JP6893649B2 - Method for producing gel-like body and gel-like body, and method for producing composite material and composite material - Google Patents

Description

The present invention relates to a method for producing a gel-like body and a gel-like body using cellulose nanofibers, and a method for producing a composite material and a composite material.

Conventionally, there is an application of using a liquid as a pressure medium. For example, there is drilling fluid (also called mudwater) in oil well drilling in the development of brake fluid and oil / natural gas in vehicles and the like. Drilling fluid is used when deeply excavating the ground using an oil well drilling device, and drills such as polymer dispersants and thickeners to carry excavation debris to the ground and maintain the well wall. A muddy water conditioner is used (see Patent Document 1).

When drilling an oil well using drilling fluid, it is required that the drilling fluid can be used as a liquid, but it is difficult to flow in order to prevent the drilling fluid from escaping from cracks in the stratum of the well wall. It is required to be.
In addition, highly viscous fracturing fluid used for hydraulic fracturing in wells that extract oil, gas, etc. from the ground, cementing fluid used for cementing and plug treatment of wells, and temporary plugs. There are well treatment fluids used for various well treatments such as fluids. It has been proposed that the well treatment fluid contains a biodegradable fiber material that facilitates disposal and the like (see Patent Document 2).

On the other hand, in recent years, attention has been paid to cellulose nanofibers obtained by defibrating natural cellulose fibers into nano-sized fibers. Natural cellulose fiber is a biomass made from pulp such as wood, and it is expected that the environmental load will be reduced by effectively using it.

Cellulose nanofibers are offered on the market as aqueous dispersions, but they have been difficult to process for compounding with elastomers and synthetic resins. Since the cellulose nanofibers form hydrogen bonds and aggregate in the drying step of removing water from the aqueous dispersion, the cellulose nanofibers cannot exist in a highly defibrated state in the composite process, and the composite material is formed. It could not be sufficiently reinforced by cellulose nanofibers.

Therefore, a method of mixing a cellulose nanofiber aqueous dispersion with a rubber latex or a resin emulsion has been proposed (see Patent Documents 3 and 4).

However, composite materials produced by these methods have been affected by the properties of rubber latex or resin emulsions. In addition, it could not be applied to rubbers and resins that are not on the market as rubber latex or resin emulsion.

International Publication No. WO00 / 59964 International Publication No. WO13 / 161754 Japanese Unexamined Patent Publication No. 2015-98576 Japanese Unexamined Patent Publication No. 2016-29169

An object of the present invention is to provide a gel-like body using cellulose nanofibers, which has a high storage elastic modulus at the time of low strain and flows at the time of high strain, and a method for producing the same. Another object of the present invention is to provide a composite material using the gel-like body and a method for producing the same.

[Application Example 1] The gel-like body according to this application example is
A gel-like body consisting only of cellulose nanofibers, an ion cluster forming agent, and water.
The ion cluster forming agent is a monovalent metal salt and
The monovalent metal salt is sodium acrylate, potassium acrylate, sodium methacrylate or potassium methacrylate.
The mass ratio of the monovalent metal salt to the cellulose nanofibers in the gel form is 0.2 to 2 times.
Strain 1 when a gel-like body is sandwiched between conical disks with a diameter of 40 mm, and dynamic viscoelasticity measurements are performed at a conical disk spacing of 0.023 mm, a temperature of 23 ° C to 26 ° C, and a velocity of 1 radian / sec. The storage elastic modulus in% is 60 Pa to 25000 Pa, and the storage elastic modulus is smaller than the loss elastic modulus at 1000% strain.

[Application Example 2] The gel-like body according to this application example is
A gel-like body consisting only of cellulose nanofibers, an ion cluster forming agent, and water.
The ion cluster forming agent is a divalent metal salt and
The divalent metal salt is an unsaturated acid metal salt monomer, and is
The mass ratio of the divalent metal salt to the cellulose nanofibers in the gel form is 0.03 to 2 times.
Strain 1 when a gel-like body is sandwiched between conical disks with a diameter of 40 mm, and dynamic viscoelasticity measurements are performed at a conical disk spacing of 0.023 mm, a temperature of 23 ° C to 26 ° C, and a velocity of 1 radian / sec. The storage elastic modulus in% is 60 Pa to 25000 Pa, and the storage elastic modulus is smaller than the loss elastic modulus at 1000% strain.

[Application Example 3] The gel-like body according to this application example is
A gel-like body consisting only of cellulose nanofibers, an ion cluster forming agent, and water.
The cations of the ion cluster forming agent are bound to the cellulose nanofibers and are bonded to the cellulose nanofibers.
The cellulose nanofibers were in a defibrated state and did not precipitate in the water.
The ion cluster forming agent is maleic anhydride or oxalic acid .
The maleic anhydride or the oxalic acid has a mass ratio of 0.01 to 2 times with respect to the cellulose nanofibers.
Strain 1 when a gel-like body is sandwiched between conical disks with a diameter of 40 mm, and dynamic viscoelasticity measurements are performed at a conical disk spacing of 0.023 mm, a temperature of 23 ° C to 26 ° C, and a velocity of 1 radian / sec. The storage elastic modulus in% is 60 Pa to 25000 Pa, and the storage elastic modulus is smaller than the loss elastic modulus at 1000% strain.

[Application example 4]
The composite material according to this application example is
It is characterized by containing cellulose nanofibers using the gel-like body of the application example and an elastomer or a synthetic resin.

[Application example 5]
The method for producing a gel-like body according to this application example is as follows.
A mixing step of mixing cellulose nanofibers, an ion cluster forming agent, and water to obtain a gel-like substance by binding the cations ionized by the ion cluster forming agent to the cellulose nanofibers is included.
The ion cluster forming agent is a monovalent metal salt such as sodium acrylate, potassium acrylate, sodium methacrylate or potassium methacrylate.
In the gel-like body, the cellulose nanofibers were not precipitated, and the gel-like body had no precipitate.
The mass ratio of the ion cluster forming agent to the cellulose nanofibers in the gel form is 0.01 to 2 times.
When the gel-like body is sandwiched between conical disks having a diameter of 40 mm and the dynamic elastic modulus is measured at a distance of 0.023 mm and a temperature of 23 ° C. to 26 ° C. at 1 radian / sec, the strain is 1%. The storage elastic modulus is 60 Pa to 25000 Pa, and the storage elastic modulus at 1000% strain is smaller than the loss elastic modulus.

[Application example 6]
The method for producing a gel-like body according to this application example is as follows.
A mixing step of mixing cellulose nanofibers, an ion cluster forming agent, and water to obtain a gel-like substance by binding the cations ionized by the ion cluster forming agent to the cellulose nanofibers is included.
The ion cluster forming agent is a divalent metal salt and
The divalent metal salt is an unsaturated acid metal salt monomer, and is
In the gel-like body, the cellulose nanofibers were not precipitated, and the gel-like body had no precipitate.
The mass ratio of the ion cluster forming agent to the cellulose nanofibers in the gel form is 0.01 to 2 times.
When the gel-like body is sandwiched between conical disks having a diameter of 40 mm and the dynamic elastic modulus is measured at a distance of 0.023 mm and a temperature of 23 ° C. to 26 ° C. at 1 radian / sec, the strain is 1%. The storage elastic modulus is 60 Pa to 25000 Pa, and the storage elastic modulus at 1000% strain is smaller than the loss elastic modulus.
[Application 7]
A mixing step of mixing cellulose nanofibers, an ion cluster forming agent, and water to obtain a gel-like substance by binding the cations ionized by the ion cluster forming agent to the cellulose nanofibers is included.
The ion cluster forming agent is maleic anhydride or oxalic acid.
In the gel-like body, the cellulose nanofibers were not precipitated, and the gel-like body had no precipitate.
The mass ratio of the ion cluster forming agent to the cellulose nanofibers in the gel form is 0.01 to 2 times.
When the gel-like body is sandwiched between conical disks having a diameter of 40 mm and the dynamic elastic modulus is measured at a distance of 0.023 mm and a temperature of 23 ° C. to 26 ° C. at 1 radian / sec, the strain is 1%. The storage elastic modulus is 60 Pa to 25000 Pa, and the storage elastic modulus at 1000% strain is smaller than the loss elastic modulus .

[Application example 8 ]
The method for producing the composite material according to this application example is as follows.
A drying step of removing water from the gel-like body of the application example to obtain a fiber material, and
A swelling step of swelling the fiber material with water to obtain a swelling fiber material,
A kneading step of mixing the swollen fiber material with an elastomer to obtain a composite material,
Including
The kneading step is characterized by including a step of thinning using an open roll having a roll interval of 0.1 mm to 0.5 mm and a roll temperature of 0 ° C. to 50 ° C.

[Application example 9 ]
The method for producing the composite material according to this application example is as follows.
A drying step of removing water from the gel-like body of the application example to obtain a fiber material, and
A swelling step of swelling the fiber material with water to obtain a swelling fiber material,
A kneading step of mixing the swollen fiber material with a synthetic resin to obtain a composite material,
Is further included.

[Application example 10 ]
In the method for producing a composite material according to the above application example,
The synthetic resin is a thermoplastic resin and
In the kneading step, the processing region development temperature at the storage elastic modulus of the thermoplastic resin composition near the melting point (Tm ° C.) of the thermoplastic resin is 1.06 times the flat region development temperature (T3 ° C.) at the storage elastic modulus. The step of kneading at a kneading temperature in the range up to the temperature of (T3 ° C. × 1.06) can be included.

[Application example 11 ]
In the method for producing a composite material according to the above application example,
The synthetic resin is a thermosetting resin and is
In the kneading step, the swollen fiber material is mixed with the main agent of the thermosetting resin and kneaded at a kneading temperature in the range of a temperature 20 ° C. lower than the softening point of the main agent to a temperature 10 ° C. higher than the softening point. , Further can include the step of mixing the curing agent.

[Application example 12 ]
In the method for producing a composite material according to the above application example,
A dehydration step of dehydrating the composite material obtained in the kneading step can be further included.

According to the present invention, it is possible to provide a gel-like body using cellulose nanofibers having a high storage elastic modulus at the time of low strain and flowing at the time of high strain, and a method for producing the same. Further, according to the present invention, it is possible to provide a composite material using the gel-like body and a method for producing the same.

It is a flowchart which shows the manufacturing method of the gel-like body which concerns on one Embodiment. It is a flowchart which shows the manufacturing method of the composite material which concerns on one Embodiment. It is a figure which shows typically the kneading process in the manufacturing method of the composite material which concerns on one Embodiment. It is a figure which shows typically the kneading process in the manufacturing method of the composite material which concerns on one Embodiment. It is a figure which shows typically the kneading process in the manufacturing method of the composite material which concerns on one Embodiment. It is a figure which shows the electron micrograph of the tensile fracture cross section of the composite material of Example 43. It is a figure which shows the electron micrograph of the tensile fracture cross section of the composite material of Example 45. It is a figure which shows the electron micrograph of the tensile fracture cross section of the composite material of the comparative example 3. It is a figure which shows the electron micrograph of the tensile fracture cross section of the composite material of Comparative Example 10. It is a figure which shows the graph of the stress-strain of the composite material of Examples 56, 57. It is a figure which shows the graph of the coefficient of linear expansion-temperature of the composite material of Example 58. It is a graph which shows the relationship between the storage elastic modulus and the temperature of the sample of Example 59 explaining the method for obtaining the 2nd temperature range.

Hereinafter, preferred embodiments of the present invention will be described in detail with reference to the drawings. The embodiments described below do not unreasonably limit the content of the present invention described in the claims. Moreover, not all of the configurations described below are essential constituent requirements of the present invention.

1. 1. Method for Producing Gel-like Body With reference to FIG. 1, a method for producing a gel-like body according to an embodiment will be described. FIG. 1 is a flowchart showing a method for producing a gel-like body according to an embodiment.

As shown in FIG. 1, the method for producing a gel-like body according to the present embodiment includes a mixing step (S10) of mixing cellulose nanofibers, an ion cluster forming agent, and water to obtain a gel-like body. Here, the mass ratio of the ion cluster forming agent to the cellulose nanofibers in the gel form is 0.01 to 2 times.

1-1. Mixing step The mixing step (S10) is a step of mixing cellulose nanofibers, an ion cluster forming agent, and an aqueous solvent to obtain a gel-like substance.

In the mixing step (S10), the ion cluster forming agent is added to the cellulose nanofiber dispersion liquid as a raw material, and the mixture can be mixed using a known stirrer, for example, a propeller stirrer, a rotary stirrer, a three-roll or the like. The cellulose nanofiber dispersion liquid and the ion cluster forming agent dispersion liquid in which the ion cluster forming agent is dissolved or dispersed may be mixed.

1-1-1. Cellulose nanofiber dispersion liquid As the cellulose nanofiber dispersion liquid as a raw material, those available on the market from Daiichi Kogyo Seiyaku Co., Ltd. and the like can be used. Generally, commercially available cellulose nanofibers are provided in a state of being dispersed in an aqueous solution at, for example, a concentration of 2%.

The cellulose nanofiber dispersion liquid as a raw material can be obtained by a production method including, for example, an oxidation step of oxidizing natural cellulose fibers to obtain oxidized cellulose fibers and a miniaturization step of refining the oxidized cellulose fibers. Here, a method for producing a cellulose nanofiber dispersion liquid using an oxidation step will be described, but those obtained by other production methods may also be used.

First, in the oxidation step, water is added to the natural cellulose fiber as a raw material and treated with a mixer or the like to prepare a slurry in which the natural cellulose fiber is dispersed in water.

Here, examples of natural cellulose fibers include wood pulp, cotton pulp, bacterial cellulose and the like. More specifically, examples of wood pulp include softwood pulp, hardwood pulp and the like, examples of cotton pulp include cotton linter and cotton lint, and examples of non-wood pulp include cotton linter and cotton lint. Straw pulp, bagus pulp and the like can be mentioned. At least one of these can be used as the natural cellulose fiber.

Natural cellulose fibers have a structure composed of cellulose microfibril bundles and lignin and hemicellulose that fill the spaces between them. That is, it is presumed that hemicellulose covers the cellulose microfibrils and / or the cellulose microfibril bundles, and lignin covers them. Cellulose microfibrils and / or cellulose microfibril bundles are firmly adhered by lignin to form plant fibers. Therefore, it is preferable that the lignin in the plant fiber is removed in advance from the viewpoint that the aggregation of the cellulose fiber in the plant fiber can be prevented. Specifically, the lignin content in the plant fiber-containing material is usually about 40% by mass or less, preferably about 10% by mass or less. Further, the lower limit of the removal rate of lignin is not particularly limited, and it is preferable that it is close to 0% by mass. The lignin content can be measured by the Klason method.

As the cellulose microfibril, a cellulose microfibril having a width of about 4 nm exists as the smallest unit, and this can be called a single cellulose nanofiber. In the present invention, the "cellulose nanofiber" is a natural cellulose fiber and / or an oxidized cellulose fiber unraveled to a nano-size level, and in particular, the average value of the fiber diameter can be 1 nm to 200 nm, and further 1 nm. It can be up to 150 nm, especially cellulose microfibrils and / or cellulose microfibril bundles of 1 nm to 100 nm. That is, the cellulose nanofibers can include a single cellulose nanofibers or a bundle of a plurality of single cellulose nanofibers.

The aspect ratio (fiber length / fiber diameter) of the cellulose nanofibers can be 10 to 1000 on average, further 10 to 500, and particularly 100 to 350.

The average value of the fiber diameter and the fiber length of the cellulose nanofibers is an arithmetic mean value measured for at least 50 or more cellulose nanofibers in the field of view of the electron microscope.

Next, as an oxidation step, natural cellulose fibers are oxidized in water using an N-oxyl compound as an oxidation catalyst to obtain oxidized cellulose fibers. Examples of the N-oxyl compound that can be used as an oxidation catalyst for cellulose include 2,2,6,6-tetramethyl-1-piperidin-N-oxyl (hereinafter, also referred to as TEMPO), 4-acetamide-TEMPO, and the like. 4-carboxy-TEMPO, 4-phosphonooxy-TEMPO and the like can be used.

After the oxidation step, for example, a purification step of repeating washing and filtration can be carried out to remove impurities other than the oxidized cellulose fibers contained in the slurry, such as unreacted oxidizing agents and various by-products. The solvent containing the cellulose oxide fiber is, for example, impregnated with water, and at this stage, the cellulose oxide fiber is not defibrated to the unit of the cellulose nanofiber. Water can be used as the solvent, but for example, an organic solvent (alcohols, ethers, ketones, etc.) soluble in water can be used in addition to water depending on the purpose.

The cellulose oxide fiber has a carboxyl group in which a part of the hydroxyl group of the cellulose nanofiber is modified with a substituent having a carboxyl group. The average value of the fiber diameter of the oxidized cellulose fiber can be 10 μm to 30 μm. The average value of the fiber diameters of the cellulose oxide fibers is an arithmetic mean value measured for at least 50 or more cellulose oxide fibers in the field of view of the electron microscope. Oxidized cellulose fibers can be bundles of cellulose microfibrils. Oxidized cellulose fibers can be defibrated into cellulose nanofibers in the miniaturization step.

In the miniaturization step, the cellulose oxide fibers can be agitated in a solvent such as water, and cellulose nanofibers can be obtained.

In the miniaturization step, the solvent as the dispersion medium can be water. Further, as a solvent other than water, an organic solvent soluble in water, for example, alcohols, ethers, ketones and the like can be used alone or in combination.

The stirring process in the miniaturization process includes, for example, a breaker, a beater, a low-pressure homogenizer, a high-pressure homogenizer, a grinder, a cutter mill, a ball mill, a jet mill, a short-screw extruder, a twin-screw extruder, an ultrasonic stirrer, and a household juicer mixer. Etc. can be used.

Further, the solid content concentration of the solvent containing the oxidized cellulose fibers in the miniaturization treatment can be, for example, 50% by mass or less. If the solid content concentration exceeds 50% by mass, high energy is required for dispersion.

A cellulose nanofiber dispersion liquid containing cellulose nanofibers can be obtained by the miniaturization step. The cellulose nanofiber dispersion can be a colorless transparent or translucent suspension. In the suspension, cellulose nanofibers, which are fibers that have been surface-oxidized and defibrated to be finely divided, are dispersed in water. That is, in this dispersion, cellulose nanofibers can be obtained by weakening the strong cohesive force between microfibrils (hydrogen bonds between surfaces) by introducing a carboxyl group in an oxidation step and further undergoing a micronization step. Then, by adjusting the conditions of the oxidation step, the carboxyl group content, polarity, average fiber diameter, average fiber length, average aspect ratio and the like can be controlled.

The cellulose nanofiber dispersion liquid thus obtained can contain 0.1% by mass to 10% by mass of cellulose nanofibers. Further, for example, it can be a dispersion liquid diluted to 1% by mass of the solid content of the cellulose nanofibers. Further, the dispersion liquid can have a light transmittance of 40% or more, further can have a light transmittance of 60% or more, and can be particularly 80% or more. The transmittance of the dispersion liquid can be measured as the transmittance at a wavelength of 660 nm using an ultraviolet-visible spectroscopic hardness tester.

1-1-2. Ion cluster forming agent When the ion cluster forming agent is mixed with the cellulose nanofiber dispersion liquid, the cations separated from the ion cluster forming agent can be ion-bonded to the cellulose nanofiber. A plurality of cations separated from the ion cluster forming agent gather to form an ion cluster. Each of the cations binds to cellulose nanofibers, forming a network of cellulose nanofibers via ion clusters. The ion cluster forming agent contains at least one of a metal salt and a hydrogen compound.

The metal salt can include at least one of a monovalent metal salt, a divalent metal salt and a trivalent metal salt. As the metal salt, a monovalent metal salt and a divalent metal salt are preferable. The monovalent metal salt is sodium acrylate, potassium acrylate, sodium methacrylate, potassium methacrylate. The divalent metal salt is an unsaturated metal salt monomer , and the unsaturated metal salt monomer is a salt containing magnesium, calcium, barium, zinc, copper, iron, lead, nickel, manganese, tin and the like. for example, zinc acrylate, magnesium acrylate, calcium acrylate, zinc methacrylate, magnesium methacrylate, and etc. calcium methacrylate. Examples of the trivalent metal salt include neodymium methacrylate, aluminum chloride (AlCl ₃ ), iron chloride (FeCl ₃ ) and the like. The metal salt is preferably water-soluble in order to form a gel.

Hydrogen compounds, for example, a non-aqueous maleic acid or oxalic acid.

The mass ratio of the ion cluster forming agent to the cellulose nanofibers in the gel form is 0.01 to 2 times. This is because a gel body having a high storage elastic modulus at the time of low strain and flowing at the time of high strain can be obtained. In particular, when the mass ratio of the ion cluster forming agent to the cellulose nanofibers exceeds twice, the ion cluster forming agent that does not bind to the cellulose nanofibers is precipitated at the stage of the fiber material. The precipitated ion cluster forming agent may affect the physical properties of the elastomer and the like in the kneading step described later.

When the ion cluster forming agent is a monovalent metal salt, the mass ratio of the monovalent metal salt to the cellulose nanofibers in the gel form can be 0.2 to 2 times, and further 0.5 times to 2 times. It can be 1.5 times. When the ion cluster forming agent is a divalent metal salt, the mass ratio of the divalent metal salt to the cellulose nanofibers in the gel form can be 0.03 to 2 times, and further 0.1 times to 2 times. It can be 1.5 times. As a result of the experiment, it can be inferred that the blending amount of the monovalent metal salt or the divalent metal salt and the cellulose nanofibers affects the processability in the kneading step described later.

When the ion cluster forming agent is a hydrogen compound, the mass ratio of the hydrogen compound to the cellulose nanofibers in the gel form can be 0.01 to 2 times, and further 0.01 to 1 times. be able to.

Water may contain components other than water.

1-1-3. Gel-like body The gel-like body is a mixture of cellulose nanofibers, an ion cluster forming agent, and water. The ion cluster forming agent is ionized and cations are bound to the cellulose nanofibers. The cation is ionically bonded by substituting ^{Na +} , which is ionically bonded to the carboxy group of the cellulose nanofiber. It is considered that the water-soluble cations in the gel form are formed by gathering a plurality of cations to form an ion cluster. Then, it is considered that cellulose nanofibers are bound to the ion cluster (it is considered to be ionized in water). The size of the ion cluster is several tens of nm to several hundreds nm. The ion cluster forming agent is preferably a water-soluble one that does not precipitate cellulose nanofibers.

Water-soluble cations are dispersed throughout the gel-like body in a defibrated state of cellulose nanofibers. It is considered that a plurality of ion clusters in which cations are aggregated are formed in a gel-like body and are scattered throughout. Since each of the cations in the ion cluster is ionic bonded to the cellulose nanofiber, the cellulose nanofiber forms a structure on the network via the ion cluster in the gel-like body. The network structure of the cellulose nanofibers generates a high storage elastic modulus at the time of low strain of the gel-like body.

The gel-like body is a gel-like body using cellulose nanofibers, has a high storage elastic modulus at the time of low strain, and flows at the time of high strain.

For the gel-like body, the gel-like body was sandwiched between conical disks having a diameter of 40 mm, and dynamic viscoelastic measurements were performed at a distance of 0.023 mm between the conical disks, a temperature of 23 ° C. to 26 ° C., and a speed of 1 radian / sec. At that time, the storage elastic modulus at 1% strain is 60 Pa to 25000 Pa, and the storage elastic modulus is smaller than the loss elastic modulus at 1000% strain. A known rheometer can be used for the dynamic viscoelasticity measurement. For example, the dynamic viscoelasticity measurement can be performed by attaching a conical disk to an ARES-G2 rheometer manufactured by TA Instruments and repeating rotation and inversion. The conical disk, also called a cone and plate, has a diameter of 40 mm and θ = 1 °, and the distance between the tip of the cone and the plate is set to 0.023 mm. The measurement mode is oscillation, the angular velocity is 1 radian / sec, and the temperature of the conical disk is room temperature (23 ° C to 26 ° C).

The gel-like body can be used, for example, as a brake fluid in a vehicle or the like, or as drilling fluid (also called mudwater) in oil well drilling in the development of oil / natural gas. Drilling fluid is used when excavating the ground deeply using an oil well drilling device, and carries out drilling debris to the ground and maintains the well wall. When using the gel as drilling fluid,
Since it is a solid that can be used as a liquid when excavating an oil well and has a predetermined storage elastic modulus when no pressure is applied to the gel-like body, the gel-like body escapes from cracks in the formation of the well wall. Can be prevented. Further, the gel-like body can be used as a well processing fluid (fracturing fluid, cementing fluid, temporary plug fluid, etc.) for extracting petroleum, natural gas, etc. from the ground. When the gel-like body is used, for example, as a fracturing fluid among well-treated fluids, it can be infiltrated into the formation as a fluid when pressure is applied, and can be infiltrated into the formation as a solid when no pressure is applied. Can stay. Since cellulose nanofibers are used in the gel form, the environmental load is small when used as a well treatment fluid.
2. Method for Producing Composite Material With reference to FIG. 2, a method for producing a composite material according to an embodiment will be described. FIG. 2 is a flowchart showing a method for manufacturing a composite material according to an embodiment.

As shown in FIG. 2, the method for producing the composite material according to the present embodiment includes a drying step (S12) of removing water from the gel-like body obtained in the mixing step (S10) to obtain a fiber material, and a fiber material. Is further included in the kneading step (S16) of mixing with an elastomer or a synthetic resin to obtain a composite material. For example, a method for producing a composite material includes a swelling step (S14) in which the fiber material is swollen with water, and a kneading step (S16) in which the swollen swelling fiber material is mixed with an elastomer or a synthetic resin to obtain a composite material. A dehydration step (S18) of removing water from the material can be included.

2-1. Drying step The drying step (S12) is a step of removing water from the gel-like body obtained in the mixing step (S10) to obtain a fiber material. As a method for removing water from the gel-like body, a known method can be used, and for example, it may be dried by heating.

For example, a gel-like body is poured into a container (such as a vat), and the container is placed in an oven to evaporate water at 30 ° C. to 100 ° C.

2-2. Fiber material The fiber material obtained in the drying step contains cellulose nanofibers to which elements derived from ion cluster forming agents are bound.

The fiber material can be pulverized in the form of powder in consideration of processability in the kneading process.

Due to the removal of water, the cellulose nanofibers in the fiber material again form hydrogen bonds on the surface of the cellulose nanofibers, so that they reaggregate into, for example, a sheet-like solid. Even if the fiber material is mixed with the elastomer or the like as it is, the cellulose nanofibers are not defibrated, and the crushed solid matter is only dispersed in the elastomer.

In order to obtain the effect of reinforcing the cellulose nanofibers, which are nano-sized fibers, by mixing the fiber material with an elastomer or the like, the cellulose nanofibers are loosened one by one as in the gel form. Must be dispersed in the composite material.

2-3. Swelling step The swelling step (S14) is a step of swelling the fiber material with water.

By impregnating the fiber material with a predetermined amount of water, the peelability between the cellulose nanofibers firmly bonded in the fiber material is improved. It is thought that the elements bound to the cellulose nanofibers are reionized by the water absorbed by the fiber material (in the case of metal salts, they become metal ions), weakening the hydrogen bonds between the cellulose nanofibers and the ionic bonds with the metal ion clusters. Be done.

In the swelling step (S14), the fiber material and a predetermined amount of water are placed in a closed container, heated for a predetermined time, and held. For example, it is about 1 hour at 70 ° C. Water that has become saturated water vapor in the closed container is absorbed by the fiber material, and the fiber material swells. A glass container can be used as the closed container, and an autoclave device can be used.

The mass ratio of the predetermined amount of water contained in the fiber material in the swelling step (S14) to the cellulose nanofibers contained in the fiber material can be 0.5 to 4 times. If the mass ratio of water to the cellulose nanofibers is less than 0.5 times, the processability in the kneading step (S16) is lowered. If the mass ratio of water to the cellulose nanofibers exceeds 4 times, it becomes difficult to mix with the elastomer or the like, and the processing time becomes long. The predetermined amount of water contained in the fiber material in the swelling step (S14) can further have a mass ratio of 1 to 3.5 times to the cellulose nanofibers, and particularly a mass ratio to 1 to 3 times to the cellulose nanofibers. Can be doubled.

The swelling step (S14) is for improving workability and defibration in the kneading step. Therefore, it is sufficient that the fiber material used in the kneading step contains a predetermined amount of water without going through the swelling step (S14). For example, the water is removed in the drying step (S12) until the water content reaches a predetermined amount. You may. A fiber material containing a predetermined amount of water is called a swollen fiber material.

2-4. Kneading step The conditions of the kneading step (S16) differ depending on the material used as the matrix of the composite material. Thermoplastic resins and thermosetting resins will be described as elastomers and synthetic resins, respectively.

2-4-1. Kneading Step Using Elastomer The kneading step (S16) of kneading the fiber material with the elastomer will be described with reference to FIGS. 3 to 5. 3 to 5 are diagrams schematically showing a method for producing a composite material according to an embodiment. The kneading step (S16) is characterized by including a thinning step of thinning using an open roll having a roll interval of 0.1 mm to 0.5 mm and a roll temperature of 0 ° C. to 50 ° C.

First, before the thinning step, as shown in FIG. 3, the elastomer 30 wound around the first roll 10 can be kneaded, and the molecular chain of the elastomer 30 is appropriately cut to release free radicals. Generate. The free radicals of the elastomer 30 produced by kneading are easily combined with the cellulose nanofibers. As the elastomer 30, natural rubber, synthetic rubber and thermoplastic elastomer can be used.

Next, as shown in FIG. 4, a step of gradually putting the swelling fiber material 80 into the bank 34 of the elastomer 30 wound around the first roll 10 and kneading it to obtain an intermediate mixture can be performed. Here, in addition to the cellulose nanofibers, the swelling fiber material 80 includes, for example, a cross-linking agent, a vulcanizing agent, a vulcanization accelerator, a vulcanization retarder, a softening agent, a plasticizer, a curing agent, a reinforcing agent, a filler, and an antiaging agent. Agents, colorants, acid acceptors and the like can be included. The compounding agents other than these cellulose nanofibers can be added to the elastomer 30 at an appropriate time in the mixing process.

The step of obtaining the intermediate mixture of FIGS. 3 and 4 is not limited to the open roll method, and for example, a closed kneading method or a multi-screw extrusion kneading method can also be used.

Further, as shown in FIG. 5, a thinning step can be performed. In the thinning step, an open roll 2 having a roll interval of 0.5 mm or less can be used to perform thinning at 0 ° C. to 50 ° C. to obtain an uncrosslinked composite material 50. In this step, the first roll 10 and the second roll
The roll distance d with the roll 20 is set to, for example, 0.5 mm or less, more preferably 0.1 mm to 0.5 mm, and the intermediate mixture 36 obtained in FIG. 2 is put into the open roll 2 to be thin. The threading can be performed once to multiple times. The number of thinnings can be, for example, about 1 to 10 times. Assuming that the surface velocity of the first roll 10 is V1 and the surface velocity of the second roll 20 is V2, the surface velocity ratio (V1 / V2) of both in thinning is 1.05 to 3.00. It can be 1.05 to 1.2. By using such a surface velocity ratio, a desired shearing force can be obtained.

The composite material 50 extruded from such a narrow roll is greatly deformed as shown in FIG. 5 by the restoring force due to the elasticity of the elastomer, and at that time, the cellulose nanofibers move greatly together with the elastomer. The composite material 50 obtained through thinning is rolled by a roll and dispensed into a sheet having a predetermined thickness, for example, 100 μm to 500 μm.

In this thinning step, in order to obtain as high a shearing force as possible, the roll temperature can be set to, for example, 0 ° C to 50 ° C, and further set to a relatively low temperature of 5 ° C to 30 ° C. Can be done. The measured temperature of the composite material 50 can also be adjusted to 0 ° C. to 50 ° C., and further adjusted to 5 ° C. to 30 ° C.

By adjusting to such a temperature range, cellulose nanofibers can be defibrated by utilizing the elasticity of the elastomer, and the defibrated cellulose nanofibers can be dispersed in the composite material 50.

Due to the high shearing force in this thinning step, a high shearing force acts on the elastomer, and the cellulose nanofibers in the swelling fiber material are separated from each other so as to be pulled out one by one by the molecules of the elastomer and dispersed in the elastomer. .. This is because the elements bonded to the cellulose nanofibers are ionized by the swelling of the fiber material, weakening the bonding force between the cellulose nanofibers. Since metal ions derived from metal salts tend to separate cellulose nanofibers from each other, it is preferable to use metal salts as an ion cluster forming agent for composite materials. In particular, since the elastomer has elasticity and viscosity, cellulose nanofibers can be defibrated and dispersed. Then, it is possible to obtain a composite material 50 having excellent dispersibility and dispersion stability of the cellulose nanofibers (the cellulose nanofibers are less likely to reaggregate).

More specifically, when the elastomer and the cellulose nanofibers are mixed with an open roll, the viscous elastomers invade each other of the cellulose nanofibers. If the surface of the cellulose nanofibers is moderately active, for example, by oxidation treatment, it can be particularly easily bonded to elastomer molecules. Next, when a strong shearing force acts on the elastomer, the cellulose nanofibers also move with the movement of the elastomer molecules, and the agglomerated cellulose nanofibers are separated by the restoring force of the elastomer due to the elasticity after shearing. , Will be dispersed in the elastomer. In particular, the open roll method is preferable because it can measure and control the actual temperature of the mixture as well as control the roll temperature.

Next, a method for producing a composite material when a synthetic resin is used will be described.

2-4-2. Kneading process using a thermoplastic resin A kneading process using a thermoplastic resin as a synthetic resin will be described. In the kneading step, the processing region development temperature at the storage elastic modulus of the thermoplastic resin composition near the melting point (Tm ° C.) of the thermoplastic resin is 1.06 times (T3) the flat region development temperature (T3 ° C.) at the storage elastic modulus. The step of kneading at a kneading temperature in the range up to the temperature of ° C. × 1.06) can be included.

In the kneading step, an apparatus for melting and forming a thermoplastic resin, for example, an open roll, a closed kneader, an extruder, an injection molding machine, or the like can be used. For example, it can be carried out by using an extrusion molding machine having a conical screw or an open roll 2 as shown in FIGS. 3 to 5.

The kneading step is, for example, a first temperature mixing step of kneading the thermoplastic resin and the swollen fiber material at a first temperature to obtain a first mixture, and a lower temperature step of adjusting the temperature of the first mixture to a second temperature. And a low temperature kneading step of kneading the first mixture at the second temperature. The first temperature is a temperature higher than the second temperature, and the second temperature is from the processing region development temperature in the storage elastic modulus of the composite material near the melting point (Tm ° C.) of the thermoplastic resin to the flat region development in the storage elastic modulus. It is in the range up to a temperature of 1.06 times (T3 ° C. × 1.06) of the temperature (T3 ° C.).

2-2-2-1. First Temperature Mixing Step In the first temperature mixing step, the thermoplastic resin and the swollen fiber material are kneaded at the first temperature to obtain a first mixture.

The first temperature mixing step is a step until the planned amount of the swelling fiber material is charged into the thermoplastic resin, and preferably, the cellulose nanofibers are visually mixed with the entire thermoplastic resin by the operator. It can be a process until it recognizes that. As in the case of the elastomer described above, this can be carried out as shown in FIGS. 3 and 4.

The first temperature is higher than the melting point (Tm) of the thermoplastic resin. The first temperature is a temperature higher than the second temperature. The first temperature can be 25 ° C. or higher higher than the melting point (Tm) of the thermoplastic resin. The first temperature can be 25 ° C. or higher and 70 ° C. or lower higher than the melting point (Tm) of the thermoplastic resin, and can be 25 ° C. or higher and 60 ° C. or lower higher than the melting point (Tm). The first temperature is the actual temperature of the thermoplastic resin during the first temperature mixing step, not the temperature of the processing apparatus. The molding processing temperature of a thermoplastic resin is generally expressed by the set temperature of the heating cylinder in the case of a processing device such as an extruder or an injection molding machine, but is usually higher than the set temperature of the processing device due to shear heat generation during kneading. However, the actual temperature of the resin becomes high. Since the first temperature is the temperature during processing, it is desirable to measure the actual surface temperature of the resin as much as possible, but if it cannot be measured, measure the surface temperature of the resin immediately after taking out the first mixture from the processing apparatus. It can be the temperature. The first temperature is not the temperature immediately after the resin is charged into the processing apparatus, but the temperature at which the swollen fiber material is completely charged and mixed.

In the present invention, "melting point (Tm)" refers to a melting peak value measured according to JIS K7121 using differential scanning calorimetry (DSC).

The cellulose nanofibers in the first mixture obtained in the first temperature mixing step are dispersed and exist in the same aggregate as the raw material. Therefore, the first mixture will have defects in its material, and when, for example, a tensile test is performed, the elongation at the time of cutting is significantly lower than that of the raw material thermoplastic resin alone.

2-2-2-2. Low temperature step In the low temperature step, the temperature of the first mixture is adjusted to the second temperature.

Here, the second temperature will be described.

The general processing set temperature in the first temperature mixing step, that is, the set temperature of the processing apparatus, is recommended as the processing set temperature of the thermoplastic resin in order to sufficiently melt the thermoplastic resin in a short time and process it quickly. The temperature is higher than the temperature at which it is. Therefore, the thermoplastic resin is not processed near its melting point. As described above, the surface temperature of the thermoplastic resin during processing is higher than the set processing temperature.

In particular, when a filler such as cellulose nanofiber is mixed in the thermoplastic resin, the processing set temperature is usually higher than the general processing set temperature. is there. Further, when the blending amount of the cellulose nanofibers is increased, the temperature of the first mixture in the first temperature mixing step rises sharply due to heat generated by shearing.

Therefore, in order to carry out the low temperature kneading step, it is necessary to lower the temperature of the first mixture. Since the temperature of the first mixture rises when kneading is performed, it may be difficult to lower the temperature while continuing kneading. Therefore, in the low temperature step, after kneading, the kneader can be stopped for a predetermined time, or the first mixture can be taken out from the kneader and allowed to cool to the second temperature. Further, the first mixture can be positively cooled by using a cooling device provided with a cooling mechanism such as a fan, a spot cooler, or a chiller. Machining time can be shortened by actively cooling.

The second temperature is 1.06 from the processed region development temperature in the storage elastic modulus of the composite material near the melting point (Tm ° C.) of the thermoplastic resin used in this production method to the flat region development temperature (T3 ° C.) in the storage elastic modulus. It is in the range up to twice the temperature (T3 ° C. × 1.06).

Studies by the inventors have shown that when a dynamic viscoelasticity test (hereinafter referred to as a DMA test) is performed on a composite material, it behaves differently from the raw material thermoplastic resin. The raw material thermoplastic resin flows with a sharp decrease in storage elastic modulus (E') near the melting point (Tm). However, the composite material mixed with cellulose nanofibers has a flat region in which the storage elastic modulus (E') hardly decreases even if the melting point is exceeded by dispersing the cellulose nanofibers in a predetermined amount or more, that is, rubber such as elastomer. It was found that an elastic region was developed.

The low-temperature kneading step utilizes the temperature near the melting point to a part of this flat region to defibrate the aggregated cellulose nanofibers so as to loosen them and disperse them in the thermoplastic resin. In order to set the second temperature range, it is necessary to perform a DMA test in advance on a sample of the composite material in the formulation. Specifically, it is as follows.

First, the first temperature mixing step of 2-2-2-1 is carried out with a predetermined formulation to obtain a first mixture. Next, for the first mixture, the same step as the low temperature kneading step described later is carried out with the temperature near the melting point of the thermoplastic resin as the matrix (for example, the processable range of + 10 + 20 ° C. of the melting point) as the kneading temperature. To obtain a composite material sample. In this sample, it is desirable that cellulose nanofibers and the like are defibrated and dispersed, but even if the defibration is insufficient, a clear change in characteristics can be confirmed near the inflection point or the flat region development temperature. A DMA test is performed on this composite material sample, and if a flat region is confirmed by graphing the relationship between the storage elastic modulus (E') and the temperature (° C.), this DMA test result is used. If a flat region cannot be confirmed in this composite material sample, a new composite material sample is obtained by the above method with the temperature near the inflection point as the second temperature, and a DMA test is performed to graph the composite material sample in the same manner. .. Such work is repeated until the flat region is clearly expressed.

A method of setting the kneading temperature (second temperature) in the low-temperature kneading step will be described using the DMA test results of the composite material sample of Example 59 described later produced using the kneading temperature thus obtained. FIG. 12 is a graph showing the DMA measurement result (temperature dependence of the storage elastic modulus E') in the sample of Example 59. In FIG. 12, the horizontal axis is the temperature (° C.), the vertical axis on the left is the logarithmic value (log (E')) of the storage elastic modulus (E'), and the graph of the log (E') is a solid line. Indicated. In FIG. 12, the vertical axis on the right side is the differential value (d (log (E')) / dT) of the logarithmic value (log (E')) of the storage elastic modulus (E'), and d (log (E')). The graph of')) / dT is shown by a broken line.

The thermoplastic resin of Example 59 is linear short chain branched polyethylene (LLDPE) having a melting point of 115 ° C., and the graph of log (E') has an inflection point P1 at 121.5 ° C. The inflection point P1 clearly appears in the graph of d (log (E')) / dT. The inflection point appears at slightly different temperatures by varying the amount of cellulose nanofibers. The inflection point P1 also differs depending on the melting point of the thermoplastic resin.

Next, the "processed region expression temperature T2" in the storage elastic modulus (E') is obtained from the graph of the log (E') in FIG. The slope of the log (E') graph is constant below 78 ° C., and the storage elastic modulus (E') sharply decreases near the melting point (Tm) of 115 ° C., and the flow starts. When the thermoplastic resin alone without cellulose nanofibers starts to flow, the storage elastic modulus (E') continues to decrease and flows, but in the composite material, the rapid decrease in the log (E') graph stops. It becomes a flat region and does not flow. The first region W1 having a constant slope in the region below the melting point before the start of flow clearly appears in the graph of d (log (E')) / dT, and it can be seen that it is in the range of 62 ° C to 78 ° C. .. The temperature at the first intersection P2 between the tangent line L2 of the graph of log (E') in the first region W1 and the tangent line L1 of the graph of log (E') at the inflection point P1 is the processing region expression temperature T2. (108 ° C.). The processing region development temperature T2 is the lower limit temperature at which kneading can be performed in the low temperature kneading step.

Further, the "flat region (rubber elastic region) expression temperature T3" in the storage elastic modulus (E') is obtained from the graph of the log (E') in FIG. In FIG. 12, the inclination is constant in the range of 128 ° C. to 142 ° C. The second region W2 with a constant slope starting from the end of the sharp drop in the log (E') graph at a temperature above the melting point clearly appears in the d (log (E')) / dT graph. .. The temperature of the second intersection P3 between the tangent line L3 of the graph of log (E') in the second region W2 and the tangent line L1 of the graph of log (E') at the inflection point P1 is the flat region development temperature T3. Is.

In addition, in the region (W1, W2) where the slope is constant, it is assumed that the region where the slope of the log (E') graph is constant exists in a temperature range of at least 10 ° C. or higher. The flat region is the second region W2.

1 of a temperature higher than the temperature T1 of the inflection point P1 thus obtained and a temperature at which the viscosity of the composite material sample becomes low and does not flow out, for example, the flat region development temperature T3 (125 ° C. in FIG. 12). The upper limit of the kneading temperature is T4 (132.5 ° C. in FIG. 12) at a temperature of .06 times (T3 ° C. × 1.06). It is considered that agglomerates of cellulose nanofibers can be defibrated with any thermoplastic resin up to a temperature T4 which is 1.06 times (T3 ° C. × 1.06) the flat region expression temperature T3.

Within the temperature range from the processing region development temperature T2 to the flat region development temperature T3 1.06 times (T3 ° C. × 1.06) temperature T4, the second mixture has moderate elasticity and moderate viscosity. Therefore, it can be processed and the cellulose nanofibers can be defibrated. Studies by the present inventors have found that the temperature range from T3 to T4 tends to increase as the melting point increases.

The lower limit of the kneading temperature in the low temperature kneading step may be set to be equal to or higher than the inflection point temperature T1 at the inflection point P1. This is because the processing of the second mixture becomes easier. By changing the blending amount of the cellulose nanofibers, the temperature T2 and the temperature T4 become slightly different temperatures.

According to the research by the present inventors, the low temperature kneading step is performed by setting the kneading temperature in the range from a temperature slightly lower than the turning point temperature T1 to a temperature T4 which is 1.06 times (T3 ° C. × 1.06) the flat region development temperature T3. By carrying out the above, it was convinced that the agglomerated cellulose nanofibers could be defibrated so as to be loosened and dispersed in the thermoplastic resin.

The second temperature is a relatively low temperature that is not adopted as the processing temperature of the thermoplastic resin, and in particular, is a low temperature range that has not been adopted as the processing temperature of the second mixture.

The first mixture, whose temperature has dropped to the second temperature, can be placed in, for example, an oven set to the second temperature and maintained at a predetermined temperature within the range of the second temperature. The temperature of the first mixture taken out from the kneader is lowered, so that the processing quality is stabilized.

Further, when a pellet containing commercially available cellulose nanofibers is used as the first mixture, a reheating step is required between the first temperature mixing step and the low temperature lowering step. The reheating step can be performed by heating above the melting temperature of the thermoplastic resin.

2-2-2-3. Low temperature kneading step In the low temperature kneading step, the first mixture is kneaded at the second temperature.

As the first mixture, the one obtained by the first temperature mixing step of 2-2-2-1 can be used.

In this step, for example, the roll distance d between the first roll 10 and the second roll 20 is set to, for example, 0.5 mm or less, more preferably 0 mm, in the same manner as in FIG. 5 in which the elastomer is used under conditions other than the roll temperature. The interval is set to about 0.5 mm, and the first mixture obtained in the first temperature mixing step can be put into the open roll 2 for kneading.

The first mixture extruded from such a narrow roll is due to the elasticity of the thermoplastic resin because the second temperature is in the temperature range having appropriate elasticity and appropriate viscosity. It is greatly deformed by the restoring force, and the cellulose nanofibers can move greatly with the deformation of the thermoplastic resin at that time.

The second temperature is the surface temperature of the first mixture in the low temperature kneading step, not the set temperature of the processing apparatus. As explained in the first temperature, it is desirable to measure the actual surface temperature of the resin as much as possible in the second temperature, but if it cannot be measured, measure the surface temperature of the resin immediately after the composite material is taken out from the processing device. From that temperature, it can be set to the second temperature during processing.

In the case of the open roll 2, the surface temperature can be measured using a non-contact thermometer, and the non-contact thermometer 40 may be arranged at a position other than the position immediately after passing through the nip, and is preferably the first position. Above the roll 10. Immediately after passing through the nip, the temperature of the first mixture changes rapidly and is an unstable temperature, so it is desirable to avoid it.

Further, when the surface temperature of the first mixture in the low temperature kneading step cannot be measured, such as in a closed kneader or an extruder, the surface temperature of the composite material immediately after being kneaded and taken out from the apparatus is used. It can be measured and confirmed to be within the range of the second temperature.

The low temperature kneading step can be, for example, 4 to 20 minutes at the second temperature, further 5 to 12 minutes. By taking a sufficient kneading time at the second temperature, the defibration of the cellulose nanofibers can be carried out more reliably.

The processability of the first mixture is lowered due to the inclusion of cellulose nanofibers, and the temperature of the first mixture becomes even higher than the set temperature of the apparatus due to the heat generated by shearing due to kneading the first mixture. Therefore, in order to maintain the surface temperature of the first mixture in the second temperature range suitable for the low temperature kneading step, if it is an open roll, the temperature of the roll is adjusted so that the temperature of the first mixture does not rise. The temperature must be adjusted so that it cools positively. This also applies to a closed kneader, an extruder, an injection molding machine, etc., and the surface temperature of the first mixture is kept constant in the second temperature range by adjusting the processing set temperature of the device so as to be positively cooled. Time can be maintained. For example, in an extruder, the set temperature of the heating cylinder is set to a temperature higher than the general processing temperature in the vicinity of supplying the material, the other zones are set to a temperature lower than the second temperature, and the resin being processed. The surface temperature of the can be adjusted to be the second temperature.

The composite material obtained by the low-temperature kneading step can be put into a mold and press-processed, or is further processed into pellets using an extruder, for example, and is a known thermoplastic resin. It can be formed into a desired shape by using the processing method of.

Due to the shearing force obtained in the low-temperature kneading process, a high shearing force acts on the thermoplastic resin, and the aggregated cellulose nanofibers are separated from each other so as to be pulled out one by one by the molecules of the thermoplastic resin, and the fibers are defibrated. And dispersed in the thermoplastic resin. This is because the swelling of the fiber material causes the ion cluster forming agent (for example, a metal in the case of a metal salt) bound to the cellulose nanofibers to be ionized, weakening the binding force between the cellulose nanofibers. In particular, since the thermoplastic resin has elasticity and viscosity in the second temperature range, the cellulose nanofibers can be defibrated and dispersed. Then, it is possible to obtain a composite material having excellent dispersibility and dispersion stability of the cellulose nanofibers (the cellulose nanofibers are less likely to reaggregate).

2-4-3. Kneading step using a thermosetting resin A kneading step using a thermosetting resin as a synthetic resin will be described. Here, a two-component mixed type resin using a main agent such as an epoxy resin, a phenol resin, or a urethane resin and a curing agent as the thermosetting resin will be described, but the present invention is not limited thereto.
In the kneading step, the swollen fiber material is mixed with the main agent of the thermosetting resin, kneaded at a kneading temperature in the range of 20 ° C. lower than the softening point of the main agent to 10 ° C. higher than the softening point, and then the curing agent is further added. The step of mixing can be included. If the temperature is near the softening point of the main agent, it is not completely liquid, and according to the test results, it is appropriate at the kneading temperature in the range from 20 ° C lower than the softening point to 10 ° C higher than the softening point. It can be elastic and viscous.
In the case of an epoxy resin, a resin such as bisphenol A type, which is solid at room temperature and has a melting point of 100 ° C. or less, can be used as the main agent. The softening point of the main agent can be determined by the ring-ball method. As the ring-and-ball method, for example, the softening point test method specified in JIS K 7234 can be used. Further, as the curing agent for the epoxy resin, for example, an amine-based or amidoamine-based curing agent that is liquid at room temperature can be used. The fiber material to be mixed with the main agent of the thermosetting resin can be a swollen fiber material.
In the case of phenol resin, for example, novolak resin can be used as the main agent, and hexamethylenetetramine or the like can be used as the curing agent. The softening point of the main agent can be determined by the ring-ball method.
If the main agent is solid at room temperature and has a softening point of 100 ° C. or lower, it is excellent in kneading workability, and in particular, it is easy to process by applying a shearing force at the time of kneading by utilizing the restoring force due to the elasticity of the main agent.

As the kneading step, for example, an open roll, a closed kneader, an extruder and the like can be used. For example, it can be performed by using the open roll 2 as shown in FIGS. 3 to 5.

The basic procedure is the same as for the elastomer, but here, the case of the epoxy resin will be described by taking a bisphenol A type main agent (solid at room temperature and softening point 64 ° C.) as an example. First, the first roll 10 is kneaded at a temperature of 60 to 70 ° C. and the second roll 20 is kneaded at a temperature of 50 to 60 ° C. in FIG. Next, as shown in FIG. 4, the swelling fiber material is gradually added to the main agent and mixed. After that, the thinning step as shown in FIG. 5 can be performed, for example, by setting the roll interval d to 0 mm to 0.5 mm. The surface velocity ratio of the roll is the same as for the elastomer. This is because the cellulose nanofibers are defibrated by utilizing the appropriate elasticity and the appropriate viscosity of the main agent, as in the thinning step using the elastomer.
The reason why the roll temperature is controlled near the softening point of the main agent and the temperature difference between the roll 10 and the roll 20 is about 10 ° C. depends on the processability of the main agent. When such a main agent is used, it easily adheres to the rolls. Therefore, when the two rolls 10 and 20 have the same temperature, they simply separate and adhere to both rolls 10 and 20. Therefore, it is difficult for shearing force to be applied to the main agent, and it is difficult for cellulose nanofibers to be defibrated. Therefore, by providing such a temperature difference, the main agent can be wound around the second roll 20 on the low temperature side, and a desired shearing force can be given to the main agent, and as a result, the cellulose nanofibers can be effectively used. Can be defibrated.
Further, in this kneading step, the metal bonded to the cellulose nanofibers is ionized by the water content of the swollen fiber material. Therefore, the shearing force of kneading is applied in a state where the bonding force between the cellulose nanofibers is weakened by metal ions, and the restoring force due to the elasticity of the main agent in the thinning process is used to widen the interval between the cellulose nanofibers. Is possible, and uniform defibration and dispersion of cellulose nanofibers are performed.
The step of mixing the curing agent is preferably performed after the dehydration step. This is to improve the quality of the processed product.
After kneading the main agent and the cellulose nanofibers, a curing agent (for example, polyamide amine) may be further added and kneaded again under the same method and conditions as in the case of the main agent to uniformly mix the curing agent. it can. By performing the mixing method of the curing agent in the same manner as the kneading method of the main agent, the defibration state of the cellulose nanofibers in the main agent is not deteriorated, and a uniform mixed and dispersed state is maintained. Then, molding (pressing, compression molding, extrusion molding, etc.) is performed, for example, the mixture is allowed to cure at room temperature for 1 day, and then post-baked (80 ° C., 15 hours) to obtain a composite material.

2-5. Dehydration step The dehydration step (S18) is a step of dehydrating the composite material obtained in the kneading step (S16). Further, in the method for producing a composite material using a thermosetting resin, as described above, after the kneading step of the main agent and the cellulose nanofibers, the dehydration step (S18) is performed, and then the curing agent is mixed to obtain the composite material. Is preferable.

In the dehydration step (S18), the composite material can be heated to evaporate the water content. For example, the composite material may be placed in an oven, heated and evacuated inside the oven.

Further, when the water in the fiber material is removed in the middle of the kneading step (S16), it is not necessary to provide the dehydration step (S18). For example, when the kneading step (S16) is performed by an open roll, the roll may be heated after thinning to remove water, and in the case of a closed kneader, a device having a dehydrating function may be used. May be good.

In the case of a composite material using an elastomer, known rubber chemicals such as a vulcanization accelerator, a vulcanizing agent, an antiaging agent, a reinforcing agent, and a coupling agent are further blended and vulcanized by a heating press or the like. It may be molded into a desired shape. Further, in order to obtain the desired physical properties of the rubber product, a known reinforcing agent such as carbon black, silica or carbon nanotube may be added to the elastomer in the kneading step (S16).

2-6. Composite Material The composite material is characterized by not containing cellulose nanofiber agglomerates having a maximum width of 50 μm or more. Cellulose nanofiber agglomerates are scattered in a matrix in which a plurality of cellulose nanofibers are gathered together and aggregated in the form of particles. The maximum width of the cellulose nanofiber agglomerates is measured by observing the particulate agglomerates scattered in the matrix material by observing the fracture surface of the composite material with a scanning electron microscope.

The composite material contains cellulose nanofibers to which elements derived from the ion cluster forming agent in the gel form are bound. Since the composite material has high rigidity, it is considered that the elements derived from the ion cluster forming agent in the composite material exist in close proximity to each other and form ion clusters again. It can be inferred that a reinforcing structure made of fibers can be obtained by forming a three-dimensional pseudo network of cellulose nanofibers that form ion clusters, for example, bound to a metal in a composite material. This is because, in the polymer that does not react with the silane coupling agent, the rigidity of the composite material is not improved even if the composite material is produced in a state where the cellulose nanofibers are defibrated by the silane coupling agent or the like that does not form ion clusters.

In the composite material, the cellulose nanofibers contained in the fiber material are separated into individual fibers by a kneading step against hydrogen bonds between the cellulose nanofibers and dispersed in the composite material.

The composite material can include cellulose nanofibers defibrated from the fiber material and an elastomer or synthetic resin. The fibrous material in the composite material exists as cellulose nanofibers in a defibrated state in a matrix of elastomers or synthetic resins. It is preferable that all of the cellulose nanofibers in the composite material are defibrated, but at least when the tensile fracture surface is observed with an electron microscope, the cellulose nanofiber agglomerates having a maximum width of 50 μm or more are not contained. preferable. This is because if such agglomerates are contained, not only the reinforcing effect as a fiber cannot be obtained, but also a fracture starting point in a tensile test may be obtained.

Examples of the present invention will be described below, but the present invention is not limited thereto.

(A) Preparation of gel-like body (A-1) Preparation of samples of Examples 1 to 4, 9 to 21, 30 to 36 and Reference Examples 1 to 17 Mixing step: Cellulose nanofiber dispersion liquid (Daiichi Kogyo Seiyaku Co., Ltd.) 2% concentration TEMPO oxidized cellulose nanofibers) is diluted with water to prepare a dispersion liquid (solvent is water) having a 1% concentration of cellulose nanofibers, and the types of ion cluster forming agents shown in Tables 1 to 11 are added to the dispersion liquid. Was mixed by stirring with a propeller type stirrer to obtain a gel-like sample.

In Tables 1 to 11,
"Mixing of gel-like body": Mass ratio of cellulose nanofibers and ion cluster forming agent in the gel-like body when the cellulose nanofibers are set to 1.
"Cation filling amount of added cations for 1 g of CNF (mol / g)": Cation filling amount of the ion cluster forming agent for 1 g of cellulose nanofibers in a gel form,
"Raw material": 2% concentration TEMPO oxidized cellulose nanofiber dispersion liquid manufactured by Daiichi Kogyo Seiyaku Co., Ltd. diluted with water, 1% concentration cellulose nanofiber dispersion liquid,
"CNF": TEMPO oxidized cellulose nanofibers (cellulose nanofibers have an average fiber diameter of 3.3 nm and an average aspect ratio of 225),
"Na acrylate": Sodium acrylate manufactured by Asada Chemical Industry Co., Ltd. (metal content 20 to 24%, acrylic acid content 60 to 75%),
"NaCl": Sodium chloride manufactured by Wako Pure Chemical Industries, Ltd. (purity 99%, reagent deer first grade),
"Na methacrylic acid": Sodium methacrylate (metal content 19 to 21%, methacrylic acid content 75 to 80%) manufactured by Asada Chemical Industry Co., Ltd.,
"Na polyacrylate (1)": manufactured by Wako Pure Chemical Industries, Ltd. (degree of polymerization 2700 to 7500) (Examples 13 to 15),
"Na polyacrylate (2)": manufactured by Wako Pure Chemical Industries, Ltd. (degree of polymerization 22,000 to 70,000) (Examples 16 and 17),
"Ca acrylate": Calcium acrylate manufactured by Asada Chemical Industry Co., Ltd. (metal content 18-22%, acrylic acid content 60-75%)
Met.

(A-2) Evaluation Method Using an ARES-G2 rheometer manufactured by TA Instruments, the gel-like bodies of Examples 1 to 4, 9 to 21, 30 to 36 and Reference Examples 1 to 17 have a diameter of 40 mm. It is sandwiched between conical discs with θ = 1 °, and the distance between the conical discs is 0.023 mm, the temperature is 23 ° C to 26 ° C, the speed is 1 radian / sec, and the strain is continuously reciprocated from 1% to 1000%. The viscoelasticity was measured. The conical disk was brought to room temperature (23 ° C. to 26 ° C.) using GEOM40MM1deg and CONE316SST manufactured by TA Instruments. The measurement mode was oscillation and the angular velocity was 1 radian / sec. The measurement results are shown in the column of "Dynamic viscoelasticity of gel-like body" in Tables 1 to 11.

In Tables 1 to 11,
"G'(Pa) at 1% strain" is the average storage elastic modulus (Pa) when the strain is 1% and one round trip is performed.
"G'' (Pa) at 1% strain" is the average loss elastic modulus (Pa) when one round trip is performed with the strain as 1%.
"G'(Pa) at 1000% strain" is the average storage elastic modulus (Pa) when the strain is 1000% and one round trip is performed.
“G'' (Pa) at 1000% strain” was the average storage elastic modulus (Pa) when the strain was set to 1000% and made one round trip.

(A-3) Evaluation In Examples 1 to 4, 9 to 21, 30 to 36 and Reference Examples 1 to 17 , "G'(Pa) at 1% strain" was 60 Pa or more. Further, in Examples 1 to 4, 9 to 21, 30 to 36 and Reference Examples 1 to 17 , the value of "G'(Pa) at 1% strain" is "G'(Pa) at 1% strain". It was found to be larger than the value and solid at 1% strain. In Examples 1 to 4, 9 to 21, 30 to 36 and Reference Examples 1 to 17 , the value of "G'(Pa) at 1000% strain" is higher than the value of "G'(Pa) at 1000% strain". It was found to be small and liquid at 1000% strain.

Further, in Examples 1 to 4, 9 to 21, 30 to 36 and Reference Examples 1 to 17 , "G'(Pa) at 1% strain" was larger than that of the cellulose nanofiber dispersion liquid as a raw material.

(B) Preparation of sample using elastomer (B-1) Preparation of sample of Examples 42 to 51, 53 to 55 and Reference Example 18 Mixing step: Cellulose nanofiber dispersion liquid (2% concentration manufactured by Daiichi Kogyo Seiyaku Co., Ltd.) TEMPO-oxidized cellulose nanofibers) is diluted with water to prepare a dispersion liquid (solvent is water) having a concentration of cellulose nanofibers of 1%, and the dispersion liquid contains ion cluster forming agents (metal salts) of the types shown in Tables 12 to 15. Was mixed by stirring with a propeller type stirrer to obtain a gel-like body.

In Tables 12 to 15,
"CNF": TEMPO oxidized cellulose nanofibers (cellulose nanofibers have an average fiber diameter of 3.3 nm and an average aspect ratio of 225),
"Na methacrylic acid": Sodium methacrylate (metal content 19 to 21%, methacrylic acid content 75 to 80%) manufactured by Asada Chemical Industry Co., Ltd.,
"Zn methacrylic acid": Zinc methacrylate R-20S (metal content 25 to 27%, methacrylic acid content 60 to 64%) manufactured by Asada Chemical Industry Co., Ltd.,
"Zn acrylic acid": Zinc acrylate RSS manufactured by Asada Chemical Industry Co., Ltd. (metal content 27% or more, acrylic acid content 56% or more),
"Ca acrylate": Calcium acrylate (metal content 18-22%, acrylic acid content 60-75%) manufactured by Asada Chemical Industry Co., Ltd.,
"CaCl2": Calcium chloride manufactured by Wako Pure Chemical Industries, Ltd. (special grade reagent, purity 95% or more)
Met.

“Combining of fiber materials” in Tables 12 to 15 is represented by the ratio of each compounding amount when CNF in the swelling fiber material after the swelling step is 1.

Drying step: Water was removed from the gel to obtain a fibrous material. More specifically, the gel-like body was poured into a vat and dried in an oven at 80 ° C. for 24 hours to remove water to obtain a fiber material. In the fiber materials used in Examples 42 to 51, 53 to 55 and Reference Example 18 , precipitation of an ion cluster forming agent could not be visually confirmed on the surface.

Swelling step: The fiber material was swollen with water to obtain a swollen fiber material. More specifically, a fiber material and a predetermined amount of water were placed in a closed glass container and held at 70 ° C. for 1 hour in the closed container for swelling to obtain a swelling fiber material. The amount of water is shown by the ratio of the blending amount when CNF shown in Tables 1 to 5 is 1.

Kneading step: The swollen fiber material was mixed with the elastomers shown in Tables 12 to 15 to obtain a composite material. More specifically, the swelling fiber material is gradually added to the elastomer kneaded using two rolls and kneaded to obtain an intermediate mixture, which is thinly passed (roll temperature 10 ° C. to 30 ° C., roll interval 0. A composite material was obtained by 3 mm and a roll rate ratio of 1.1).

In Tables 12 to 15, "composite material blending" represents the blending amount of the cellulose nanofibers and the metal salt contained in the swelling fiber material in the kneading step in parts by mass (phr). Samples of the composite material were made using 100 g of elastomer.

In Tables 12 to 15,
"HNBR": Zeon Corporation Zet Pole 2010 (Zet Pole is a registered trademark) (median bound acrylonitrile amount 11 (%), median iodine value 7 or less (mg / 100 mg), Mooney viscosity (center value) 85),
"EPDM": JSR EP24 (JSR is a registered trademark) (ENB content 4.5 (%), ethylene content 54 (%), Mooney viscosity 42 (ML (1 + 4) 100 ° C.), oil spread 0 (PHR) )),
Met.

Dehydration step: The composite material obtained in the kneading step was dehydrated. More specifically, it was dried in an oven at 40 ° C. to 90 ° C. for 12 hours to remove the water added in the swelling step from the composite material.

Pressing step: A cross-linking agent, an anti-aging agent, etc. were mixed with the dehydrated composite material in two rolls, and then the composite material was placed in a mold and pressure-molded under vacuum to prepare a sample. In vacuum pressure molding, the mold is heated to 165 ° C., press-molded for 25 minutes while pressurizing (for the mold), and the mold is moved to the cooling press to pressurize (for the mold). While cooling to room temperature, sheet-shaped samples of Examples 42 to 51, 53 to 55 and Reference Example 18 having a thickness of 1 mm were obtained.

(B-2) Preparation of Samples of Comparative Examples 1 to 11 The samples of Comparative Examples 1 to 11 were prepared according to the blending amounts of Tables 6 to 18.

For the samples of Comparative Examples 1 and 11, pure rubber was press-molded in the same manner as in Examples to obtain samples. Comparative Example 1 was "HNBR" and Comparative Example 11 was "EPDM".

The samples of Comparative Examples 2 and 3 were samples to which no metal salt was added. The samples of Comparative Examples 2 and 3 were obtained in the same manner as in Example 42 except that the mixing step was omitted (Comparative Example 2 also included the swelling step) and a resin material containing no metal salt was used.

For the samples of Comparative Examples 4 to 7, a silane coupling agent was used instead of the metal salt, and other samples were obtained in the same manner as in Example 42.

In Tables 17 and 18,
Coupling agent 1 is "3-methacryloxypropyltrimethoxysilane": KBM-503 manufactured by Shin-Etsu Chemical Co., Ltd.,
Coupling agent 2 is "3-glycidoxypropyltrimethoxysilane": KBM-403, manufactured by Shin-Etsu Chemical Co., Ltd.
Coupling agent 3 is "N-2- (aminoethyl) -3-aminopropyltrimethoxysilane": KBM-603 manufactured by Shin-Etsu Chemical Co., Ltd.,
Coupling agent 4 is "3-isocyanatepropyltriethoxysilane": KBE-9007 manufactured by Shin-Etsu Chemical Co., Ltd.,
Coupling agent 5 is "3-mercaptopropylmethyldimethoxysilane": KBM-803 manufactured by Shin-Etsu Chemical Co., Ltd.,
Met.

(C) Evaluation method (C-1) Hardness measurement The rubber hardness (Hs (JIS A)) of the samples of Examples and Comparative Examples was measured based on the JIS K6253 test. The measurement results are shown in Tables 12 to 18.

(C-2) Tensile Test For the samples of Examples and Comparative Examples, a test piece punched into a JIS6 dumbbell shape was used at 23 ± 2 ° C. using a tensile tester of Autograph AG-X manufactured by Shimadzu Corporation. Tensile tests were conducted based on JIS K6251 at a standard line distance of 20 mm and a tensile speed of 500 mm / min, and tensile strength (TS (MPa)), elongation during cutting (Eb (%)) and 50% modulus (σ50 (MPa)). ) Was measured. The measurement results are shown in Tables 12 to 18.

(C-3) Evaluation of workability The samples of Examples and Comparative Examples were evaluated for workability in the above kneading step at the time of trial production with 100 g of HNBR or 100 g of EPDM. Evaluation results (○ indicates that the processing time is within 30 minutes and the roll wrapping property is good, Δ indicates that the processing time exceeds 30 minutes to 1 hour and the roll wrapping property is good, and × indicates that the processing time exceeds 1 hour and the roll wrapping property is poor. Are shown in Tables 12 to 18.

(C-4) Evaluation of defibration and dispersibility The defibability and dispersibility of the composite material were evaluated for the samples of Examples and Comparative Examples. The tensile fracture surface of each sample was observed with a scanning electron microscope. The evaluation results (○ indicates that there was no agglutinate having a maximum width of 50 μm or more, Δ indicates that there was an agglutinate having a maximum width of 50 to 100 μm, and × indicates that there was an agglutinate having a maximum width of 100 μm or more) are shown in Tables 12 to 18. .. Further, the electron micrographs of Examples 43 and 45 are shown in FIGS. 6 and 7 as samples of "○", and the electron micrographs of Comparative Example 3 are shown in FIG. 8 as samples of "x", and the sample of "Δ" is shown. An electron micrograph of Comparative Example 10 is shown in FIG.

(D) Evaluation Results As shown in Tables 12 to 15, the samples of Examples 42 to 51, 53 to 55 and Reference Example 18 used the first metal salt and the second metal salt as the ion cluster forming agent. The evaluation of "workability" and "deflection and dispersibility" in the kneading process was "○". As shown in FIGS. 6 and 7, in the sample in which the evaluation of "defibration and dispersibility" was "○", no agglomerates of the fiber material having a maximum width of 50 μm or more remained, and the cellulose nanofibers were dissolved. It turned out to be fiber.

The samples of Examples 42 to 51 and Reference Example 18 using HNBR shown in Tables 12 to 14 have larger values of "σ50" and "TS" than the pure rubber sample of Comparative Example 1 shown in Table 16. , It was found that there is a reinforcing effect by cellulose nanofibers. Further, the samples of Examples 42 to 46, 49, 50 using HNBR shown in Tables 12 to 14 had a larger “σ50” than Comparative Examples 2 and 3 having the same amount of CNF shown in Table 16, and were metal salts. It was found that the reinforcing effect can be obtained by the cellulose nanofibers defibrated by.

In the samples of Comparative Examples 4 to 10 shown in Tables 17 and 18, various silane coupling agents were used instead of the metal salt, but by blending a predetermined amount of the silane coupling agent, "workability" was achieved. However, the "deflection and dispersibility" did not reach that of the samples of Examples 42 to 51 and Reference Example 18 using the metal salt.

The samples of Examples 53 to 55 using EPDM shown in Table 15 have larger values of "σ50" and "TS" than the samples of Comparative Example 11 shown in Table 18, and have a reinforcing effect by cellulose nanofibers. I understood.

(E) Preparation of Sample Using Thermosetting Resin The sample of Example 56 was prepared as follows. Two epoxy resin main agents (bisphenol A, solid type jER1001 manufactured by Mitsubishi Chemical Corporation (“jER” is a registered trademark), epoxy equivalent 450 to 500, softening point (ring ball method) 64 ° C., specific gravity 1.19, molecular weight 900) After being charged into a roll, a swelling fiber material (CNF1: Ca 0.1 acrylate: water 4.0) prepared by changing the water content of Example 51 to 4.0 was gradually added to the main agent. The temperature of the first roll 10 was set to 60 to 70 ° C., the temperature of the second roll 20 was set to 50 to 60 ° C., and the kneading step was performed in the same manner as in Example 51. Then, the mixture obtained in the kneading step is dried, powdered, put into two rolls again, further kneaded by adding a curing agent jER ST12 (polyamide amine, "jER" is a registered trademark), and pressed under reduced pressure. It was molded and cured at room temperature for 1 day, and then cured (post-baked) at 80 ° C. for 15 hours to obtain a sample of a composite material (epoxy resin 100 phr: CNF 20 phr).

Further, as a sample of Example 57, a sample of a composite material was obtained in the same manner as in Example 56, with the blending amount of Ca acrylate being 0.5.

A sample of Example 58 was prepared as follows. The main agent (novolac resin, softening point (ring ball method) 80 ° C. (estimated)) of phenol resin (manufactured by Asahi Organic Materials Co., Ltd., AV light (registered trademark)) was put into two rolls, and then the same as in Example 45 above. The swollen fiber material (CNF1: Na acrylate: water 2.5) prepared in the above step was gradually added to the main agent, the roll temperature was set to 60 ° C., and the kneading step was carried out in the same manner as in Example 45. It was. Then, a curing agent was added to the mixture obtained in the kneading step, the mixture was further kneaded, and the mixture was further put into an extruder, kneaded, extruded and cured to obtain a sample of a composite material (phenol resin 100 phr: CNF 20 phr).

(F) Evaluation Method The composite material samples of Examples 56 and 57 were subjected to a tensile test in the same manner as in (B-2) above. The result of the tensile test is shown in FIG. 10 as a stress-strain curve.

For the composite material sample of Example 58, the coefficient of linear expansion was measured under the condition of stress of 100 kPa using a thermal analysis rheology device manufactured by SII Nanotechnology Co., Ltd., and the temperature was -10 ° C to 190 ° C. The change in the coefficient of linear expansion in the range is shown in the graph of FIG.

(G) Evaluation As shown in FIG. 10, in the samples of Examples 56 and 57, the stress at the time of 2% strain increased 1.7 times as compared with the sample of the epoxy alone. The composite was reinforced with defibrated cellulose nanofibers.

As shown in FIG. 11, the sample of Example 58 had an average coefficient of linear expansion in the range of 30 ° C. to 120 ° C., which was one-fifth or less of the average coefficient of linear expansion of the sample of phenol alone. It was found that the defibrated cellulose nanofibers suppressed the thermal expansion deformation of the composite material.

(H) Preparation of Sample Using Thermoplastic Resin First Temperature Mixing Step: The thermoplastic resin was put into a tabletop twin-screw kneader MC15 manufactured by Xplore Instruments and melted. Next, the swollen fiber material of Example 46 was put into a tabletop twin-screw kneader and kneaded at a first temperature to obtain a first mixture. The set temperature of the tabletop twin-screw kneader was 165 ° C., the measured resin temperature was 155 ° C., and the kneading time was 3 minutes. The blending amounts (units are "wt%" and "phr") of each example are shown in Table 19.

Low temperature step: The set temperature of the tabletop kneader was lowered to the set temperature (137 ° C.) of the low temperature kneading step.

Low temperature kneading step: The first mixture was kneaded by tabletop biaxial kneading at a set temperature of the tabletop kneader at 137 ° C. (measured resin temperature 130 ° C.). The kneading time was 8 minutes.

Extrusion process: After the set temperature of the tabletop kneader was raised to 165 ° C (measured resin temperature 155 ° C), injection molding was performed with a tabletop twin-screw kneader to obtain a JIS K7161 1BA dumbbell test piece molded from a composite material. ..

In Comparative Example 12, a similar dumbbell test piece was injection-molded with a single thermoplastic resin (LLDPE), and in Comparative Example 13, a cellulose nanofiber dispersion as a raw material not containing Na acrylate was dried instead of the swollen fiber material. A dumbbell test piece was prepared using the powder in the same manner as in Example 59.

In each table,
-"LLDPE": Prime Polymer Ultzex 15150J, melting point 115 ° C,
-"CNF": TEMPO oxidized cellulose nanofibers manufactured by Daiichi Kogyo Seiyaku Co., Ltd. (average fiber diameter of cellulose nanofibers is 3.3 nm, average aspect ratio is 225),
-"Na methacrylic acid": Sodium methacrylate (metal content 19 to 21%, methacrylic acid content 75 to 80%) manufactured by Asada Chemical Industry Co., Ltd.

Since the second temperature in Table 19 must be set within the range of the second temperature of each sample, the second temperature of the low temperature kneading step is set to 130 ° C. (measured resin temperature) as described above. A sample for measuring the second temperature of the composite material was obtained. The second temperature measurement sample of the formulation of each example was subjected to DMA measurement by the same method as in (I) below. From the measurement results, a graph of storage elastic modulus (E') and temperature was created, and by the method described above, for example, in the case of the sample of Example 59, the inflection point temperature T1 (121.5 ° C.) was processed. The temperature development temperature T2 (108 ° C.) and the temperature T4 (132.5 ° C.), which is 1.06 times (T3 ° C. × 1.06) of the flat region development temperature T3 (125 ° C.), were determined. The method for determining the second temperature range of each sample was as described above, and the temperature dependence of the storage elastic modulus measured by DMA in Example 59 was as shown in FIG.

As a result of DMA measurement of the second temperature measurement samples of Examples 59 to 61, the range of the temperature T2 to the temperature T4 of all the samples included the second temperature used in the low temperature kneading step.

(I) Evaluation method (I-1) Tensile test For the samples of Examples 59 to 61 and Comparative Examples 12 and 13, for the JIS K7161 1BA dumbbell test piece, a tensile tester of Autograph AG-X manufactured by Shimadzu Corporation was used. Using, a tensile test was conducted based on JIS K7161 at 23 ± 2 ° C., a standard line distance of 25 mm, and a tensile speed of 25 mm / min. Tensile strength (TS (MPa)), elongation at cutting (Eb (%)), And the yield point tensile stress (σy (MPa)) was measured. The measurement results are shown in Table 19.

(I-2) DMA measurement For the samples of Examples 59 to 61 and Comparative Examples 12 and 13, a dynamic viscoelasticity tester DMS6100 manufactured by SII was used for a test piece cut into a strip shape (30 × 5 × 2 mm). A DMA test (dynamic viscoelasticity test) was performed based on JIS K7244 at a distance between chucks of 10 mm, a measurement temperature of 20 to 200 ° C., a temperature rise pace of 1.5 ° C., a dynamic strain of ± 0.05%, and a frequency of 1 Hz. went. The temperature dependence of the storage elastic modulus of the sample of Example 59 is shown in FIG.

(J) Evaluation The samples of Examples 59 to 61 have tensile strength (TS (MPa)), elongation at cutting (Eb (%)), and yield point tensile stress (σy) as compared with Comparative Examples 12 and 13. (MPa)) was large.

2 ... open roll, 10 ... first roll, 20 ... second roll, 30 ... elastomer, 34 ... bank, 36 ... intermediate mixture, 50 ... composite material, 80 ... swollen fiber material

Claims (12)

A gel-like body consisting only of cellulose nanofibers, an ion cluster forming agent, and water.
The ion cluster forming agent is a monovalent metal salt and
The monovalent metal salt is sodium acrylate, potassium acrylate, sodium methacrylate or potassium methacrylate.
The mass ratio of the monovalent metal salt to the cellulose nanofibers in the gel form is 0.2 to 2 times.
Strain 1 when a gel-like body is sandwiched between conical disks with a diameter of 40 mm, and dynamic viscoelasticity measurements are performed at a conical disk spacing of 0.023 mm, a temperature of 23 ° C to 26 ° C, and a velocity of 1 radian / sec. A gel-like body having a storage elastic modulus in% of 60 Pa to 25000 Pa, and a storage elastic modulus smaller than a loss elastic modulus at a strain of 1000%. A gel-like body consisting only of cellulose nanofibers, an ion cluster forming agent, and water.
The ion cluster forming agent is a divalent metal salt and
The divalent metal salt is an unsaturated acid metal salt monomer, and is
The mass ratio of the divalent metal salt to the cellulose nanofibers in the gel form is 0.03 to 2 times.
Strain 1 when a gel-like body is sandwiched between conical disks with a diameter of 40 mm, and dynamic viscoelasticity measurements are performed at a conical disk spacing of 0.023 mm, a temperature of 23 ° C to 26 ° C, and a velocity of 1 radian / sec. A gel-like body having a storage elastic modulus in% of 60 Pa to 25000 Pa, and a storage elastic modulus smaller than a loss elastic modulus at a strain of 1000%. A gel-like body consisting only of cellulose nanofibers, an ion cluster forming agent, and water.
The cations of the ion cluster forming agent are bound to the cellulose nanofibers and are bonded to the cellulose nanofibers.
The cellulose nanofibers were in a defibrated state and did not precipitate in the water.
The ion cluster forming agent is maleic anhydride or oxalic acid .
The maleic anhydride or the oxalic acid has a mass ratio of 0.01 to 2 times with respect to the cellulose nanofibers.
Strain 1 when a gel-like body is sandwiched between conical disks with a diameter of 40 mm, and dynamic viscoelasticity measurements are performed at a conical disk spacing of 0.023 mm, a temperature of 23 ° C to 26 ° C, and a velocity of 1 radian / sec. A gel-like body having a storage elastic modulus in% of 60 Pa to 25000 Pa, and a storage elastic modulus smaller than a loss elastic modulus at a strain of 1000%. A composite material containing cellulose nanofibers using the gel-like body according to any one of claims 1 to 3 and an elastomer or a synthetic resin. A mixing step of mixing cellulose nanofibers, an ion cluster forming agent, and water to obtain a gel-like substance by binding the cations ionized by the ion cluster forming agent to the cellulose nanofibers is included.
The ion cluster forming agent is a monovalent metal salt such as sodium acrylate, potassium acrylate, sodium methacrylate or potassium methacrylate.
In the gel-like body, the cellulose nanofibers were not precipitated, and the gel-like body had no precipitate.
The mass ratio of the ion cluster forming agent to the cellulose nanofibers in the gel form is 0.01 to 2 times.
When the gel-like body is sandwiched between conical disks having a diameter of 40 mm and the dynamic elastic modulus is measured at a distance of 0.023 mm and a temperature of 23 ° C. to 26 ° C. at 1 radian / sec, the strain is 1%. A method for producing a gel-like body, wherein the storage elastic modulus is 60 Pa to 25000 Pa, and the storage elastic modulus at 1000% strain is smaller than the loss elastic modulus. A mixing step of mixing cellulose nanofibers, an ion cluster forming agent, and water to obtain a gel-like substance by binding the cations ionized by the ion cluster forming agent to the cellulose nanofibers is included.
The ion cluster forming agent is a divalent metal salt and
The divalent metal salt is an unsaturated acid metal salt monomer, and is
In the gel-like body, the cellulose nanofibers were not precipitated and
The mass ratio of the ion cluster forming agent to the cellulose nanofibers in the gel form is 0.01 to 2 times.
When the gel-like body is sandwiched between conical disks having a diameter of 40 mm and the dynamic elastic modulus is measured at a distance of 0.023 mm and a temperature of 23 ° C. to 26 ° C. at 1 radian / sec, the strain is 1%. A method for producing a gel-like body, wherein the storage elastic modulus is 60 Pa to 25000 Pa, and the storage elastic modulus at 1000% strain is smaller than the loss elastic modulus. A mixing step of mixing cellulose nanofibers, an ion cluster forming agent, and water to obtain a gel-like substance by binding the cations ionized by the ion cluster forming agent to the cellulose nanofibers is included.
The ion cluster forming agent is maleic anhydride or oxalic acid.
In the gel-like body, the cellulose nanofibers were not precipitated, and the gel-like body had no precipitate.
The mass ratio of the ion cluster forming agent to the cellulose nanofibers in the gel form is 0.01 to 2 times.
When the gel-like body is sandwiched between conical discs having a diameter of 40 mm and dynamic viscoelasticity is measured at a distance of 0.023 mm and a temperature of 23 ° C. to 26 ° C. and 1 radian / sec, the strain is 1%. Saving
A method for producing a gel-like body, wherein the storage elastic modulus is 60 Pa to 25000 Pa, and the storage elastic modulus at 1000% strain is smaller than the loss elastic modulus. A drying step of removing water from the gel-like body according to any one of claims 5 to 7 to obtain a fiber material, and a drying step.
A swelling step of swelling the fiber material with water to obtain a swelling fiber material,
The kneading step of mixing the swollen fiber material with an elastomer to obtain a composite material is further included.
The kneading step is a method for producing a composite material, which comprises a step of thinning using an open roll having a roll interval of 0.1 mm to 0.5 mm and a roll temperature of 0 ° C. to 50 ° C. A drying step of removing water from the gel-like body according to any one of claims 5 to 7 to obtain a fiber material, and a drying step.
A swelling step of swelling the fiber material with water to obtain a swelling fiber material,
A method for producing a composite material, further comprising a kneading step of mixing the swollen fiber material with a synthetic resin to obtain a composite material. In claim 9 .
The synthetic resin is a thermoplastic resin and
In the kneading step, the processing region development temperature at the storage elastic modulus of the thermoplastic resin composition near the melting point (Tm ° C.) of the thermoplastic resin is 1.06 times the flat region development temperature (T3 ° C.) at the storage elastic modulus. A method for producing a composite material, which comprises a step of kneading at a kneading temperature in the range up to a temperature of (T3 ° C. × 1.06). In claim 9 .
The synthetic resin is a thermosetting resin and is
In the kneading step, the swollen fiber material was mixed with the main agent of the thermosetting resin, and then kneaded at a kneading temperature in the range from a temperature 20 ° C. lower than the softening point of the main agent to a temperature 10 ° C. higher than the softening point. After that, a method for producing a composite material, which comprises a step of further mixing a curing agent. In any one of claims 9 to 11,
A method for producing a composite material, further comprising a dehydration step of dehydrating the composite material obtained in the kneading step.

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