when comparing to wood fibers and thus alsoused in a paper manufacturing to reduce the costs of papermaking rawmaterials. Also drying of the filler-bearing paper web requires less energy. lnspite of their inexpensive price and positive effects to paper properties, fillershave also negative features. They interfere inter-fiber bonding by adsorbing orprecipitating on fiber surfaces. Because of this, paper tensile strength andtensile stiffness are reduced and linting can appear in printing. Also abrasionon paper machine can increase because of fillers. Their retention is usuallyquite poor and it can cause two-sidedness on paper. ln packaging board grades, fillers are not typically used or used in a verylow amounts compared to other paper grades. Typical reasons for this arethat they increase weight of the board without giving strength properties andthat they reduce calibre in the same grammage. Calibre is most importantparameter for bending stiffness. Also the fillers reduce elastic modulus, whichis an important parameter for bending stiffness.
    High brightness bleached pulp is quite often used in the top ply of theboard. Target with this is to have higher brightness and generally improvedappearance of the board. Even on such cases only very low filler amountsare used and typically quite expensive fillers, such as TiO2, calclned kaolinetc., are used to optimize elastic modulus of the top ply and maximize boardbending stiffness. Quite often top ply grammage is optimized against 2 whiteness and visual appearance instead of optimizing it against maximalbending stiffness.
    Thus there would be a high need to improve whiteness and opacity of theboard top ply with maintaining board bending stlffness and same time use lowcost flllers.
    One quite typical filler used in paper making is precipitated calciumcarbonate (PCC). Typically the production of PCC has been producedseparately from the actual paper making process. PCC is normally producedat a dedicated plant located close the paper mill. ln WO 2011110744, a method and a reactor for in-line production ofcalcium carbonate (PCC) in connection with the production process of afibrous web is disclosed. This relates to in-line production of PCC into asuspension to be used in the production of the fibrous web, especiallypreferably directly into the flow of fibrous pulp, one of its partial pulp flows or afiltrate flow used in the production of fibrous pulp. This method has severaladvantages as reduced investment costs, since there is no need to have aseparate PCC plant. Further there is a reduced need of retention chemicalsas PCC is at least partially precipitated directly onto fibres. ln EP2287398A1 a method for obtaining a calcium carbonate, possiblyfibers and fiber fibril containing composite is obtained in which the calciumcarbonate particles, if needed with the fibrils and fibers are connected, whichis characterized by good dewatering capability and which for the manufactureof paper with a large amount of filler, with a great strength and having a largespecific volume. This invention is achieved by the combination of fivemeasures, the use of specific calcium carbonate particles, which is (d so) andhas a scalenohedral morphology and an average particle diameter of morethan 2 , 5 pm and a maximum of4 pm, by the setting of a weight ratio of fibrilsto calcium carbonate in the suspension before the coprecipitation of 0.2:1 to4:1, by the use of fiber fibrils and through the setting of a weight ratio ofcalcium carbonate into the fibrils before the coprecipitation of 0.02:1 to 0.2:1.However this method describes a traditional off-line precipitated calciumcarbonate process using carbon dioxide and milk of lime.
    There is thus a need for a new ply for a paper or paperboard and aprocess for the production of said board ply having a desirable visualappearance, but also an optimized elastic modulus.
    Summary lt is an object of the present disclosure, to provide an improved ply fora paper or paperboard which eliminates or alleviates at least some of thedisadvantages of the prior art plies.
    The object is wholly or partially achieved by a ply and a methodaccording to the appended independent ciaims. Embodiments are set forth inthe appended dependent claims, and in the following description anddrawings.
    According to a first aspect, there is provided a ply for a paper andpaperboard made from a ply substrate material, wherein the ply comprises ahybrid material, in an amount of 1-25 wt-% of the ply. The hybrid material isintroduced into a target suspension of the short circulation of a fibrous webforming process of a fibrous web machine, in an in-line process, wherein saidtarget suspension forms the ply substrate material, and the hybrid materialcomprises an alkaline earth carbonate precipitated onto or into fibers or fibrilsof a nanofibrillated polysaccharide According to the first aspect the ply may comprise the hybrid materialin an amount of 1 to 15 wt-%.
    The alkaline earth carbonate may be any one of a calcium carbonate, amagnesium carbonate and a combination of a calcium and magnesiumcarbonate.
    According to one embodiment the alkaline earth carbonate may be acalcium carbonate.
    According to yet an embodiment of the first aspect the nanofibrillatedpolysaccharide may be a microfibrillated cellulose.
    The hybrid material may thus be formed by a calcium carbonateprecipitated onto or into the fibers or fibrils of the microfibrillated cellulose(MFC). Said calcium carbonate may be added and formed into the targetsuspension as disclosed in WO 2011/110744 A2. The calcium carbonate mayaccording to this method be formed or precipitated directly onto the surface ofthe MFC. The precipitated calcium carbonate may therefore be a so calledPCC filler. The target suspension thus forms the ply substrate material orcomposition with the PCC filler formed therein and directly onto or into thefibers or fibrils of the MFC.
    The nano- och microfibrillated cellulose may be obtained throughconventional methods such as mechanical liberation of fibrils or by acidhydrolysis of cellulosic materials, e.g. disclosed in WO 2009021687 A1, orMFC suspension produced by enzymatic hydrolysis of Kraft pulp cellulose 4 following a mechanical treatment step, e.g. disclosed in WO2011004300 A1,acid hydrolysis followed by high pressure homogenization, e.g. disclosed inUS20100279019, or by any other means known to the skilled person. Theconcentration of MFC in such suspensions is usually about 1-6 wt-% and theremaining part is water and/or additives used to improve the production or tomodify the MFC.
    According to one embodiment of the first aspect said calciumcarbonate may be added or formed, and precipitated into the ply substratematerial through an in-line process and into a target suspension of a fibrousweb forming process of a fibrous web machine, substantially simultaneouslywith a suitable amount of an aqueous suspension of a microfibrillatedcellulose.
    Usage of microfibrillated cellulose/nanocellulose has been studied inpaper making quite widely. lt has been found out that even though MFCimproves strength properties (including elastic modulus - important for boardtop ply), it reduced porosity and increased drying shrinkage at the sametime. These, however, have negative effects on board making in the fact thatthe top ply porosity is reduced due to the addition of MFC, which leads to arisk of blowing or blistering. Drying will form steam inside of the board and asthis steam cannot escape fast enough due to reduced porosity, the board willbe easier delaminated.
    By combining the so called in-line PCC process (i.e. dosing of calciumcarbonate or carbon dioxide and milk of lime) with a simultaneous dosing orintroduction of MFC several improvements in top ply properties have beenobserved. This method allows for the incorporation of a hybrid material,comprising for instance calcium carbonate precipitated onto the fibers orfibrils of a microfibrillated cellulose, into the ply. This allows for an increasedwhiteness of ply of the board and also decrease cloudiness of white surfaceand an increased of the ply smoothness.
    This further allows for an increase in elastic modulus in the sameporosity and improved whiteness of the ply.
    By using in-line PCC there may be provided for reduced costs forprocess chemicals, and an increased board machine process purity, such asless web brakes, less dirty spots, no accumulations on pipelines. lt has surprisingly been found that precipitation of the PCC particleshappens most likely on the surface of fine particles that exists in the process waters, which is related to the surface energy, high surface area and pHproperties of these fine particles.
    By introducing the microfibrillated cellulose or “nanocellulose" (MFC)into the milk lime of the in-line calcium carbonate process the amount of finesneeded to obtain a satisfactory whiteness and visual appearance while stillbeing able to control the drying shrinkage and maintain the improvement inelastic modulus may be easily controlled, in that the larger part of the calciumcarbonate is precipitated onto/into MFC.
    Thus by introducing, or dosing, MFC into an in-line PCC process thereis provided a way to control the amount of fines needed, as the surface pHand chemistry of the MFC can be adjusted, and thus, the particle size anddimensions of the PCC that is introduced into the fiber flow or targetsuspension may be controlled, this means that the quality of the ply substratematerial can be controlled and improved in this manner.
    Also by having the PCC particles onto the MFC surface the porosity ofthe ply may be controlled, the drying shrinkage can be controlled and theimproved elastic modulus provided by the MFC may be maintained. Byhaving the PCC particles on the ply, whiteness and printability may beimproved without reduced bending stiffness.
    Since in-line PCC is a relatively cheap filler the costs of the board maybe reduced, in relation to using more expensive fillers.
    There is also an increased cleanliness of the ply and board makingmachine.
    The ply according to the first aspect may be any one of a top andbottom ply for a board.
    According to one embodiment of the first aspect the target suspensionof the fibrous web forming process may comprise at least one of the followingcomponents: virgin pulp suspension (long-fiber pulp, short-fiber pulp,mechanical pulp, chemo mechanical pulp, chemical pulp, microfiber pulp,nanofiber pulp), recycled pulp suspension (recycled pulp, reject, fiber fractionfrom the fiber recovery filter), additive suspension and solids-containingfiltrate and forming the ply substrate material.
    According to a second aspect there is provided an in-line productionmethod for providing a hybrid material for a ply for a board, the methodcomprising the following steps (i) providing a liquid flow of an alkaline earthcarbonate or at least one precursor thereof, in a target suspension, of theshort circulation and into the liquid flow of a paper making stock of a fiber web 6 machine by feeding the liquid flow of said alkaline earth carbonate or at leastone precursor thereof to the liquid flow of the short circulation, said targetsuspension forming a ply substrate material; and (ii) providing a suitableamount of a nanofibrillated polysaccharide substantially simultaneously withthe feeding of liquid flow of the alkaline earth carbonate or at least oneprecursor thereof, thereby forming a hybrid material, wherein the hybridmaterial comprises said alkaline earth carbonate precipitated onto or intofibers and/or fibrils of said nanofibrillated polysaccharide.
    According to the second aspect the alkaline earth carbonate may aprecipitated calcium carbonate, formed from a reaction between twoprecursor materials, said precursor materials being carbon dioxide and limemilk, wherein said carbon dioxide and lime milk being fed to the shortcirculation substantially simultaneously.
    By “lime milk” is also meant hydrated lime, builders lime, slack lime, orpickling lime.
    Further, the feeding into the short circulation may performed byinjecting the alkaline earth carbonate or precursor materials and/ornanofibrillated polysaccharide into the target suspension of the liquid flow ofthe paper making stock.
    According to one embodiment of the second aspect the feeding intothe short circulation may be performed by injecting at least either carbondioxide, lime milk and/or microfibrillated cellulose into the target suspension ofthe liquid flow of the paper making stock.
    The wherein the carbon dioxide, lime milk and/or microfibrillatedcellulose may be fed separately by injection.
    The microfibrillated cellulose may further be provided in the liquid flowof a paper making stock and the lime milk and carbon dioxide may be fedseparately or simultaneously by injection.
    According to one alternative the lime milk and microfibrillated cellulosemay be mixed prior to the injection into the liquid flow of a paper making stockand the carbon dioxide may be fed separately from the lime milk andmicrofibrillated cellulose mixture.
    According to another alternative the microfibrillated cellulose may bemixed with other optional additives and the mixture may be fed separatelyfrom the feeding of lime milk and carbon dioxide.
    According to yet an alternative of the second aspect the injection intothe liquid flow of a paper making stock may be performed from one more 7 several nozzles in a direction substantially transverse to the direction of theliquid flow, and at a flow rate that is higher than that of the liquid flow.
    The liquid flow of paper making stock may comprise at least one of thefollowing components: virgin pulp suspension (long-fiber pulp, short-fiberpulp, mechanical pulp, chemo mechanical pulp, chemical pulp, microfiberpulp, nanofiber pulp), recycled pulp suspension (recycled pulp, reject, fiberfraction from the fiber recovery filter), additive suspension and solids-containing filtrate.
    Brief Description of the DrawinqsEmbodiments of the present solution will now be described, by way ofexample, with reference to the accompanying schematic drawings.
    Fig. 1 shows schematically a short circulation arrangement accordingto prior art.
    Fig. 2 shows schematically a short circulation arrangement accordingto one embodiment of the invention.
    Figs 3a-b shows schematically a short circulation arrangementaccording to one alternative embodiment of the invention.
    Fig. 4 shows schematically a short circulation arrangement accordingto yet an alternative embodiment of the invention.
    Fig. 5 shows schematically a short circulation arrangement accordingto yet another alternative embodiment of the invention Description of EmbodimentsDefinition of nanofibrillated polvsaccharide This definition includes bacterial cellulose or nanocellulose spun witheither traditional spinning techniques or then with electrostatic spinning. lnthese cases, the material is preferably a polysaccharide but not limited tosolely a polysaccharide.
    Also whiskers, microcrystalline cellulose or regenerated cellulose andnanocellulose crystals is included in this definition.
    Definition of microfibrillated cellulose The microfibrillated cellulose (MFC) is also known as nanocellulose. lt is amaterial typically made from wood cellulose fibers, both from hardwood orsoftwood fibers. lt can also be made from microbial sources, agricultural fibers such as wheat straw pulp, bamboo or other non-wood fiber sources. lnmicrofibriilated cellulose the individual microfibrils or elementary fibrils havebeen partly or totally detached from each other. A microfibriilated cellulosefibril is normally very thin (~20 nm) and the length is often between 100 nm to10 pm. However, the microfibrils may also be longer, for example between10-200 pm, but lengths even 2000 pm can be found due to wide lengthdistribution. Fibers that has been fibrillated and which have microfibrils on thesurface and microfibrils that are separated and located in a water phase of aslurry are included in the definition MFC. Furthermore, whiskers are alsoincluded in the definition MFC.
    Even though it is known that microfibriilated cellulose (MFC) increaseelastic modulus of paper, microfibriilated cellulose (MFC) is not good for topply of board due to reduced porosity (poor porosity/elastic modulus ratio) andincreased drying shrinkage.
    However there is a need to increase whiteness of board grades, butthis has not been possible previously efficiently with fillers due to reduction ofelastic modulus. ln duplex type boards (3 ply board with brown middle ply)this is done mainly with top ply grammage increase (and 3% filler).
    Definition of precipitated calcium carbonate (PCC) Almost all PCC is made by direct carbonation of hydrated lime, knownas the milk of lime process. Lime (CaO) and carbon dioxide, which can becaptured and reused is formed in this process. The lime is slaked with waterto form Ca(OH)2 and in order to form the precipitated calcium carbonate(insoluble in water) the slaked lime is combined with the (captured) carbondioxide. The PCC may then be used in paper industry as a filler orpigmentation, mineral or coating mineral or in plastic or barrier layers. lt canalso be used as filler in plastics or as additive in home care products, toothpastes, food, pharmaceuticals, paints, inks etc.
    Definition of in-line precipitated calcium carbonate process By “in-line production” is meant that the precipitated calcium carbonate(PCC) is produced directly into the flow of the paper making stock, i.e. thecaptured carbon dioxide is combined with slaked lime milk inline, instead ofbeing produced separately from the paper making process. Separateproduction of PCC further requires the use of retention chemicals to have thePCC adsorbed or fixed onto the fibers. An in-line PCC process is generally 9 recognized as providing a clean paper machine system, and there is areduced need of retention chemicals. An in-line PCC process is for instancedisclosed in WO2011/110744.
    Fig. 1 shows a prior art method for inline production of precipitatedcalcium carbonate, as disclosed in US2011/0000633 and a schematicprocess arrangement for a paper making machine 2. The white water F, iscarried to e.g. a mixing tank or filtrate tank 4, to which various fibrouscomponents are introduced for the paper making stock preparation. Fromfittings at least one of virgin pulp suspension (long-fiber pulp, short-fiber pulp,mechanicai pulp, chemomechanical pulp, chemical pulp, microfiber pulp,nanofiber pulp), recycled pulp suspension (recycled pulp, reject, fiber fractionfrom the fiber recovery filter), additive suspension and solids-containingfiltrate is carried to the mixing tank, and from there conveyed by a mixingpump 14 to a vortex cleaner 16, where heavier particles are separated. Theaccept of the vortex cleaning continues to a gas separation tank 18, where airand/or other gases are removed from the paper making stock. The papermaking stock is then transported to a feed pump 20 of the headbox, whichpumps the paper making stock to a so-called headbox screen 22, where largesized particles are separated from the paper making stock. The accept factionis carried to the paper making machine 2 through its headbox. The shortcirculation of fiber web machines producing less demanding end productsmay, however, not have a vortex cleaner, gas separation plant and/orheadbox. ln the prior art process the PCC production is performed in the shortcirculation of the paper making machine, before the vortex cleaning plant 16.The carbon dioxide (C02) is injected on the pressure side of the vortexcleaner and the lime milk (MoL) is injected a few meters after the carbondioxide has dissolved in the same pipe. lt is however conceivable that thisPCC production could take place closer to the headbox, or that the distancebetween the injectors is very small, virtually injecting carbon dioxide and limemilk at the same location in the short circulation. This depends on the requirements of the end product and the design of the paper making machine.
    According to the invention there is provided an inline productionmethod where additives, such as carbon dioxide, milk lime etc., are fed intothe short circulation of the paper making machine, i.e. into the fibrous web orpaper making stock, and where a suitable amount of a microfibrillated cellulose, MFC, is provided substantially simultaneously as these additivesare being fed into the short circulation.
    What is meant by “substantially simultaneously” may vary as describedbelow, however in this context it is to be understood that the MFC is providedsuch that the additive, such as e.g. PCC may be formed, i.e. crystailized ontoor into the MFC.
    Where two or more additives are fed into the short circulation these arepreferably allowed to react with one another, which means that they are fedinto the short circulation in a manner which allows for the additives to react, inthe case of lime milk and carbon dioxide, such that precipitated calciumcarbonate is formed onto or into the MFC.
    According to one embodiment of the present invention, an in-line PCCprocess is combined with the dosage of MFC into the in-line PCC process.This provides for a completely new way of providing PCC to for instance afibrous web in a paper making process. ln one embodiment of the present invention, as shown in Fig. 2 limemilk, carbon dioxide and MFC are injected separately into the short circulationand fibrous web of the paper making machine. ln an alternative embodiment, as shown in Figs 3a and 3b the MFC isprovided e.g. in the preparation of the paper making stock, and thus ispresent in the paper making stock and the carbon dioxide and lime milk areinjected separately (Fig. 3a) or simultaneously (Fig. 3b) into the shortcirculation. ln yet an alternative embodiment, as shown in Fig. 4 the lime milk andthe MFC are mixed before the injection into the short circulation and thecarbon dioxide is injected separately from this mixture. ln yet another alternative embodiment the, as shown in Fig. 5, the MFCis mixed with other additives and this mixture is injected separately from thelime milk and carbon dioxide. ln all of the above described embodiments it is to be understood thatthe order of injection of the additives, i.e. lime milk, carbon dioxide, MFC andpossibly other additives may occur in a different order or at a different stage inthe short circulation. lt is conceivable that the injection occurs very close tothe headbox, or that the MFC is dosage prior to the addition of the carbondioxide or that the distances between the “injection points” is shorter or longerthan described above. Thus the MFC, lime milk and carbon dioxide may beinjected into the short circulation substantially at the same injection point. 11 The point or point where the injection takes place thus forms a “PCCreaction zone”.
    According to one embodiment the MFC provides for an increased fibersurface area onto which the lime milk can adsorb and/or PCC mayprecipitate.
    By modifying and adjusting the surface energy, reaction sites, pH andsurface chemistry of the MFC there is provided a completely new way ofcontrolling how the PCC crystals are formed on the surface of the MFC. Thecrystals formed on the surface of the MFC particle may take on differentshapes and configurations.
    By combining the in-line PCC process with a dosing or introduction ofMFC there is provided a new way of controlling the paper making processwithout, e.g. modifying the entire white water circulation.
    Further in the application of the fibrous web forming a top ply, severalimprovements have been observed, such as an increased whiteness of boardand also decrease cloudiness of white surface and an increase of the boardsmoothness. There is also an increased elastic modulus in the same porosityand improved whiteness.
    By using PCC there is a reduced cost for process chemicals, and anincrease in board machine process purity, such as less web brakes, less dirtyspots, no accumulations on pipelines. ln EP1219344 B1 there a method and apparatus which are particularlywell applicable to homogeneous adding of a liquid chemical into a liquid floware disclosed. ln this method a mixer nozzle is utilized, and the liquidchemical is fed into the mixer nozzle and a second liquid is introduced into thesame mixer nozzle, such that the chemical and second liquid are brought intocommunication with each other substantially at the same time as the chemicalis discharged together with the second liquid from the mixer nozzle at highspeed into the process liquid, and transverse to the process liquid flow in theflow channel. The chemical and second liquid may be discharged directly intothe fiber suspension flowing towards the headbox of the paper machine. Thesecond liquid may be a circulation liquid from the paper process, such aswhite water, or may be fresh water depending on the requirements of theliquid chemical to be added to the fiber flow. The flow speed from the mixernozzle may be around five times the flow speed of the fiber suspension intowhich the chemical and second liquid is discharged. 12 By using this type of fast addition of the PCC and MFC there isprovided a way of forming the PCC crystals on the MFC very quickly. Thisfast formation of the PCC crystals provides for new PCC-fiber complexes inwhich the PCC grows in a cubic formation around the strings and wires of theMFC. This provides for less steric hindrance and provides great strength forthe structure. A further advantage of this new crystal formation is that itprovides for a very clean process without any up-build of PCC in pipes etc.
    Also as the PCC is formed around the MFC or nanocellulose, and isbound very tightly to the fibre the hazards of using such small particles as theMFC is greatly reduced.
    According to one embodiment the amount of precipitated calciumcarbonate in the ply is less than 25 wt-%, more preferred less than 15 wt-%and even more preferred less than 8 wt-% and most preferred below 6 wt-%.
    权利要求:
    Claims (20)
    [1] 1. A ply for a paper and paperboard made from a ply substratematerial, wherein the ply comprises a hybrid material, in an amount of 1-25%-wt of the ply, characterized in that the hybrid material is introduced into a target suspension of the shortcirculation of a fibrous web forming process of a fibrous web machine, in anin-line process, wherein said target suspension forms the ply substratematerial, and in that the hybrid material comprises an alkaline earth oarbonateprecipitated onto or into fibers and/or fibrils of a nanofibrillatedpolysaccharide.
    [2] 2. The ply as claimed in claim 1, wherein the ply comprises the hybridmaterial in an amount of 1 to 15 wt-%.
    [3] 3. The ply as claimed in claim 1, wherein the alkaline earth oarbonateis any one of a calcium oarbonate, a magnesium oarbonate and acombination of a calcium and magnesium oarbonate.
    [4] 4. The ply as claimed in claim 3, wherein the alkaline earth oarbonateis a calcium carbonate.
    [5] 5. The ply as claimed in any one of the preceding claims, wherein thenanofibrillated polysaccharide is any one of a microfibrillated cellulose, aregenerated cellulose and a nanofibril from a non-wood material.
    [6] 6. The ply as claimed in any one of the preceding claims, wherein saidcalcium carbonate is added or formed, and precipitated into the ply substratematerial through an in-line process and into a target suspension of a fibrousweb forming process of a fibrous web machine, substantially simultaneouslywith a suitable amount of an aqueous suspension of a microfibrillatedcellulose. 14
    [7] 7. The ply as claimed in any one of the preceding claims, wherein theply is any one of a top and bottom ply for a board.
    [8] 8. The ply as claimed in any one of the preceding claims, wherein thetarget suspension of the fibrous web forming process comprising at least oneof the following components: virgin pulp suspension (long-fiber pulp, short-fiber pulp, mechanical pulp, chemo mechanical pulp, chemical pulp,microfiber pulp, nanofiber pulp), recycled pulp suspension (recycled pulp,reject, fiber fraction from the fiber recovery filter), additive suspension andsolids-containing filtrate and forming the ply substrate material.
    [9] 9. An in-line production method for providing a hybrid material for a plyfor a board, the method comprising the following steps: (i) providing a liquid flow of an alkaline earth carbonate or at least oneprecursor thereof, in a target suspension, of the short circulation and into theliquid flow of a paper making stock of a fiber web machine by feeding theliquid flow of said alkaline earth carbonate or at least one precursor thereof tothe liquid flow of the short circulation, said target suspension forming a plysubstrate material; and (ii) providing a suitable amount of a nanofibrillated polysaccharidesubstantially simultaneously with the feeding of liquid flow of the alkaline earthcarbonate or at least one precursor thereof, thereby forming a hybrid material,wherein the hybrid material comprises said alkaline earth carbonateprecipitated onto or into fibers and/or fibrils of said nanofibrillatedpolysaccharide.
    [10] 10. The method as claimed in claim 9, wherein the alkaline earthcarbonate is any one of a calcium carbonate, a magnesium carbonate and acombination thereof.
    [11] 11. The method as claimed in any one of claims 9 or 10, wherein,when there are two or more precursors, the method further comprisesallowing these to react with one another.
    [12] 12. The method as claimed in claim 11, wherein the precursors arecarbon dioxide and lime milk, and wherein said carbon dioxide and lime milkbeing fed to the short circulation.
    [13] 13. The method as claimed in any one of claims 9-12, wherein thefeeding into the short circulation is performed by injecting the alkaline earthcarbonate or at least one precursor thereof and/or nanofibrillatedpolysaccharide into the target suspension of the liquid flow of the papermaking stock.
    [14] 14. The method as claimed in claim 13, wherein the feeding into theshort circulation is performed by injecting at least either carbon dioxide, limemilk and/or microfibrillated cellulose into the target suspension of the liquidflow of the paper making stock.
    [15] 15. The method as claimed in any one of claims 9-14, wherein thecarbon dioxide, lime milk and/or microfibrillated cellulose are fed separatelyby injection.
    [16] 16. The method as claimed in any one of claims 9-14, wherein themicrofibrillated cellulose is provided in the liquid flow of a paper making stockand the lime milk and carbon dioxide are fed separately or simultaneously byinjection.
    [17] 17. The method as claimed in any one of claims 9-14, wherein limemilk and microfibrillated cellulose are mixed prior to the injection into the liquidflow of a paper making stock and the carbon dioxide is fed separately fromthe lime milk and microfibrillated cellulose mixture.
    [18] 18. The method as claimed in any one of claims 9-14, wherein themicrofibrillated cellulose is mixed with other optional additives and the mixtureis fed separately from the feeding of lime milk and carbon dioxide.
    [19] 19. The method as claimed in any one of claims 9-18, wherein theinjection into the liquid flow of a paper making stock is performed from onemore several nozzles in a direction substantially transverse to the direction ofthe liquid flow, and at a flow rate that is higher than that of the liquid flow.
    [20] 20. The method as claimed in any one of claims 9-19, wherein theliquid flow of paper making stock comprises at least one of the following 16 components: virgin pulp suspension (long-fiber pulp, short-fiber pulp,mechanical pulp, chemomechanicai pulp, chemical pulp, microfiber pulp,nanofiber pulp), recycled pulp suspension (recycled pulp, reject, fiber fractionfrom the fiber recovery filter), additive suspension and soiids-containingfiltrate.
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    同族专利:
    公开号 | 公开日
    CN105121741A|2015-12-02|
    UY35122A|2014-05-30|
    CN105121741B|2021-04-20|
    BR112015010600A2|2017-07-11|
    EP2917404B1|2018-07-11|
    SE538246C2|2016-04-12|
    PL2917404T3|2019-03-29|
    US20150315748A1|2015-11-05|
    WO2014072912A1|2014-05-15|
    EP2917404A4|2016-06-01|
    US9863093B2|2018-01-09|
    ES2689549T3|2018-11-14|
    EP2917404A1|2015-09-16|
    CA2890311A1|2014-05-15|
    引用文献:
    公开号 | 申请日 | 公开日 | 申请人 | 专利标题
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    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    SE1251279A|SE538246C2|2012-11-09|2012-11-09|Cardboard layers in an in-line production process|SE1251279A| SE538246C2|2012-11-09|2012-11-09|Cardboard layers in an in-line production process|
    UY0001035122A| UY35122A|2012-11-09|2013-11-05|ONLINE PRODUCTION PROCESS FOR A CARDBOARD COAT|
    CA2890311A| CA2890311A1|2012-11-09|2013-11-06|Ply for a board from an in-line production process|
    BR112015010600A| BR112015010600A2|2012-11-09|2013-11-06|folds to cardboard from a process implemented on the production line ".|
    US14/441,257| US9863093B2|2012-11-09|2013-11-06|Ply for a board from an in-line production process|
    PCT/IB2013/059944| WO2014072912A1|2012-11-09|2013-11-06|Ply for a board from an in-line production process|
    ES13853964.8T| ES2689549T3|2012-11-09|2013-11-06|Layer for a cardboard of an online production process|
    PL13853964T| PL2917404T3|2012-11-09|2013-11-06|Ply for a board from an in-line production process|
    EP13853964.8A| EP2917404B1|2012-11-09|2013-11-06|Ply for a board from an in-line production process|
    CN201380069849.8A| CN105121741B|2012-11-09|2013-11-06|Ply for paperboard from an on-line production process|
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