• 专利附录
  • 专利说明
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    • 专利摘要:
    The present invention relates to a method for manufacturing modified cellulose fibers for a moldable cellulose fiber based material, said method comprising: a) providing a chemical or semi-chemical wood pulp comprising cellulose fibers, and optionally subjecting the pulp to alkaline extraction to obtain an alkaline extracted pulp; and b) subjecting the pulp or the alkaline extracted pulp of step a) to a chemical treatment with an alkaline solution and/or an organic solvent to obtain a treated pulp or treated alkaline extracted pulp comprising modified cellulose fibers for a moldable cellulose fiber based material. The invention further relates to a moldable cellulose fiber based material comprising at least 70% by dry weight of modified cellulose fibers obtainable by the method.
    公开号:SE1950835A1
    申请号:SE1950835
    申请日:2019-07-03
    公开日:2021-01-04
    发明作者:Ali Harlin；Christiane Laine；Hanna Koskela；Harri Setälä；Jukka Ketoja；Kari Kammiovirta；Tuomo Hjelt
    申请人:Stora Enso Oyj；
    IPC主号:
    专利说明:

    |/IOLDABLE CELLULOSE FIBER BASED IVIATERIAL Technical fieldThe present disclosure relates to moldable cellulose fiber based materials and to methods for preparing such materials.
    BackgroundPaper-based packaging materials, as renewable materials, have a growing market potential due to their sustainability. However, the development of new packagingconcepts requires improvement in the mechanical properties of paper. Highextensibility is one of these properties. Highly extensible papers would have thepotential to replace certain kinds of plastics used in packaging.
    Formability of a paper-based material can be defined as the ability of a material todeform without breaking. However, formability is not a specific mechanicalproperty, but can be regarded as a generic term for explaining how well the paperdeforms during a particular forming process. Formability can for example beestimated on the basis of a 2D experimental test method that simulates theprocess conditions in a fixed blank thermoforming process as described by Vishtal& Retulainen, 2014 (Improving the extensibility, wet web and dry strength of paperby addition of agar, Nord Pulp Pap Res J, 29:434-443). ln the fixed blank process,the formability is determined by the extensibility and tensile strength of the paper.As yet, the fixed blank forming process has not been widely applied in industry forpaperboard. Pulp fibers constitute the load-bearing components of paper. Kraftpulp fibers primarily consist of cellulose and hemicellulose. Cellulose is acrystalline, strong and stiff material with low extensibility making cellulosic fibersstrong and stiff. However, mechanical treatment at high consistency possiblycombined with a low consistency refining phase has been shown to improve theelongation potential of paper. Chemical treatment of pulp has been applied inorder to modify the fiber material, especially the fiber surface, and its compatibilitywith polymer dispersions. 2 Elongation of some thermoplastic polymers can reach 400-800°/> and therefore, itis reasonable to expect that the addition of such polymers to the fiber network willimprove the formability of the paper. Bio-based thermoplastic polymers aregenerally not hazardous to health and are also bio-degradable, which makes themsuitable for use in food packages. Challenges of polymer applications to the pulpsuspension are low retention in the fiber network and insufficient adhesion to thefibers. On the other hand, in cases where the polymer is applied on a formed fibernetwork, the retention is a less severe problem, but difficulties arise in the limitedpenetration of the polymer into the fiber network, and possibly in the limitedadhesion. ln general, the forming processes for paper-based materials can be divided intotwo main categories: sliding and fixed blank processes. ln the forming processwith sliding blank (deep-drawing, stamping), forming proceeds due to the sliding ofpaper into the mold and lateral contraction of paper that causes microfolding of thepaper. ln the fixed blank process (hot pressing, hydroforming, air forming andvacuum forming) paper is formed via straining of the paper.
    Usually, the sliding blank process produces shapes with a relatively high depth,while those produced in the fixed blank have significant limitations in depth. This isdue to the fact that in the fixed blank process tensile deformation of paper prevailsover compressive deformation. This means that only paper grades with highextensibility, high strength and post-forming stiffness are suitable for the fixedblank forming process. l/loreover, fixed blank forming process yields shapes withsmooth and even edges that enables the gas-tight sealing of formed shapes withbarrier films. ln contrast, the shapes produced in the sliding blank process havelimitations in sealability due to microfolding/wrinkling, which also causes shape instability and impaired visual appearance.
    Currently, there are two types of forming processes for paper substrate incommercial use: stamping for the production of trays and plates, and thel/lultivac® process (vacuum-assisted air forming) for the production of sealabletrays for sliced cold cuts and cheeses. The emerging technologies in paper 3 forming include deep-drawing, hydroforming and hot pressing (stamping with afixed blank). lt can be concluded from the above discussion that paper substrates withimproved extensibility and strength, or toughness, might open up new possibilitiesin the preparation of deep 3D shapes with smooth edges. Therefore, there remains a need for strategies for improving the paper toughness.
    Summary of the invention lt is an object of the present disclosure to alleviate at least some of the problemswith the use of paper-based materials in preparation of deep 3D shapes withsmooth edges. lt is a further object of the present disclosure to provide a cellulose fiber basedmaterial with improved formability, i.e. improved extensibility and strength, ortoughness.
    The above mentioned objects, as well as other objects as will be realized by theskilled person in the light of the present disclosure are achieved by the various aspects of the present disclosure.
    The present inventors have surprisingly found that subjecting a chemical or semi-chemical wood pulp to chemical treatment with an alkaline solution and/or anorganic solvent produces modified cellulose fibers providing significantly improvedformability properties when used in a moldable cellulose fiber based material forforming deep 3D shapes with smooth edges.
    According to a first aspect illustrated herein, there is provided a method formanufacturing modified cellulose fibers for a moldable cellulose fiber basedmaterial, said method comprising: a) providing a chemical or semi-chemical wood pulp comprising cellulosefibers, and optionally subjecting the pulp to alkaline extraction to obtain an alkalineextracted pulp; and b) subjecting the pulp or the alkaline extracted pulp of step a) to achemical treatment with an alkaline solution and/or an organic solvent to obtain atreated pulp or treated alkaline extracted pulp comprising modified cellulose fibersfor a moldable cellulose fiber based material.
    The chemical treatment with an alkaline solution and/or an organic solvent of theoptionally alkaline extracted pulp has been found to significantly improve themoldability of foam formed board containing the modified cellulose fiberscompared to a corresponding foam formed board containing conventional untreated softwood pulp fibers.
    Without wishing to be bound to any particular scientific theory, it is noted that thetreated pulp has more curly fibers than conventional pulp. This is shown in Figure1. These curly fibers create loops to the board structure. One hypothesis is thatthese loops will straighten out as the board is stretched during a molding process.
    Also, the modified fibers of the treated pulp do not bond as strongly as in the caseof normal softwood fibers, which together with the curliness of the fibers leads to amore horizontal stress-strain curve after the yield point as shown in Figure 2. Thisstress-strain behaviour distributes the stresses in the fiber network evenly andincreases the breaking strain. lt has further been found that the material obtained according to the inventivemethod tolerates elevated temperatures during subsequent molding steps, whichprovides the advantage that molding can be done in existing equipment availableand today used for plastics.
    The modified cellulose fibers are especially useful in moldable webs used as aprecursor for preparation of deep 3D shaped articles. The term web as usedherein refers generally to a continuous sheet of paper or paperboardmanufactured or undergoing manufacture on a paper machine. The term web asused herein further refers to paper or paperboard substrate used for conversion into other physical forms, e.g. in the preparation of 3D shaped articles by deep drawing. ln some embodiments, the moldable cellulose fiber based material is amoldable cellulose fiber based web material.
    The web may for example be a water formed or foam formed web. ln foam formingfibers and other furnish components are mixed with foam instead of water. Thefoam consists of water, foaming agent and air. Typical air content is in the range of 50-70°/>. The air bubbles prevent flocculation of fibers in the headbox.
    The pulp used as the starting material for preparation of the modified pulp is achemical or semi-chemical wood pulp. Chemical pulps are composed of cellulose,hemicelluloses and lignin, the latter of which is often present in very smallquantities. However, unbleached and especially mechanical pulps havesignificantly higher lignin contents. l/lechanical pulps are not preferred in thepresent invention, since the high lignin content may have a negative effect onpaper extensibility. Webs prepared from mechanical pulps therefore typically havesignificantly lower elongation than webs prepared from chemical pulps. ln someembodiments, the chemical or semi-chemical wood pulp is a softwood pulp.
    The chemical or semi-chemical wood pulp comprising cellulose fibers can be usedas is, or it can be subjected to alkaline extraction to obtain an alkaline extractedpulp. The alkaline extraction, whereby the pulp is subjected to extraction with analkaline extraction solution, reduces the hemicellulose content of the pulp, which insome cases has been found to favorably influence the elongation of paper formedfrom the pulp. The alkaline extraction generally comprises contacting the pulp withan alkaline extraction solution, removing the alkaline extraction solution to obtainan alkaline extracted pulp, and optionally washing the alkaline extracted pulp. lnsome embodiments, the alkaline extraction comprises the steps: a1) contacting the pulp with an alkaline extraction solution for 1-360 minutes,a2) removing the alkaline extraction solution to obtain an alkaline extractedpulp, and a3) optionally washing the alkaline extracted pulp. 6 As readily understood by the skilled person, various alkaline extraction solutionsmay be used for the optional alkaline extraction step. ln some embodiments, thealkaline extraction solution is a NaOH, KOH or lVlg(OH)2 solution, preferably anaqueous solution. ln some embodiments, the concentration of said alkalineextraction solution is in the range of O.5-4 l/l, preferably in the range of 1-3 l/l.
    The alkaline extraction may preferably be performed at room temperature, i.e. atemperature in the range of 20-25 °C, but may also be performed at a temperature above or below room temperature.
    The alkaline extraction may preferably be performed at atmospheric pressure, butmay also be performed at a pressure above or below atmospheric pressure.
    For practical reasons, the alkaline extraction contacting time is at least 1 minute.The contacting time may generally be in the range of 1-360 minutes. ln someembodiments, the contacting time is in the range of 30-90 minutes.
    The alkaline extracted pulp typically has a lower hemicellulose content ascompared to the corresponding unextracted pulp. The alkaline extracted pulp may therefore also in some cases be referred to as hemipoor pulp.
    The pulp or alkaline extracted pulp of step a) is then subjected to a chemicaltreatment in order to modify the cellulose fibers to make them more useful in amoldable cellulose fiber based material. The chemical treatment generallycomprises contacting the pulp or alkaline extracted pulp of step a) with an alkalinesolution and/or an organic solvent, removing the alkaline solution and/or organicsolvent to obtain a treated pulp or a treated alkaline extracted pulp comprisingmodified cellulose fibers for a moldable cellulose fiber based material, andoptionally washing the treated pulp or treated alkaline extracted pulp. ln some embodiments, the chemical treatment comprises:b1) contacting the pulp or alkaline extracted pulp of step a) with an alkalinesolution and/or an organic solvent for at least 5 minutes, 7 b2) removing the alkaline solution and/or organic solvent to obtain a treatedpulp or a treated alkaline extracted pulp comprising modified cellulose fibers fora moldable cellulose fiber based material, and b3) optionally washing the treated pulp or treated alkaline extracted pulp. ln some embodiments, the chemical treatment comprises contacting the pulp or the alkaline extracted pulp of step a) with an alkaline solution. ln some embodiments, the chemical treatment comprises contacting the pulp orthe alkaline extracted pulp of step a) with an organic solvent. ln some embodiments, the chemical treatment comprises contacting the pulp orthe alkaline extracted pulp of step a) with a mixture of an alkaline solution and anorganic solvent. A mixture of an alkaline solution and an organic solvent is alsosometimes referred to herein as an alkaline solvent. The alkaline solvent maycomprise 1-99 °/> by weight of an alkaline solution and 1-99°/> by weight of an organic solvent, based on the total weight of the mixture. ln some embodiments, the alkaline solution is a NaOH, KOH or l/lg(OH)2 solution.ln some embodiments, the concentration of said alkaline solution is in the range of O.5-4 l/l, preferably in the range of 1-3 l/l. ln some embodiments, the solvent of the alkaline solution is water. ln someembodiments, the solvent of the alkaline solution is a mixture of water and an organic solvent.
    The organic solvent is preferably water miscible. ln some embodiments, theorganic solvent is a polar organic solvent, preferably a protic organic solvent, morepreferably an alcohol, such as ethanol, isopropanol or tert-butanol. ln some embodiments the alkaline solution and/or an organic solvent comprises amixture of an aqueous NaOH solution and tert-butanol. ln some embodiments theconcentration of NaOH in the mixture is in the range of O.5-4 l/I in respect of total amount of water in the mixture. 8 The chemical treatment may preferably be performed at a temperature in therange of 20-60 °C. ln some embodiments, the chemical treatment is performed ata temperature in the range of 40-50 °C. The chemical treatment may also beperformed at room temperature, i.e. at a temperature in the range of 20-25 °C.
    The chemical treatment may preferably be performed at atmospheric pressure, but may also be performed at a pressure above or below atmospheric pressure.
    For practical reasons, the chemical treatment contacting time is at least 5 minutes.The contacting time may generally be in the range of 5 minutes to 96 hours. ln some embodiments, the contacting time is in the range of 24-60 hours.
    Following chemical treatment with an alkaline solution, the treated pulp ispreferably neutralized by an acid, preferably mineral acid, for example sulfuricacid.
    The treated pulp or treated alkaline extracted pulp obtained in accordance with thefirst aspect, comprising modified cellulose fibers for a moldable cellulose fiberbased material, are advantageously used in a moldable cellulose fiber basedmaterial. The chemical treatment with an alkaline solution and/or an organicsolvent of the optionally alkaline extracted pulp has been found to significantlyimprove the moldability of foam formed board containing the modified cellulosefibers compared to a corresponding foam formed board containing conventional untreated softwood pulp fibers.
    The modified cellulose fibers are especially useful in moldable webs used as aprecursor for preparation of deep 3D shaped articles. ln some embodiments, themoldable cellulose fiber based material is a moldable cellulose fiber based web material. The web may for example be a water formed or foam formed web. lt has been found that it is possible to mold board made of the inventive materialwithout heat treatment, i.e. increased temperature during molding is not needed.However, the material obtained according to the inventive method also tolerates 9 elevated temperatures and thus current machinery (typically used for plastics) can be utilized.
    According to a second aspect illustrated herein, there is provided a method formanufacturing a moldable cellulose fiber based material, said method comprising: a) providing a treated pulp or treated alkaline extracted pulp comprisingmodified cellulose fibers for a moldable cellulose fiber based material accordingthe first aspect; and b) forming the treated pulp or treated alkaline extracted pulp, optionallytogether with additional components, into a dry moldable material.
    The dry moldable material may for example be a cellulose fiber based web material or a premoulded structure. ln some embodiments, the moldable cellulose fiber based material formed is amoldable cellulose fiber based web material. The web material may for examplebe formed by water forming or by foam forming. The web material can then beused as a blank for preparation of deep 3D shaped articles by deep drawing techniques. ln order to optimally retain the improved moldability obtained by the chemicaltreatment, the treated pulp should not be dried until the moldable material, e.g. theweb or premoulded structure, has been formed. lt is believed that the chemicaltreatment changes the fiber walls of the cellulose, and this leads to increasedstretchability of the fibers. Therefore, in some embodiments, the treated pulp ortreated alkaline extracted pulp has not been dried before the moldable material has been formed.
    According to a third aspect illustrated herein, there is provided a moldablecellulose fiber based material comprising at least 50%, and preferably at least70%, by dry weight of modified cellulose fibers obtainable by, or obtained by, the method according to the first aspect. ln some embodiments, the moldable cellulose fiber based material comprises atleast 80% by dry weight, preferably at least 90% by dry weight, more preferably atleast 95% by dry weight, of the modified cellulose fibers. ln some embodiments, 100% of the cellulose fibers in the moldable cellulose fiberbased web material are modified cellulose fibers obtainable by the method according to the first aspect. ln some embodiments, the moldable cellulose fiber based material comprises lessthan 30% by dry weight, preferably less than 20% by dry weight, more preferablyless than 10% by dry weight, of added polymer. ln some embodiments, the moldable cellulose fiber based material comprises upto 30% by dry weight of an added polymer selected from the group consisting ofstarch, cellulose or other polysaccharides including their derivatives, polylacticacid, polyurethane, polyolefins, dispersions of acrylates, styrene/butadiene or vinylacetate, and mixtures thereof. ln some embodiments, the moldable cellulose fiber based material comprises upto 25 °/>, or even up to 50%, by dry weight of inorganic or organic fillers forexample particles selected from the group consisting of gypsum, silicate, talc,plastic pigment particles, kaolin, mica, calcium carbonate, including ground andprecipitated calcium carbonate, bentonite, alumina trihydrate, titanium dioxide,phyllosilicate, synthetic silica particles, organic pigment particles and mixturesthereof. ln some embodiments, the moldable cellulose fiber based material is a moldablecellulose fiber based web material. The web may for example be a water formedor foam formed web. ln some embodiments, the modified cellulose fibers of the moldable cellulose fiberbased web material have not been dried subsequent to the chemical treatment. ln some embodiments, the moldable cellulose fiber based web material has a 2Delongation at least 10% higher, preferably at least 20% higher, preferably at least 11 % higher, preferably at least 40% higher, preferably at least 50% higher,preferably at least 60% higher, preferably at least 70% higher, preferably at least80% higher, preferably at least 90% higher, preferably at least 100% higher, thanthe 2D elongation of a corresponding cellulose fiber based web material whereinthe cellulose fibers are unmodified. ln some embodiments, the moldable cellulosefiber based web material has a 2D elongation of at least 10%, preferably at least20%. The 2D elongation of a corresponding cellulose fiber based web material wherein the cellulose fibers are unmodified is typically around 5 °/-.~.
    The moldable cellulose fiber based web material preferably has a basis weight andthickness suitable for conversion into deep 3D shaped articles by deep drawingtechniques. ln some embodiments, the moldable cellulose fiber based web material has a basis weight in the range of 50-500 g/m2. ln some embodiments, the moldable cellulose fiber based web material is polymercoated. The polymer coating of the polymer coated web material may compriseany of the polymers commonly used in paper or paperboard based packagingmaterials in general or polymers used in liquid packaging board in particular.Examples include polyethylene (PE), polyethylene terephthalate (PET),polypropylene (PP) and polylactic acid (PLA). Polyethylenes, especially lowdensity polyethylene (LDPE) and high density polyethylene (HDPE), are the mostcommon and versatile polymers used in packaging board for liquid containing foodproducts.
    The polymer coating preferably comprises a heat sealable polymer. Using a heatsealable polymer allows for efficient sealing of the container by heat sealing of alid or sealing film to the container.
    The polymer coating preferably comprises a thermoplastic polymer. ln someembodiments, the polymer coating comprises a polyolefin. Thermoplasticpolymers, and particularly polyolefins are useful since they provide good heatsealing properties and can be conveniently processed by extrusion coating 12 techniques to form very thin and homogenous films with good liquid barrierproperties. ln some embodiments, the polymer layer comprises a polypropylene ora polyethylene. ln preferred embodiments, the polymer layer comprises apolyethylene, more preferably LDPE or HDPE.
    The basis weight of the polymer layer of the inventive gas barrier film is preferablyless than 50 g/m2. ln order to achieve a continuous and substantially defect freefilm, a basis weight of the polymer layer of at least 8 g/m2, preferably at least 12g/m2 is typically required. ln some embodiments, the basis weight of the polymerlayer is in the range of 8-50 g/m2, preferably in the range of 12-50 g/m2.
    According to a fourth aspect illustrated herein, there is provided a molded productcomprising modified cellulose fibers obtainable by the method according to the firstaspect.
    The molded product may for example be a 3D shaped receptacle. Non-limitingexamples of such receptacles include trays, plates, bowls and cups. Thereceptacles may for example have a substantially square (e.g. quadratic orrectangular), substantially polygonal (e.g. hexagonal) or substantially round (e.g.circular or elliptic) geometry. The receptacle may be used, among other purposes,for storage and transport of fresh or frozen food. ln some embodiments, thecontainers may also be used for conventional or microwave preparation of food.The receptacle is preferably formed from a single piece of substrate material.Within the context of this document, the phrase a "single piece of material"includes a single piece of material that comprises a single layer or multiple layersof the same material or multiple layers of different materials. These multi-layeredmaterials could include, for example, layers of two or more paper and/orpaperboard substrates completely bonded together and/or partially bondedtogether, such as a corrugated board material, with or without any other layer orlayers of any other materials such as metal, foil, plastic, and so forth. Thus,laminates formed from two or more differing types of material are nonetheless encompassed by the phrase a "single piece of material". 13 The molded product is preferably prepared by deep drawing techniques using amoldable cellulose fiber based web material. ln some embodiments, the moldedproduct is made of a moldable cellulose fiber based web material according to thethird aspect. ln a preferred embodiment, the molded product is made of a singlepiece of a moldable cellulose fiber based web material according to the thirdaspect.
    The invention will now be described more in detail with reference to specific examples.
    While the invention is described herein with reference to various exemplaryembodiments, it will be understood by those skilled in the art that various changesmay be made and equivalents may be substituted for elements thereof withoutdeparting from the scope of the invention. ln addition, many modifications may bemade to adapt a particular situation or material to the teachings of the inventionwithout departing from the essential scope thereof. Therefore, it is intended thatthe invention not be limited to the particular embodiment disclosed as the bestmode contemplated for carrying out this invention, but that the invention willinclude all embodiments falling within the scope of the appended claims.
    Brief description of the drawinos Figure 1 shows CCD camera images of (a) a conventional, untreated softwood pulp,and (b) the inventive moldable pulp.
    Figure 2 is a diagram showing stress - strain curves of conventional, untreatedsoftwood pulp, mechanically treated pulp, and the inventive moldable pulp.
    Figure 3 is a picture showing the 2D formability tester used for measuring theformability strain and strength of the modified sheets.
    Figure 4 shows the 2D tension vs. strain curves to different pulps. 14 Examples Example 1 - Alkaline extraction of cellulose pulp Softwood kraft cellulose pulp (SE SW) was first extracted with 2.5 l/I NaOH (100 gNaOH/L) at 20-25 °C for 1 h in pulp consistency 10 wt°/>. The extracted pulp waswashed by filtering and pH was adjusted to pH 8-9. The dry matter content ofextracted pulp was approximately 35 wt%. The yield of extracted pulp was 86.5°/>(average of four extraction batches, +/- 1.3%). This cellulose pulp, referred toherein as Reference 1, was then used as a starting material for the chemical treatment.
    Example 2 - Chemical treatment of alkaline extracted cellulose pulp 1500 g of Reference 1 pulp was weighed and added into a 60 L reaction flask with14000 ml of water and with 13000 ml of 90% aqueous tert-butanol. Then 1220 g of50% NaOH solution was added to adjust the molarity of NaOH to 1.1-1.5 M in respectof the total amount of water in the reaction mixture. The reaction mixture was stirredfor 48 h at 45 °C. The reaction mixture was then neutralized with 400 ml ofconcentrated sulfuric acid diluted with water to 1/10 before addition into the reactor.The samples were filtrated and washed carefully with 10 L of 100 % ethanol, andfinally 3x20 L of water to remove organic solvents and salts. The obtained chemically treated kraft cellulose pulp is referred to herein as Reference 2.
    Example 3 - Chemical treatment of non-extracted cellulose pulp Softwood kraft cellulose pulp as used in Example 1, was used as the startingmaterial. 500 g of the starting material was weighed and added into a 60 L reactionflask with 4000 ml of water and with 3000 ml of 90% aqueous tert-butanol. Then 400 gof 50% NaOH solution was added to adjust the molarity of NaOH to 1.1-1.5 M inrespect of the total amount of water in the reaction mixture. The reaction mixture wasstirred for 48 h at +45 °C. The reaction mixture was then neutralized with 130 ml ofconcentrated sulfuric acid diluted with water to 1/10 before addition into the reactor.The samples were filtrated and washed carefully with 3 L of 100% ethanol, and finally3x10 L of water to remove organic solvents and salts. The obtained chemically treated non-extracted pulp is referred to herein as Reference 3.
    Example 4 - Preparation of laboratorv sheets bv foam forming The foam formed laboratory sheets were prepared as follows: 1. Foam was produced by mixing the cellulose pulp, with water, surface activeagent (SDS), and optional additives, until the air content of foam was ~60-70°/>.Also retention aids or fixative were used in some trial points. The basis weight was200 g/m2. 2. Foam was poured into a hand sheet mold. 3. Sheet was formed to the screen by removing the foam with a vacuum. 4. Sheet was removed with the wire from the mold and pre-dried by transferringwire on a special suction table by using an exhauster. The suction table has asuction slit, width 5 mm, and it sucks air through the sheet with 0.2 bar vacuum.5. No wet pressing was done. 6. The pre-dried sheets were dried overnight. The drying shrinkage wasrestrained.
    Example 5 - Analvsis of hand sheets Formability strain and strength of modified sheets were measured using a 2Dformability tester developed by VTT in Jyväskylä, Finland. The 2D formabilitytester is shown in Figure 3. The objective of the 2D formability tester is to simulatethe thermoforming process in 2D-scale. The unit is equipped with a double-curvedheated press and bottom support (allowing for temperatures up to 250 °C) andblank holders. Typically, a paper with a grammage range from 80 to 250 g/m2 canbe preheated to the die temperature within 0.5-0.7 s. ln practice, this means that the temperature of the paper at the moment of forming is close to that of the die.
    The testing proceeds as follows: the two blank holders fix a paper sample (20-30mm wide and more than 100 mm long). The press is then moved into contact withthe sample and retained still for 0.5 s in order to preheat the sample. Then, thepress continues a downward movement until breakage of the sample.Displacement and load of the press is measured by a displacement sensor andload sensor respectively. The velocity of the forming press was 1 mm/s. Theformability strain and strength of the samples was measured as an average valuecollected from 7 samples at die temperature of 90-140 °C. 16 The geometry of the press surface, as well as the geometry of the sample holder was taken into account when calculating the 2D formability strain value. The sample holders have an absolute blank holding, so no slipping of the sample took5 place during the test.
    The results of the measurements are presented in Figure 4 and in Table 1.
    Table 1.
    Formulation 2D strain, %100% Ref.2 + SDS without additives 10,5 100% Ref.2 + SDS with additives 14,3 50% Ref.2 + 50% SE SW pulp + SDS with additives 10,7 100°/> Ref.3 + SDS with additives 14,5 100°/> SE SW + SDS without additives 5,4 Additives = 30% polyurethane (lmpranil DL 519, Covestro) and 600g/tn CPAl/I(Perform PC 435, Solenis) and microparticles (Perform 7200, Solenis)
    权利要求:
    Claims (22)
    [1] 1. A method for manufacturing modified cellulose fibers for a moldable cellulose fiber based material, said method comprising: a) providing a chemical or semi-chemical wood pulp comprising cellulosefibers, and optionally subjecting the pulp to alkaline extraction to obtain analkaline extracted pulp; and b) subjecting the pulp or the alkaline extracted pulp of step a) to a chemicaltreatment with an alkaline solution and/or an organic solvent to obtain atreated pulp or treated alkaline extracted pulp comprising modified cellulose fibers for a moldable cellulose fiber based material.
    [2] 2. The method according to claim 1, wherein the moldable cellulose fiber based material is a moldable cellulose fiber based web material.
    [3] 3. The method according to any one of the preceding claims, wherein said chemical or semi-chemical wood pulp is a softwood pulp.
    [4] 4. The method according to any one of the preceding claims, wherein saidalkaline extraction comprises: a1) contacting the pulp with an alkaline extraction solution for 1-360 minutes,a2) removing the alkaline extraction solution to obtain an alkaline extractedpulp, and a3) optionally washing the alkaline extracted pulp.
    [5] 5. The method according to any one of the preceding claims, wherein saidalkaline extraction solution is a NaOH, KOH or l/lg(OH)2 solution.
    [6] 6. The method according to claim 5, wherein the concentration of said alkalineextraction solution is in the range of O.5-4 l/l, preferably in the range of 1-3 l/l. 18
    [7] 7. The method according to any one of the preceding claims, wherein saidchemical treatment comprises: b1) Contacting the pulp or alkaline extracted pulp of step a) with an alkalinesolution and/or an organic solvent for at least 5 minutes,b2) removing the alkaline solution and/or organic solvent to obtain a treatedpulp or a treated alkaline extracted pulp comprising modified cellulose fibers fora moldable cellulose fiber based material, andb3) optionally washing the treated pulp or treated alkaline extracted pulp.
    [8] 8. The method according to any one of the preceding claims, wherein saidchemical treatment comprises contacting the pulp or the alkaline extracted pulp ofstep a) with a mixture of an alkaline solution and an organic solvent.
    [9] 9. The method according to any one of the preceding claims, wherein said alkaline solution is a NaOH, KOH or IVIg(OH)2 solution.
    [10] 10. The method according to claim 9, wherein the concentration of said alkalinesolution is in the range of O.5-4 l/l, preferably in the range of 1-3 l/l.
    [11] 11. The method according to any one of the preceding claims, wherein saidorganic solvent is a polar organic solvent, preferably a protic organic solvent, morepreferably an alcohol, such as ethanol, isopropanol or tert-butanol.
    [12] 12. A method for manufacturing a moldable cellulose fiber based material, said method comprising: a) providing a treated pulp or treated alkaline extracted pulp comprisingmodified cellulose fibers for a moldable cellulose fiber based materialaccording to any one of claims 1-11; and b) forming the treated pulp or treated alkaline extracted pulp, optionallytogether with additional components, into a moldable cellulose fiber based material. 19
    [13] 13. The method according to claim 12, wherein the moldable cellulose fiberbased material is a moldable cellulose fiber based web material.
    [14] 14. The method according to any one of claims 12-13, wherein the treated pulpor treated alkaline extracted has not been dried before the moldable material hasbeen formed.
    [15] 15. A moldable cellulose fiber based material comprising at least 70% by dryweight of modified cellulose fibers obtainable by the method according to any oneof claims 1-11.
    [16] 16. The moldable cellulose fiber based material according to claim 16,comprising at least 80% by dry weight, preferably at least 90% by dry weight, morepreferably at least 95% by dry weight, of modified cellulose fibers obtainable by the method according to any one of claims 1-11.
    [17] 17. The moldable cellulose fiber based material according to any one of claims15-16, wherein 100% of the cellulose fibers in the moldable cellulose fiber basedweb material are modified cellulose fibers obtainable by the method according to any one of claims 1-11.
    [18] 18. The moldable cellulose fiber based material according to any one of claims15-17, comprising less than 30% by dry weight, preferably less than 20% by dryweight, more preferably less than 10% by dry weight, of added polymer.
    [19] 19. The moldable cellulose fiber based material according to any one of claims15-18, wherein the moldable cellulose fiber based material is a moldable cellulose fiber based web material.
    [20] 20. The moldable cellulose fiber based web material according to claim 19,wherein said moldable cellulose fiber based web material has a 2D elongation atleast 10% higher, preferably at least 20% higher, preferably at least 30% higher,preferably at least 40% higher, preferably at least 50% higher, than the 2D elongation of a corresponding ce|u|ose fiber based web material wherein thece|u|ose fibers are unmodified.
    [21] 21. The moldable ce|u|ose fiber based web material according to any one ofclaims 15-20, having a basis weight in the range of 50-500 g/m2.
    [22] 22. A molded product comprising a moldable ce|u|ose fiber based web materialaccording to any one of claims 15-21.
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    同族专利:
    公开号 | 公开日
    SE543676C2|2021-05-25|
    WO2021001779A8|2021-08-19|
    WO2021001779A1|2021-01-07|
    CA3145652A1|2021-01-07|
    引用文献:
    公开号 | 申请日 | 公开日 | 申请人 | 专利标题
    JP2002212889A|2001-01-12|2002-07-31|Nippon Paper Industries Co Ltd|Method for producing bulky pulp|
    JP2004204397A|2002-12-25|2004-07-22|Kao Corp|Molded pulp product|
    CN101490090B|2006-07-19|2013-01-02|国立大学法人京都大学|Microfibrillated cellulose having cellulose type-II crystalline structure, and molded article containing the microfibrillated cellulose|
    EP2308907B1|2008-07-31|2014-01-01|Kyoto University|Molding material containing unsaturated polyester resin and microfibrillated plant fiber|
    WO2011087438A1|2010-01-12|2011-07-21|Innventia Ab|Mouldable material|
    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    SE1950835A|SE543676C2|2019-07-03|2019-07-03|Moldable cellulose fiber based material|SE1950835A| SE543676C2|2019-07-03|2019-07-03|Moldable cellulose fiber based material|
    CA3145652A| CA3145652A1|2019-07-03|2020-07-02|Moldable cellulose fiber based material|
    PCT/IB2020/056250| WO2021001779A1|2019-07-03|2020-07-02|Moldable cellulose fiber based material|
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