Patent Application
20240183107
The present disclosure relates to a dispersion and a composite, and producing methods thereof.
Due to growing environmental awareness, studies for the practical applications of biomass-derived materials have been conducted around the world. A cellulose nanofiber (hereinafter also referred to as “CNF” as appropriate) obtained by fibrillating a cellulose fiber derived from a wooden material (for example, a wood chip) to nanosize, and a cellulose nanocrystal (hereinafter also referred to as “CNC” as appropriate) obtained by hydrolyzing an amorphous part of a cellulose fiber with an acid have been attracting attention as environmentally compatible novel materials. For example, Patent Literature 1 discloses a sulfate-esterified CNF and a producing method thereof, and Non Patent Literatures 1 to 3 describe composite films containing CNF and CNC.
The composites containing CNF and CNC as described in Non Patent Literatures 1 to 3 are produced by applying and/or filtrating a dispersion containing CNF and CNC and drying the resultant. From the aspect of reducing the production cost of the composite, it is advantageous that a dispersion is dried to remove a dispersion medium and obtain a dried body, the dried body is transported and/or stored, after which a dispersion medium is added to the dried body to obtain a dispersion again, and then the dispersion is used to produce the composite. Therefore, the dispersion preferably has a physical property (specifically, viscosity) that changes little even after drying and redispersing. The dispersion preferably has a long pot life (usable time). Furthermore, the composite containing CNF and CNC is required to have a higher rupture strength and a higher oxygen gas barrier property when used as a packaging material or a container material.
Therefore, the present disclosure provides a dispersion of CNF and CNC that maintains its physical property even after drying and redispersing and has a long pot life. Additionally, the present disclosure provides a composite of CNF and CNC having a higher rupture strength and a higher oxygen gas barrier property. Furthermore, the present disclosure provides methods for producing the dispersion and the composite.
According to one aspect of the present disclosure, a dispersion comprising a cellulose nanofiber having a sulfate ester group and a cellulose nanocrystal having a sulfate ester group is provided.
According to one aspect of the present disclosure, a composite comprising a cellulose nanofiber having a sulfate ester group and a cellulose nanocrystal having a sulfate ester group is provided.
According to one aspect of the present disclosure, a method for preparing the dispersion as defined in the above-described aspect is provided. The method comprises mixing a dispersion of a cellulose nanofiber having a sulfate ester group with a dispersion of a cellulose nanocrystal having a sulfate ester group while applying a shear force.
According to one aspect of the present disclosure, a method for producing the composite as defined in the above-described aspect is provided. The method comprises: (a) forming a first layer containing a liquid and one of a cellulose nanofiber having a sulfate ester group or a cellulose nanocrystal having a sulfate ester group; (b) forming a second layer on the first layer by supplying a dispersion containing another of the cellulose nanofiber having a sulfate ester group or the cellulose nanocrystal having a sulfate ester group on the first layer; and (c) removing the liquid from the first layer and the second layer.
The present application claims the benefit of priority to Japanese Patent Application No. 2021-059274, the contents of which are incorporated herein by reference.
The dispersion of the present disclosure maintains the physical property even after drying and redispersing and has a long pot life. Additionally, the composite of the present disclosure has the higher rupture strength and the higher oxygen gas barrier property.
The following describes embodiments with reference to the drawings as appropriate. The present disclosure is not limited to the following embodiments, and can be subjected to various kinds of changes in design without departing from the scope of the claims. For convenience of explanation, dimensional ratios and shapes of respective parts in the drawings may be exaggerated, and different from actual dimensional ratios and shapes in some cases. A numerical range expressed herein using the term “to” includes respective values described before and after the term “to” as a lower limit value and an upper limit value.
A dispersion (dispersion liquid) according to the embodiment contains a CNF having a sulfate ester group (also referred to as a sulfate-esterified CNF) and a CNC having a sulfate ester group (also referred to as a sulfate-esterified CNC) as dispersoids (dispersed material).
The CNF is a fiber containing cellulose. Cellulose is a polysaccharide in which glucose is bonded by a β-1,4 glycosidic bond, and is represented by (C6H10O5)n. The CNF generally has a fiber width (fiber diameter (diameter of a circle of equivalent projection area)) in a range of 4 nm to 100 nm, and a fiber length in a range of 0.5 μm to 100 μm. The fiber width and the fiber length can be determined by, for example, measuring fiber widths and fiber lengths of randomly selected 50 CNFs using an atomic force microscope (SPM-9700HT, manufactured by Shimadzu Corporation) and calculating the respective arithmetic means.
The CNC is a needle-shaped crystal containing cellulose. The CNC generally has a short axis with a length in a range of 4 nm to 100 nm, and a long axis with a length of more than or equal to 50 nm and less than 0.5 μm. The lengths of the short axis and the long axis can be determined by, for example, measuring the lengths of the long axis and the short axis of randomly selected 50 CNCs using an atomic force microscope (SPM-9700HT, manufactured by Shimadzu Corporation) and calculating the respective arithmetic means.
The sulfate-esterified CNF is a CNF containing cellulose having at least one OH group substituted with a sulfate ester group. Similarly, the sulfate-esterified CNC is a CNC containing cellulose having at least one OH group substituted with a sulfate ester group. Here, the sulfate ester group may be a sulfate ester group represented by a formula (1):
wherein M represents a monovalent to trivalent cation. When M is a divalent or trivalent cation, M is ionically bonded to two or three —OSO3−.
Examples of the monovalent to trivalent cation include a hydrogen ion, a metal ion, and an ammonium ion. Examples of the metal ion include an alkali metal ion, an alkaline earth metal ion, a transition metal ion, and other metal ions. Examples of the alkali metal include lithium, sodium, potassium, rubidium, and cesium. Examples of the alkaline earth metal include calcium and strontium. Examples of the transition metal include iron, nickel, palladium, copper, and silver. Examples of the other metal include beryllium, magnesium, zinc, aluminum. Examples of the ammonium ion include NH4+ as well as ammonium ions derived from various kinds of amine in which one or more hydrogen atoms of NH4+ is substituted with an organic group (e.g. quaternary ammonium cation, alkanolamine ion, and pyridinium ion). The cation may be any one of the listed cations or a combination of two or more of the listed cations.
Examples of the sulfate-esterified CNF and the sulfate-esterified CNC are illustrated in
Since the sulfate-esterified CNF and the sulfate-esterified CNC both have the sulfate ester groups on their surfaces, they strongly electrostatically repel each other. Therefore, a dispersion according to the embodiment is excellent in easy dispersibility and dispersion stability. The sulfate-esterified CNF and the sulfate-esterified CNC have high affinities for one another because they have similar surface conditions. Therefore, in the dispersion according to the embodiment, the sulfate-esterified CNF and the sulfate-esterified CNC are uniformly mixed, and microphase-separation into a CNF-rich phase and a CNC-rich phase is less likely to occur. Because of these causes, the dispersion according to the embodiment maintains the physical property even after drying and redispersing, and has a long pot life. Furthermore, the dispersion according to the embodiment can be used to produce a composite containing the CNF and the CNC mixed uniformly, and the composite produced can have a high rupture strength and a high oxygen gas barrier property.
At least one of the sulfate-esterified CNF or the sulfate-esterified CNC may have another substituent in addition to the sulfate ester group. The other substituent may substitute at least one of the OH groups in the cellulose constituting the CNF or the CNC. The other substituent may be, for example, an anionic substituent and its salt, an ester group, an ether group, an acyl group, an aldehyde group, an alkyl group, an alkylene group, or an aryl group, or may include two or more thereof. From the aspect of improving the dispersibility, the other substituent may be an anionic substituent or its salt, or an acyl group. Examples of the anionic substituent include a carboxy group, a phosphate ester group, a phosphite ester group, and a xanthate group. From the aspect of improving the dispersibility, the salt of the anionic substituent may be sodium salt, potassium salt, or calcium salt. From the aspect of improving the dispersibility, the acyl group may be an acetyl group.
A sulfate esterification modification proportion in the sulfate-esterified CNF can be set to any appropriate value depending on the usage and the like. The sulfate esterification modification proportion in the sulfate-esterified CNF can be indicated by a sulfur content (mass %) in the sulfate-esterified CNF. The sulfur content (mass %) in the sulfate-esterified CNF is generally 0.05 mass % to 30 mass %, preferably 0.1 weight % to 25 weight %, and more preferably 0.5 weight % to 22 weight %, but not limited thereto. The sulfate-esterified CNF with the sulfur content of 30 weight % or less can have a sufficient crystallinity and a sufficient heat resistance. The sulfate-esterified CNF with the sulfur content of 0.05 weight % or more can be efficiently produced. This is because the CNFs electrostatically repel to one another due to the sufficient amount of the sulfate ester groups, and this reduces an energy necessary for obtaining the sulfate-esterified CNF by fibrillating a sulfate-esterified pulp in the production process as described later.
The sulfate esterification modification proportion in the sulfate-esterified CNC can be set to any appropriate value depending on the usage and the like. The sulfate esterification modification proportion in the sulfate-esterified CNC can be indicated by a sulfur content (mass %) in the sulfate-esterified CNC, and generally in a range of 0.05 mass % to 15 mass %, although not limited thereto.
The sulfur contents (mass %) in the sulfate-esterified CNF and the sulfate-esterified CNC can be determined as follows, for example, by a combustion absorption-ion chromatography (IC) method.
sulfur content (mass %)=sulfate ion concentration (mass %)×32/96
The sulfate-esterified CNF can be produced by, for example, sulfate-esterifying a raw pulp to obtain a sulfate-esterified pulp, and fibrillating the sulfate-esterified pulp as described later. Thus obtained sulfate-esterified CNF has a crystalline part and an amorphous part. The crystallinity of the sulfate-esterified CNF depends on its raw material (cotton, wood, and the like). The sulfate-esterified CNF generally has the crystallinity of 20% to 99%, preferably 30% to 95%, more preferably 40% to 90%, and further preferably 50% to 85%. The sulfate-esterified CNF with the crystallinity of 20% or more can have a sufficient heat resistance and a sufficient rigidity. For the sulfate-esterified CNF with the crystallinity of exceeding 99%, production of the sulfate-esterified CNF having a sufficient fiber length tends to be difficult.
The sulfate-esterified CNC can be obtained by hydrolyzing the amorphous part of the raw pulp with sulfuric acid. The sulfate-esterified CNC generally has a crystallinity of 85% to 100%, in particular, 90% or more.
The crystallinities of the sulfate-esterified CNF and the sulfate-esterified CNC can be determined by dividing an area of a peak derived from crystalline cellulose by a sum of an area of halo derived from amorphous cellulose and the area of the peak derived from crystalline cellulose in an X-ray diffraction pattern.
Amass ratio of the sulfate-esterified CNF to the sulfate-esterified CNC contained in the dispersion according to the embodiment may be in a range of 1:99 to 99:1. This allows further improvement in the rupture strength and the oxygen gas barrier property of the composite produced using the dispersion, as indicated in the examples described below.
The dispersion according to the embodiment further contains a dispersion medium. The dispersion medium may be a polar medium such as water, dimethylsulfoxide, dimethylformamide, ethylene glycol, diethyl ether, dioxane, tetrahydrofuran, methyltetrahydrofuran, or a mixture thereof. Especially, the dispersion medium may contain a liquid having a relative permittivity of 38 or more in an amount of 50 to 100 volume %, preferably 75 to 100 volume %, based on the total volume of the dispersion medium. Especially, the dispersion medium may contain a liquid having a relative permittivity of 38 or more in an amount of 80 to 100 volume % based on the total volume of the dispersion medium. This allows the pot life of the dispersion to be further extended as indicated in the examples described below.
The dispersion according to the embodiment may optionally further contain an additive as a dispersoid. The additive may be an inorganic additive or an organic additive.
The inorganic additive may be inorganic particles, such as particles of silica, mica, talc, clay, carbon, carbonate (for example, calcium carbonate, magnesium carbonate), oxide (for example, aluminum oxide, titanium oxide, zinc oxide, iron oxide), ceramic (for example, ferrite), or a mixture thereof. The inorganic particles may be contained in an amount of 0.09 to 5 mass % based on the total weight of the dispersoid. This allows further improvement in the rupture strength of the composite produced using the dispersion, as indicated in the examples described below.
Examples of the organic additive include organic particles and a functional compound. Examples of the organic particles include particles of at least one substance selected from the group consisting of resins and rubbers, for example, particles of phenolic resin, melamine resin, urea resin, alkyd resin, epoxy resin, unsaturated polyester resin, polyurethane resin, polyethylene resin (for example, high-density polyethylene, medium-density polyethylene, and low-density polyethylene), polypropylene resin, polystyrene resin, acrylic resin, polyvinyl alcohol, acrylamide resin, silicone resin, natural rubber, synthetic rubber, and a mixture thereof. Examples of the functional compound include pigment, UV absorber, antioxidant, antistatic agent, and surfactant.
The dispersion according to the embodiment can be dried by any method, such as freeze drying and spray drying, as necessary. By adding a dispersion medium to a dried body and mixing them, the dispersion can be obtained again.
An example of a method for preparing the dispersion containing the sulfate-esterified CNF and the sulfate-esterified CNC as described above will be described. The method for preparing the dispersion containing the sulfate-esterified CNF and the sulfate-esterified CNC according to the embodiment includes mixing a sulfate-esterified CNF dispersion and a sulfate-esterified CNC dispersion.
The sulfate-esterified CNF dispersion may be prepared by any method. For example, a solution containing dimethylsulfoxide, sulfuric acid, and at least one of acetic anhydride or propionic acid anhydride is mixed with a raw pulp, thereby obtaining a sulfate-esterified pulp. Subsequently, the sulfate-esterified pulp is combined with the above-described dispersion medium and mixed together. The mixing may be performed by, for example, an ultrasonication. Thus, the sulfate-esterified pulp is fibrillated, and the sulfate-esterified CNF dispersion is obtained.
The sulfate-esterified CNC dispersion may be prepared by any method. For example, the amorphous part of cellulose in the raw pulp is hydrolyzed with sulfuric acid, and the resulting solid is washed, and then combined with an appropriate dispersion medium and mixed together, and thus the sulfate-esterified CNC dispersion can be obtained.
The sulfate-esterified CNF dispersion is mixed with the sulfate-esterified CNC dispersion. The above-described additive may be further added here. The mixing may be performed while a shear force is applied. This allows satisfactory mixing of the sulfate-esterified CNF and the sulfate-esterified CNC. The composite produced using the satisfactorily mixed dispersion can have further higher rupture strength and oxygen gas barrier property as indicated in the examples described below. For the mixing, an apparatus, such as stirrer, three-roll machine, twin screw kneader, triaxial planetary kneader, disperser, paint shaker, bead mill, cutter mixer, or planetary mixer, may be used.
The mixing may be performed under any condition, and for example, the mixing may be performed at 20° C. to 150° C. for five minutes to one hour.
The composite according to the embodiment contains the sulfate-esterified CNF and the sulfate-esterified CNC. In one embodiment, as schematically illustrated in
Since the sulfate-esterified CNF and the sulfate-esterified CNC are described above in detail, detailed descriptions of them are omitted here. The sulfate-esterified CNF and the sulfate-esterified CNC have high affinities for one another because they both have the sulfate ester groups on their surfaces and have similar surface conditions. This allows the sulfate-esterified CNF and the sulfate-esterified CNC in the mixed composite to be in a uniformly mixed state without being separated into phases, which leads to a high rupture strength and a high oxygen gas barrier property of the mixed composite.
Amass ratio of the sulfate-esterified CNF to the sulfate-esterified CNC contained in the mixed composite may be in a range of 1:99 to 99:1. This allows further improvement in the rupture strength and the oxygen gas barrier property of the mixed composite, as indicated in the examples described below.
The mixed composite may further contain an additive mixed with the sulfate-esterified CNF and the sulfate-esterified CNC. The additive may be an inorganic additive or an organic additive.
As illustrated in
As illustrated in
As illustrated in
The presence of the cross-linkage can be confirmed by any method, such as infrared spectroscopy method, near-infrared spectroscopy method, Raman spectroscopy method, nuclear magnetic resonance spectroscopy method, elementary analysis, gel permeation chromatography, or differential scanning calorimetry. The type of the chemical bond forming the cross-linkage can be identified by any method, such as infrared spectroscopy method, near-infrared spectroscopy method, Raman spectroscopy method, or nuclear magnetic resonance spectroscopy method.
As illustrated in
Cellulose as the main component of the paper substrate has an OH group forming a considerably strong hydrogen bond with the sulfate ester group. Therefore, the mixed composite containing the sulfate-esterified CNF and the sulfate-esterified CNC can be adhered to the paper substrate with a sufficient strength. Additionally, the composite including the paper substrate and the mixed composite supported on the paper substrate can have a higher gas barrier property and a higher rupture strength than those of a single body of the paper substrate. Accordingly, the composite can be used as a substitute, having the improved function, for a paper product, such as a packaging material, a packing material (for example, cardboard), or a container material.
In the layered composite, at least one CNF layer and at least one CNC layer are adjacent to one another. At least one CNF layer and at least one CNC layer may be alternately layered. For example, in one embodiment, as illustrated in
Since the sulfate-esterified CNF and the sulfate-esterified CNC are described above in detail, detailed descriptions of them are omitted here. The sulfate-esterified CNF and the sulfate-esterified CNC have high affinities for one another because they both have the sulfate ester groups on their surfaces and have the similar surface conditions. This allows the CNF layer and the CNC layer adhere to each other with high adhesive strength, which leads to a high rupture strength and the high oxygen gas barrier property of the mixed composite.
At least one layer of the CNF layer(s) or the CNC layer(s) may further contain an additive. The additive may be an inorganic additive or an organic additive described above. At least one layer of the CNF layer(s) or the CNC layer(s) may contain inorganic particles in an amount of 0.09 to 5 mass % based on the total mass of the layer. This allows further improvement in the rupture strength of the layered composite. An interface between an inorganic particle-containing layer and a layer adjacent to the inorganic particle-containing layer is uneven due to the presence of the inorganic particles, which provides an anchoring effect that further increases the adhesive strength between the adjacent layers.
At least one layer of the CNF layer(s) or the CNC layer(s) may further contain at least one substance selected from the group consisting of resins and rubbers. This allows further improvement in the rupture strength of the layered composite. Examples of the resin and the rubber include phenolic resin, melamine resin, urea resin, alkyd resin, epoxy resin, unsaturated polyester resin, polyurethane resin, polyethylene resin (for example, high-density polyethylene, medium-density polyethylene, and low-density polyethylene), polypropylene resin, polystyrene resin, acrylic resin, polyvinyl alcohol, acrylamide resin, silicone resin, natural rubber, and synthetic rubber.
At least one layer of the CNF layer(s) or the CNC layer(s) may have a crosslinked structure. In the CNF layer, a cross-linkage may be formed between at least one of the sulfate-esterified CNFs and at least one of the sulfate-esterified CNFs or the at least one substance selected from the group consisting of resins and rubbers. Additionally or alternatively, in the CNC layer, a cross-linkage may be formed between at least one of the sulfate-esterified CNCs and at least one of the sulfate-esterified CNCs or the at least one substance selected from the group consisting of resins and rubbers. The cross-linkage can be formed by a condensation reaction or an addition reaction to bond a hydroxy group of the cellulose to another hydroxy group of the cellulose or a reactive moiety (for example, hydroxy group, aldehyde group, carboxy group, methoxy group, carbonyl group, alkene moiety, and ether moiety) of the at least one substance selected from the group consisting of resins and rubbers. While the type of the bond is not specifically limited, examples of the bond include a urethane bond, an ester bond, an ether bond, an amide bond, and a urea bond. In particular, the cross-linkage structure including the urethane bond can improve the oxygen gas barrier property of the layered composite.
The presence of the cross-linkage can be confirmed by any method, such as infrared spectroscopy method, near-infrared spectroscopy method, Raman spectroscopy method, nuclear magnetic resonance spectroscopy method, elementary analysis, gel permeation chromatography, or differential scanning calorimetry. The type of the chemical bond forming the cross-linkage can be identified by any method, such as infrared spectroscopy method, near-infrared spectroscopy method, Raman spectroscopy method, or nuclear magnetic resonance spectroscopy method.
The layered composite may be supported on a substrate. In other words, as illustrated in
Cellulose as the main component of the paper substrate has an OH group forming a considerably strong hydrogen bond with the sulfate ester groups of the sulfate-esterified CNF and/or the sulfate-esterified CNC. Therefore, the layered composite can be adhered to the paper substrate with a sufficient strength. Additionally, the composite including the paper substrate and the layered composite supported on the paper substrate can have a higher gas barrier property and a higher rupture strength than those of a single body of the paper substrate. Accordingly, the composite can be used as a substitute, having the improved function, for a paper product, such as a packaging material, a packing material (for example, cardboard), or a container material.
The above-described mixed composite can be produced by drying the above-described dispersion containing the sulfate-esterified CNF and the sulfate-esterified CNC to remove the dispersion medium.
When the mixed composite contains the at least one substance selected from the group consisting of resins and rubbers, the mixed composite can be produced by drying a dispersion further containing particles of the at least one substance selected from the group consisting of resins and rubbers. During the drying, the dispersion may be heated and/or pressed. A dried body after the drying may be heated and/or pressed. Alternatively, the mixed composite containing the at least one substance selected from the group consisting of resins and rubbers can be produced also by drying the dispersion containing the sulfate-esterified CNF and the sulfate-esterified CNC to obtain a mixed powder of the sulfate-esterified CNF and the sulfate-esterified CNC, adding the at least one substance selected from the group consisting of resins and rubbers to the mixed powder and mixing them, and heating and/or pressing the mixture.
When the mixed composite has the crosslinked structure, the mixed composite can be produced by adding a crosslinking agent to the above-described dispersion containing the sulfate-esterified CNF and the sulfate-esterified CNC to cause a cross-linking reaction, and subsequently drying the dispersion.
The mixed composite may be formed into any desired shape depending on the usage.
The dispersion may be dried on the above-described substrate, especially the paper substrate, thereby producing a composite including a mixed composite and the substrate supporting the mixed composite. Since the dispersion on the paper substrate can be quickly dried, the composite can be produced in a short time.
An example of a method for producing the above-described layered composite will be described. The method for producing the layered composite includes: (a) forming a first layer containing a liquid and one of a sulfate-esterified CNF or a sulfate-esterified CNC; (b) forming a second layer on the first layer by supplying a dispersion containing the other of the sulfate-esterified CNF or the sulfate-esterified CNC on the first layer; and (c) removing the liquid from the first layer and the second layer.
In the step (a), a layer of a dispersion containing one of the sulfate-esterified CNF or the sulfate-esterified CNC is formed, thus forming a first layer. A liquid content in the first layer may be more than 0 mass %, and especially may be 5 mass % or more. This allows improvement in the adhesiveness between the first layer and the second layer formed on the first layer, as indicated in the examples described below. This would be due to the presence of a layer of a predetermined thickness or more in which the sulfate-esterified CNF and the sulfate-esterified CNC are mixed and entangled at the interface between the first layer and the second layer. The liquid content in the first layer may be 30 mass % or less, especially 20 mass % or less. The liquid content in the first layer can be adjusted by, after forming a layer of the dispersion, drying the layer to reduce the dispersion medium.
In the step (b), a dispersion containing the other of the sulfate-esterified CNF or the sulfate-esterified CNC is supplied over the first layer, thus forming a second layer on the first layer.
The step (a) and the step (b) may be alternately repeated to form a total of three or more layers of the first layer and the second layer. In this case, in the step (b), the second layer may be dried to adjust the liquid content in the second layer. The liquid content in the second layer after the drying may be more than 0 mass %, especially 5 mass % or more. This allows improvement in the adhesiveness between the second layer and the first layer formed on the second layer. The liquid content in the second layer after the drying may be 30 mass % or less, especially 20 mass % or less.
Subsequently, in the step (c), the first layer and the second layer are dried to remove the dispersion media contained in the first layer and the second layer. Any drying method, such as natural drying, drying under reduced pressure, or hot air drying, can be used. Thus, a layered mixture as described above is obtained.
In the step (a), the first layer may be formed on the above-described substrate, especially the paper substrate, thereby producing a composite including a layered composite and the substrate supporting the layered composite. Since the dispersion on the paper substrate can be quickly dried, such a composite can be produced in a short time.
While the embodiments of the present disclosure are described above in detail, the scope of the claims is not limited to the above-described embodiments, and various changes can be made without departing from the scope of the claims.
The following specifically describes the present disclosure with examples, but the present disclosure is not limited to these examples.
300 g of dimethylsulfoxide, 33.3 g of acetic anhydride, and 4.3 g of sulfuric acid having a concentration of 98 mass % were mixed in a 1 L flask by stirring with a stirrer tip. Subsequently, 10 g of needle bleached kraft pulp (NBKP) (“CARIBOO” manufactured by Cariboo Pulp and Paper Company) was added, and stirred at room temperature for four hours, thereby sulfate-esterifying the NBKP. Then, 5% aqueous solution of sodium hydroxide was added dropwise, thus obtaining a reaction mixture with pH 7.0. Subsequently, the reaction mixture was filtrated through a nylon mesh (“PA-11μ” manufactured by AS ONE CORPORATION), and simultaneously rinsed with distilled water. Thus, a sulfate-esterified pulp was obtained. The sulfate-esterified pulp was put in a 1 L flask, distilled water was added to a solid content of 1%, and an ultrasonic treatment was performed. Thus, a sulfate-esterified CNF dispersion in water having a solid content of 1 mass % (Sample A) was obtained.
A sulfate-esterified CNF dispersion in DMF having a solid content of 1 mass % (Sample B) was obtained similarly to Sample A except that DMF was used instead of the distilled water.
A sulfate-esterified CNF dispersion in ethylene glycol having a solid content of 1 mass % (Sample C) was obtained similarly to Sample A except that ethylene glycol was used instead of the distilled water.
A sulfate-esterified CNF dispersion in a mixture of water and ethanol having a solid content of 1 mass % (Sample D) was obtained similarly to Sample A except that a mixture of water and ethanol (water:ethanol (volume ratio)=80:20) was used instead of the distilled water.
A sulfate-esterified CNF dispersion in a mixture of water and ethanol having a solid content of 1 mass % (Sample E) was obtained similarly to Sample A except that a mixture of water and ethanol (water:ethanol (volume ratio)=75:25) was used instead of the distilled water.
A sulfate-esterified CNF dispersion in a mixture of ethylene glycol and ethanol having a solid content of 1 mass % (Sample F) was obtained similarly to Sample A except that a mixture of ethylene glycol and ethanol (ethylene glycol:ethanol (volume ratio)=80:20) was used instead of the distilled water.
A sulfate-esterified CNF dispersion in a mixture of ethylene glycol and ethanol having a solid content of 1 mass % (Sample G) was obtained similarly to Sample A except that a mixture of ethylene glycol and ethanol (ethylene glycol:ethanol (volume ratio)=75:25) was used instead of the distilled water.
A sulfate-esterified CNF dispersion in formamide having a solid content of 1 mass % (Sample H) was obtained similarly to Sample A except that formamide was used instead of the distilled water.
A sulfate-esterified CNF dispersion in a mixture of formamide and ethylene glycol (formamide:ethylene glycol (volume ratio)=50:50) having a solid content of 1 mass % (Sample I) was obtained similarly to Sample A except that a mixture of formamide and ethylene glycol (formamide:ethylene glycol (volume ratio)=50:50) was used instead of the distilled water.
A sulfate-esterified CNF dispersion in a mixture of water and ethylene glycol having a solid content of 1 mass % (Sample J) was obtained similarly to Sample A except that a mixture of distilled water and ethylene glycol (water:ethylene glycol (volume ratio)=50:50) was used instead of the distilled water.
A sulfate-esterified CNF dispersion in a mixture of water and ethylene glycol having a solid content of 1 mass % (Sample K) was obtained similarly to Sample A except that a mixture of distilled water and ethylene glycol (water:ethylene glycol (volume ratio)=80:20) was used instead of the distilled water.
0.25 mmol of 2,2,6,6-tetramethylpiperidine-N-oxide (TEMPO) and 20 mmol of sodium bromide were dissolved in water, thus obtaining 500 mL of an aqueous solution. 10 g of absolutely dried (i.e., having a water content of 0%) NBKP (“CARIBOO” manufactured by Cariboo Pulp and Paper Company) was added to the aqueous solution, and stirred until the pulp was uniformly dispersed. The temperature of the mixture was made 20° C., and then 64 mmol of an aqueous solution of sodium hypochlorite (manufactured by FUJIFILM Wako Pure Chemical Corporation) was added to start an oxidation reaction. During the reaction, the temperature in the reaction system was kept at 20° C., and pH was kept at 10 by sequentially adding 3N aqueous solution of sodium hydroxide. After the reaction for three hours, the resultant was filtrated with a glass filter, and the filtration residue (filter residue) was sufficiently washed by water. Thus, an oxidized pulp was obtained.
Distilled water was added to the oxidized pulp to a solid content of 1 mass % to obtain a slurry, and the slurry was treated three times at 140 MPa using an ultra-high pressure homogenizer. Thus, a transparent gel-like TEMPO-oxidized CNF dispersion in water (sample L) was obtained.
10 g of urea, 5.53 g of sodium dihydrogen phosphate dihydrate, and 4.13 g of disodium hydrogen phosphate were dissolved in 10.9 g of water, thus preparing a phosphorylation reagent. A sheet obtained by paper making from dried NBKP (“CARIBOO” manufactured by Cariboo Pulp and Paper Company) was treated with a cutter mill and a pin mill to prepare cotton-like fiber. The phosphorylation reagent was evenly sprayed to 10 g (absolute dry mass) of the cotton-like fibers, and the fibers were kneaded by hand to obtain an impregnated pulp. The impregnated pulp was heat-treated for 80 minutes in an air-blow dryer with a damper heated to 140° C. Thus, a phosphorylated pulp was obtained.
1 L of an ion exchanged water was added to 10 g of the phosphorylated pulp, which was then uniformly dispersed by stirring, and the dispersion was filtrated and dehydrated to obtain a sheet. The obtained sheet and 1 L of an ion exchanged water were stirred to be uniformly dispersed, and the dispersion was filtrated and dehydrated to obtain a sheet. The obtained sheet was similarly treated once more. Subsequently, the obtained sheet and 1 L of an ion exchanged water were stirred while 1N aqueous solution of sodium hydroxide was added little by little, thus obtaining a pulp slurry having a pH of 12 to 13. The pulp slurry was dehydrated to obtain a sheet. The sheet and 1 L of an ion exchanged water were stirred to be uniformly dispersed, and the dispersion was filtrated and dehydrated to obtain a sheet. The obtained sheet was similarly treated two more times. The obtained sheet and the ion exchanged water were mixed to obtain 0.5 mass % of a slurry. The slurry was subjected to fibrillation treatment for 180 minutes under a condition of 6900 rpm using a fibrillation treatment apparatus (“Clearmix-11S” manufactured by M Technique Co., Ltd.). The ion exchanged water was added to adjust the solid content in the slurry to 1 mass %. Thus, a phosphate-esterified CNF dispersion in water having a solid content of 1 mass % (Sample M) was obtained.
800 mL of 58% sulfuric acid was heated to 50° C. in a 2 L flask. 100 g of absolutely dried NBKP (“CARIBOO” manufactured by Cariboo Pulp and Paper Company) was put in the flask, and stirred for three hours. The resultant was treated at 20,000 G for 10 minutes with a centrifugal separator (“CT18R” manufactured by Eppendorf Himac Technologies Co., Ltd.). Subsequently, a supernatant liquid was removed by decantation, and 400 mL of distilled water was added to cause a pellet to be suspended. Similar centrifugal separation treatment, decantation, addition of distilled water, and suspension treatment were performed two more times. Thus, a sulfate-esterified CNC dispersion in water (Sample N) was obtained.
Sample N was dried with a freeze dryer (“FDU-12AS” manufactured by AS ONE CORPORATION), thereby obtaining a CNC powder. DMF was added to the CNC powder so as to have a solid content of 1 mass %, which was treated for two minutes with Homodisperser Model 2.5 manufactured by Primix. Thus, a CNC dispersion in DMF having a solid content of 1 mass % (Sample O) was obtained.
A CNC dispersion in ethylene glycol having a solid content of 1 mass % (sample P) was obtained similarly to Sample O except that ethylene glycol was used instead of DMF.
A sulfate-esterified CNC dispersion in a mixture of water and ethanol having a solid content of 1 mass % (Sample Q) was obtained similarly to Sample O except that a mixture of water and ethanol (water:ethanol (volume ratio)=80:20) was used instead of DMF.
A sulfate-esterified CNC dispersion in a mixture of water and ethanol having a solid content of 1 mass % (Sample R) was obtained similarly to Sample O except that a mixture of water and ethanol (water:ethanol (volume ratio)=75:25) was used instead of DMF.
A sulfate-esterified CNC dispersion in a mixture of ethylene glycol and ethanol having a solid content of 1 mass % (Sample S) was obtained similarly to Sample O except that a mixture of ethylene glycol and ethanol (ethylene glycol:ethanol (volume ratio)=80:20) was used instead of DMF.
A sulfate-esterified CNC dispersion in a mixture of ethylene glycol and ethanol having a solid content of 1 mass % (Sample T) was obtained similarly to Sample O except that a mixture of ethylene glycol and ethanol (ethylene glycol:ethanol (volume ratio)=75:25) was used instead of DMF.
A CNC dispersion in formamide having a solid content of 1 mass % (Sample U) was obtained similarly to Sample O except that formamide was used instead of DMF.
A sulfate-esterified CNC dispersion in a mixture of formamide and ethylene glycol having a solid content of 1 mass % (Sample V) was obtained similarly to Sample O except that a mixture of formamide and ethylene glycol (formamide:ethylene glycol (volume ratio)=50:50) was used instead of DMF.
A sulfate-esterified CNC dispersion in a mixture of water and ethylene glycol having a solid content of 1 mass % (Sample W) was obtained similarly to Sample O except that a mixture of water and ethylene glycol (water:ethylene glycol (volume ratio)=50:50) was used instead of DMF.
A sulfate-esterified CNC dispersion in a mixture of water and ethylene glycol having a solid content of 1 mass % (Sample X) was obtained similarly to Sample O except that a mixture of water and ethylene glycol (water:ethylene glycol (volume ratio)=80:20) was used instead of DMF.
75 mL of Sample A and 75 mL of Sample N were mixed in a 300 mL polypropylene beaker for five minutes with Homodisperser Model 2.5 manufactured by Primix, thereby obtaining a dispersion in which the sulfate-esterified CNF and the sulfate-esterified CNC (CNF:CNC=50:50 (mass ratio)) were dispersed in water (relative permittivity 80.4).
The entire amount of the dispersion was poured into a square PTFE container with inside dimensions of 20 cm×20 cm×5 cm, and naturally dried at room temperature for two weeks to form a film. The film was extracted from the PTFE container and cut by a sample cutter (“SDL200” manufactured by DUMBBELL CO., LTD.), thereby producing a dumbbell-shaped composite containing the sulfate-esterified CNF and the sulfate-esterified CNC (CNF:CNC=50:50 (mass ratio)). The composite had a part for testing with a thickness of 25 μm, a width of 10 mm, and a length of 100 mm.
A dispersion in which the sulfate-esterified CNF and the sulfate-esterified CNC (CNF:CNC=0.5:99.5 (mass ratio)) were dispersed in water and a dumbbell-shaped composite containing the sulfate-esterified CNF and the sulfate-esterified CNC (CNF:CNC=0.5:99.5 (mass ratio)) were obtained similarly to Example 1 except that 0.75 mL of Sample A and 149.25 mL of Sample N were used instead of 75 mL of Sample A and 75 mL of Sample N.
A dispersion in which the sulfate-esterified CNF and the sulfate-esterified CNC (CNF:CNC=1:99 (mass ratio)) were dispersed in water and a dumbbell-shaped composite containing the sulfate-esterified CNF and the sulfate-esterified CNC (CNF:CNC=1:99 (mass ratio)) were obtained similarly to Example 1 except that 1.5 mL of Sample A and 148.5 mL of Sample N were used instead of 75 mL of Sample A and 75 mL of Sample N.
A dispersion in which the sulfate-esterified CNF and the sulfate-esterified CNC (CNF:CNC=25:75 (mass ratio)) were dispersed in water and a dumbbell-shaped composite containing the sulfate-esterified CNF and the sulfate-esterified CNC (CNF:CNC=25:75 (mass ratio)) were obtained similarly to Example 1 except that 37.5 mL of Sample A and 112.5 mL of Sample N were used instead of 75 mL of Sample A and 75 mL of Sample N.
A dispersion in which the sulfate-esterified CNF and the sulfate-esterified CNC (CNF:CNC=75:25 (mass ratio)) were dispersed in water and a dumbbell-shaped composite containing the sulfate-esterified CNF and the sulfate-esterified CNC (CNF:CNC=75:25 (mass ratio)) were obtained similarly to Example 1 except that 112.5 mL of Sample A and 37.5 mL of Sample N were used instead of 75 mL of Sample A and 75 mL of Sample N.
A dispersion in which the sulfate-esterified CNF and the sulfate-esterified CNC (CNF:CNC=99:1 (mass ratio)) were dispersed in water and a dumbbell-shaped composite containing the sulfate-esterified CNF and the sulfate-esterified CNC (CNF:CNC=99:1 (mass ratio)) were obtained similarly to Example 1 except that 148.5 mL of Sample A and 1.5 mL of Sample N were used instead of 75 mL of Sample A and 75 mL of Sample N.
A dispersion in which the sulfate-esterified CNF and the sulfate-esterified CNC (CNF:CNC=99.5:0.5 (mass ratio)) were dispersed in water and a dumbbell-shaped composite containing the sulfate-esterified CNF and the sulfate-esterified CNC (CNF:CNC=99.5:0.5 (mass ratio)) were obtained similarly to Example 1 except that 149.25 mL of Sample A and 0.75 mL of Sample N were used instead of 75 mL of Sample A and 75 mL of Sample N.
A dispersion in which the sulfate-esterified CNF and the sulfate-esterified CNC (CNF:CNC=50:50 (mass ratio)) were dispersed in DMF (relative permittivity 38) was obtained similarly to Example 1 except that 75 mL of Sample B and 75 mL of Sample O were used instead of 75 mL of Sample A and 75 mL of Sample N. From this dispersion, a dumbbell-shaped composite containing the sulfate-esterified CNF and the sulfate-esterified CNC (CNF:CNC=50:50 (mass ratio)) was obtained similarly to Example 1 except that the dispersion was dried at 150° C. for five hours under reduced pressure with a vacuum dryer (“APD200” manufactured by Yamato Scientific Co., Ltd.) instead of the natural drying.
A dispersion in which the sulfate-esterified CNF and the sulfate-esterified CNC (CNF:CNC=50:50 (mass ratio)) were dispersed in ethylene glycol (relative permittivity 38.7) and a dumbbell-shaped composite containing the sulfate-esterified CNF and the sulfate-esterified CNC (CNF:CNC=50:50 (mass ratio)) were obtained similarly to Example 8 except that 75 mL of Sample C and 75 mL of Sample P were used instead of 75 mL of Sample B and 75 mL of Sample O.
A dispersion in which the sulfate-esterified CNF and the sulfate-esterified CNC (CNF:CNC=50:50 (mass ratio)) were dispersed in a mixture of water (relative permittivity 80.4) and ethanol (relative permittivity 25.3) (water:ethanol (volume ratio)=80:20), and a dumbbell-shaped composite containing the sulfate-esterified CNF and the sulfate-esterified CNC (CNF:CNC=50:50 (mass ratio)) were obtained similarly to Example 1 except that 75 mL of Sample D and 75 mL of Sample Q were used instead of 75 mL of Sample A and 75 mL of Sample N.
A dispersion in which the sulfate-esterified CNF and the sulfate-esterified CNC (CNF:CNC=50:50 (mass ratio)) were dispersed in a mixture of water and ethanol (water:ethanol (volume ratio)=75:25), and a dumbbell-shaped composite containing the sulfate-esterified CNF and the sulfate-esterified CNC (CNF:CNC=50:50 (mass ratio)) were obtained similarly to Example 1 except that 75 mL of Sample E and 75 mL of Sample R were used instead of 75 mL of Sample A and 75 mL of Sample N.
A dispersion in which the sulfate-esterified CNF and the sulfate-esterified CNC (CNF:CNC=50:50 (mass ratio)) were dispersed in a mixture of ethylene glycol and ethanol (ethylene glycol:ethanol (volume ratio)=80:20), and a dumbbell-shaped composite containing the sulfate-esterified CNF and the sulfate-esterified CNC (CNF:CNC=50:50 (mass ratio)) were obtained similarly to Example 8 except that 75 mL of Sample F and 75 mL of Sample S were used instead of 75 mL of Sample B and 75 mL of Sample O.
A dispersion in which the sulfate-esterified CNF and the sulfate-esterified CNC (CNF:CNC=50:50 (mass ratio)) were dispersed in a mixture of ethylene glycol and ethanol (ethylene glycol:ethanol (volume ratio)=75:25), and a dumbbell-shaped composite containing the sulfate-esterified CNF and the sulfate-esterified CNC (CNF:CNC=50:50 (mass ratio)) were obtained similarly to Example 8 except that 75 mL of Sample G and 75 mL of Sample T were used instead of 75 mL of Sample B and 75 mL of Sample O.
A dispersion in which the sulfate-esterified CNF and the sulfate-esterified CNC (CNF:CNC=50:50 (mass ratio)) were dispersed in formamide (relative permittivity 110) was obtained similarly to Example 1 except that 75 mL of Sample H and 75 mL of Sample U were used instead of 75 mL of Sample A and 75 mL of Sample N. From this dispersion, a dumbbell-shaped composite containing the sulfate-esterified CNF and the sulfate-esterified CNC (CNF:CNC=50:50 (mass ratio)) was obtained similarly to Example 1 except that the dispersion was dried at 150° C. for ten hours under reduced pressure with a vacuum dryer (“APD200” manufactured by Yamato Scientific Co., Ltd.) instead of the natural drying.
A dispersion in which the sulfate-esterified CNF and the sulfate-esterified CNC (CNF:CNC=50:50 (mass ratio)) were dispersed in a mixture of formamide and ethylene glycol (formamide:ethylene glycol (volume ratio)=50:50), and a dumbbell-shaped composite containing the sulfate-esterified CNF and the sulfate-esterified CNC (CNF:CNC=50:50 (mass ratio)) were obtained similarly to Example 14 except that 75 mL of Sample I and 75 mL of Sample V were used instead of 75 mL of Sample H and 75 mL of Sample U.
A dispersion in which the sulfate-esterified CNF and the sulfate-esterified CNC (CNF:CNC=50:50 (mass ratio)) were dispersed in a mixture of water and ethylene glycol (water:ethylene glycol (volume ratio)=50:50), and a dumbbell-shaped composite containing the sulfate-esterified CNF and the sulfate-esterified CNC (CNF:CNC=50:50 (mass ratio)) were obtained similarly to Example 14 except that 75 mL of Sample J and 75 mL of Sample W were used instead of 75 mL of Sample H and 75 mL of Sample U.
A dispersion in which the sulfate-esterified CNF and the sulfate-esterified CNC (CNF:CNC=50:50 (mass ratio)) were dispersed in a mixture of water and ethylene glycol (water:ethylene glycol (volume ratio)=80:20), and a dumbbell-shaped composite containing the sulfate-esterified CNF and the sulfate-esterified CNC (CNF:CNC=50:50 (mass ratio)) were obtained similarly to Example 14 except that 75 mL of Sample K and 75 mL of Sample X were used instead of 75 mL of Sample H and 75 mL of Sample U.
150 mL of Sample A, 150 mL of Sample N, and 0.0015 g of silica microparticles (“HS-208” manufactured by NIPPON STEEL Chemical & Material CO., LTD.) were mixed in a 300 mL polypropylene beaker for five minutes with Homodisperser Model 2.5 manufactured by Primix, thereby obtaining a dispersion in which the sulfate-esterified CNF, the sulfate-esterified CNC, and silica microparticles (CNF:CNC:silica=50:50:0.05 (mass ratio)) were dispersed in water. Using half of the dispersion, a dumbbell-shaped composite containing the sulfate-esterified CNF, the sulfate-esterified CNC, and the silica microparticles (CNF:CNC:silica=50:50:0.05 (mass ratio)) was produced similarly to Example 1.
A dispersion in which the sulfate-esterified CNF, the sulfate-esterified CNC, and the silica microparticles (CNF:CNC:silica=50:50:0.1 (mass ratio)) were dispersed in water and a dumbbell-shaped composite containing the sulfate-esterified CNF, the sulfate-esterified CNC, and the silica microparticles (CNF:CNC:silica=50:50:0.1 (mass ratio)) were obtained similarly to Example 18 except that 0.003 g of silica microparticles was used.
A dispersion in which the sulfate-esterified CNF, the sulfate-esterified CNC, and the silica microparticles (CNF:CNC:silica=50:50:2.5 (mass ratio)) were dispersed in water and a dumbbell-shaped composite containing the sulfate-esterified CNF, the sulfate-esterified CNC, and the silica microparticles (CNF:CNC:silica=50:50:2.5 (mass ratio)) were obtained similarly to Example 18 except that 0.075 g of silica microparticles was used.
A dispersion in which the sulfate-esterified CNF, the sulfate-esterified CNC, and the silica microparticles (CNF:CNC:silica=50:50:5.0 (mass ratio)) were dispersed in water and a dumbbell-shaped composite containing the sulfate-esterified CNF, the sulfate-esterified CNC, and the silica microparticles (CNF:CNC:silica=50:50:5.0 (mass ratio)) were obtained similarly to Example 18 except that 0.15 g of silica microparticles was used.
A dispersion in which the sulfate-esterified CNF, the sulfate-esterified CNC, and the silica microparticles (CNF:CNC:silica=50:50:6.0 (mass ratio)) were dispersed in water and a dumbbell-shaped composite containing the sulfate-esterified CNF, the sulfate-esterified CNC, and the silica microparticles (CNF:CNC:silica=50:50:6.0 (mass ratio)) were obtained similarly to Example 18 except that 0.18 g of silica microparticles was used.
375 mL of Sample A and 375 mL of Sample N were treated at 150 MPa three times using a microfluidizer (“M-110EH” manufactured by Microfluidics) to be mixed. Thus, a dispersion in which the sulfate-esterified CNF and the sulfate-esterified CNC (CNF:CNC=50:50 (mass ratio)) were dispersed in water was obtained. Using 150 mL of the dispersion, a dumbbell-shaped composite containing the sulfate-esterified CNF and the sulfate-esterified CNC (CNF:CNC=50:50 (mass ratio)) was produced similarly to Example 1.
75 mL of Sample A and 75 mL of Sample N were poured into a 500 mL polypropylene bottle and sealed, and the bottle was allowed to stand in a water bath at 80° C. for 24 hours. Sample A and Sample N were mixed due to heat convection. Thus, a dispersion in which the sulfate-esterified CNF and the sulfate-esterified CNC (CNF:CNC=50:50 (mass ratio)) were dispersed in water was obtained. Using the entire amount of the dispersion, a dumbbell-shaped composite containing the sulfate-esterified CNF and the sulfate-esterified CNC (CNF:CNC=50:50 (mass ratio)) was produced similarly to Example 1.
A dispersion in which the TEMPO-oxidized CNF and the sulfate-esterified CNC (CNF:CNC=50:50 (mass ratio)) were dispersed in water and a dumbbell-shaped composite containing the TEMPO-oxidized CNF and the sulfate-esterified CNC (CNF:CNC=50:50 (mass ratio)) were obtained similarly to Example 1 except that Sample L was used instead of Sample A.
A dispersion in which the phosphate-esterified CNF and the sulfate-esterified CNC (CNF:CNC=50:50 (mass ratio)) were dispersed in water and a dumbbell-shaped composite containing the phosphate-esterified CNF and the sulfate-esterified CNC (CNF:CNC=50:50 (mass ratio)) were obtained similarly to Example 1 except that Sample M was used instead of Sample A.
The dispersion of CNF and CNC prepared similarly to Example 1 was dried with a freeze dryer (“FDU-12AS” manufactured by AS ONE CORPORATION), thereby obtaining a dry powder. 3 g of the dry powder was combined with 97 g of a polyurethane pellet (“Elastollan” manufactured by BASF) and rolled four times at 100° C. through a three-roll mill (manufactured by Imoto machinery Co., LTD., 1983 model). The obtained film was cut by a sample cutter (“SDL200” manufactured by DUMBBELL CO., LTD.), thereby producing a dumbbell-shaped composite containing the sulfate-esterified CNF and the sulfate-esterified CNC (CNF:CNC=50:50 (mass ratio)), and a polyurethane resin.
4.68 mL of the dispersion of CNF and CNC prepared similarly to Example 1, 1.5 g of polyvinyl alcohol microparticles (“KURARAY POVAL” manufactured by Kuraray Co., Ltd.), and 100 mL of distilled water were stirred in a beaker for 24 hours, thereby obtaining a dispersion. Using the obtained dispersion, a dumbbell-shaped composite containing the sulfate-esterified CNF and the sulfate-esterified CNC (CNF:CNC=50:50 (mass ratio)), and polyvinyl alcohol was produced similarly to Example 1.
300 mL of a dispersion in which the sulfate-esterified CNF and the sulfate-esterified CNC (CNF:CNC=50:50 (mass ratio)) were dispersed in water was obtained similarly to Example 1 except that 150 mL of Sample A and 150 mL of Sample N were used. The dispersion was mixed with 194 g of a natural rubber latex having a solid content of 50 mass % (manufactured by KENIS LIMITED) at ordinary temperature. 3 g of a radical generator (“PERHEXA 25B-40” manufactured by NOF CORPORATION) was added thereto, and the mixture was put in a Teflon (registered trademark) tray and dried at 80° C. for three days. The resultant was rolled four times at 100° C. through a three-roll mill (manufactured by Imoto machinery Co., LTD., 1983 model). The obtained film was cut by a sample cutter (“SDL200” manufactured by DUMBBELL CO., LTD.), thereby producing a dumbbell-shaped composite containing the sulfate-esterified CNF and the sulfate-esterified CNC (CNF:CNC=50:50 (mass ratio)), and a natural rubber.
4.68 mL of the dispersion of CNF and CNC prepared similarly to Example 1, 1.5 g of polyvinyl alcohol microparticles (“KURARAY POVAL” manufactured by Kuraray Co., Ltd.), and 100 mL of distilled water were stirred in a beaker for 24 hours, thereby obtaining a dispersion. 0.01 g of TN hydrochloric acid and 0.3 g of 37 mass % aqueous solution of formaldehyde were added to the obtained dispersion. Thus, a crosslinked structure via an acetal bond was formed. Using the dispersion after the cross-linking reaction, a dumbbell-shaped composite was produced similarly to Example 1.
41 g of diphenylmethane diisocyanate was added to 150 g of the dispersion of CNF and CNC prepared similarly to Example 9, which was stirred at 50° C. for three hours. Thus, an OH group of CNF, CNC, and ethylene glycol reacted with an NCO group of diphenylmethane diisocyanate, thereby forming a urethane bond. As a result, a crosslinked material containing CNF, CNC, and a urethane resin crosslinked through the urethane bond was obtained. After the reaction, the dispersion was rolled four times at 100° C. through a three-roll mill (manufactured by Imoto machinery Co., LTD., 1983 model). The obtained film was cut by a sample cutter (“SDL200” manufactured by DUMBBELL CO., LTD.), thereby producing a dumbbell-shaped composite.
4.68 mL of the dispersion of CNF and CNC prepared similarly to Example 1, 1.5 g of polyvinyl alcohol microparticles (“KURARAY POVAL” manufactured by Kuraray Co., Ltd.), 100 mL of distilled water, and 0.05 g of diphenylmethane diisocyanate were stirred at 50° C. for 24 hours. Thus, a crosslinked structure via a urethane bond was formed. After the cross-linking reaction, the dispersion was used to produce a dumbbell-shaped composite similarly to Example 1.
20.5 g of diphenylmethane diisocyanate was added to 150 g of the dispersion of CNF and CNC prepared similarly to Example 16, which was stirred at 50° C. for three hours. Thus, an OH group of CNF, CNC, and ethylene glycol reacted with an NCO group of diphenylmethane diisocyanate, thereby forming a urethane bond. As a result, a crosslinked material containing CNF, CNC, and a urethane resin crosslinked through the urethane bond was obtained. After the reaction, the dispersion was rolled four times at 100° C. through a three-roll mill (manufactured by Imoto machinery Co., LTD., 1983 model). The obtained film was cut by a sample cutter (“SDL200” manufactured by DUMBBELL CO., LTD.), thereby producing a dumbbell-shaped composite.
75 mL of Sample A was poured into a square PTFE container with inside dimensions of 20 cm×20 cm×5 cm, and naturally dried until its liquid content became 20 mass %. The liquid content was monitored based on the change in mass. 75 mL of Sample N was further poured into the PTFE container, and naturally dried for two weeks. A film formed in the PTFE container was extracted, and a dumbbell-shaped composite was produced similarly to Example 1.
50 mL of Sample A was poured into a square PTFE container with inside dimensions of 20 cm×20 cm×5 cm, and naturally dried until its liquid content became 20 mass %. The liquid content was monitored based on the change in mass. 50 mL of Sample N was further poured into the PTFE container, and naturally dried until its liquid content became 20 mass %. 50 mL of Sample A was further poured into the PTFE container, and naturally dried for two weeks. A film formed in the PTFE container was extracted, and a dumbbell-shaped composite was produced similarly to Example 1.
50 mL of Sample N was poured into a square PTFE container with inside dimensions of 20 cm×20 cm×5 cm, and naturally dried until its liquid content became 20 mass %. The liquid content was monitored based on the change in mass. 50 mL of Sample A was further poured into the PTFE container, and naturally dried until its liquid content became 20 mass %. 50 mL of Sample N was further poured into the PTFE container, and naturally dried for two weeks. A film formed in the PTFE container was extracted, and a dumbbell-shaped composite was produced similarly to Example 1.
500 mL of Sample A and 0.0025 g of silica microparticles (“HS-208” manufactured by NIPPON STEEL Chemical & Material CO., LTD.) were mixed for five minutes with Homodisperser Model 2.5 manufactured by Primix, thereby obtaining a dispersion in which CNF and silica microparticles were dispersed in water. Additionally, 500 mL of Sample N and 0.0025 g of silica microparticles (“HS-208” manufactured by NIPPON STEEL Chemical & Material CO., LTD.) were mixed for five minutes with Homodisperser Model 2.5 manufactured by Primix, thereby obtaining a dispersion in which CNC and silica microparticles were dispersed in water.
75 mL of the dispersion of CNF and silica microparticles was poured into a square PTFE container with inside dimensions of 20 cm×20 cm×5 cm, and naturally dried until its liquid content became 20 mass %. The liquid content was monitored based on the change in mass. 75 mL of the dispersion of CNC and silica microparticles was further poured into the PTFE container, and naturally dried for two weeks. A film formed in the PTFE container was extracted, and a dumbbell-shaped composite was produced similarly to Example 1.
A dumbbell-shaped composite was produced similarly to Example 35 except that the respective amounts of the silica microparticles mixed with Sample A and Sample N were changed to 0.005 g.
A dumbbell-shaped composite was produced similarly to Example 35 except that the respective amounts of the silica microparticles mixed with Sample A and Sample N were changed to 0.125 g.
A dumbbell-shaped composite was produced similarly to Example 35 except that the respective amounts of the silica microparticles mixed with Sample A and Sample N were changed to 0.25 g.
A dumbbell-shaped composite was produced similarly to Example 35 except that the respective amounts of the silica microparticles mixed with Sample A and Sample N were changed to 0.30 g.
A dumbbell-shaped composite was produced similarly to Example 35 except that the amount of the silica microparticles mixed with Sample A was changed to 0.005 g and no silica microparticle was mixed with Sample N.
A dumbbell-shaped composite was produced similarly to Example 35 except that no silica microparticle was mixed with Sample A and the amount of the silica microparticles mixed with Sample N was not 0.005 g.
2.34 mL of Sample A, 0.75 g of polyvinyl alcohol microparticles (“KURARAY POVAL” manufactured by Kuraray Co., Ltd.), and 100 mL of distilled water were stirred in a beaker for 24 hours, thereby obtaining a dispersion containing CNF and polyvinyl alcohol.
The obtained dispersion was poured into a square PTFE container with inside dimensions of 20 cm×20 cm×5 cm, and naturally dried until its liquid content became 20 mass %. The liquid content was monitored based on the change in mass. 75 mL of Sample N was further poured into the PTFE container, and naturally dried for two weeks. A film formed in the PTFE container was extracted, and a dumbbell-shaped composite was produced similarly to Example 1.
2.34 mL of Sample N, 0.75 g of polyvinyl alcohol microparticles (“KURARAY POVAL” manufactured by Kuraray Co., Ltd.), and 100 mL of distilled water were stirred in a beaker for 24 hours, thereby obtaining a dispersion containing CNC and polyvinyl alcohol.
75 mL of Sample A was poured into a square PTFE container with inside dimensions of 20 cm×20 cm×5 cm, and naturally dried until its liquid content became 20 mass %. The liquid content was monitored based on the change in mass. The dispersion containing CNC and polyvinyl alcohol was further poured into the PTFE container, and naturally dried for two weeks. A film formed in the PTFE container was extracted, and a dumbbell-shaped composite was produced similarly to Example 1.
A dispersion containing CNF and polyvinyl alcohol was prepared similarly to Example 42. Additionally, a dispersion containing CNC and polyvinyl alcohol was prepared similarly to Example 43.
The dispersion containing CNF and polyvinyl alcohol was poured into a square PTFE container with inside dimensions of 20 cm×20 cm×5 cm, and naturally dried until its liquid content became 20 mass %. The liquid content was monitored based on the change in mass. The dispersion containing CNC and polyvinyl alcohol was further poured into the PTFE container, and naturally dried for two weeks. A film formed in the PTFE container was extracted, and a dumbbell-shaped composite was produced similarly to Example 1.
2.34 mL of Sample A, 0.75 g of polyvinyl alcohol microparticles (“KURARAY POVAL” manufactured by Kuraray Co., Ltd.), and 100 mL of distilled water were stirred in a beaker for 24 hours, thereby obtaining a dispersion containing CNF and polyvinyl alcohol. 0.01 g of 1N hydrochloric acid and 0.3 g of 37 mass % aqueous solution of formaldehyde were added to the obtained dispersion. Thus, a crosslinked structure via an acetal bond was formed.
2.34 mL of Sample N, 0.75 g of polyvinyl alcohol microparticles (“KURARAY POVAL” manufactured by Kuraray Co., Ltd.), and 100 mL of distilled water were stirred in a beaker for 24 hours, thereby obtaining a dispersion containing CNC and polyvinyl alcohol. 0.01 g of TN hydrochloric acid and 0.3 g of 37 mass % aqueous solution of formaldehyde were added to the obtained dispersion. Thus, a crosslinked structure via an acetal bond was formed.
The dispersion containing CNF and polyvinyl alcohol after the cross-linking reaction was poured into a square PTFE container with inside dimensions of 20 cm×20 cm×5 cm, and naturally dried until its liquid content became 20 mass %. The liquid content was monitored based on the change in mass. The dispersion containing CNC and polyvinyl alcohol after the cross-linking reaction was further poured into the PTFE container, and naturally dried for two weeks. A film formed in the PTFE container was extracted, and a dumbbell-shaped composite was produced similarly to Example 1.
2.34 mL of Sample A, 0.75 g of polyvinyl alcohol microparticles (“KURARAY POVAL” manufactured by Kuraray Co., Ltd.), 100 mL of distilled water, and 0.025 g of diphenylmethane diisocyanate were stirred at 50° C. for three hours. Thus, a crosslinked structure via a urethane bond was formed.
2.34 mL of Sample N, 0.75 g of polyvinyl alcohol microparticles (“KURARAY POVAL” manufactured by Kuraray Co., Ltd.), 100 mL of distilled water, and 0.025 g of diphenylmethane diisocyanate were stirred at 50° C. for three hours. Thus, a crosslinked structure via a urethane bond was formed.
The dispersion containing CNF and polyvinyl alcohol after the cross-linking reaction was poured into a square PTFE container with inside dimensions of 20 cm×20 cm×5 cm, and naturally dried until its liquid content became 20 mass %. The liquid content was monitored based on the change in mass. The dispersion containing CNC and polyvinyl alcohol after the cross-linking reaction was further poured into the PTFE container, and naturally dried for two weeks. A film formed in the PTFE container was extracted, and a dumbbell-shaped composite was produced similarly to Example 1.
A dumbbell-shaped composite was produced similarly to Example 32 except that Sample A was naturally dried until its liquid content became 5 mass % instead of performing the natural drying until the liquid content became 20 mass %.
A dumbbell-shaped composite was produced similarly to Example 32 except that Sample A was dried at 105° C. for three hours to reach the liquid content of 0 mass % instead of performing the natural drying until the liquid content became 20 mass %.
A paper substrate (qualitative filter paper No. 1, manufactured by ADVANTEC CO., LTD.) was cut into a square shape with a size of 19.5 cm×19.5 cm, and put in a square PTFE container with inside dimensions of 20 cm×20 cm×5 cm. The entire amount of the dispersion of CNF and CNC prepared similarly to Example 1 was poured into the PTFE container, and naturally dried at room temperature for two weeks to form a film. The paper substrate and the film were extracted from the PTFE container, and cut by a sample cutter (“SDL200” manufactured by DUMBBELL CO., LTD.). Thus, a dumbbell-shaped composite that includes the paper substrate and the film containing the sulfate-esterified CNF and the sulfate-esterified CNC (CNF:CNC=50:50 (mass ratio)) was obtained.
A dumbbell-shaped composite was produced similarly to Example 49 except that a cardboard base paper (“LCC120” manufactured by Rengo Co., Ltd.) was used as the paper substrate.
A paper substrate (qualitative filter paper No. 1, manufactured by ADVANTEC CO., LTD.) was cut into a square shape with a size of 19.5 cm×19.5 cm, and put in a square PTFE container with inside dimensions of 20 cm×20 cm×5 cm. 75 mL of Sample A was poured into the PTFE container, and naturally dried until its liquid content became 20 mass %. The liquid content was monitored based on the change in mass. 75 mL of Sample N was further poured into the PTFE container, and naturally dried for two weeks. The paper substrate and the film were extracted from the PTFE container, and cut by a sample cutter (“SDL200” manufactured by DUMBBELL CO., LTD.). Thus, a dumbbell-shaped composite that includes the paper substrate, a CNF layer, and a CNC layer was obtained.
A dumbbell-shaped composite was produced similarly to Example 51 except that a cardboard base paper (“LCC120” manufactured by Rengo Co., Ltd.) was used as the paper substrate.
Tables 1, 2 simply indicate the various conditions of Examples 1 to 52 and Comparative Examples 1 and 2.
(3) Evaluation of Redispersibility of Dispersion after Drying
Initial viscosities of the dispersions of Examples 1 to 24 and Comparative Examples 1, 2 were measured three times with a B-type viscometer (“TVB10” manufactured by Toki Sangyo Co., Ltd.), and their averages were obtained.
Subsequently, the respective dispersions of Examples 1 to 7, 18 to 24 and Comparative Examples 1, 2, 100 g for each, were frozen at −18° C., and dried with a freeze dryer (“FDU1110” manufactured by TOKYO RIKAKIKAI CO., LTD.). The respective dispersions of Examples 8 to 17 were treated at 10,000 G for five minutes with a centrifugal separator (“Heraeus Megafuge 8R centrifuge” manufactured by Thermo Fisher Scientific K.K.), supernatants were removed, and distilled water was added. This operation was repeated to replace the dispersion media to water. Then, the dispersions, 100 g for each, were frozen at −18° C., and dried with a freeze dryer (“FDU1110” manufactured by TOKYO RIKAKIKAI CO., LTD.) to obtain dried bodies.
A dispersion medium was added to the respective dried bodies to have the same compositions as those whose initial viscosities were measured, and then treated for two minutes with a disperser (Homodisperser Model 2.5 manufactured by Primix), thereby obtaining dispersions. Viscosities of the obtained dispersions were measured three times with a B-type viscometer (“TVB10” manufactured by Toki Sangyo Co., Ltd), and their averages were obtained.
Rates of the viscosity change after drying and redispersing were calculated, and redispersibilities of the respective dispersions of Examples 1 to 20 and Comparative Examples 1, 2 after drying were evaluated based on the following criterion. Table 3 indicates the result.
Initial viscosities of the dispersions of Examples 1 to 24 and Comparative Examples 1, 2 were measured three times with a B-type viscometer (“TVB10” manufactured by Toki Sangyo Co., Ltd.), and their averages were obtained. The respective dispersions were stored at room temperature, and the viscosities of the dispersions were measured three times with the B-type viscometer (“TVB10” manufactured by Toki Sangyo Co., Ltd.) every one month, and their averages were obtained.
Rates of the viscosity change of the dispersions after the storage were obtained, and pot lives of the respective dispersions of Examples 1 to 24 and Comparative Examples 1, 2 were evaluated based on the following criterion. Table 3 indicates the result.
Rupture strengths of the dumbbell-shaped composites of Examples 1 to 52 and Comparative Examples 1, 2 were measured three times according to Japanese Industrial Standard (JIS) C2151 and ASTM D882 with a Tensilon universal material testing machine (“RTF-2410” manufactured by A&D Company, Limited), and their averages were obtained. In the rupture strength measurement, the grip interval was 50 mm, and the tension speed was 200 mm/minute.
The rupture strengths of the composites of Examples 1 to 52 and Comparative Examples 1, 2 were evaluated based on the following criterion. Table 3 indicates the result.
Oxygen gas permeation rates of the composites of Examples 1 to 52 and Comparative Examples 1, 2 were measured three times under conditions of the temperature of 23° C. and the humidity of 50% according to JIS K7126-2 (temperature and humidity condition: 23° C., 50%) with an oxygen gas permeability meter (“OX-TRAN 2/22” manufactured by MOCON), and their averages were obtained.
The oxygen gas barrier properties of the composites of Examples 1 to 52 and Comparative Examples 1, 2 were evaluated based on the following criterion. Table 3 indicates the result.
The composites of Examples 32 to 52 were cut into the size of 5 cm×5 cm, attached to smooth acrylic boards with an adhesive double coated tape (“NICETACK” manufactured by Nichiban Co., Ltd.), and cured for one hour. Subsequently, a cross-cut test was performed according to JIS K5600-5-6. Specifically, the composite was cut at intervals of 2 mm with a cutter knife, thus forming a grid of 10×10. A cellophane tape was attached to the composite, and an end of the cellophane tape was held and quickly pulled in a direction of 45° to remove the cellophane tape. The surface of the composite was visually observed, and the presence/absence of film delamination from the lower layer or the substrate was determined.
The adhesiveness of the composites of Examples 32 to 52 were evaluated based on the following criterion. Table 3 indicates the result.
The dispersions of Examples 1 to 24 exhibited 1 to 24 exhibited the more satisfactory redispersibility after drying and the longer pot life than those of the dispersions of Comparative Examples 1 and 2. The composites of Examples 1 to 48 exhibited the higher rupture strength and the higher oxygen gas barrier property than those of the composites of Comparative Examples 1 and 2. This indicates that the combination of the sulfate-esterified CNF and the sulfate-esterified CNC provides the satisfactory redispersibility after drying, the long pot life, the high rupture strength, and the high oxygen gas barrier property.
The evaluation result of the composites of Examples 1 to 7 indicated that the mass ratio of the sulfate-esterified CNF to the sulfate-esterified CNC in a range of 1:99 to 99:1 provides the higher rupture strength and the higher oxygen gas barrier property.
The evaluation result of the dispersions of Examples 1 and 8 to 17 indicated that the dispersion medium containing a liquid having a relative permittivity of 38 or more (such as water, DMF, ethylene glycol, and formamide) in an amount of 80 to 100 volume % based on the total volume of the dispersion medium provides the longer pot life.
The evaluation result of the composites of Examples 1 and 18 to 22 indicated that the composite containing inorganic particles, such as silica, in an amount of 0.09 to 5 mass % based on the total mass of the composite provide the higher rupture strength.
The evaluation result of the composites of Examples 1, 23, and 24 indicated that the preparation of the dispersion by applying the shear force with the means such as a disperser and a microfluidizer allows the composite with the higher rupture strength and the higher oxygen gas barrier property to be produced.
The evaluation result of the composites of Examples 1, 9, and 25 to 31 indicated that the addition of a resin, such as polyurethane and PVA, or a rubber, such as a natural rubber, improves the rupture strength of the composite. Additionally, it is indicated that the composite may have a crosslinked structure, and especially, a cross-linkage via a urethane bond improves the oxygen gas barrier property of the composite.
The composites including a plurality of stacked layers of Examples 32 to 48 also exhibited the high rupture strength and the high oxygen gas barrier property.
The evaluation result of the composites of Examples 32 and 35 to 41 indicated that when at least one layer of the plurality of layers of the composite contains inorganic particles in an amount of 0.09 to 5 mass % based on the total mass of the layer, the higher rupture strength is achieved, and the adhesiveness between the layers is improved.
The evaluation result of the composites of Examples 32 and 42 to 46 indicated that adding a resin or a rubber improves the rupture strength of the composite. Additionally, it is also indicated that the composite may have a crosslinked structure, and especially, a cross-linkage via a urethane bond improves the oxygen gas barrier property of the composite.
The evaluation result of the composites of Examples 32, 47, and 48 indicated that, in the production of the composite including the stacked upper layer and lower layer, supplying a dispersion for forming the upper layer over the lower layer containing a liquid (especially, a lower layer containing a liquid in an amount of more than 0 mass % and less than or equal to 30 mass %, or more than 5 mass % and less than or equal to 25 mass %) and subsequently removing the liquids from the upper layer and the lower layer allow improvement in the adhesiveness between the upper layer and the lower layer as compared with a case in which the upper layer is formed after the liquid in the lower layer is completely removed.
The evaluation result of the composites of Examples 49 to 52 indicated that the composite including the paper substrate derived from biomass, such as a filter paper and a cardboard, and the CNC and the CNF supported on the paper substrate has the high rupture strength, the high gas barrier property, and the high adhesiveness.
All the publications, patents, and patent applications cited in Description are directly incorporated herein as references.
| Number | Date | Country | Kind |
|---|---|---|---|
| 2021-059274 | Mar 2021 | JP | national |
| Filing Document | Filing Date | Country | Kind |
|---|---|---|---|
| PCT/JP2022/013379 | 3/23/2022 | WO |
