JP6374824B2 - Fiber composite and method for producing the same - Google Patents

Description

  The present invention relates to a composite of silica or alumina and fiber, and a method for producing the same.

  In general, calcium carbonate is produced by physically pulverizing and classifying natural limestone and weathered shells as raw materials, and "synthetic calcium carbonate" produced by chemically reacting limestone as a raw material ( Light calcium carbonate). As a synthetic method of synthetic calcium carbonate, a carbon dioxide gas method, a lime / soda method, and a soda method are known. Although the lime / soda method and the soda method are partially used for special purposes, they are industrially used. The synthesis of calcium carbonate is generally performed by the carbon dioxide method.

The synthesis of calcium carbonate by the carbon dioxide method is carried out by reacting quick lime and carbon dioxide, and generally, a dehydration step of adding water to quick lime CaO to obtain slaked lime Ca (OH) ₂ , and carbon dioxide CO ₂ into the slaked lime. _And carbonation step of obtaining calcium carbonate CaCO ₃ by blowing ₂ . Today, various techniques for controlling the particle shape and particle diameter of the product calcium carbonate by controlling the reaction conditions of the calcium carbonate synthesis process, particularly the carbonation process, have been proposed.

  Various techniques for depositing calcium carbonate on fibers such as pulp have also been proposed. Patent Document 1 describes a composite in which crystalline calcium carbonate is mechanically bonded onto a fiber. Patent Document 2 describes a technique for producing a composite of pulp and calcium carbonate by precipitating calcium carbonate in a pulp suspension by a carbon dioxide method. Patent Document 3 discloses a method for improving the whiteness and cleanliness of waste paper fibers by adding a large amount of filler to the fibers for paper and paperboard, and sending the slurry of waste paper pulp to a gas-liquid contact device. On the other hand, a technique is described in which an alkali salt slurry is contacted in the direction of flow with pulp in the contact zone, and a suitable reactive gas is fed and mixed with the sedimentary filler to adhere the filler to the fiber surface.

Japanese Patent Laid-Open No. 06-158585 US Pat. No. 5,679,220 US Pat. No. 5,665,205

  The present inventors are to develop a composite of silica or alumina and fiber and a method for producing the same.

  The present inventors have developed a composite of calcium carbonate fine particles and fibers. By synthesizing silica and alumina while jetting a liquid in the presence of the fibers, a composite of silica, alumina and fibers is obtained. Has been found to be able to be produced efficiently, and the present invention has been completed.

That is, the present invention includes, but is not limited to, the following inventions.
(1) A method for producing a fiber composite, comprising synthesizing silica and / or alumina in the presence of fibers while jetting a liquid into a reaction vessel.
(2) The method according to (1), wherein silica and / or alumina is synthesized in the presence of cavitation bubbles.
(3) The method as described in (1) or (2) which synthesize | combines using any one or more of an inorganic acid or aluminum salt, and silicic acid alkali salt.
(4) The method according to any one of (1) to (3), which is synthesized using sulfuric acid or aluminum sulfate and sodium silicate.
(5) The method according to any one of (1) to (4), wherein the average primary particle diameter of silica and / or alumina on the fiber composite is 100 nm or less.
(6) The method according to any one of (1) to (5), wherein the fibers are pulp fibers.
(7) The method according to any one of (1) to (6), comprising circulating the reaction liquid and injecting the reaction liquid into the reaction vessel.

  According to the present invention, a composite of silica, alumina and fibers can be produced by synthesizing silica or alumina in the presence of fibers while jetting a liquid.

FIG. 1 is a schematic view showing a reaction apparatus used in an experimental example of the present invention. FIG. 2 is an electron micrograph of a hardwood pulp fiber (CV-treated pulp) whose surface used in Experiment 1 is microfibrillated (magnification: 200 times). FIG. 3 is an electron micrograph of the cellulose nanofiber used in Experiment 1 (magnification: 200 times). FIG. 4 is an electron micrograph of a composite of calcium carbonate fine particles and fibers (CV-treated pulp) synthesized in Experiment 1 (magnification: left 10,000 times, right 50,000 times). FIG. 5 is an electron micrograph of a composite of calcium carbonate fine particles and fibers (cellulose nanofiber: CNF) synthesized in Experiment 1 (magnification: left 10,000 times, right 50,000 times). FIG. 6 is an electron micrograph of a composite of calcium carbonate fine particles and fibers (TMP) synthesized in Experiment 1 (magnification: 2000 times). FIG. 7 is an electron micrograph of a composite of calcium carbonate fine particles synthesized in Experiment 1 and fibers (CV-treated hemp pulp) (magnification: 2000 times). FIG. 8 is a photograph of Experiment 2-1 (Sample C0) (magnification: 2000 times from the left). FIG. 9 is a photograph of Experiment 2-2 (Sample C1) (magnification: 2000x, 10000x, 50000x from the left). FIG. 109 is a photograph of Experiment 2-3 (Sample C2) (magnification: 50000 times). FIG. 11 is a photograph of Experiment 2-4 (Sample C3) (magnification: 2000x, 10000x, 50000x from the left). FIG. 12 is a photograph of Experiment 2-5 (Sample C4) (magnification: 2000x, 10000x, 50000x from the left). FIG. 13 is a photograph of Experiment 2-6 (Sample C5) (magnification: 2000 ×, 10000 ×, 50000 × from the left). FIG. 14 is a photograph of Experiment 3-1 (Sample C6) (magnification: 2000x, 10000x, 50000x from the left). FIG. 15 is a photograph of Experiment 3-2 (Sample C7) (magnification: 2000x, 10000x, 50000x from the left). FIG. 16 is a photograph of Experiment 3-3 (Sample C8) (magnification: 2000x, 10000x, 50000x from the left). FIG. 17 is a photograph of Experiment 3-4 (Sample C9) (magnification: 2000 ×, 50000 × from the left).

  In the present invention, a composite (fiber composite) of silica or alumina fine particles and fibers is produced by synthesizing silica and / or alumina while jetting a liquid in a solution containing fibers.

Silica and / or Alumina According to the present invention, silica and / or alumina having a small average particle diameter can be complexed with the fiber. The average primary particle diameter of the silica and / or alumina fine particles constituting the composite according to the present invention is less than 1 μm, but the average primary particle diameter may be less than 500 nm, less than 200 nm, or even 100 nm or less. Moreover, the average primary particle diameter of silica and / or alumina fine particles can be 10 nm or more.

  Further, the silica and / or alumina obtained in the present invention may take the form of secondary particles in which fine primary particles are aggregated, and secondary particles can be generated according to the application by an aging step, The agglomerates can also be made fine by grinding. For grinding, ball mill, sand grinder mill, impact mill, high-pressure homogenizer, low-pressure homogenizer, dyno mill, ultrasonic mill, kanda grinder, attritor, stone mill, vibration mill, cutter mill, jet mill, breaker, beater Short shaft extruder, twin screw extruder, ultrasonic stirrer, household juicer mixer and the like.

  The composite obtained by the present invention can be used in various shapes, for example, powders, pellets, molds, aqueous suspensions, pastes, sheets, and other shapes. Moreover, it can also be set as molded objects, such as a mold, particle | grains, and a pellet, with a composite as a main component and other materials. There is no particular limitation on the dryer in the case of drying into a powder, but for example, an air dryer, a band dryer, a spray dryer or the like can be preferably used.

  According to the present invention, since a composite of inorganic fine particles and fibers having a small primary particle size and a narrow particle size distribution can be obtained, it is different from conventional calcium carbonate for papermaking having a particle size of more than 1 μm. Can exhibit its characteristics. Furthermore, unlike the case where inorganic fine particles having a small primary particle diameter are simply blended into the fiber, the composite of the present invention forms a composite with the fiber, so that the inorganic fine particles are not only easily retained on the sheet but also aggregated. And a uniformly dispersed sheet can be obtained. From the result of electron microscope observation, the composite particles of the present invention are not only fixed on the outer surface of the fiber and the inside of the lumen, but also formed on the inside of the microfibril.

  The average particle diameter, shape, and the like of the inorganic fine particles constituting the composite of the present invention can be confirmed by observation with an electron microscope. Furthermore, fine particles having various sizes and shapes can be combined with fibers by adjusting the conditions for synthesizing the inorganic fine particles.

  The composite obtained by the present invention can be used for various applications. Examples include, but are not limited to, paper, fibers, cellulosic composites, filter materials, paints, plastics and other resins, rubber, elastomers, ceramics, glass, tires, building materials (asphalt, asbestos, cement , Board, concrete, brick, tile, plywood, fiberboard, etc.), various carriers (catalyst carrier, pharmaceutical carrier, agricultural chemical carrier, microbial carrier, etc.), adsorbent (impurity removal, deodorization, dehumidification, etc.), wrinkle prevention agent, Clay, polishing material, modifier, repair material, heat insulating material, moisture proof material, water repellent material, water resistant material, light shielding material, sealant, shield material, insect repellent, adhesive, ink, cosmetics, medical materials, paste materials, etc. It can be widely used for any application. Moreover, it can be used for various fillers and coating agents in the above applications.

  Among them, the composite of the present invention is easy to apply to papermaking applications, for example, printing paper, newspaper, inkjet paper, PPC paper, kraft paper, fine paper, coated paper, fine coated paper, wrapping paper, thin paper, and color quality. Paper, cast coated paper, non-carbon paper, label paper, thermal paper, various fancy papers, water-soluble paper, release paper, process paper, base paper for wallpaper, non-combustible paper, flame retardant paper, base paper for laminated board, battery separator, cushion paper , Tracing paper, impregnated paper, ODP paper, building paper, decorative paper, envelope paper, tape paper, heat exchange paper, chemical fiber paper, sterilized paper, water resistant paper, oil resistant paper, heat resistant paper, photocatalytic paper, decorative paper ( Degreased paper), various sanitary paper (toilet paper, tissue paper, wipers, diapers, sanitary products, etc.), tobacco paper, paperboard (liner, core base paper, white paperboard, etc.), paper plate Paper, cup base paper, baking paper, abrasive paper, and synthetic paper.

  Moreover, when using the calcium carbonate composite obtained by this invention, the particle | grains generally called an inorganic filler and an organic filler, and various fibers can be used together. For example, as inorganic filler, calcium carbonate (light calcium carbonate, heavy calcium carbonate), magnesium carbonate, barium carbonate, aluminum hydroxide, calcium hydroxide, magnesium hydroxide, zinc hydroxide, clay (kaolin, calcined kaolin, deramikaolin) ), Talc, zinc oxide, zinc stearate, titanium dioxide, silica made from sodium silicate and mineral acid (white carbon, silica / calcium carbonate composite, silica / titanium dioxide composite), white clay, bentonite, diatomaceous earth, Examples thereof include calcium sulfate, zeolite, an inorganic filler that regenerates and uses the ash obtained from the deinking process, and an inorganic filler that forms a complex with silica or calcium carbonate in the process of regeneration. As the calcium carbonate-silica composite, amorphous silica such as white carbon may be used together with calcium carbonate and / or light calcium carbonate-silica composite. Organic fillers include urea-formalin resin, polystyrene resin, phenol resin, fine hollow particles, acrylamide composites, wood-derived materials (fine fibers, microfibril fibers, powder kenaf), modified insolubilized starch, ungelatinized starch, etc. Is mentioned. Fibers include natural fibers such as cellulose, synthetic fibers that are artificially synthesized from raw materials such as petroleum, regenerated fibers (semi-synthetic fibers) such as rayon and lyocell, and inorganic fibers. Can be used. In addition to the above, the natural fibers include protein fibers such as wool, silk thread and collagen fibers, and complex sugar chain fibers such as chitin / chitosan fibers and alginic acid fibers. Examples of cellulosic materials include pulp fibers (wood pulp and non-wood pulp) and bacterial cellulose. Wood pulp may be produced by pulping wood materials. Wood raw materials include red pine, black pine, todomatsu, spruce, beech pine, larch, fir, tsuga, cedar, hinoki, larch, shirabe, spruce, hiba, douglas fir, hemlock, white fur, spruce, balsam fur, cedar, pine, Coniferous trees such as Merck pine, Radiata pine, etc., and mixed materials thereof, beech, hippopotamus, alder tree, oak, tab, shii, birch, broadleaf tree, poplar, tamo, dragonfly, eucalyptus, mangrove, lawan, acacia, etc. Examples are materials. The method for pulping the wood raw material is not particularly limited, and examples thereof include a pulping method generally used in the paper industry. Wood pulp can be classified by pulping method, for example, chemical pulp digested by methods such as kraft method, sulfite method, soda method, polysulfide method; mechanical pulp obtained by pulping by mechanical force such as refiner, grinder; Semi-chemical pulp obtained by carrying out pulping by mechanical force after pretreatment by; waste paper pulp; deinked pulp and the like. Wood pulp may be unbleached (before bleaching) or bleached (after bleaching). Examples of the non-wood-derived pulp include cotton, hemp, sisal hemp, manila hemp, flax, straw, bamboo, bagasse, kenaf and the like. Wood pulp and non-wood pulp may be either unbeaten or beaten. Synthetic fibers include polyester, polyamide, polyolefin, acrylic fiber, semi-spun fibers include rayon and acetate, and inorganic fibers include glass fiber, carbon fiber, and various metal fibers. About these, these may be used alone or in combination of two or more.

Injecting Liquid In the method for producing a composite according to the present invention, silica and / or alumina is synthesized in the presence of fibers while injecting a liquid.

  In the present invention, cavitation may be generated by ejecting a liquid. In the present invention, cavitation is a physical phenomenon in which bubbles are generated and disappear in a short time due to a pressure difference in a fluid flow, and is also referred to as a cavity phenomenon. Bubbles generated by cavitation (cavitation bubbles) are generated with very small “bubble nuclei” of 100 microns or less existing in the liquid as the nucleus when the pressure in the fluid becomes lower than the saturated vapor pressure for a very short time.

  In the present invention, cavitation bubbles can be generated in the reaction vessel by a known method. For example, cavitation bubbles are generated by jetting fluid at high pressure, cavitation is generated by stirring at high speed in the fluid, cavitation is generated by causing explosion in the fluid, ultrasonic vibration It can be considered that cavitation is generated by a child (vibratory cavitation).

  In particular, in the present invention, since cavitation bubbles are easily generated and controlled, it is preferable to generate cavitation bubbles by ejecting a fluid at a high pressure. In this aspect, by compressing the jet liquid using a pump or the like and jetting it through a nozzle or the like at high speed, cavitation bubbles are generated at the same time as the liquid itself expands due to extremely high shearing force near the nozzle and sudden pressure reduction. . The method using a fluid jet has high generation efficiency of cavitation bubbles, and can generate cavitation bubbles having a stronger collapse impact force. In the present invention, controlled cavitation bubbles are present when synthesizing calcium carbonate, which is clearly different from cavitation bubbles that cause uncontrollable harm that naturally occurs in fluid machinery.

  In the present invention, a reaction solution such as a raw material can be injected as an injection liquid as it is, or some fluid can be injected into the reaction vessel. The fluid in which the liquid jet forms a jet may be any liquid, gas, solid such as powder or pulp, or a mixture thereof as long as it is in a fluid state. Further, if necessary, another fluid such as carbon dioxide can be added to the above fluid as a new fluid. The fluid and the new fluid may be uniformly mixed and ejected, but may be ejected separately.

  The liquid jet is a jet of a fluid or a fluid in which solid particles or gas are dispersed or mixed in the liquid, and refers to a liquid jet containing a slurry or bubbles of pulp or inorganic particles. The gas referred to here may include bubbles due to cavitation.

  Since cavitation occurs when a liquid is accelerated and the local pressure is lower than the vapor pressure of the liquid, flow rate and pressure are particularly important. From this, the basic dimensionless number representing the cavitation state, the cavitation number σ is defined as the following formula 1 (Yoji Kato's new edition of cavitation, basics and recent progress, Kashiwa Shoten 1999).

  Here, a large number of cavitations indicates that the flow field is in a state where cavitation is difficult to occur. In particular, when cavitation is generated through a nozzle or orifice pipe such as a cavitation jet, the cavitation number σ is expressed by the following equation (2) from the nozzle upstream pressure p1, the nozzle downstream pressure p2, and the saturated water vapor pressure pv of the sample water. In the cavitation jet, the pressure difference between p1, p2, and pv is large and p1 >> p2 >> pv. Therefore, the cavitation number σ can be further approximated as in the following Expression 2. (H. Soyama, J. Soc. Mat. Sci. Japan, 47 (4), 381, 1998).

  The cavitation condition in the present invention is such that the above-described cavitation number σ is preferably 0.001 or more and 0.5 or less, preferably 0.003 or more and 0.2 or less, and 0.01 or more and 0.1 or less. It is particularly preferred that If the cavitation number σ is less than 0.001, the effect is small because the pressure difference with the surroundings when the cavitation bubbles collapse is low, and if it is greater than 0.5, the flow pressure difference is low and cavitation occurs. It becomes difficult to occur.

  In addition, when the injection liquid is injected through the nozzle or the orifice tube to generate cavitation, the pressure of the injection liquid (upstream pressure) is more preferably 2 MPa or more and 15 MPa or less. When the upstream pressure is less than 0.01 MPa, it is difficult to produce a pressure difference with the downstream pressure, and the effect is small. On the other hand, when the pressure is higher than 30 MPa, a special pump and a pressure vessel are required, and energy consumption increases, which is disadvantageous in terms of cost. On the other hand, the pressure in the container (downstream pressure) is preferably 0.005 MPa to 0.9 MPa in static pressure. Moreover, the ratio of the pressure in the container and the pressure of the jet liquid is preferably in the range of 0.001 to 0.5.

  The jet velocity of the jet liquid is desirably in the range of 1 m / second to 200 m / second, and preferably in the range of 20 m / second to 100 m / second. When the jet velocity is less than 1 m / sec, the effect is weak because the pressure drop is low and cavitation hardly occurs. On the other hand, when it is higher than 200 m / sec, a high pressure is required and a special device is required, which is disadvantageous in terms of cost.

  What is necessary is just to generate the cavitation generation | occurrence | production place in this invention in the reaction container which synthesize | combines microparticles | fine-particles. Moreover, although it is possible to process by one pass, it can also circulate as many times as necessary. Furthermore, it can be processed in parallel or in permutation using a plurality of generating means.

  The liquid injection for generating cavitation may be performed in a container open to the atmosphere, but is preferably performed in a pressure container in order to control cavitation.

  In the present invention, the pH of the reaction solution is basic at the start of the reaction when an alkali silicate salt is used as the starting material, and acidic when an inorganic acid or aluminum salt is used as the starting material. It changes to neutral as it progresses. Therefore, the reaction can be controlled by monitoring the pH of the reaction solution.

  In the present invention, by increasing the jetting pressure of the liquid, the flow velocity of the jetting liquid is increased, and accordingly, the pressure is lowered, and stronger cavitation can be generated. Further, by pressurizing the pressure in the reaction vessel, the pressure in the region where the cavitation bubbles collapse is increased and the pressure difference between the bubbles and the surroundings increases, so that the bubbles collapse violently and the impact force can be increased. Moreover, when introducing gas, such as a carbon dioxide gas, melt | dissolution and dispersion | distribution of gas can be accelerated | stimulated. The reaction temperature is preferably 0 ° C. or higher and 90 ° C. or lower, and particularly preferably 10 ° C. or higher and 60 ° C. or lower. In general, the impact force is considered to be the maximum at the midpoint between the melting point and the boiling point. Therefore, in the case of an aqueous solution, a temperature around 50 ° C. is suitable, but even below that temperature is affected by the vapor pressure. Therefore, a high effect can be obtained within the above range.

  In the present invention, the energy necessary for generating cavitation can be reduced by adding a surfactant. As the surfactant to be used, known or novel surfactants, for example, nonionic surfactants such as fatty acid salts, higher alkyl sulfates, alkylbenzene sulfonates, higher alcohols, alkylphenols, alkylene oxide adducts such as fatty acids, etc. , Anionic surfactants, cationic surfactants, amphoteric surfactants and the like. These may consist of a single component or a mixture of two or more components. The addition amount may be an amount necessary for reducing the surface tension of the jet liquid and / or the liquid to be jetted.

Reaction Conditions In the present invention, alumina and / or silica may be synthesized in the presence of fibers while jetting a liquid. When one or more of an inorganic acid or an aluminum salt is used as a starting material for the reaction, it is synthesized by adding an alkali silicate salt. It can be synthesized by using alkali silicate as a starting material and adding one or more of inorganic acid or aluminum salt, but it is produced when inorganic acid and / or aluminum salt is used as starting material. The fixing of the product to the fiber is good. It does not specifically limit as an inorganic acid, For example, a sulfuric acid, hydrochloric acid, nitric acid etc. can be used. Among these, sulfuric acid is particularly preferable from the viewpoint of cost and handling. Examples of the aluminum salt include a sulfate band, aluminum chloride, polyaluminum chloride, alum, potash alum and the like, and among them, a sulfate band can be preferably used. Examples of the alkali silicate include sodium silicate and potassium silicate, but sodium silicate is preferable because it is easily available. The molar ratio of silicic acid and alkali may be any, but what is generally circulated as No. 3 silicic acid has a molar ratio of about SiO ₂ : Na ₂ O = 3 to 3.4: 1. Can be used. In the present invention, water is used for the preparation of a suspension and the like, and as this water, normal tap water, industrial water, ground water, well water, etc. can be used, ion-exchanged water, distilled water, Ultrapure water, industrial wastewater, and water obtained in the carbonation step can be suitably used.

  In the present invention, the reaction solution can be circulated for use. By circulating the reaction solution in this manner, the reaction efficiency is increased and it becomes easy to obtain the complex efficiently.

  When producing the composite of the present invention, various known auxiliaries can be further added. For example, chelating agents can be added to the carbonation reaction, specifically, polyhydroxycarboxylic acids such as citric acid, malic acid and tartaric acid, dicarboxylic acids such as oxalic acid, sugar acids such as gluconic acid, Aminopolycarboxylic acids such as acetic acid and ethylenediaminetetraacetic acid and their alkali metal salts, alkali metal salts of polyphosphoric acid such as hexametaphosphoric acid and tripolyphosphoric acid, amino acids such as glutamic acid and aspartic acid and their alkali metal salts, acetylacetone, acetoacetic acid Examples thereof include ketones such as methyl and allyl acetoacetate, saccharides such as sucrose, and polyols such as sorbitol. In addition, as surface treatment agents, saturated fatty acids such as palmitic acid and stearic acid, unsaturated fatty acids such as oleic acid and linoleic acid, resin acids such as alicyclic carboxylic acid and abietic acid, salts, esters and ethers thereof, alcohols Activators, sorbitan fatty acid esters, amide or amine surfactants, polyoxyalkylene alkyl ethers, polyoxyethylene nonyl phenyl ether, sodium alpha olefin sulfonate, long chain alkyl amino acids, amine oxides, alkyl amines, fourth A quaternary ammonium salt, aminocarboxylic acid, phosphonic acid, polyvalent carboxylic acid, condensed phosphoric acid and the like can be added. Moreover, a dispersing agent can also be used as needed. Examples of the dispersant include sodium polyacrylate, sucrose fatty acid ester, glycerin fatty acid ester, acrylic acid-maleic acid copolymer ammonium salt, methacrylic acid-naphthoxypolyethylene glycol acrylate copolymer, methacrylic acid-polyethylene glycol. Examples include monomethacrylate copolymer ammonium salts and polyethylene glycol monoacrylate. These can be used alone or in combination. The timing of addition is not particularly limited, and such an additive can be added in an amount of preferably 0.001 to 20%, more preferably 0.1 to 10%.

  In the present invention, the reaction conditions are not particularly limited, and can be appropriately set according to the application. For example, the temperature of the reaction can be 10 to 100 ° C., and preferably 20 to 90 ° C. The reaction temperature can be controlled by a temperature controller, and if the temperature is low, the reaction efficiency decreases and the cost increases. On the other hand, if the temperature exceeds 90 ° C., coarse particles tend to increase.

  In the present invention, the reaction can be a batch reaction or a continuous reaction. In general, it is preferable to perform a batch reaction step for the convenience of discharging the residue after the reaction. The scale of the reaction is not particularly limited, but the reaction may be performed on a scale of 100 L or less, or may be performed on a scale of more than 100 L. The size of the reaction vessel can be, for example, about 10 L to 100 L, or about 100 L to 1000 L.

  Furthermore, the reaction can be controlled by monitoring the pH of the reaction suspension. Depending on the pH profile of the reaction solution, for example, around pH 4-11, preferably pH 5-10, more preferably pH 6-9. The reaction can be carried out until the value is reached.

  Furthermore, the reaction can be controlled by the reaction time, and specifically, it can be controlled by adjusting the time during which the reaction product stays in the reaction vessel. In addition, in this invention, reaction can also be controlled by stirring the reaction liquid of a reaction tank or making it a multistage reaction.

  In the present invention, since the complex which is a reaction product is obtained as a suspension, it can be stored in a storage tank or subjected to processing such as concentration, dehydration, pulverization, classification, aging, and dispersion as necessary. Can do. These can be performed by known processes, and may be appropriately determined in consideration of the application and energy efficiency. For example, the concentration / dehydration treatment is performed using a centrifugal dehydrator, a sedimentation concentrator, or the like. Examples of the centrifugal dehydrator include a decanter and a screw decanter. When using a filter or a dehydrator, the type is not particularly limited and a general one can be used. For example, a pressure-type dehydrator such as a filter press, a drum filter, a belt press, a tube press, A calcium carbonate cake can be obtained by suitably using a vacuum drum dehydrator such as an Oliver filter. For grinding, ball mill, sand grinder mill, impact mill, high-pressure homogenizer, low-pressure homogenizer, dyno mill, ultrasonic mill, kanda grinder, attritor, stone mill, vibration mill, cutter mill, jet mill, breaker, beater Short shaft extruder, twin screw extruder, ultrasonic stirrer, household juicer mixer and the like. Examples of the classification method include a sieve such as a mesh, an outward type or inward type slit or round hole screen, a vibrating screen, a heavy foreign matter cleaner, a lightweight foreign matter cleaner, a reverse cleaner, a sieving tester, and the like. Examples of the dispersion method include a high-speed disperser and a low-speed kneader.

  The composite obtained by the present invention can be blended in a filler or pigment in a suspension state without being completely dehydrated, but can also be dried to form a powder. Although there is no restriction | limiting in particular also about the dryer in this case, For example, an airflow dryer, a band dryer, a spray dryer etc. can be used conveniently.

  The composite obtained by the present invention can be modified by a known method. For example, in an embodiment, the surface can be hydrophobized to improve miscibility with a resin or the like.

Fiber In the present invention, inorganic fine particles and fibers are combined. The fiber constituting the composite is not particularly limited. For example, natural fibers such as cellulose, synthetic fibers artificially synthesized from raw materials such as petroleum, semi-synthetic fibers such as rayon, and inorganic fibers are also included. Etc. can be used without limitation. In addition to the above, the natural fibers include protein fibers such as wool, silk thread and collagen fibers, and complex sugar chain fibers such as chitin / chitosan fibers and alginic acid fibers. Examples of cellulosic materials include pulp fibers (wood pulp and non-wood pulp) and bacterial cellulose. Wood pulp may be produced by pulping wood materials. Wood raw materials include red pine, black pine, todomatsu, spruce, beech pine, larch, fir, tsuga, cedar, hinoki, larch, shirabe, spruce, hiba, douglas fir, hemlock, white fur, spruce, balsam fur, cedar, pine, Coniferous trees such as Merck pine, Radiata pine, etc., and mixed materials thereof, beech, hippopotamus, alder tree, oak, tab, shii, birch, broadleaf tree, poplar, tamo, dragonfly, eucalyptus, mangrove, lawan, acacia, etc. Examples are materials.

  The method for pulping the wood raw material is not particularly limited, and examples thereof include a pulping method generally used in the paper industry. Wood pulp can be classified by pulping method, for example, chemical pulp digested by methods such as kraft method, sulfite method, soda method, polysulfide method; mechanical pulp obtained by pulping by mechanical force such as refiner, grinder; Semi-chemical pulp obtained by carrying out pulping by mechanical force after pretreatment by; waste paper pulp; deinked pulp and the like. Wood pulp may be unbleached (before bleaching) or bleached (after bleaching).

  Examples of the non-wood-derived pulp include cotton, hemp, sisal hemp, manila hemp, flax, straw, bamboo, bagasse, kenaf and the like.

  The pulp fiber may be either unbeaten or beaten, and may be selected according to the physical properties of the composite sheet, but it is preferable to beaten. Thereby, improvement of sheet strength and promotion of calcium carbonate fixation can be expected.

  Synthetic fibers include polyester, polyamide, polyolefin, acrylic fiber, semi-spun fibers include rayon and acetate, and inorganic fibers include glass fiber, carbon fiber, and various metal fibers.

  The fibers shown above may be used alone or in combination. Especially, it is preferable that wood pulp is included or the combination of wood pulp, non-wood pulp, and / or synthetic fiber is included, and it is more preferable that it is only wood pulp.

  In a preferred embodiment, the fibers constituting the composite of the present invention are pulp fibers. Further, for example, a fibrous substance recovered from the wastewater of a paper mill may be supplied to the carbonation reaction of the present invention. By supplying such a substance to the reaction vessel, various composite particles can be synthesized, and fibrous particles and the like can be synthesized in terms of shape.

  In the present invention, in addition to the fibers, a substance that is not directly involved in the generation of inorganic particles but is taken into the inorganic particles to generate composite particles can be used. In the present invention, fibers such as pulp fibers are used. In addition, these substances are further incorporated by synthesizing silica or alumina in a solution containing inorganic particles, organic particles, polymers and the like. Composite particles can be produced.

Silica and / or alumina In the present invention, fine particles of silica and / or alumina are synthesized while jetting a liquid in a solution containing fibers. The synthesis method can be performed by a known method. In the present invention, not only fine particles of silica and alumina but also other inorganic particles can be combined with the fiber.

  In a preferred embodiment, in the present invention, not only silica and alumina but also calcium carbonate fine particles can be complexed with fibers. In this case, the average primary particle diameter of the calcium carbonate fine particles constituting the composite is less than 1 μm, but the calcium carbonate having an average primary particle diameter of less than 500 nm, the calcium carbonate having an average primary particle diameter of less than 200 nm, or even 100 nm or less. Calcium carbonate can be used. The average primary particle diameter of the calcium carbonate fine particles can be 10 nm or more.

  In addition, the calcium carbonate obtained in the present invention may take the form of secondary particles in which fine primary particles are aggregated, and can generate secondary particles according to the application by an aging process, and aggregate by pulverization. A lump can be made fine. For grinding, ball mill, sand grinder mill, impact mill, high-pressure homogenizer, low-pressure homogenizer, dyno mill, ultrasonic mill, kanda grinder, attritor, stone mill, vibration mill, cutter mill, jet mill, breaker, beater Short shaft extruder, twin screw extruder, ultrasonic stirrer, household juicer mixer and the like.

  The average particle diameter, shape, and the like of calcium carbonate constituting the composite of the present invention can be confirmed by observation with an electron microscope. Furthermore, by adjusting the conditions for synthesizing calcium carbonate, calcium carbonate fine particles having various sizes and shapes can be combined with fibers.

  The method for synthesizing calcium carbonate is not particularly limited. For example, calcium carbonate can be synthesized by a carbon dioxide method, a soluble salt reaction method, a lime / soda method, a soda method, or the like. In a preferred embodiment, calcium carbonate is synthesized by a carbon dioxide method. Is synthesized.

In general, when calcium carbonate is produced by the carbon dioxide method, lime is used as a calcium source, water is added to quick lime CaO to obtain slaked lime Ca (OH) ₂ , and carbon dioxide CO ₂ is added to the slaked lime. Calcium carbonate is synthesized by the carbonation step of blowing calcium to obtain calcium carbonate CaCO ₃ . At this time, a slaked lime suspension prepared by adding water to quick lime may be passed through a screen to remove low-solubility lime particles contained in the suspension. Further, slaked lime may be directly used as a calcium source. In the present invention, when calcium carbonate is synthesized by the carbon dioxide method, the carbonation reaction may be performed in the presence of cavitation bubbles.

  Generally, a gas blowing type carbonator and a mechanical stirring type carbonator are known as reaction vessels (carbonation reactor: carbonator) for producing calcium carbonate by the carbon dioxide method. In a gas blowing type carbonator, carbon dioxide gas is blown into a carbonation reaction tank containing slaked lime suspension (lime milk) to react slaked lime with carbon dioxide gas. Is difficult to control uniformly and finely, and is limited in terms of reaction efficiency. On the other hand, in the mechanical agitator type carbonator, a stirrer is provided inside the carbonator, and carbon dioxide gas is introduced near the stirrer to make the carbon dioxide gas fine bubbles, improving the reaction efficiency between slaked lime and carbon dioxide gas. (“Cement, Gypsum, Lime Handbook”, Gihodo Publishing, 1995, 495 pages).

  However, when stirring with a stirrer provided inside the carbonation reaction tank, such as a mechanical stirring type carbonator, if the concentration of the reaction liquid is high or the carbonation reaction proceeds, the resistance of the reaction liquid is large and it is difficult to sufficiently stir Therefore, it is difficult to precisely control the carbonation reaction, and in order to perform sufficient stirring, a considerable load is applied to the stirrer, which may be disadvantageous in terms of energy. In addition, the gas inlet is located at the bottom of the carbonator, and the blades of the stirrer are installed near the bottom of the carbonator to improve the stirring. Lime screen residue with low solubility is always settled at the bottom due to fast sedimentation, which may block the gas blowing port or break the balance of the stirrer. Furthermore, in the conventional method, in addition to the carbonator, a stirrer and equipment for introducing carbon dioxide into the carbonator are necessary, and the equipment is also expensive. In the mechanical stirring type carbonator, the carbon dioxide gas supplied near the stirrer is refined by the stirrer to improve the reaction efficiency between slaked lime and carbon dioxide gas. However, when the concentration of the reaction liquid is high, the carbon dioxide gas is sufficient. In view of the carbonation reaction, it is sometimes difficult to accurately control the form of calcium carbonate produced. In the present invention, by synthesizing calcium carbonate in the presence of cavitation bubbles, it becomes possible to efficiently advance the carbonation reaction and produce uniform calcium carbonate fine particles. In particular, by using jet cavitation, sufficient stirring can be performed without a mechanical stirrer such as a blade. In the present invention, conventionally known reaction vessels can be used, and of course, the above-described gas blowing type carbonator and mechanical stirring type carbonator can be used without any problem. You may combine jet cavitation using.

  When synthesizing calcium carbonate by the carbon dioxide method, the solid content concentration of the aqueous suspension of slaked lime is preferably 0.1 to 40% by weight, more preferably 0.5 to 30% by weight, and further preferably 1 to 20%. It is about wt%. If the solid content concentration is low, the reaction efficiency is low and the production cost is high. If the solid content concentration is too high, the fluidity is deteriorated and the reaction efficiency is lowered. In the present invention, since calcium carbonate is synthesized in the presence of cavitation bubbles, the reaction solution and carbon dioxide can be suitably mixed even when a suspension (slurry) having a high solid content is used.

  As an aqueous suspension containing slaked lime, those generally used for calcium carbonate synthesis can be used, for example, prepared by mixing slaked lime with water, or slaked (digested) quick lime (calcium oxide) with water. Can be prepared. There are no particular restrictions on the conditions for soaking, but for example, the concentration of CaO is 0.1% by weight or more, preferably 1% by weight or more, and the temperature is 20 to 100 ° C., preferably 30 to 100 ° C. . Moreover, the average residence time in the soaking reaction tank (slaker) is not particularly limited, but can be, for example, 5 minutes to 5 hours, and preferably within 2 hours. Of course, the slaker may be batch or continuous. In the present invention, the carbonation reaction tank (carbonator) and the decontamination reaction tank (slaker) may be separated, and one reaction tank may be used as the carbonation reaction tank and the decontamination reaction tank. Good.

  In the present invention, a gas containing carbon dioxide (carbon dioxide gas) is blown into the reaction vessel and mixed with the reaction solution. According to the present invention, carbon dioxide can be supplied to the reaction solution without a gas supply device such as a fan or blower, and the carbonation can be efficiently performed because carbon dioxide is refined by cavitation bubbles. Can do.

  In the present invention, the carbon dioxide concentration of the gas containing carbon dioxide is not particularly limited, but a higher carbon dioxide concentration is preferable. Moreover, there is no restriction | limiting in the quantity of the carbon dioxide gas introduce | transduced into an injector, Although it can select suitably, For example, it is preferable to use the carbon dioxide gas of the flow rate of 100-10000L / hour per kg of slaked lime.

  The gas containing carbon dioxide of the present invention may be substantially pure carbon dioxide gas or a mixture with other gases. For example, in addition to carbon dioxide gas, a gas containing an inert gas such as air or nitrogen can be used as a gas containing carbon dioxide. Further, as the gas containing carbon dioxide, in addition to carbon dioxide gas (carbon dioxide gas), exhaust gas discharged from an incinerator of a paper mill, a coal boiler, a heavy oil boiler, or the like can be suitably used as the carbon dioxide-containing gas. In addition, a carbonation reaction can also be performed using carbon dioxide generated from the lime baking step.

Using the complex according to the molding invention conjugates, as appropriate, it is also possible to produce a molded product (the body). For example, when the composite obtained by the present invention is made into a sheet, a high ash content sheet can be easily obtained. Examples of the paper machine (paper machine) used for sheet production include a long paper machine, a round paper machine, a gap former, a hybrid former, a multilayer paper machine, and a known paper machine that combines the paper making methods of these devices. It is done. The press linear pressure in the paper machine and the calendar linear pressure in the case where the calendar process is performed later can be determined within a range that does not hinder the operability and the performance of the composite sheet. In addition, starch, various polymers, pigments, and mixtures thereof may be applied to the formed sheet by impregnation or coating.

  When forming into a sheet, a wet and / or dry paper strength agent (paper strength enhancer) can be added. Thereby, the intensity | strength of a composite sheet can be improved. Examples of paper strength agents include urea formaldehyde resin, melamine formaldehyde resin, polyamide, polyamine, epichlorohydrin resin, vegetable gum, latex, polyethyleneimine, glyoxal, gum, mannogalactan polyethyleneimine, polyacrylamide resin, polyvinylamine. And a resin such as polyvinyl alcohol; a composite polymer or copolymer composed of two or more selected from the above resins; starch and processed starch; carboxymethylcellulose, guar gum, urea resin, and the like. The addition amount of the paper strength agent is not particularly limited.

  Moreover, in order to promote the fixing of the filler to the fiber or to improve the yield of the filler or fiber, a high molecular weight polymer or an inorganic substance can be added. For example, polyethyleneimine and modified polyethyleneimines containing tertiary and / or quaternary ammonium groups, polyalkylenimines, dicyandiamide polymers, polyamines, polyamine / epichlorohydrin polymers, and dialkyldiallyl quaternary ammonium monomers, dialkyls as coagulants Cations such as aminoalkyl acrylate, dialkylaminoalkyl methacrylate, dialkylaminoalkyl acrylamide and polymers of acrylamide and dialkylaminoalkyl methacrylamide, polymers of monoamines and epihalohydrin, polymers with polyvinylamine and vinylamine moieties, and mixtures thereof In addition to the functional polymer, a polymer obtained by copolymerizing an anionic group such as a carboxyl group or a sulfone group in the polymer molecule. Onritchi of zwitterionic polymer, and a mixture of cationic polymer and an anionic or zwitterionic polymers may be used. As a retention agent, a cationic, anionic, or amphoteric polyacrylamide-based material can be used. In addition to these, a retention system called a so-called dual polymer that uses at least one kind of cation or anionic polymer can also be applied, and at least one kind of anionic bentonite, colloidal silica, polysilicic acid, It is a multi-component yield system that uses inorganic fine particles such as polysilicic acid or polysilicate microgels and their modified aluminum products, or one or more organic fine particles having a particle size of 100 μm or less, called so-called micropolymers obtained by crosslinking polymerization of acrylamide. Also good. In particular, when the polyacrylamide material used alone or in combination has a weight average molecular weight of 2 million daltons or more by the intrinsic viscosity method, a good yield can be obtained, preferably 5 million daltons or more, more preferably Can obtain a very high yield in the case of the above-mentioned acrylamide-based material of 10 million daltons or more and less than 30 million daltons. The form of the polyacrylamide-based material may be an emulsion type or a solution type. The specific composition is not particularly limited as long as the substance contains an acrylamide monomer unit as a structural unit. For example, a copolymer of quaternary ammonium salt of acrylate ester and acrylamide, or acrylamide And a quaternized ammonium salt after copolymerization of acrylate and acrylate. The cationic charge density of the cationic polyacrylamide material is not particularly limited.

  In addition, according to the purpose, inorganic particles such as drainage improver, internal sizing agent, pH adjuster, antifoaming agent, pitch control agent, slime control agent, bulking agent, calcium carbonate, kaolin, talc, silica (so-called Etc.). The amount of each additive used is not particularly limited.

  It is also possible to use a molding method other than sheeting, for example, a method of pouring raw materials into a mold and drawing it by suction dehydration and drying as called a pulp mold, or spreading and drying on the surface of a molded product such as resin or metal Thereafter, molded articles having various shapes can be obtained by a method of peeling from the substrate. Further, it can be molded into a plastic like by mixing a resin, or it can be shaped like a ceramic by adding a mineral such as silica or alumina and firing. In the blending / drying / molding described above, only one type of composite can be used, or two or more types of composites can be mixed and used. When two or more types of composites are used, those obtained by mixing them in advance can be used, or those obtained by blending, drying and molding each can be mixed later.

  Further, various organic substances such as polymers and various inorganic substances such as pigments may be added to the composite molded article later.

  The present invention will be described more specifically with reference to experimental examples below, but the present invention is not limited to such experimental examples. Unless otherwise specified in the present specification, concentrations and parts are based on weight, and numerical ranges are described as including the end points.

Experiment 1 (reference example): Synthesis of calcium carbonate fine particle and fiber composite < Synthesis of calcium carbonate / fiber composite>
An aqueous suspension containing calcium hydroxide (slaked lime: Ca (OH) ₂ , Wako Pure Chemicals, 2% by weight) and fiber (0.5%) was prepared. 9.5 L of this aqueous suspension was put into a 45 L cavitation apparatus, carbon dioxide gas was blown into the reaction vessel, and a composite of calcium carbonate fine particles and fibers was synthesized by the carbon dioxide gas method. The reaction temperature was about 25 ° C., carbon dioxide was supplied from a commercial liquefied gas, the amount of carbon dioxide blown was 12 L / min, and the reaction was stopped when the pH of the reaction solution reached about 7 (before the reaction). PH is about 12.8).

  In the synthesis of the complex, cavitation bubbles were generated in the reaction vessel by circulating the reaction solution and injecting it into the reaction vessel as shown in FIG. Specifically, the reaction solution was injected at high pressure through a nozzle (nozzle diameter: 1.5 mm) to generate cavitation bubbles. The jet velocity was about 70 m / s, and the inlet pressure (upstream pressure) was The outlet pressure (downstream pressure) was 7 MPa and 0.3 MPa.

In this experiment, the following four types were used as fibers for forming a complex with calcium carbonate fine particles. Details of each fiber are shown below.
(1) Hardwood pulp fiber whose surface is microfibrillated (CV-treated pulp)
(2) Cellulose nanofiber (TEMPO oxidized pulp)
(3) Thermomechanical pulp (TMP)
(4) Hemp pulp fiber whose surface is microfibrillated (Hardwood pulp fiber whose surface is microfibrillated) LBKP having a Canadian standard freeness (CSF) of about 400 mL is disaggregated in water to obtain a pulp suspension (concentration: 0.5%) was prepared. Cavitation bubbles were generated by putting the pulp suspension in a reaction vessel and introducing a jet into the reaction vessel. Cavitation bubbles were generated by spraying the reaction solution at high pressure through a nozzle (nozzle diameter: 1.5 mm). The jet velocity was about 70 m / s, the inlet pressure (upstream pressure) was 7 MPa, and the outlet pressure (downstream pressure) was 0.3 MPa. This cavitation treatment was performed for about 1 hour until the CSF of LBKP was less than 100 mL.

  An electron micrograph of the pulp thus obtained is shown in FIG. 2, and the microfibrils on the fiber surface were peeled in layers, and the average fiber length measured with a fiber tester (Lorentzen & Wettre) was 0.69 mm. .

  (Cellulose nanofiber) NBKP oxidized with an N-oxyl compound was beaten with a Niagara beater for about 15 minutes until the CSF was less than 100 mL to obtain cellulose nanofiber. The average fiber length of the obtained fiber was 0.84 mm (an electron micrograph is shown in FIG. 3).

(Thermomechanical pulp) Thermomechanical pulp (TMP) beaten to about 400 mL by CSF
(Hemp pulp fiber whose surface was microfibrillated) Similarly to the above-mentioned hardwood pulp fiber, CV treatment was performed on hemp pulp until the CSF was lower than 100 mL to obtain hemp pulp whose surface was microfibrillated.

<Evaluation of complex>
Electron micrographs of the obtained composite are shown in FIGS. FIG. 4 is an electron micrograph of a composite of hardwood pulp fiber and calcium carbonate fine particles treated by cavitation. As apparent from FIG. 4, in this composite, a large number of fine calcium carbonate particles were deposited on the fiber surface, and the primary particle diameter of calcium carbonate was about 40 to 100 nm (average: about 80 nm). In particular, many calcium carbonate fine particles were generated in the fibril part of the pulp fiber.

  FIG. 5 is an electron micrograph of a composite of TEMPO oxidized pulp and calcium carbonate fine particles. As is clear from FIG. 5, even in this composite, a large number of calcium carbonate fine particles were deposited on the fiber surface, and the primary particle size of the calcium carbonate fine particles was about 40 to 100 nm (average: about 80 nm). Even in this composite, many calcium carbonate fine particles were generated in the fibril portion of the pulp fiber.

  Further, even when TMP was used (FIG. 6) and hemp pulp was used (FIG. 7), it was observed that calcium carbonate having a primary particle size of 40 to 80 nm covered the fiber surface and self-fixed. .

  When the reaction solution containing the composite was observed by suction filtration with a filter paper, the composite of the fiber and calcium carbonate fine particles existed stably, and the calcium carbonate fine particles did not fall off from the fiber.

  Moreover, when the ash content of these composites was measured, it was 81 to 82% by weight of the composites, which was consistent with the theoretical value of 82% by weight calculated from the raw material (pulp / calcium hydroxide) charge ratio. Here, the ash content of the composite was calculated from the ratio between the weight of the remaining ash and the original solid content after the composite was heated at 525 ° C. for about 2 hours (JIS P 8251: 2003).

Experiment 2 (Reference Example): Synthesis of Composite of Calcium Carbonate Fine Particles and Fiber A composite was synthesized under various conditions, and an electron micrograph was taken.
(Experiment 2-1: Sample C0, FIG. 8)
A composite was synthesized in the same manner as in Experiment 1 except that hardwood bleached kraft pulp (LBKP, CSF: 460 mL, without cavitation treatment) was used as the fiber. As a result of observation by an electron microscope, calcium carbonate having a primary particle size of 40 to 100 nm was self-fixed on the fiber surface. The ash content of the composite was 83%, which was almost equivalent to the theoretical value (84%) calculated from the charged amount.
(Experiment 2-2: Sample C1, FIG. 9)
Synthesis was performed in the same manner as in Experiment 1, except that 1250 g of LBKP (CSF: 460 mL, not subjected to cavitation treatment) and 1250 g of calcium hydroxide were used as the fibers and the total amount of the aqueous suspension of Ca (OH) ₂ was 100 L. . As a result of observation by an electron microscope, it was observed that calcium carbonate having a primary particle size of 60 to 90 nm covered the fiber surface and was self-fixed. As a result of measuring the ash content, it was 56%, which was almost equal to the theoretical value (58%).
(Experiment 2-3: Sample C2, FIG. 10)
8300 g of LBKP / NBKP mixed pulp as a fiber (weight ratio: 8/2, CSF: 50 ml, without cavitation treatment), 8300 g of calcium hydroxide, 415 L of the total amount of aqueous suspension of Ca (OH) ₂ A composite was synthesized in the same manner as in Experiment 1 except that the flow rate of carbon dioxide was 40 L / min and the reaction start temperature was 16 ° C.

As a result of observation by an electron microscope, it was observed that calcium carbonate having a primary particle size of 60 to 90 nm covered the fiber surface and was self-fixed. As a result of measuring the ash content, it was 56%, which was almost equal to the theoretical value (58%).
(Experiment 2-4: Sample C3, FIG. 11)
A composite was synthesized in the same manner as in Experiment 1 except that the calcium hydroxide charge concentration was 0.74% and the carbon dioxide flow rate was 5 L / min.

As a result of observation by an electron microscope, it was observed that calcium carbonate having a primary particle size of 30 to 80 nm covered the fiber surface and was self-fixed. As a result of measuring the ash content, all were 48%, which was almost equal to the theoretical value (50%).
(Experiment 2-5: Sample C4, FIG. 12)
The cavitation nozzle used was synthesized in the same manner as Sample C3, except that the cavitation nozzle used was changed to two fluids (the calcium hydroxide suspension was mixed with carbon dioxide gas immediately before being discharged from the nozzle).

As a result of observation by an electron microscope, it was observed that calcium carbonate having a primary particle size of 30 to 80 nm covered the fiber surface and was self-fixed. As a result of measuring the ash content, all were 48%, which was almost equal to the theoretical value (50%).
(Experiment 2-6: Sample C5, FIG. 13)
It was synthesized in the same manner as Sample C4, except that the raw material used was quick lime. As a result of observation by an electron microscope, it was observed that calcium carbonate having a primary particle size of 40 to 80 nm covered the fiber surface and was self-fixed.

Experiment 3: Synthesis of Composite of Silica and / or Alumina Fine Particles and Fiber A fiber composite was synthesized under the following conditions, and an electron micrograph was taken.
(Experiment 3-1: Sample C6, FIG. 14)
280 g of calcium hydroxide and 70 g of pulp (LBKP, CSF: about 460 mL) were mixed, and tap water was added to make 14 L. After adding 400 g of sodium silicate (about 30% in terms of SiO ₂ ), the mixture was put into a reaction vessel. Subsequent procedures and reaction conditions were the same as in Experiment 1, but the reaction was stopped when the pH reached about 6.7.

As a result of observation with an electron microscope, it was observed that particles having a primary particle diameter of about 20 to 50 nm, which seems to be silica, were deposited on the surface of calcium carbonate. Moreover, when the abundance ratio of silica (silicon dioxide, SiO ₂ ) and calcium carbonate (CaCO ₃ ) was analyzed by fluorescent X-ray, it was confirmed that both silica and calcium carbonate were present (Table 2).
(Experiment 3-2: Sample C7, FIG. 15)
In Experiment 3-1, after the pH reached about 6.7, an aqueous aluminum sulfate solution (0.8% in terms of alumina) was further added and reacted until the pH reached 6.2.

As a result of observation with an electron microscope, it was observed that particles having a primary particle diameter of about 20 to 50 nm, which seems to be silica, were deposited on the surface of calcium carbonate.
(Experiment 3-3: Sample C8, FIG. 16)
29 kg of sodium silicate (approximately 30% in terms of SiO ₂ ) is added to 1 kg of the composite slurry of sample C0 (concentration 2.9%) and stirred with a laboratory mixer, and 41 g of sulfuric acid aqueous solution (10%) is added to form the composite. Synthesized.

As a result of observation with an electron microscope, it was confirmed that silica having the same size as the primary particle form of calcium carbonate having a size of about 80 nm was present on the fiber (LBKP). When the abundance ratio of silica (SiO ₂ ) and calcium carbonate (CaCO ₃ ) was analyzed by fluorescent X-ray, it was confirmed that both silica and calcium carbonate were present (Table 2).
(Experiment 3-4: Sample C9, FIG. 17)
60 g of pulp (LBKP / NBKP = 8/2, CSF: about 50 mL) and an aqueous sulfuric acid band solution (alumina conversion 0.8%, 58 mL) were mixed, and tap water was added to 12 L. Subsequent procedures and reaction conditions were the same as in Experiment 1, but instead of blowing carbon dioxide, 380 g of sodium silicate (about 30% in terms of SiO ₂ ) was dropped in the middle of the reaction, and the pH was about 9.1. At this stage, the reaction was stopped.

  As a result of observation with an electron microscope, it was confirmed that a composite crystal of alumina and silica having a primary particle shape of 20 to 50 nm was precipitated on the pulp fiber (LBKP).

Claims (7)

  A method for producing a fiber composite, comprising synthesizing silica and / or alumina in the presence of fibers while injecting a liquid into a reaction vessel.   The method according to claim 1, wherein silica and / or alumina is synthesized in the presence of cavitation bubbles.   The method of Claim 1 or 2 synthesize | combining using any one or more of an inorganic acid or aluminum salt, and an alkali silicate salt.   The method according to claim 1, which is synthesized using sulfuric acid or aluminum sulfate and sodium silicate.   The method in any one of Claims 1-4 whose average primary particle diameter of the silica and / or alumina on a fiber composite is 100 nm or less.   The method according to claim 1, wherein the fibers are pulp fibers.   The method in any one of Claims 1-6 including circulating the reaction liquid and injecting in a reaction container.