JP2016030809A - Method for producing cellulose nanofiber - Google Patents

Abstract

PROBLEM TO BE SOLVED: To provide a method for producing a cellulose nanofiber containing less impurities at low cost.SOLUTION: There can be produced a cellulose nanofiber containing less impurities at low cost by treating a cellulose-based raw material by adding an oxidant to obtain a cellulose-based raw material oxide, followed by performing mechanical treatment such as ultrasonic treatment, mixer treatment and heater treatment. The addition rate of the oxidant preferably is preferably 10 to 300 mass% based on the dry solid content of the cellulose-based raw material.SELECTED DRAWING: Figure 1

Description

The present invention relates to a method for producing cellulose nanofibers.

Conventionally, as a method for producing cellulose nanofibers, plant fiber pulp and wood pulp from which lignin and hemicellulose have been removed are treated with a refiner and the cell wall is cut several times in the transverse direction, and then kneaded with a biaxial kneader to be strong. There is a method for defibrating the secondary wall, but with this method, a mixture of cellulose fibers having a fiber width of about 10 nm to 5 μm is obtained, and cellulose nanofibers having a uniform fiber width cannot be obtained. .
In addition, there are methods such as a high-pressure homogenizer and a microfluidizer (Non-patent Documents 1 and 2), but there are drawbacks in that the treatment needs to be repeated many times in order to proceed with defibration.
When cellulose raw material is treated in the presence of 2,2,6,6-tetramethyl-1-piperidine-N-oxy radical (hereinafter referred to as TEMPO) and sodium hypochlorite, the surface of cellulose microfibrils It is known that a cellulose nanofiber aqueous dispersion can be obtained by treating a cellulose-based raw material into which this carboxyl group has been introduced with a mixer or the like in water (Non-patent Document 3, Patent Document 1 and 2).
However, since TEMPO is very expensive, there is a problem that the manufacturing cost is high. Moreover, there exists a problem that an N-oxyl compound remains in the oxidized cellulose manufactured by this method and the cellulose nanofiber obtained by defibrating this oxidized cellulose.

JP 2008-001728 A JP 2010-235679 A Enzymatic Hydrology Combined with Mechanical Shearing and High-Pressure Homogenization for Nanoscale Cellulose Fibrils and Strong Gels, 19: Bio6, 19 Cellulose Fabrics for Polymer Reinforcement: ADVANCED ENGINEERING MATERIALS 2004, 6, No. 9,755-761 Saito, T .; , Et al. Cellulose Commun. , 14 (2), 62 (2007)

It is an object to produce cellulose nanofibers by a simple and inexpensive method with few impurities such as chemical substances.

As a result of the study, the inventors of the present invention can obtain cellulose nanofibers that are inexpensive and low in impurities by further performing mechanical treatment such as ultrasonic treatment and mixer treatment after oxidizing the cellulosic raw material with an oxidizing agent. I found.

According to the present invention, cellulose nanofibers can be produced by oxidizing a cellulosic material using only an oxidizing agent and then performing mechanical treatment such as ultrasonic treatment and mixer treatment. Cellulose nanofibers can be produced easily with low impurities and at low cost.

The present invention will be described below. The cellulose-based raw material used in the present invention is not particularly limited, and it is purified by chemical treatment such as kraft or sulfite pulp derived from various woods, powdered cellulose obtained by pulverizing them with a high-pressure homogenizer, a mill or the like, or acid hydrolysis. Microcrystalline cellulose powder can be used. Of these, bleached kraft pulp or bleached sulfite pulp is preferably used.

Hereinafter, kraft pulp will be described as an example, but the present invention is not limited to kraft pulp. The kraft pulp is preferably treated with a beater or the like. Water is added to the kraft pulp to make a slurry. If the dry solid content is too low, the processing efficiency decreases, and if it is too high, it becomes solid and it becomes difficult to uniformly distribute the oxidizing agent. For this reason, the dry solid content is preferably 1% by mass to 30% by mass.

An oxidizing agent is added here and it disperse | distributes uniformly by stirring etc. The oxidizing agent to be used is one selected from hydrogen peroxide, hypohalous acid or a salt thereof, halous acid or a salt thereof, perhalogenic acid or a salt thereof, a perorganic acid, or a persulfate. Among these, when hydrogen peroxide is used, cellulose nanofibers free from impurities derived from the oxidizing agent can be obtained, so hydrogen peroxide is preferable. The addition rate of the oxidizing agent is in the range of 10 to 300% by mass, preferably 30 to 300% by mass, based on the kraft pulp dry solid content. When the addition rate of the oxidizing agent is less than 10% by mass, the oxidation is insufficient, and when it exceeds 300% by mass, the oxidation reaction proceeds and a large amount of water-soluble components are generated. It is preferable to heat and hold after that because the reaction is accelerated. The temperature of the oxidation reaction is preferably 50 to 100 ° C. When the temperature is 50 ° C. or lower, the oxidation reaction takes a long time. 60-90 degreeC is still more preferable. The time for the oxidation reaction depends on the temperature, but is usually 1 to 20 hours.

During the oxidation reaction, an oxidation catalyst such as iron sulfate or copper sulfate may be added. Thereby, the oxidation reaction can be accelerated.

After the oxidation reaction, the oxidized pulp is taken out by solid-liquid separation. Next, the oxidized pulp is suspended in water. When the pulp concentration is too high, the viscosity of the cellulose nanofiber dispersion obtained is too high, and therefore it is preferably 5% by mass or less. A transparent cellulose nanofiber dispersion can be produced by subjecting the oxidized pulp suspension to ultrasonic irradiation or mechanical treatment such as mixer treatment, homogenizer treatment, beater treatment, refiner treatment, and grinder treatment. . This mechanical treatment can be applied with any force as long as the cellulose can be made fine, and is appropriately adjusted depending on the selected mechanical treatment. It is preferable to make the pH in the system weakly alkaline before performing the mechanical treatment. A preferred pH is 8-12. This is thought to be due to the defibration of the pulp being promoted by electrostatic repulsion of the carboxyl groups on the pulp.

The fiber width of the cellulose nanofiber in the present invention is in the range of about 4 nm to 500 nm and a length of about 0.5 μm to several μm.

The cellulose nanofibers obtained in the present invention can be used for papermaking additives, viscosity modifiers, transparent paper, gas barrier paper, resin functionalizing agents and the like.

The present invention will be described in more detail with reference to the following examples, but the present invention is not limited thereto.

(Raw pulp)
Hardwood bleached kraft pulp (LBKP) beaten with a beater (beating degree 300 mL) was used. The pulp concentration was 1.9% by mass.

Example 1
200.8 g of 1.9% by mass pulp liquid was dehydrated by suction filtration (using ADVANTEC, No. 5A filter paper). The weight of the obtained hydrous pulp was 45.8 g. To this, 8.09 g of 35% by mass hydrogen peroxide was added and stirred. The flask was kept at a temperature of 80 ° C. for 10 hours. Thereafter, suction filtration was performed to recover 8.8 g of a water-containing solid. 0.5 g of the water-containing solid was suspended in 25 g of demineralized water, adjusted to pH 10 with sodium hydroxide, and then subjected to ultrasonic treatment. The ultrasonic treatment was performed under the condition of 100% amplification using UP200S manufactured by Hielscher Ultrasound Technology. Since the pH dropped midway, sodium hydroxide was added to adjust the pH to 10. The ultrasonic treatment was performed for a total of 30 minutes to obtain a translucent viscous dispersion. What was observed with SEM (scanning electron microscope, HITACHI Miniscope TM-1000 use) after freeze-drying is shown in FIG. Cellulose nanofibers having a fiber width of several tens of nanometers were confirmed.

(Example 2)
Water was added to 2.5 g of the water-containing solid obtained in Example 1 to make 150 g. Sodium hydroxide was added to adjust the pH to 11. This was mixed. The mixer treatment was performed using a high shear mixer L5M-A manufactured by SILVERSON under the condition of 10000 rpm for 60 minutes. A translucent viscous dispersion was obtained. What was observed with SEM (scanning electron microscope, HITACHI Miniscope TM-1000 use) after freeze-drying is shown in FIG. Cellulose nanofibers having a fiber width of several tens of nanometers were confirmed.

(Example 3)
201.3 g of 1.9% by weight pulp liquid was dehydrated by suction filtration (using ADVANTEC, No. 5A filter paper). The mass of the obtained hydrous pulp was 42.1 g. To this, 4.07 g of 35% by mass hydrogen peroxide was added and stirred. The flask was kept at a temperature of 80 ° C. for 8 hours. Thereafter, suction filtration was performed to recover 18.8 g of a water-containing solid. 1.1 g of a water-containing solid was suspended in 30 g of demineralized water, adjusted to pH 10 with sodium hydroxide, and then subjected to ultrasonic treatment. The ultrasonic treatment was performed under the same conditions as in Example 1. Since the pH dropped midway, sodium hydroxide was added to adjust the pH to 10. The ultrasonic treatment was performed for a total of 30 minutes to obtain a translucent viscous dispersion. What was observed with SEM (scanning electron microscope, HITACHI Miniscope TM-1000 use) after freeze-drying is shown in FIG. Cellulose nanofibers having a fiber width of several tens of nanometers were confirmed.

Example 4
100.0 g of 1.9% by mass pulp liquid was dehydrated by suction filtration (ADVANTEC, No. 5A filter paper used). The mass of the obtained hydrous pulp was 42.9 g. A solution prepared by dissolving 2.17 g of ammonium persulfate in 14 g of demineralized water was added and stirred. The flask was kept at a temperature of 90 ° C. for 4 hours. Thereafter, suction filtration was performed to recover 9.8 g of a water-containing solid. 0.36 g of a water-containing solid was suspended in 25 g of demineralized water, adjusted to pH 11 with sodium hydroxide, and then subjected to ultrasonic treatment. The ultrasonic treatment was performed under the same conditions as in Example 1. Since the pH dropped midway, sodium hydroxide was added to adjust the pH to 10. The sonication was performed for a total of 20 minutes to obtain a translucent viscous dispersion. What was observed with SEM (scanning electron microscope, HITACHI Miniscope TM-1000 use) after freeze-drying is shown in FIG. Cellulose nanofibers having a fiber width of several tens of nanometers were confirmed.

Scanning electron micrograph of the cellulose nanofiber produced in Example 1 (magnification 10,000 times, scale 1 μm) Scanning electron micrograph of the cellulose nanofiber produced in Example 2 (magnification 10,000 times, scale 1 μm) Scanning electron micrograph of the cellulose nanofiber produced in Example 3 (magnification 10,000 times, scale 1 μm) Scanning electron micrograph of cellulose nanofiber produced in Example 4 (magnification 10,000 times, scale 1 μm)

Claims (3)

A method for producing cellulose nanofibers by treating a cellulose-based raw material with an oxidizing agent and then adding a mechanical treatment. The manufacturing method according to claim 1, wherein the addition rate of the oxidizing agent is 10 to 300% by mass with respect to the dry solid content of the cellulosic material. The manufacturing method according to claim 1, wherein the oxidizing agent is hydrogen peroxide.