process for producing a porous structure composed of partially interconnected cellulose-based sheets

专利摘要:
POROUS STRUCTURE COMPOUND OF AT LEAST PARTIALLY INTERCONNECTED SHEETS, PROCESS FOR PRODUCING A POROUS STRUCTURE COMPOUND OF PARTIALLY INTERCONNECTED CELLULOSE-BASED SHEETS, AND POWDER CONSISTING OF NCC FIBERS The invention disclosed here provides a unique class of foam materials characterized by the regions of unidirectionality of material. Foam materials are suitable for a wide variety of end-use applications as core materials or as materials in the construction of multi-layer structures. The ingenious new process for manufacturing the composite materials of the invention allows you to modify the foam materials to suit any specific end use.
公开号:BR112016017448B1
申请号:R112016017448-8
申请日:2015-01-29
公开日:2021-06-08
发明作者:Shaul Lapidot；Sigal ROTH SHALEV；Rikard SLATTEGARD；Oded Shoseyov；Clarite AZERRAF；Ido Braslavsky；Victor YASHUNSKY
申请人:Yissum Research Development Company Of The Hebrew University Of Jerusalem Ltd.；Melodea Ltd；
IPC主号:

专利说明:

FIELD OF TECHNIQUE
[001] The present invention relates to structures constructed of nanocrystalline cellulose. BACKGROUND OF THE INVENTION
[002] Polymeric foams are materials of high importance in the field of composite materials and are used for many applications, for example, for insulation, structural parts such as car panels, as well as for core materials in the manufacture of composite sandwich panels that feature high strength, improved energy dissipation, insulation and light weight. Polymeric foams lead to high insulating and weight reduction properties; however, some have low resistance.
[003] Sandwich structure composites can be described by thin, hard coatings that are secured to a thick, light weight core. The core material is a material of normally limited strength, but its higher thickness provides sandwich composite with high flexural stiffness and low overall density. Combining the properties of the coatings and the core results in structures that are extremely light and strong.
[004] The materials used for the core in sandwich structures can be divided into rigid foams or honeycomb structures. Expanded PVC and PET foams are examples of commonly used rigid foams. These foams are produced by chemical blowing (foaming) of polymers and form rigid isotropic sponge-like structures. Beehive-type structures such as aluminum, Kevlar, polypropylene or cardboard form anisotropic structures with high compressive and shear strengths on the Z axis of the structure. Beehive-like structures that are by nature anisotropic are very useful as a core for composites. Such cores resist shear loads, increase structure rigidity by keeping cladding covers separate and providing continuous support to flanges or cladding covers, thus producing evenly hardened structures.
[005] Recently, it was shown that nanocrystalline cellulose (NCC) as well as nanofibers can be processed into foams through various methods. NCC is a fibrous material produced from cellulose, typically being high purity single crystals that have an elongated shape. These constitute a generic class of materials that have mechanical strengths equivalent to the bond strengths of adjacent atoms. The resulting ordered structure is typically characterized by high mechanical strengths; NCC's tensile strength properties are well above those of currently available high volume content reinforcements [1-3].
[006] Regardless of the processes used to produce these foams, such as supercritical fluid extraction, microfluidics, etc., these foams have low resistance to compression and, therefore, their use as core materials is limited [3].
[007] An available method for cellulose-based foaming is called "foaming", according to which method the cellulose pulp fibers are mixed with a detergent and the foam is therefore produced following the methods of making paper patterns on a machine for making paper. The resulting product is a lightweight, flexible, soft foam paper sheet with a microporous structure and a low degree of orientation.
[008] Another available method for producing cellulosic foams involves casting an NCC or a suspension of nanofibers in molds followed by freeze-drying [4-10]. Such foams self-organize due to the formation of ice that pushes the NCC particles against each other. Therefore, the control of ice growth results in controlled patterning of the foams. This process, called “ice shaping”, was developed to control the assembly of a variety of materials and is typically used for the assembly of colloidal suspensions on solids. Until now, the use of ice shaping has been tested on a laboratory scale and found to produce foams with significantly inferior properties compared to rigid synthetic foams.
[009] Common freezing processes, as mentioned above, can result in the formation of light weight but very soft structures, easily disintegrated and of low compressive strength, mainly due to the difficulty in controlling the rate of ice formation during the process of freezing. Ice growth in super-cooled environments results in dendrites that resemble snowflakes in their morphology and that negatively affect foam morphology and structure. In addition, freezing in uncontrolled systems, where NCC slurry is exposed to low temperatures from different directions, has little control in the direction of ice crystal formation and, as a result, cross sections of fortuitously crystallized foams may exhibit local orientation in planes facing different directions parallel to the direction of formed ice crystals; therefore leading to inferior mechanical properties.
[010] Production of composite foams made from NCC reinforced with bioresins as core materials for sandwich composite applications has also been described [11]. Such composites usually have higher densities and therefore may have less applicability as low weight and high strength composite materials are better suited and more desirable. REFERENCES[1] De Souza Lima, M. and R. Borsali, Macromolecular Rapid Communications 2004, 25(7), 771-787[2] Samir, M., F. Alloin and A. Dufresne, Biomacromolecules 2005, 6(2 ), 612-626[3] Eichhorn, S., et al., Journal of Materials Science 2010, 45(1), 1-33 [4] Deville S., J. Mater. Res. 2013, 28(17), 2202-2219[5] Svagan et al, Adv. Mater. 2008, 20, 1263-1269[6] Svagan et al, J. Mater. Chem. 2010, 20, 6646-6654[7] Ali et al., Soft Matter 2013, 9, 580-1588[8] Dash et al, Carbohydrate Polymers 2012, 88(2), 789-792[9] Kohnke et al, GreenChem. 2012, 14, 1864-1869[10] Lee J. et al., Soft Matter 2011, 7, 6034-6040[11] WO 2012/032514 GENERAL DESCRIPTION
[011] The inventors of the invention, disclosed here, have developed a unique class of foam materials that are characterized by regions of material unidirectionality. Foam materials are suitable for a wide variety of end use applications as core materials or as materials in the construction of multilayer structures. The ingenious new process for producing the composite materials of the invention allows to modify the foam materials to suit any specific end use.
[012] The unique structures of the foam materials of the invention endow the materials with any one or more of the following qualities: - light weight, - high compressive and shear strength, - thermal insulation, - sound insulation, - flame retardancy, - hydrophobicity and structural and mechanical anisotropy, in which each of these characteristics can be specifically and independently optimized or modulated in order to adapt the materials for any final use.
[013] Foam materials are generally highly oriented NCC-based structures that have the stated improved mechanical properties.
[014] Thus, in one of its aspects, the invention provides a porous structure composed of sheets at least partially interconnected, the sheets being substantially unidirectionally oriented, the sheets comprising a cellulose-based material selected from nanocrystalline cellulose (NCC), microfibrillary cellulose (MFC) and mixtures thereof.
[015] In another aspect, the invention provides a porous structure formed of at least partially interconnected sheets, the sheets defining a plurality of substantially elongated open pores, the pores being substantially unidirectionally oriented, the sheets comprising a material to the cellulose base selected from nanocrystalline cellulose (NCC), microfibrillar cellulose (MFC) and mixtures thereof.
[016] In another aspect, a porous structure is provided formed of sheets at least partially interconnected unidirectionally oriented, the sheets defining a plurality of open pores that is positioned within said sheets, wherein the sheets comprise a material based on cellulose selected from nanocrystalline cellulose (NCC), microfibrillary cellulose (MFC) and mixtures thereof.
[017] The cellulose-based foam material of the invention comprises a plurality of cavities, each of said plurality of cavities has a wall surface comprising (or consists of) a cellulose material, with at least one region of the foam being unidirectionally oriented as defined. In some embodiments, the cavities within the foam having unidirectionality have a mixed structure in which some of the cells have a unidirectional orientation while the other cavities have an isotropic structure, as discussed in detail here.
[018] In some embodiments, the foam has an isotropic structure, as discussed in detail here.
[019] Nanocrystalline Cellulose "NCC", also known as Cellulose Whiskers (CW) or Crystalline Nanocellulose (CNC), is used to define a material in the form of fibers produced from cellulose, typically being single crystals of high purity cellulose . Microfibrillar cellulose, "MFC", also sometimes referred to as nanofibrillated cellulose (NFC), is commonly produced with or without chemical or enzymatic treatment of mainly bleached pulp, followed by shearing and homogenizing the mainly bleached pulp, resulting in micrometer-length fibers with a nanometer diameter.
[020] As known in the art, NCCs are elongated crystalline nanoparticles similar to rods (structure in "rice grains") and MFCs are elongated strands (like structure to "spaghetti") consisting of alternating crystalline and amorphous segments. As used herein, MFC also encompasses nanofibrillated cellulose (NFC). Cellulose fibrils, being generally of higher crystallinity and purity than those obtained from plant sources, are inherently nanosized.
[021] In some embodiments, the cellulose-based material is characterized by having at least 50% crystallinity. In further embodiments, the cellulose-based material is monocrystalline.
[022] In some embodiments, the nanocrystals or fibrils of the cellulose-based material have a length of at least about 50 nm. In other embodiments, they are at least about 100 nm in length or are at most 1000 µm in length. In other embodiments, the nanocrystals or fibrils are between about 100 nm and 1000 µm in length, between about 100 nm and 900 µm in length, between about 100 nm and 600 µm in length, or between about 100 nm and 500 µm in length.
[023] In some embodiments, the nanocrystals or fibrils of the cellulose-based material are between about 10 nm and 100 nm in length, between 100 nm and 1000 nm in length, between about 100 nm and 900 nm in length, between about 100 nm and 800 nm in length, between about 100 nm and 600 nm in length, between about 100 nm and 500 nm in length, between about 100 nm and 400 nm in length, between about 100 nm and 300 nm in length or between about 100 nm and 200 nm in length.
[024] The nanocrystals or fibrils of the cellulose-based material can have an aspect ratio (length-to-diameter ratio) of 10 or more. In some embodiments, the aspect ratio is between 10 and 100, or between 20 and 100, or between 30 and 100, or between 40 and 100, or between 50 and 100, or between 60 and 100, or between 70 and 100, or between 80 and 100, or between 90 and 100, or between 61 and 100, or between 62 and 100, or between 63 and 100, or between 64 and 100, or between 65 and 100, or between 66 and 100, or between 67 and 100, or between 68 and 100, or between 69 and 100.
[025] In some embodiments, the aspect ratio is between 67 and 100.
[026] The fibers of NCC or MFC constitute the sheets that are at least partially interconnected, thus forming the porous structures of the invention. Therefore, pores are defined by the walls of the sheets and formed between them. In some embodiments, the pores are substantially elongated. In other embodiments, the pores are substantially rounded (like a bubble). In other embodiments, the pores are a mixture of elongated and round pores.
[027] The term “partially interconnected” refers to the observation that nanocellulose sheets are connected to each other at one or more nodes or points or regions of their surfaces; they are not associated with each other along their respective entire surfaces. Namely, within the context of the present disclosure, the term is intended to encompass adjacent or neighboring sheets that have at least one node or point or region of connection between their surfaces, and at least one other portion that is not connected to one( s) adjacent sheet(s). Without sticking to theory, the sheets are typically interconnected through hydrogen bonds (other bonding interactions may also be present depending on the specific nature and composition of the foam material). This allows the formation of a network of sheets defined by nodes or connection points or regions between adjacent sheets, while the unconnected portions define the pore walls.
[028] The sheets are arranged in the porous structure in a substantially unidirectional orientation, that is, most of the sheets are arranged in the same direction and substantially parallel to each other, the direction being normal to the plane of growth of the sheets (crystals of ice). When referring to pores, the term "substantially unidirectionally oriented", or any variation thereof, is intended to refer to a porous structure in which most of the elongated or other pores present are arranged so that their longitudinal axes are directed in substantially the same direction.
[029] In some embodiments, the foam material is characterized by a structure that has the sheets arranged unidirectionally. In other embodiments, some regions of the foam material are completely directional, with others being anisotropic.
[030] As the cellulose-based material is of a fibrous nature, in some embodiments, the sheets can be composed of aligned cellulose nanocrystals or aligned cellulose fibrils. The term "aligned", or any variation thereof, denotes an arrangement in which at least a portion, in some embodiments, most of the nanocrystals or fibrils are substantially positioned parallel to one another, forming a( s) sorted sheet(s).
[031] In some embodiments, the sheets have a thickness of between about 5 and 50 nm. In some embodiments, the sheets have a thickness of between about 10 and 50 nm. In some embodiments, the sheets have a thickness of between about 15 and 50 nm. In some embodiments, the sheets have a thickness of between about 20 and 50 nm. In some embodiments, the sheets have a thickness of between about 25 and 50 nm. In some embodiments, the sheets have a thickness of between about 30 and 50 nm. In some embodiments, the sheets have a thickness of between about 35 and 50 nm. In some embodiments, the sheets have a thickness of between about 40 and 50 nm. In some embodiments, the sheets have a thickness of between about 45 and 50 nm. In some embodiments, the sheets have a thickness of between about 5 and 40 nm. In some embodiments, the sheets have a thickness of between about 5 and 30 nm. In some embodiments, the sheets have a thickness of between about 5 and 20 nm. In some embodiments, the sheets have a thickness of between about 5 and 10 nm. In some embodiments, the sheets are between about 10 and 20 nm thick. In some embodiments, the sheets have a thickness of between about 10 and 30 nm. In some embodiments, the sheets are between about 10 and 40 nm thick.
[032] In other embodiments, the sheets define planar or curved surfaces. In other embodiments, each sheet can be flat, curved, or it can have some flat regions while other regions are curved.
[033] The porous structures of the invention are characterized by improved mechanical properties, as explained in detail above. Such properties, like those mentioned above, can be modulated and adjusted to suit a particular end use. In some embodiments, porous structures have compressive strengths of at least about 0.1 MPa. In some embodiments, the compressive strength is a maximum of 15 MPa. In some embodiments, the compressive strength is between 0.1 MPa to 15 MPa.
[034] In other embodiments, the porous structures have a density of between about 10 kg/m3 and 250 kg/m3, thus allowing to maintain various weights (or low self-weights) without impairing the mechanical properties of the structures or articles made from them .
[035] In some embodiments, the structures of the invention are comprised of NCC.
[036] When detergents are used in a process to produce the porous structures of the invention, the structures present a plurality of spherical open cell structures (spherical cavities or pores of any shape, structure and size) that are connected to one another, forming an interconnected network.
[037] The structures of the invention can be used as composite materials. The structures of the invention can serve as scaffolds on which and/or within which at least one additional component can be introduced to give additional features to it. In some embodiments, the structure of the invention can be infused with a polymeric resin selected from natural or synthetic thermosetting polymer resins and thermoplastic polymer resins.
[038] Thereby, the invention further provides a structure according to the invention which further comprises at least one polymer or a reinforcing material. The polymer material can be selected from thermosetting polymers and/or thermoplastic polymers which undergo curing by heating, a chemical reaction and/or irradiation.
[039] In some embodiments, the polymer is at least one thermosetting polymer resin, being synthetic, semi-synthetic or biobased obtained from a natural source (or as a modified or unmodified resin material). Non-limiting examples of such thermosetting resins include: thermosetting silicone polymers such as cured silicone elastomers, silicone gels and silicone resins; and thermosetting organic polymers such as furan resins, epoxy resin, amino resins, polyurethanes (polyols and isothiocyanates), polyimides, phenolic resins, cyanate ester resins, bismaleimide resins, polyesters, acrylic resins, and the like.
[040] In some embodiments, the at least one polymer is biobased. Non-limiting examples of such biobased resins include: UV-curable epoxidized soybean oil acrylate (UCB, Ebecryl 860), flaxseed triglycerides and polycarboxylic acid anhydrides (Biocomposites and more, PTP), triglyceride acrylate (Cogins, Tribest S531) , epoxidized residual pine oil (Amroy, EPOBIOX™), DSM PalapregR ECO P55-01, Ashland EnvirezR Unsaturated Polyester Resins from Renewable and Recycled Resources, Unsaturated Polyester Soy Oil (Reichhold, POLYLITE 31325-00), Liquid Epoxy Resins with glycerin base (Huntsman) and the like.
[041] In other embodiments, the polymer is at least one thermoplastic resin. Non-limiting examples of such thermoplastic resins include: polyolefins, polar thermoplastics, polystyrene, polyvinyl chloride (PVC), acrylonitrile-butadiene-styrene (ABS), styrene copolymers, polyacrylonitrile, polyacrylates, polyacrylamides, vinyl acetate polymers, polymers vinyl alcohol, cellulose plastics, thermoplastic elastomers, thermoplastic polyurethanes, polyester-based thermoplastic elastomers, thermoplastic polyesters, polyethylene terephthalate, polybutylene terephthalate, compatibilized thermoplastic blends, polyacetal, polyethers, polyarylates, polybenzides, polyimidazoles , aromatic polyhydrazides and polyoxadiazoles, polyphenyl quinoxalines, polyphenylene sulfide, polyphenylene vinylene, conductive thermoplastics, conductive thermoplastic composites, poly(arylether sulfone)s, poly(aryletherketone)s, poly(aryletherketones-co-sulfones ), poly(aryletherketone amide)s, polytetrafluoroethylene and mi tures thereof.
[042] In other embodiments, the at least one resin is selected from a standard polyester, an epoxy, and natural rubber.
[043] To endow the structures of the invention with increased mechanical stability, depending on the final intended application, the porous structure according to the invention can, in some embodiments, be associated with at least one layer of a lamination material, so that the sheets of the structure are oriented normal to said layer. This forms a laminated article. Such an arrangement endows the article with improved resistance to compressive loads exerted in the direction of the orientation of the sheets within the article.
[044] Thus, the invention also provides articles comprising one or more layers of a foam material according to the invention, wherein each of one or more layers can be separated from the other by a laminating sheet or a film polymeric. In some embodiments, the article comprises one or more layers of a foam material according to the invention, wherein the layers are stacked on top of one another without any intermediate or separating film or sheet.
[045] For example, where the article is substantially flat, it can be laminated on one or both of its faces with one or more layers of lamination. Where the article is constructed as a three-dimensional cube, it can be laminated on all of its faces. The lamination film can be any material suitable for the intended use. In some embodiments, on top of a lamination sheet, another structure of a foam material of the invention may be positioned.
[046] In some embodiments, the lamination material is selected from a natural material and a synthetic material. Exemplary, non-limiting natural materials may be selected from natural fabrics including linen, sisal, wood fiber hemp, cotton and the like. Synthetic laminating materials can be selected from mineral wool fiber, glass wool, glass fibers, synthetic fibers such as aramid, paper materials, plastic materials, carbon fibers, metallic sheets, polymeric sheets, polymeric films etc.
[047] In general, the articles of the invention can be constructed by bonding at least one sheet of a laminating material on an outer surface (face) of a porous structure (a foam material). Typically, when forming a flat article, the porous structure is sandwiched between two layers of lamination materials, each of which can be made of similar or different materials. Lamination can be accomplished by applying pressure and/or heat. Thus, for example, an article of the invention can be laminated on one side with a paper material and on the other side with a natural fabric such as linen.
[048] The articles of the invention can be manipulated to any shape and size desired.
[049] In some embodiments, the structure or article of the invention has a honeycomb-like structure. The honeycomb structure is composed of a plurality of substantially elongated open pores, the pores being substantially unidirectionally oriented, the cellulose-based material being selected from nanocrystalline cellulose (NCC), microfibrillary cellulose (MFC) and mixtures thereof.
[050] In some embodiments, the honeycomb-like structure is composed of a plurality of open pores, the pores being surrounded by walls of a cellulose-based material selected from nanocrystalline cellulose (NCC), microfibrillary cellulose (MFC) and mixtures of the same.
[051] In some embodiments, any of the articles, foams, composites or other products according to the invention comprise or consist of NCC fibers that have an average length of 250 ± 100 nm. Such fibers, as further discussed below, are unique in that their length is much longer (longer) than previously prepared and reported NCC fibers.
[052] In another aspect, the invention further provides a structure or an article or a composite or a product, as defined herein, comprising NCC fibers having an average length of 250 ± 100 nm.
[053] In another aspect, the invention provides articles, structures or products that comprise the porous structure of the invention as described herein.
[054] In another of its aspects, the invention provides a process for producing a porous structure composed partially of interconnected cellulose-based sheets, the sheets being substantially unidirectionally oriented, the process comprising: (a) unidirectionally freezing a aqueous slurry of the cellulose-based material in a vessel that has one end, for example, a base that allows efficient heat transfer to perform directional cooling, thus obtaining a porous structure wetted in water; (b) treating said porous structure wetted in water with a first solvent, thereby obtaining a solvent wetted porous structure comprised of substantially unidirectionally oriented interconnected cellulose-based sheets; and (c) optionally evaporating the solvent, to obtain a dry porous structure comprised of substantially unidirectionally oriented interconnected cellulose-based sheets.
[055] In some embodiments, the process comprises: (a) providing a slurry of cellulose-based material in an aqueous medium; (b) unidirectionally freezing said slurry in a vessel having an end, for example, a base, which allows directional cooling, thus obtaining a water-wetted porous structure; (c) treating said water-wetted porous structure with a first solvent, to obtain a solvent-wetted porous structure; and (d) evaporating the solvent, to obtain the porous structure comprised of substantially unidirectionally oriented interconnected cellulose-based sheets.
[056] In some embodiments, the cellulose-based material is selected from nanocrystalline cellulose (NCC), microfibrillary cellulose (MFC) and mixtures thereof.
[057] In some embodiments, the vessel or aqueous medium is treated with ice nucleation seeds, as may be necessary. Alternatively, ice nucleation can be induced by physical methods such as acoustic waves, electrical pulse, or introduction of an ice-containing substrate.
[058] Without sticking to theory, the porous structures of the invention are produced by directional control of ice crystallization in pore domains within the cellulose-based material and subsequently removing ice/water using a solvent exchange process . Cryo-concentration/ice molding/freeze molding methods use the solidification of a solvent (eg, water) to produce porous structures. Growing crystals reject and squeeze the particles suspended between them. In a way, the particles take the form of an inverted replica of the crystals. The confined cellulose nanoparticles self-assemble and are held together by hydrogen and Van der Waals bonds. The final microstructure of the material can be determined through several factors, inter alia, raw state of suspension (eg liquid, emulsion, foam), particle concentration, cooling geometry (thermal gradient), cooling rate, structuring additives of ice and the like.
[059] The slurry (or suspension) used in the process of the invention comprises the cellulose-based material and an aqueous medium (i.e., water or a water-based solution). In some embodiments, the slurry further comprises at least one additive selected from at least one detergent, at least one surfactant, and at least one stabilizer. In some embodiments, the slurry comprises any combination of the above additives.
[060] In some embodiments, the concentration of said cellulose-based material in said slurry is below about 50% (w/v). In some embodiments, the concentration is below about 25%.
[061] In some embodiments, the concentration is at least about 10% (w/v). In other embodiments, the concentration is at most about 10%. In still other embodiments, the concentration is between about 1 and 5% (w/v).
[062] In other embodiments, the concentration is below about 10%. Still, in additional realizations, the concentration is below about 5%.
[063] In some embodiments, the concentration of said cellulose-based material in said slurry is between about 1% and 50% (w/v), or between about 1% and 40% (w/v), or between about 1% and 30% (w/v), or between about 1% and 20% (w/v), or between about 1% and 10% (w/v), or between about 10 % and 50% (p/v), or between about 20% and 50% (p/v), or between about 30% and 50% (p/v), or between about 40% and 50% ( p/v).
[064] The slurry is thrown into a vessel that allows directional cooling, that is, slurry cooling only in one direction of the vessel walls, or any directional cooling, such as radial cooling, typically, but not limited to, cooling of the base or top of the vase. This allows for directional freezing of the aqueous medium into the slurry, gradually orienting the cellulose-based material to result in a porous structure wetted in water.
[065] The vessel can be of any desired shape, as long as the refrigeration unit, for example, the base or top, is made of a material having high thermal conductivity, such as copper, copper alloy, aluminum foil, aluminum fibers. carbon or any other material known to have high thermal conductivity. The other walls of the vessel can be made of a material of low thermal conductivity, typically a polymeric or heat insulating material, or having a structure that reduces its thermal conductivity (such as an insulating double wall structure).
[066] In some embodiments, directional cooling is performed at a constant cooling rate or by keeping one end of the vessel, eg, the base, at a constant temperature. In such embodiments, the base is cooled at a constant cooling rate of between about -1°C/min (1°C reduction per minute) and -40°C/min (40°C reduction per minute). In other embodiments, said rate is between about -1°C/min and about -10°C/min. In other embodiments, said rate is between about -1°C/min and about -5°C/min.
[067] In other embodiments, the end of the vessel, for example, the base, is maintained at a constant temperature that can be between about -40 and -80° C. In some other embodiments, the base temperature is maintained between about -50 and -80°C, between about -60 and -80°C, between about -50 and -70°C, or between about -50 and -60°C.
[068] In some embodiments, the end of the vessel, for example, the base, is maintained at a constant temperature, being between about -80° C and zero degrees. In some other embodiments, the temperature is maintained between about -50 and 0°C, between about -60 and 0°C, between about -50 and 0°C, between about -40 and 0°C, between about -30 and 0°C, between about -20 and 0°C, between about -10 and 0°C, or at 0°C.
[069] In some embodiments, the end of the vessel, e.g., the base, is maintained at a constant temperature, being between about -10 and 0°C, or between about -5 and 0°C, or between about -5 and +4°C.
[070] To allow better control of the formation and progression of the ice front through the slurry during freezing, the inner surface of the end of the vessel, for example, vessel bottom, base, can be precoated with nucleation seeds or a composition comprising them. This allows for a reduction in overfreezing and an increase in the nucleation temperature typical of the aqueous medium to only a few degrees below 0°C, thus avoiding higher overfreezing of the medium, since, under overfreezing conditions, little control of the formation and progression of the ice front.
[071] Nucleation seeds can be selected from such materials known in the art. In general, seeds can be selected from organic, inorganic and materials obtained from biological sources.
[072] The selection of nucleating seeds or nucleating agents that can be used in accordance with the present invention is mentioned or disclosed in any one or more of the following:1. Edwards, G.R., L.F. Evans, 1968: Ice Nucleation by Silver Iodide: III. The Nature of the Nucleating Site. J. Atmos. Sci., 25, 249-256.2. Vali G. Quantitative evaluation of experimental results on the heterogeneous freezing nucleation of supercooled liquids. J. Atoms Sci. 1971; 28 402-4093. Ice Nucleation Induced by Pseudomonas syringael, Environ. Microbiol. 1974, vol. 28 no. 3456-459.4. Identification and purification of bacterial ice-nucleation protein, PNAS 1986, vol. 83 no. 19, 7256-7260.5. The Nucleation of Ice Formation by Silver Iodide, B. Vonnegut J. Appl. Phys. 18, 593 (1947).6. Nucleation Catalysis, David Turnbull and Bernard Vonnegut, Industrial and Engineering Chemistry Vol. 44, No. 6 . 7. Inactivation of Ice Nucleating Activity of Silver Iodide by Antifreeze Proteins and Synthetic Polymers, J. Phys. Chem. B, 2012, 116 (18), p. 5364-5371.8. Nucleation of ice and its management in ecosystems, Philosophical Transactions of The Royal Society of London, Series A-Mathematical Physical and Engineering Sciences, Vol 361, Edition 1804 Pages: 557-574, 2003.9. Improving Ice Nucleation Activity of Zein Film through Layer-by-Layer Deposition of Extracellular Ice Nucleators, Shi, K; Yu, HL; Lee, TC; Huang, QR, ACS Applied Materials & Interfaces, Vol 5, Edition 21, 10456-10464, 2013.10. Li, J. and Lee, Tung-Ching (1995) "Bacterial Ice Nucleation and its Application in the Food Industry" Trends in Food Science and Technology 6: 259-265.
[073] In some embodiments, nucleation seeds are selected from inorganic materials. Such materials can be any one or more of silver iodide, silver bromide, bismuth triiodide and mixtures thereof.
[074] In some embodiments, nucleation seeds are selected among bacterial ice nucleation factors such as Pseudomonas syringae, Erwinia herbicola and Xanthomonas.
[075] In other embodiments, nucleation seeds are selected from bacterial proteins, insect proteins and synthetic nucleation agents as known in the art.
[076] Alternatively, ice nucleation can be induced by physical methods such as acoustic waves, electrical pulse, or introduction of an ice-containing substrate.
[077] Then, the structure wetted in water is treated with a first solvent to remove substantially all the water contained within the pores, thus obtaining a porous structure wetted in solvent. This can be achieved by treating the water-wet structure with a first solvent, typically water soluble, under conditions which permit the exchange of water contained within the structure by the first solvent. This can be done, for example, by swelling the structure soaked in water in a bath containing the first solvent.
[078] In some embodiments, the first solvent is selected from water-soluble solvents such as methanol, ethanol, propanol, iso-propanol, acetone, acetonitrile, tert-butanol, DMF, DMSO, dioxane, THF, ethylene glycol and glycerol.
[079] After water replacement has been completed, the structure wetted in solvent can be dried from the solvent, for example, by evaporation of the solvent; such drying may take place at room temperature or may require reduced pressure.
[080] Following evaporation, a water-free solvent and porous structure is obtained, which can be further used as described here.
[081] In some embodiments, the solvent-wet structure (eg, obtained in step (c) above), may be further treated (i.e., step (c')) prior to evaporation with a second, less water-miscible solvent which has low surface tension, such as hexane or t-butanol. In some embodiments, the second solvent can be selected from methanol, ethanol, propanol, iso-propanol, acetone, hexane, t-butanol, or mixtures thereof.
[082] In some embodiments, the first and second solvents are the same. In other embodiments, the first and second solvents are different from each other.
[083] The process may comprise additional steps, said steps comprising:- immersing the porous structure in a mixture of monomers or pre-polymers, and- affecting the crosslinking of said mixture of monomers or pre-polymers.
[084] In some embodiments, the mixture of prepolymers or monomers is selected from maleic anhydride, maleic acid, fumaric acid, succinic acid, succinic anhydride, 2,5-furan-dicarboxylic acid (FDCA), adipic acid, glycerol , ethylene glycol, neopentyl glycol, trimethylolpropane, pentaerythritol and vegetable oils, for example castor oil.
[085] In other embodiments, the prepolymer mixture comprises a solvent selected from methanol, ethanol, propanol, iso-propanol, acetone, acetonitrile, tert-butanol, DMF, DMSO, dioxane, THF, ethylene glycol or glycerol.
[086] According to other embodiments, the crosslinking is carried out at a temperature between about 80 °C and 200 °C.
[087] The crosslinking rate can be increased by adding catalysts such as organic or inorganic acids, eg tartaric acid, citric acid, p-toluenesulfonic acid (PTSA or pTsOH) or sulfuric acid. Crosslinking can also be optimized by the addition of radical initiators such as azo-bis-isobutyronitrile (AIBN) or peroxides, for example, such as benzoyl peroxide.
[088] The cellulose-based foams/structures of the invention can similarly be formed by mixing the cellulose-based material, for example, NCC suspensions with a detergent/surfactant. The formed dry NCC foam has, in at least one region thereof, the characteristic open cell unidirectionality described herein, and in some embodiments, may exhibit isotropic characteristics.
[089] Thus, in some embodiments, the slurry of a cellulose-based material in an aqueous medium can be formed by mixing at least one detergent or at least one surfactant. In such embodiments, the slurry may be mixed to induce the formation of detergent/surfactant bubbles, i.e., air-containing spheres, within the slurry.
[090] When detergents are used in a method of the invention, the plurality of cells form spherical open cell structures while still maintaining the characteristic unidirectionality, with the pores containing additional open cell structures (spherical cavities or pores of any shape, structure and size) that can be connected to each other, forming an interconnected network.
[091] Alternatively to using a detergent or a surfactant, the plurality of pores or cavities within the foam structure, as defined to have unidirectionality, can be formed by employing at least one material capable of forming gas filled regions or filled regions with liquid or otherwise solid particulates in a medium comprising the NCC, whereby removal of said gaseous, liquid or solid material from said gas-filled regions or regions filled with liquid or otherwise solid particulates, respectively , under conditions specified herein, allows the formation of the plurality of cavities, so that the porous foam of the invention has physical properties that are the same or substantially the same, or uniform or substantially uniform in all directions (being isotropic).
[092] In some embodiments, the cavities within the foam material are achievable by mixing at least one detergent/surfactant material and NCC to form a plurality of detergent spheres containing gas, e.g., air, in which the cladding walls of NCC from the detergent spheres (bubbles). In such embodiments, the NCC is allowed to self-assemble around the walls of said spheres, thereafter the at least one detergent is removed, leaving a plurality of cavities each having a wall surface comprising NCC.
[093] In some embodiments, cavities may be formed by mixing, in the slurry medium, a gas or a gas-forming material to affect the size and distribution of bubbles during the manufacturing process.
[094] In some embodiments, the slurry medium containing the NCC and the material that affects the bubbles in said medium, may further comprise at least one stabilizing agent to modulate the stability of the bubbles.
[095] In other embodiments, the material is achieved by mixing at least one oil to the aqueous medium containing NCC, to form a plurality of oil droplets in said medium, wherein the NCC coats the walls of the oil droplets. In such embodiments, the NCC is allowed to self-assemble around the walls of said droplets, thereafter the at least one oil is removed, leaving a plurality of cavities each having a wall surface comprising NCC.
[096] In some embodiments, where the cavities are formed by the inclusion of at least one detergent or surfactant, the at least one detergent employed according to the invention can be selected from water-based or based foaming agents organic for all purpose. In some embodiments, the at least one detergent is water-soluble or water-insoluble. In some embodiments, said at least one detergent being selected from washing agents, heavy duty washing agents and/or cleaning agents, which may be in liquid, gel or paste type form. In some embodiments, the at least one detergent may be selected from fine fabric liquid detergents, dishwashing agents, light duty or heavy duty dishwashing agents, dishwasher agents, liquid cleaning agents such as such as antibacterial types for hand washing, cleaning bars, mouthwashes, denture cleaners, car or carpet shampoos, bathroom cleaners, hair shampoos, shower gels, bubble baths and others.
[097] In some embodiments, a surfactant material may be used. Such surface active materials can generally be selected from anionic surfactants (such as sulfate esters (SDS), carboxylates or phosphate esters, SDS); cationic surfactants (such as CTAB); non-ionic surfactants; and any other known surfactant or any combination of two or more of that surfactant.
[098] In other embodiments, the foam material can be achieved by mixing an aqueous medium containing NCC, under reduced temperature conditions, as defined in a process of the invention disclosed herein, in the presence or absence of one or more additional agents , for example, detergent material, surfactant, plasticizers such as glycerol or oil and nucleating agents to allow freezing of the medium and slow formation of a structure containing gaps in the form of non-spherical gaps, tortuous channels, or gaps or cavities of substantially any size, shape or structure, where the gaps or cavities are formed by the gas phase mixed in the medium, for example the gas phase being air or any other gas. The structure can be bitten or minced or more vigorously mixed to provide ice-filled cavities of a variety of sizes, shapes and structures. In order to modulate or control the size of ice cavities, the medium can be treated with agents that increase or depress ice growth.
[099] In some embodiments, freezing is achievable in an ice cream freezer or ice cream production unit (large or small scale).
[0100] In another aspect, the invention provides a foam material comprising a plurality of cavities, each of said plurality of cavities having a wall surface comprising nanocrystalline cellulose (NCC), and wherein the NCC is randomly oriented in said material. foam.
[0101] The partially solidified or high viscosity slurry, according to the invention or produced according to processes of the invention, can be molded into a desired structure or shape before final freezing and solvent exchange.
[0102] Thus, the invention further provides a process for preparing a foam/structure of the invention, the process comprising:- mixing at least one cellulose-based material, for example, NCC, with at least one material in a aqueous medium, as disclosed herein; - molding the mixture thus formed under conditions that permit a semi-solid composite, as disclosed herein; - affecting solvent exchange with at least one organic solvent, as disclosed herein; - drying said composite of said solvent organic to obtain a foam of the invention; and - optionally treating said dry foam with a polymeric material or a prepolymer and curing said polymer or prepolymer.
[0103] In some embodiments, said at least one material being selected from at least one detergent/surfactant, at least one gaseous material, at least one material capable of generating gas, at least one oil, or any agent capable of forming a emulsion.
[0104] In some embodiments, the at least one material is a detergent/surfactant.
[0105] In some embodiments, mixing of NCC and said detergent is achieved under high shear conditions. In some embodiments, the high shear mixture provides a cream-like suspension comprising a plurality of detergent bubbles, each being coated with a film, coating or layer of NCC.
[0106] The invention further provides a process for preparing a foam of the invention, the process comprising: - mixing NCC in an aqueous medium under reduced temperature conditions to affect the freezing of said aqueous medium, as disclosed herein; - molding the frozen medium under conditions allowing a composite; - affecting solvent exchange with at least one organic solvent; - drying said composite of said organic solvent to obtain a foam; and - optionally treating said dry foam with a polymeric material or a prepolymer and curing said polymer or prepolymer.
[0107] As disclosed herein, molding can be performed by freezing molding in a mold of a predetermined shape. The mold, into which the NCC suspension is molded, can be formed into any desired architecture. This allows the production of structural parts and core materials of predetermined shapes. Different mold shapes and textures are possible, according to the present invention, allowing the production of parts with various skin textures, such as soft skin and skin with nanopatterning for self-cleaning materials. Some non-limiting examples of mold materials are aluminum, silicon, polystyrene and carbon fiber/epoxy composite molds.
[0108] In some embodiments, the foam mixture is poured into a mold and frozen at any cryotemperature. In some embodiments, the temperature at which freezing occurs is below 0°C. In other embodiments, the temperature is between about -50oC and about -90oC. In additional embodiments, the temperature is between about -60oC and about -80oC and in additional embodiments, the freezing temperature is between about -70oC and about -80oC. In some embodiments, the temperature is between about -80°C and zero degrees. In some other embodiments, the temperature is between about -50°C and 0°C, -60°C and 0°C, -50°C and 0°C, -40°C and 0°C, -30°C and 0°C, -20°C and 0 °C, -10°C and 0°C, or is 0°C.
[0109] In some embodiments, the temperature is between about -10oC and 0°C, or -5oC and 0°C, or -5oC and +4°C.
[0110] In some embodiments, solvent exchange is achieved by first treating the foam with a water-soluble solvent, for example, ethanol, methanol, acetone, iso-propanol, etc., or with a saline solution aqueous (NaCl, NaBr, KC1, KBr, and others), under conditions that allow the exchange of water contained within the foam cavities with a water-soluble solvent or with the salt. This can be achieved, for example, by soaking the foam material in a bath containing the water-soluble solvent or saline solution. In order to minimize structural damage to the foam, the solvent is typically cooled to a temperature below 0 °C.
[0111] In some embodiments, ethanol is added and the foam is allowed to thaw.
[0112] In yet another aspect, the invention provides the use of a porous structure, as described herein, in the preparation of a composite article.
[0113] In some embodiments, said composite article is selected from a panel, a flexible sheet, a tile, a wing part, a structural element, a wall panel, a floor panel, wall elements on boats and ships and others.
[0114] In some embodiments, the composite is selected from a substantially two-dimensional structure. In other embodiments, the article is a three-dimensional structure.
[0115] The invention also provides a honeycomb-like structure of a material selected from nanocrystalline cellulose (NCC), microfibrillar cellulose (MFC) or mixtures thereof, the structure comprising a plurality of cell channels formed by the channel walls. In some embodiments, the honeycomb structure is formed by a process in accordance with the invention.
[0116] In a beehive-like article of the invention, each of the channel walls being substantially unidirectionally oriented; namely, the honeycomb comprises a plurality of substantially elongated open pores, the pores being substantially unidirectionally oriented with the walls of the channel comprising a cellulose-based material selected from nanocrystalline cellulose (NCC), microfibrillar cellulose (MFC) and mixtures thereof.
[0117] A beehive can be prepared by any process known in the art, including swaging, corrugating and molding, each as known to the artisan.
[0118] In some embodiments, the hive is prepared according to a method of the invention. As can be understood, the methods disclosed herein allow for the production of bulk foams and also foams with complex internal architecture such as a honeycomb structure. In non-limiting embodiments, the honeycomb foam is formed by dipping into the NCC slurry, prior to freezing, a mold having a plurality of elongated pins, typically each pin having any cross-sectional shape, e.g., rounded or hexagonal shape, to provide an NCC structure having a honeycomb shape (the mold making the foam a honeycomb shape). Due to directional freezing, the compressive strength of the foam is increased compared to non-directional foams.
[0119] The NCC employed in a process or product according to the invention may be any NCC known in the art, or NCC as defined herein. In certain cases, the need arises to provide an exquisite NCC material that can be prepared by a well-tuned process comprising treating a cellulose-containing material with an aqueous solution comprising between 59 and 63% acid. The process can be carried out on a variety of cellulose-containing materials of any purity and consistency, such as paper mill waste, including waste in the form of pulp sludge from paper mills.
[0120] As will be demonstrated below, the NCC produced by this process which uses an acid concentration specifically selected to be between 59 and 63% is highly unique and suitable for a wide variety of uses, as compared to NCC prepared by processes known in the art.
[0121] Thus, the invention provides in other of its aspects, a process for the production of NCC, the process comprises: a) treating a material containing cellulose with a formulation comprising between 59 and 63% acid, said treatment does not change the cellulose morphology; b) cause preferential degradation of amorphous cellulose domains while keeping crystalline cellulose domains intact; and c) isolating the crystal domains.
[0122] In some embodiments, the process further comprises the step of treating the cellulose-containing material to separate from it the cellulose in pure and substantially pure form.
[0123] In further embodiments, the process comprises dispersing the product obtained in step c) to obtain NCC.
[0124] In some embodiments, acidification is achieved through an acid selected from H2SO4, HCl, HBr and HNO3. In some embodiments, the acid is H2SO4.
[0125] In some embodiments, the acid concentration is 59, 60, 61, 62 or 63%.
[0126] In some embodiments, the acid concentration is 61, 62, or 63%.
[0127] In some embodiments, the acid is H2SO4, and the concentration is 59, 60, 61, 62 or 63%.
[0128] In some embodiments, the acid used is H2SO4, at a concentration of 62 or 63%.
[0129] In some embodiments, the ratio between the weight of the material containing cellulose, for example, pulp and the volume of the acid, for example, sulfuric acid, is between 1 and 40.
[0130] In some embodiments, the NCC produced is characterized by nanocrystals having an average length of 250 ± 100 nm.
[0131] In some embodiments, the NCC produced by the process is characterized by a charge in the range of ~0.3 to 0.9 mmol/g.
[0132] In some embodiments, acidification is performed at any temperature. In some embodiments, the temperature is between 40 and 60 °C.
[0133] The process of the invention can be carried out on a variety of cellulose-containing materials. Such materials can be, for example, any "cellulose sludge source", i.e. a sludge or waste material from which separation of the cellulose is required or intended. The sludge cellulose source can contain between 5 percent and about 60 percent cellulose (based on the total amount of solid matter). In some embodiments, the cellulose sludge source is sludge from the paper industry. Within the context of the present invention, "cellulose source of paper sludge", also known as "paper mill waste" or "paper mill sludge", refers to discharges from paper mills containing remnants of pulp that remain after the paper and pulp are prepared.
[0134] In some embodiments, the sludge cellulose source is a selected source of paper pulp, paper waste water (obtained after the cellulose pulp is filtered through a high mesh filter mesh) and to any source of recycled cellulose from agricultural or industrial by-products, for example, municipal sludge (made from, for example, pieces of toilet paper, vegetable fibers, etc.), municipal sewage (such as dairy farm sludge and all from wheat straw to sunflower stalks, and other agricultural cellulosic waste, waste from the garment industry, or recycled rags and pulp discards from other sources).
[0135] In comparison to the so well known processes for producing NCC from cellulose from a variety of sources, the NCC obtained by the process of the invention was determined to be unique and superior. A comparative study is summarized in Table 1 below:

Table 1: A comparative study comparing a process according to the invention with available processes for making NCC.
[0136] As noted above, in some selected embodiments, in a process according to the invention, the following conditions are used: 59 to 63% H2SO4, 50 °C, 1 to 4h, at a ratio of 1:10 /15 gram of pulp/volume of H2SO4. In some embodiments, the ratio may be 1:40 per 15 grams of pulp per volume of acid.
[0137] As Table 1 further demonstrates, at 64% acid concentration, NCC could not be isolated. In contradiction to existing technologies, the process of the invention allows the formation and separation of NCC materials characterized by fibers having an average length between 150 and 350 nm. The fibers from the technique proved to be shorter.
[0138] Thus, in another aspect, the invention contemplates a powder consisting of NCC fibers, the fibers having an average length of 250 ± 100 nm.
[0139] In another aspect, a solution is provided consisting of NCC fibers and at least one solvent, the NCC fibers having an average length of 250 ± 100 nm. In some embodiments, the solution consists of NCC fibers and water. In some embodiments, the solution consists of an acid and NCC fibers, the acid can be in the form of an aqueous acid solution or pure. In some embodiments, the solution is a dispersion of NCC fibers in at least one organic medium.
[0140] The invention also contemplates the use of NCC produced by the process in the production of articles, films and composites thereof, as revealed here. In some embodiments, the article is a foam material or a composite.
[0141] The invention further provides foam materials, as disclosed herein, foam materials comprising NCC fibers having an average length of 250 ± 100 nm. BRIEF DESCRIPTION OF THE DRAWINGS
[0142] In order to better understand the matter disclosed here, and to exemplify how it can be done in practice, the embodiments will now be described, by way of non-limiting example only, with reference to the attached drawings, in which:
[0143] Figure 1 shows an exemplary schematic representation of a controlled cooling system used in a process of the invention.
[0144] Figure 2 shows the ice front kinetics during unidirectional freezing of 3% of NCC slurries under various cooling regimes.
[0145] Figure 3 shows the dependence of the ice front velocity on the heat flow for 3% of NCC slurries.
[0146] Figure 4A is a comparative image of samples cooled to -3°C/min, -5°C/min and at a constant temperature of -50°C. Figures 4B and 4C are SEM images of the highly oriented structures for NCC samples cooled to -3°C/min and -5°C/min, respectively.
[0147] Figure 5 shows compression tensile strength curves for samples cooled to -3°C/min, -4.8°C/min and -5°C/min.
[0148] Figure 6 provides a graphical presentation of compressive strengths of foam boards according to the invention.
[0149] Figures 7A to 7D are images showing the sequence of preparation of NCC beehive structures of the invention. DETAILED DESCRIPTION OF ACHIEVEMENTS NCC Preparation
[0150] 10 grams of 200 µm particle size microcrystalline cellulose (MCC, Avicel) were suspended in 200 ml of DDW in a glass vial. The flask was placed in a cold water bath while shaking. H2SO4 was gradually added to a final concentration of 59% while keeping the temperature at about 50°C. The suspension was transferred to a 60 °C water bath and incubated during shaking for 2 to 4 hours followed by centrifugation at 8000 rpm for 10 min. The acid was removed and the pellet was resuspended in DDW. The wash and resuspension cycles were repeated 4 to 5 times until the supernatant leaving the centrifuge was cloudy. After the final wash, NCC was suspended in around 90 ml of DDW (to give around 5% NCC concentration). A sample of the precipitate was weighed before and after drying to determine the concentration of wiskers.
[0151] The same procedure was repeated, mutatis mutandis, with an acid concentration between 60 and 63% to produce NCC of identical quality and purity.
[0152] When the acid concentration was 64% and higher or 58% and lower, NCC was not isolated. The materials obtained under these conditions contained the cellulose materials of different and variable constitutions. Comparative data are shown in Table 1. PREPARATION OF NCC FLUID PASTES
[0153] NCC suspensions were prepared either by acid hydrolysis or by mechanical disruption of cellulose fibers. The cellulose source that was used varied. At all times, NCC production followed mutatis mutandis, the process described below. It should be understood that while the present example specifically described the production of NCC from microcrystalline cellulose, NCC was similarly obtained from other sources such as pulp and paper industry waste. Hydrolysis:
[0154] Hydrolysis was achieved in a solution of 60% H2SO4, 50°C preheated. The dry pulp was added to this acidic solution at the rate of 15 L of acid/1kg of dry solids. The suspension was mixed with a mechanical stirrer for 2h. The suspension was then cooled to 15°C and transferred to centrifugation at 5,000g for 5 min. The acid was removed and the pellet was resuspended in DDW. The wash and resuspension cycles were repeated 4 to 5 times until the supernatant leaving the centrifuge was turbo and the retentate reached pH 3.
[0155] The same process was repeated at the acid concentration between 59 and 63%.
[0156] After the final wash, NCC was suspended in the required amount of DDW to give the final concentration of NCC (1% to 40%). Neutralization of NCC was done with 1M NaOH. A sample of the precipitate was weighed before and after drying to determine the concentration of NCC. 0.1 to 10% suspensions of NCC in water were prepared, followed by sonication through a probe sonicator until the solution became optically clear. The final honey-like viscosity of the liquid crystal suspension was reached after it had cooled down for a few hours. THE COOLING SYSTEM
[0157] In order to produce foams with vertically aligned pores, a microstructure that combines high compressive and shear strength, a system to control the cooling rate of NCC slurries was constructed (Figure 1). The system included a cooling stage, constructed from a heat conductive plate (104), eg steel, aluminum, copper system, and with internal circulation that allows refrigerant flow, eg liquid nitrogen/gas (102). The refrigerant (liquid or gas) was carried through the cooling system, thus controlling the temperature of the plate. The system also includes at least one temperature measurement unit to allow temperature control of the cooling stage.
[0158] The mold used to produce the NCC foams combined a heat conductive bottom (106) made of a highly thermally conductive metal, eg copper; and insulating walls (108), such as those made of Delrin®, having low thermal conductivity (high temperature resistance).
[0159] In other non-limiting examples, freezing was performed in a standard refrigerator at -80oC. Control of cooling was achieved by assembling a mold that was thermally insulated, with the bottom of the mold being made of a conductive material such as copper. Following the pouring of the beaten slurry of NCC, the mold was placed in a refrigerator at -80oC. The frozen foam was treated as described above. FOAM PREPARATION PROCESS
[0160] Before casting and freezing, the mold was pretreated by coating with ice nucleation factors (SNOMAX®), which started freezing around -3oC. The powder was dissolved and spread on the copper bottom of the mold. Subsequently, the mold was dried, resulting in coating the bottom with the nucleation factors. The use of nucleation factors allowed to reduce the supercooling water in the NCC slurries, while maintaining the gradual freezing and controlled progression of the ice crystals along the desired temperature gradient.
[0161] The NCC slurry was melted in the mold, and the mold was transferred to the cooler until the slurry stabilized at 4 °C. Then, the mold was placed in the pre-cooled (0 °C) cooling stage and the temperature was reduced either at a rate of 1 to 40 °C/min, or by keeping the cooling stage at a constant temperature below -30 °C.
[0162] After freezing was completed, cold ethanol (4 °C) was added and the frozen foam was allowed to thaw overnight. Ethanol was removed and solvent exchange was repeated twice with fresh ethanol.
[0163] Glycerol and maleic anhydride (mole ratio 1:1.5) were dissolved in ethanol. To start off 20 g of the glycerol/maleic anhydride mixture, 80 ml of ethanol was used. The density of the crosslinked foams was decided by the amount of ethanol used compared to the total weight of the mixture of glycerol and maleic anhydride. Castor oil was added to the monomers to introduce more hydrophobicity to the crosslinked foams. Typically 20% castor oil was used compared to the monomer blend, eg 4g castor oil to 20g maleic anhydride and glycerol blend.
[0164] The solution containing the monomers was used to soak the dry NCC foams or NCC foams containing a solvent, for example, ethanol. If the NCC foam contained a solvent, immersion was performed during gentle agitation for 8 to 24 hours followed by draining off the remainder of the monomer solution. The foam was then cured at lower temperatures first at about 100°C for 6 to 12 hours, followed by curing at higher temperatures of 130 to 160°C for 1 to 4 hours. OPTIMIZATION OF FREEZING CONDITIONS FOR UNIDIRECTIONAL FOAM PRODUCTION
[0165] To explore the ideal freezing conditions, different freezing rates and temperatures were tried, mainly freezing at constant temperature and at decreasing temperature.
[0166] The effect of freezing rate on ice frontal velocity was evaluated by video imaging of ice frontal progression during freezing process. To visualize and record the frontal progression of ice, a transparent mold frame was used. Freezing was performed at different freezing rates: between -0.5 and -40 °C/min. Freezing was also carried out in one stage with a constant temperature of between -50 and -70°C at the heat-conductive bottom (106, Figure 1). See comparative results in Figures 2 to 3.
[0167] After freezing, the samples were freeze-dried and analyzed using electron microscopy (SEM). It can be concluded that the most aligned pore structure for 3% NCC paste was obtained at freezing rates between 3 and 5° C/min (Figure 4). At higher freezing rates (eg 10-40°C/min), more interconnects appeared in the pore structure.
[0168] To measure the effect of morphology, the samples were tested for compressive strength using the tension tester. It was concluded that freezing rates of 3-5° C/min gave more aligned structures in the Z direction and therefore higher compressive strength in this direction (Figure 5). The foams were analyzed by compression tests using an Instron tension tester set to compression mode at a rate of 1.3 mm/min. Force (N) and displacement (mm) curves were recorded during compression. Stress/strain curves were generated by dividing the force by the surface area of the samples and dividing the displacement by the height of the samples (Figure 6). The foams were cast in 2cm diameter molds and measured for compressive strength using the Instron Model 3345 machine; 5,000N load cell. Measurements were performed at a rate of 2.5 mm/min. PRODUCTION OF 30 X 20 X 2 CM UNIDIRECTIONAL FOAM PANELS
[0169] 1500 ml of 3% NCC slurry was poured into the Delrin® copper mold and transferred to the refrigerator until the temperature was stabilized at 4°C. The pre-cooled mold was then placed in the freezing stage with liquid nitrogen flow which reduced the temperature at a rate of 3°C/min until it reached -150°C. After freezing was completed, cold ethanol was poured on top of the slurry. frozen and allowed to thaw. After thawing, the fluids were removed and another two ethanol washes were performed. The compressive strength of a foam panel according to the invention is given in Figure 6. As can be seen, the compressive strengths can vary between about 2 and 0.4 MPa due to changes in density. 100 kg/m3 foams obtain compressive strength around 0.4 MPa while 200 kg/m3 foams obtain compressive strength around 2 MPa.BEEHIVE TYPE FOAM
[0170] The above methods allow the production of bulky foams, but also foams with complex internal architecture such as a honeycomb structure. This is allowed by preparing a second mold which is immersed in the NCC slurry prior to freezing (Figure 7). The mold imparts a honeycomb-shaped foam and is removed during drying of the foam. Due to directional freezing, the compressive strength of the foam is increased compared to non-directional foams. It has been observed that freezing rates that result in frontal ice progression of above 5 mm/min, the foams shrink along the Z axis; nevertheless, this has been found to allow for the formation of film-like walls around the honeycomb-like cells, resulting in significantly increased compressive strengths.
[0171] Example 1: A 1.0 L suspension comprising 2-5% NCC was mixed with a 2% solution of xyloglucan. A 1:1 mixture of water and a commercial detergent was prepared and added to the mixture with stirring. After adding 2 ml of a detergent, stirring was continued until the volume reached 1.3 L. A solution of nucleation factors (1 pellet of Snomax snow inducer dissolved in 50 ml of DDW) was added to the top of a 360x260 mm copper plate having plastic walls (12x12 mm). The nucleation factor solution was spread evenly and dried on the plate. The foam NCC suspension was added to the surface of the copper plate and the foam surface was even made by kneading. A freezing stage was pre-cooled to -80°C and the mold containing NCC foam was applied to the top.
[0172] After freezing, cold ethanol was added to the frozen NCC foam. After thawing, more ethanol was added to the foam to remove remaining water while stirring. The foam was now ready by crosslinking. 100 g of glycerol (1.086 mol), 160 g of maleic anhydride (1.629 mol) and 50 g of castor oil (0.056 mol) were dissolved in 0.5-1 L of ethanol which was added to the foam. The amount of ethanol determined the final density of the foam. The monomer solution was removed and the swollen foam was cured at 110°C overnight. Further curing at 150 °C for 1-2 hours provided hard yellow foams.
[0173] To improve the mechanical strength and flame retardant properties, the foams were swelled with a solution of furfuryl alcohol, furan resin, boric acid and triphenyl phosphate in acetone or ethanol. The swollen foams were cured at 130-150°C until strong black foams were obtained.
[0174] Example 2: An ice cream maker was used for the following experiments with NCC and different additives.
[0175] NCC was mixed with ethanol or glycerol before mixing in the ice cream maker to obtain a sorbet or slurry like texture of NCC. In one experiment, a 5% NCC suspension was mixed with ethanol to obtain an ethanol concentration of 5%. After pre-freezing, the NCC was poured into a mold for final freezing at a lower temperature.
[0176] In another experiment, glycerol was also tested with NCC in the ice cream maker. A similar sorbet texture was obtained using 10% glycerol. In a third experiment, a pre-made 5% ethanol sorbet was added to the ice-cooled NCC. The mixture was then completely frozen at lower temperatures.
[0177] Example 3: Another approach was to use solvents with a high freezing point, eg glacial acetic acid and DMSO to create fluidity in the NCC. Acetic acid or DMSO were first frozen and then mixed with different amounts of ice-cold NCC. The NCC containing the frozen solvents was directly placed in ethanol for precipitation of the NCC and leaching of the frozen solvents. Alternatively, NCC with acetic acid or DMSO crystals was completely frozen prior to solvent exchange and drying.
[0178] Example 4: NCC emulsion with castor oil was also prepared to investigate the possibility of creating closed cell structures within NCC due to micelle formation. Detergents were used to stabilize the emulsions. The reason for using castor oil was the oil's high solubility in ethanol. Emulsions were directly frozen or placed in ethanol.
[0179] Example 5: During the experiments, it was found that when NCC was vigorously mixed with a detergent, it was concentrated on the walls of the bubbles acting as a fibrous surfactant and stabilizes the foam. As a result, thick foam was formed similar to cream or beaten eggs.
[0180] Different detergents were tested. In the initial experiments, the NCC/detergent mixtures were vigorously stirred in a homogenizer (UIltra Turrax) until homogeneous foams were obtained. Foaming was controlled by the amount of detergent and the speed of mixing. After the initial experiments, an NCC concentration was adjusted to 5% assignment of the same foam density as with the aligned NCC foams taking into account the volume increase. The mixture was adjusted to reduce speed to ensure homogeneous foaming. For 1 L of NCC with a concentration of 5%, 2 ml of a detergent-water (1:1) mixture was used. Upon reaching the volume of 1.3 L, the foams were ready for freezing.
[0181] After tapping was completed, the samples were frozen in the same freezing stage previously used for inline foams. During the freezing experiments, it was observed that the whipped foams were resistant to low temperatures without any shrinkage that was observed in the previously manufactured foams. Furthermore, it was found that the foam structure was much less susceptible to differences in freezing conditions, so it was no longer necessary to freeze in a temperature gradient and foams could be produced at a constant temperature, eg -80° Ç. This resulted in relatively quick freezing (15 to 20 minutes to completion) and also the possibility to freeze multiple foams in a row. The stage could be kept at a constant temperature by omitting the time consuming requirement to reheat the freeze to 0 °C before each freeze cycle.
[0182] Attempts have also been made to freeze the foams in freezing air (refrigerator). Compared to freezing according to processes of the invention, freezing air allowed the progression of several ice fronts from different directions and should increase the freezing rate. Once bottom freezing has been maintained, the foams still retain some degree of Z-direction orientation combined with the spherical isotropic structure which yields the foams significantly improved homogeneity, bending and shear strength.CHARACTERIZATION OF FOAM STRUCTURES AND OTHER FOAM PRODUCTS AGREEMENT WITH THE INVENTION
[0183] The foam samples were cut and analyzed by scanning electron microscopy (SEM). SEM analysis showed a clean structure of the foams. When NCC has been dried and frozen in a directional freeze, it will self-assemble into laminated structures as defined here. Interestingly, this structure was maintained in the products according to the invention.
[0184] When foams were made using a detergent as described, sheets were formed around the soap bubbles resulting in a spherical structure. The structure was formed during tapping where the liquid solution of water, NCC, xyloglucan and a detergent were concentrated on the walls of the bubbles. During freezing, the bubble structure was maintained and dictated the final foam of the spherical structure. SEM images were analyzed by “ImageJ” image processing software [Rasband, WS, ImageJ, US National Institutes of Health, Bethesda, Maryland, USA, http://rsb.info.nih.gov/ij/, 1997 -2014]. Mean pore size was determined to be 100 µm ± 32 µm. The only sheet thickness was single 5 µm, similar to laminated directional foams. Furthermore, the spheres exhibited open cell structure and were relatively homogeneous throughout the foam. The spherical structure of the foams improved their resistance to shrinkage and bending.
[0185] The initial step in preparing the foam density test was the removal of the foam edges. The foams were cut with a scroll saw in dimensions of 20 X 30 X 1 cm, weighed and the density was recorded. Using chalk on the blackboard, the foam was divided and saw cut into 5 X 5 cm. Each sample was weighed for density calculation followed by the compression test.
[0186] Once the first two foams are ready, they were cut for compression testing as described above. Statistical analysis of all foams was performed by the Analysis of Variation (ANOVA) procedure using JMP 11 software (JMP 11 Statistical Discovery™).
[0187] As shown in Table 2 below, the #1 and #2 foams met the density requirements, but their compressive strength was slightly below 1 MPa. This result required further improvement in the production method in the final stage of crosslinking. Formulation adjustments to the furfuryl alcohol and flame retardant final crosslinks allowed for significant improvements in foam strength. As shown below, improvements were made in several steps until the most satisfactory formulation was achieved. After the first improvement, a set of 3 new foams was prepared for testing (foam no. 3 to 5). Test results indicated that the improved forms foams and all three of the latter foams met the technical parameters.
[0188] Additional foams were prepared in order to try and achieve higher compressive strength results. The improvement was mainly accomplished by modifying the crosslinking reaction, optimizing the ratios between components and crosslinking time and temperatures. A set of two foams was prepared, which felt the hand print significantly stronger compared to previous foams. The tests indicated that, in fact, they were significantly stronger, but also slightly heavier, since the density was raised above 200 kg/m3 (foam #7 and 8). Consequently, the crosslinking has been fine-tuned once more to generate a set of four new foams with improved strengths compared to foams 1 to 5, as well as a density that meets the requirements. Furthermore, the foams were relatively homogeneous in their density and compressive strength (foam n° 8 to 11).

Table 2: Summary of foam compression studies
[0189] The flame retardant properties of the foam were evaluated in comparison to commercial expanded rigid PVC foam. During the development of the flame retardant formulations, qualitative evaluation of the foam samples was carried out under aggressive flame condition by applying the Bunsen burner flame for 60 seconds. During testing, it was observed that the expanded PVC foam produced relatively large flame and relatively large amounts of black smoke. Examination of the samples after firing revealed that the foam deformed and lost significant mass. Furthermore, the fire progressed and consumed much of the foam. On the other hand when the NCC foam was exposed to fire, a significantly lower flame weight was observed with significantly reduced smoke generation. Furthermore, flame damage was local and moderate structural deformation was observed.
[0190] Quantitative testing was carried out in accordance with EN ISO 11925-2:2010 standard “flammability test of construction products subjected to direct flame impact”. The foams were cut into 8 X 30 X 1 cm strips which were tested according to the pattern. The test included applying a small flame to the sample for 30 seconds. All samples that were tested did not burn at all. No droplets were observed and observation in the thermal chamber indicated that the foams cooled very quickly and could be touched within 1 minute of flame removal. The test was extended to 120 seconds with similar results.
[0191] In addition to the previous fire test, the foam samples were burned, non-destructive thermal characterization was performed. The average thermal resistance of the foams was 0.044 W/mK similar to insulation materials such as mineral wool at a density of 180 kg/m3 (0.043 W/mK).
[0192] Table 3 provides a summary of the ISO 11925-2:2010 flame test results.
[0193] Further tests were performed comparing NCC foam to commercial expanded PCV foam. During the test, different parameters were measured in order to determine the properties of the samples. Application of the flame to the expanded PVC foam resulted in the immediate formation of extensive orange flame and extensive black smoke. The expanded PVC foam failed the criteria of the “flame tip test start time to reach 150 mm” criteria which occurred in a few seconds.

Table 3: Summary of flame test resultsISO 11925-2:2010
[0194] The performance of the NCC foam was significantly superior. The flame was limited, little smoke was produced and the flame tip was kept significantly below 150 mm throughout the test.
[0195] After removal of the flame, the foam was inspected and the surface area of the damage was measured. The damage surface area of expanded PVC foam was significantly greater compared to NCC foam. In fact, the damaged area of the NCC foam was limited to the surface while the foam maintained in its structural integrity compared to expanded PVC foam had significant structural damage and deformation was observed.

权利要求:
Claims (24)
[0001]
1. PROCESS FOR THE PRODUCTION OF A POROUS STRUCTURE COMPOSED OF PARTIALLY INTERCONNECTED CELLULOSE-BASED SHEETS, the sheets being substantially unidirectionally oriented, the process being characterized by comprising: (a) freezing, in a unidirectional way, of an aqueous slurry of cellulose-based material and at least one detergent or at least one surfactant or at least one material capable of forming regions filled with gas or filled with liquid or solid particles, in a vessel having an end that allows directional cooling, thus obtaining a water-wetted porous structure; (b) treating said water-wetted porous structure with a first solvent, thereby obtaining a solvent-wetted porous structure comprised of substantially unidirectionally oriented interconnected cellulose-based sheets; and (c) optionally, evaporation of the solvent, to thereby obtain a dry porous structure comprised of substantially unidirectionally oriented interconnected cellulose-based sheets.
[0002]
2. Process according to claim 1, characterized in that it comprises: (a) supplying a slurry of the cellulose-based material in an aqueous medium; (b) freezing, in a unidirectional manner, said slurry in a vessel having an end that allows directional cooling, thus obtaining a porous structure moistened in water; (c) treating said water-wetted porous structure with a first solvent, thereby obtaining a solvent-wetted porous structure; and (d) evaporation of the solvent, to thereby obtain the porous structure comprised of substantially unidirectionally oriented interconnected cellulose-based sheets.
[0003]
3. Process according to any one of claims 1 or 2, characterized in that the cellulose-based material is selected from nanocrystalline cellulose (NCC), microfibrillar cellulose (MFC) and mixtures thereof.
[0004]
Process according to claim 3, characterized in that the concentration of the cellulose-based material in the slurry is below 50% (w/v).
[0005]
5. Process according to claim 1, characterized in that it further comprises at least one stabilizing agent.
[0006]
6. Process according to claim 1, characterized in that at least one detergent is selected from all-purpose water-based and organic-based foaming agents.
[0007]
Process according to claim 1, characterized in that at least one detergent is water-soluble or water-insoluble.
[0008]
Process according to claim 1, characterized in that at least one detergent is selected from washing agents, heavy duty washing agents and/or cleaning detergents.
[0009]
Process according to claim 8, characterized in that at least one detergent is selected from liquid detergents for fine fabric, dishwashing agents, light duty and heavy duty dishwashing agents, dishwasher agents , liquid cleaning agents such as antibacterial hand washes, cleaning bars, mouthwashes, denture cleaners, car or carpet shampoos, bathroom cleaners, hair shampoos, shower gels and bubble baths.
[0010]
10. PROCESS according to claim 1, characterized in that at least one surfactant is selected from anionic surfactants, cationic surfactants and non-ionic surfactants.
[0011]
11. PROCESS, according to any one of claims 1 or 2, characterized in that unidirectional cooling is carried out at a constant cooling rate or by maintaining the end of the vessel at a constant temperature.
[0012]
12. PROCESS according to claim 11, characterized in that the end of the vessel is cooled at a constant cooling rate between -1 and -10 °C/min.
[0013]
13. Process according to claim 11, characterized in that the end of the vessel is kept at a constant temperature, being between -40 and -80°C.
[0014]
Process according to claim 11, characterized in that the temperature is kept between -10 and 0°C, or -5 and 0°C, or -5 and +4°C.
[0015]
A process according to any one of claims 1 or 2, characterized in that the vessel or the aqueous medium is treated with ice nucleation seeds to aid in freezing the slurry.
[0016]
16. PROCESS FOR PRODUCTION OF NCC FROM A MATERIAL CONTAINING CELLULOSE, the process characterized by comprising: a) treatment of the material containing cellulose with a formulation comprising between 60 and 63% sulfuric acid, said treatment does not change the morphology of the cellulose present in the cellulose-containing material; b) keeping the cellulose-containing material treated at 50°C for a period between 1 and 4 h, thus causing preferential degradation of amorphous cellulose domains to occur while keeping the crystalline cellulose domains intact; and c) isolating the crystalline domains of NCC.
[0017]
Process according to claim 16, characterized in that the acid concentration is 60, 61 or 62%.
[0018]
18. PROCESS according to claim 16, characterized in that the process is carried out in an acid concentration between 60 and 63% of H2SO4, at 50°C, for a period between 1 and 4h, and in a ratio of 1:10 /15 gram of pulp/volume of H2SO4.
[0019]
A process according to claim 16, wherein the NCC produced is characterized by nanocrystals having an average length of 250 ± 100 nm.
[0020]
20. POWDER CONSISTING OF NCC FIBERS, characterized in that the fibers have an average length of 250 ± 100 nm.
[0021]
21. SOLUTION CONSISTING OF NCC FIBERS AND AT LEAST ONE SOLVENT, characterized in that NCC fibers have an average length of 250 ± 100 nm.
[0022]
22. SOLUTION according to claim 21, characterized in that it consists of NCC fibers and water.
[0023]
23. SOLUTION according to claim 21, characterized in that it consists of an acid and NCC fibers.
[0024]
24. SOLUTION according to claim 21, characterized in that it is a dispersion of NCC fibers in at least one organic medium.

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同族专利:

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公开号 | 公开日

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CN111217922A|2020-06-02|

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CN106068278A|2016-11-02|

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US20160369078A1|2016-12-22|

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EP3099735A1|2016-12-07|

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US10669390B2|2020-06-02|

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BR112016017448A2|2020-08-18|

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KR20160113706A|2016-09-30|

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AU2015212333A1|2016-08-11|

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JP2017506678A|2017-03-09|

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WO2015114630A1|2015-08-06|

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JP6553062B2|2019-07-31|

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CA2938142A1|2015-08-06|

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KR102358824B1|2022-02-07|

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IL246938A|2019-01-31|

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AU2015212333B2|2019-01-24|

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法律状态:
2019-12-17| B06U| Preliminary requirement: requests with searches performed by other patent offices: procedure suspended [chapter 6.21 patent gazette]|

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2021-05-11| B09A| Decision: intention to grant [chapter 9.1 patent gazette]|

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2021-06-08| B16A| Patent or certificate of addition of invention granted [chapter 16.1 patent gazette]|Free format text: PRAZO DE VALIDADE: 20 (VINTE) ANOS CONTADOS A PARTIR DE 29/01/2015, OBSERVADAS AS CONDICOES LEGAIS. |

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