JP6169926B2 - Water-absorbing resin with excellent water-absorbing resin pulverization method and salt resistance - Google Patents

Description

  The present invention relates to a method for finely pulverizing a water absorbent resin and a water absorbent resin excellent in salt resistance.

  In recent years, water-absorbing resins have been put into practical use not only for sanitary materials such as paper diapers, but also for water-stopping materials, anti-condensation materials, freshness-retaining materials, solvent dehydrating agents, etc. is there. Further, a technique has been proposed in which a water-swelling rubber is prepared by blending a rubber with a water-absorbing agent and this is used as a water-stopping material.

  In patent document 1 and patent document 2, it has high water absorption with respect to cement water and calcium chloride water, has a gel shape retention property and gel strength of water-absorbing gel, and has excellent water absorption when kneaded rubber, plastic, cement and the like. As a water-absorbing agent that exhibits its function, a sulfonic acid group-containing acrylamide monomer having a specific neutralization rate, an acrylamide monomer, and an unneutralized (meth) acrylic acid monomer in the presence of a crosslinking agent A water-absorbing agent comprising polymer cross-linked copolymer particles copolymerized with is disclosed.

  In Patent Document 3 and Patent Document 4, 2-acrylamido-2-methylpropanesulfonic acid and its alkali metal are used as a water-absorbing agent having a high absorption capacity for water containing a large amount of electrolyte (for example, seawater or salt water). And at least one monomer selected from the group consisting of salts and ammonium salts, and acrylic acid and its alkali metal salts and ammonium salts, methacrylic acid and its alkali metal salts and ammonium salts, acrylamide and vinylpyrrolidone A water absorbing agent comprising at least one monomer selected from the group and a crosslinking agent having at least two functional groups is disclosed. Furthermore, Patent Document 4 discloses a salt-resistant water-swelling material that is dispersed in a base material made of the water-absorbing resin, a thermoplastic resin, and / or rubber.

  Patent Documents 5 to 7 disclose water-swellable emulsions.

  Patent Document 8 discloses that water-absorbent resin fine powder (for example, 150 μm passing material) is unsuitable for sanitary materials such as diapers and is therefore reduced, removed, or recycled in the water-absorbent resin manufacturing process.

  Patent Document 9 and Patent Document 10 disclose the use of fine powder (300 μm or less) of a water-absorbent resin, which is inappropriate for sanitary material applications, for cat sand, building materials, and the like.

  Patent Documents 12 and 13 disclose a method of pulverizing a water absorbent resin.

  However, there is still room for improvement such as dispersibility in water-swellable rubber and water absorption performance in the presence of high-concentration metal ions such as seawater.

JP 2007-009108 A Japanese Patent Publication No. 2006-233061 Japanese Patent Laid-Open No. 03-176065 JP 03-157455 A Special table 2011-506703 JP 2000-234003 JP 09-140826 A Special table 2009-522389 Japanese Patent Application Laid-Open No. 2004-2145 Special table 2005-501960 International Publication No. 2009/059956 Pamphlet International Publication No. 2011/034146 Pamphlet International Publication No. 2011/034147 Pamphlet

To improve water dispersibility in water-swellable rubber and water absorption performance in the presence of high-concentration metal ions such as seawater, provide a method for producing a water-absorbing agent with a uniform fine particle size and a water-absorbing agent with excellent salt resistance The purpose is to do.

  As a result of intensive studies by the present inventors in order to solve the above-mentioned problems, when a specific pulverizing means is used, a water-absorbing agent pulverized into a uniform fine particle size without impairing the water-absorbing performance can be obtained. ) And the water absorption rate, and the salt resistance was remarkably improved with a specific composition, and the present invention was completed.

  That is, a method of pulverizing a water absorbent resin using a dry pulverizer, wherein the water absorbent resin is pulverized using at least two types of different impact pulverizers. It is a manufacturing method.

  Moreover, in order to measure the water absorption performance of a fine water absorbent resin powder having a volume average particle diameter of 150 μm or less, which has been difficult to evaluate in the past, a measurement method using a measurement mixed sample mixed with an inorganic compound powder is also used. I found it.

  The pulverization method of the present invention does not impair the water absorption performance, and the salt resistance is remarkably improved if the water absorption agent has a specific composition.

[1] Definition of terms (a) "Water absorbent resin"
In the present specification, the “water-absorbing resin” means a water-swellable, water-insoluble polymer gelling agent, and has the following physical properties. That is, the water absorption capacity (CRC) under no pressure is essentially 5 g / g or more, preferably 10 to 100 g / g, more preferably 20 to 80 g / g, and water-soluble components (Extractables) are essential. 0 to 50% by weight, preferably 0 to 30% by weight, more preferably 0 to 20% by weight, and particularly preferably 0 to 10% by weight.

  The total amount (100%) of the water-absorbent resin is not limited to the polymer, and may contain additives (described later) within the range that maintains the above performance. That is, even a water absorbent resin composition containing a water absorbent resin and an additive is generically referred to as a water absorbent resin in the present invention. When the water absorbent resin is a water absorbent resin composition, the content of the water absorbent resin is preferably 70 to 99% by weight, more preferably 80 to 99% by weight, and still more preferably. Is 90 to 99% by weight. As other components other than the water absorbent resin, water is preferable from the viewpoint of water absorption speed and impact resistance of the powder (particles), and if necessary, additives described later are included.

  The water-absorbing resin used in the present invention is preferably a polycarboxylic acid-based water-absorbing resin or a polysulfonic acid-based water-absorbing resin, and further, the following water-absorbing resin A or water-absorbing resin B, or water-absorbing resin It is more preferable that it is a water absorbent resin containing the resin A and the water absorbent resin B.

(A-1) Water absorbent resin A
Water-absorbing property containing a polyacrylic acid (salt) -based crosslinked polymer having a neutralization rate of 50 mol% or more (however, the repeating unit other than acrylic acid is 0 to 50 mol% of the whole, and further the following range). resin.

(A-2) Water absorbent resin B
Monomer containing 20 to 90 mol% of a sulfonic acid group-containing monomer (particularly a sulfonic acid group-containing monomer acrylamide monomer) and a salt thereof, and 80 to 10 mol% of any one or more of acrylic acid and acrylate ( (B) “EDANA” and “ERT” (b) “EDANA” and “ERT” containing 80% by mass or more of a cross-linked polymer obtained by copolymerizing other monomers (0 to 50 mol% in all monomers)
“EDANA” is an abbreviation for European Disposables and Nonwovens Associations, and “ERT” is an abbreviation for a method for measuring water-absorbent resin (ERT / EDANA Recommended Test Method) of European standards (almost world standards). In this specification, unless otherwise specified, the physical properties of the water-absorbent resin are measured based on the ERT original (known document: revised in 2002).

(C) Fine particle size absorption ratio (FGA)
The fine particle size absorptivity of the present invention was measured in accordance with the EDANA method (ERT442.2-02 (2002)), with the measurement method partially changed to (c-1) below.

(C-1) Artificial seawater absorption rate (ASW-FSC; non-pressure absorption rate)
The artificial seawater absorption capacity (sometimes referred to as Artificial Sea Water Free Swell Capacity, ASW-FSC) of the water-absorbent resin of the present invention is a fine particle size absorption capacity using artificial seawater. Artificial seawater has the following composition.

<Artificial seawater composition>
The added reagent and each added amount with respect to 1 kg of ion-exchanged water are as follows.

MgCl ₂ · 6H ₂ O: 9.474 (g)
CaCl ₂ · 2H ₂ O: 1.326 (g)
Na ₂ SO ₄ : 3.505 (g)
KCl: 0.597 (g)
NaCl: 20.747 (g)
(D) Artificial seawater absorption rate (ASW-Vortex)
The absorption rate of the water-absorbent resin of the present invention (Artificial Sea Water Vortex Time, sometimes referred to as ASW-Vortex) is measured according to the JIS method (JIS K 7224 “Test method for water absorption rate of superabsorbent resin”). did. In the present invention, the measurement solution was changed to artificial seawater having the above composition.

(E) Water content The water content of the water-absorbent resin of the present invention was measured according to the EDANA method (ERT430.2-02). In the present invention, the drying temperature was changed to 180 ° C. for measurement.

(F) Particle size The particle size of the water-absorbent resin of the present invention was measured with a light scattering particle size measuring device (LA-920, manufactured by HORIBA).

(G) "Water absorbent"
In the present specification, the “water-absorbing agent” means an aqueous liquid gelling agent mainly composed of a water-absorbing resin. The aqueous liquid is not limited to water, but may be urine, blood, feces, waste liquid, moisture or steam, ice, a mixture of water and an organic solvent and / or an inorganic solvent, rainwater, groundwater, seawater, etc. Well, it is not particularly limited if water is included. Among these, seawater and salt, especially groundwater containing a divalent salt are more preferable. The content of the water-absorbing resin according to the present invention is preferably 70 to 99% by weight, more preferably 80 to 99% by weight, still more preferably 90 to 99% by weight, based on the entire weight of the water-absorbing material. It is. As other components other than the water absorbent resin, water is preferable from the viewpoint of water absorption speed and impact resistance of the powder (particles), and if necessary, additives described later are included.

(H) “Others”
In this specification, “X to Y” indicating a range means “X or more and Y or less”. Further, “t (ton)” which is a unit of weight means “Metric ton” (metric ton).

  Further, the physical properties of the water-absorbent resin are measured under the conditions of temperature: 20 to 25 ° C. (simply referred to as “room temperature” or “room temperature”) and relative humidity: 40 to 50% unless otherwise specified. It is implemented in.

[2] Method for Producing Water Absorbent Resin (1) Polymerization Step This step is a step in which a monomer aqueous solution is polymerized to obtain a hydrogel crosslinked polymer.

(A) Monomer (excluding crosslinking agent)
(A) -1. Water absorbent resin A
The water-absorbent resin A according to the present invention preferably uses acrylic acid (salt) and acrylic acid (salt) as main components as the raw material (monomer).

  The monomer is preferably at least partially neutralized, and from the viewpoint of water absorption performance of the water-absorbent resin, a monovalent salt selected from alkali metal salts, ammonium salts, and amine salts is preferable. Is more preferable, a salt selected from a sodium salt, a lithium salt, and a potassium salt is more preferable, and a sodium salt is particularly preferable.

  Examples of the basic substance for preparing the monomer salt include alkali metal hydroxides such as sodium hydroxide, potassium hydroxide and lithium hydroxide, sodium carbonate (hydrogen), potassium carbonate (hydrogen) and the like. Basic carbonates such as carbonic acid (hydrogen) salts are preferred, and sodium hydroxide is particularly preferred.

  The neutralization rate of the monomer is preferably 10 to 100 mol%, more preferably 30 to 100 mol%, still more preferably 40 to 100 mol%, and particularly preferably 50 to 100 mol%. Moreover, it does not restrict | limit especially as temperature at the time of neutralization (neutralization temperature), Preferably it is 10-100 degreeC, More preferably, it determines suitably at 30-90 degreeC. In addition, preferable conditions for the neutralization treatment are exemplified in EP 574260, and the conditions described in the publication can also be applied to the present invention.

  The above-described monomers (including the following crosslinking agent) are usually polymerized in an aqueous solution, and the solid content concentration after neutralization is usually 10 to 90% by mass, preferably 20 to 80% by mass, and more preferably 30. It is -70 mass%, Most preferably, it is 35-60 mass%.

  In order to improve various physical properties of the water-absorbing resin obtained, water-soluble resins such as starch, polyacrylic acid (salt), polyethyleneimine, water-absorbing resins, and various foaming agents (carbonates, azo Compounds, bubbles, etc.), surfactants, and additives described below may be added as optional components. As the addition amount, the water-soluble resin or water-absorbent resin is preferably 0 to 50% by mass, more preferably 0 to 20% by mass, and particularly preferably 0 to 10% by mass with respect to the total amount of monomers. 0 to 3% by mass is most preferable. Moreover, 0-5 mass% is preferable and, as for the said foaming agent, surfactant, etc., 0-1 mass% is more preferable.

  Moreover, when adding a chelating agent, hydroxycarboxylic acid, and a reducing inorganic salt to monomer aqueous solution, the addition amount is preferable 10-5000 mass ppm with respect to a water absorbing resin, and 10-1000 mass ppm is more. Preferably, 50 to 1000 ppm by mass is more preferable, and 100 to 1000 ppm by mass is particularly preferable.

  In particular, by adding a chelating agent, the resulting water-absorbent resin can be improved in color stability (color stability when stored for a long time under high temperature and high humidity conditions) and urine resistance (preventing gel degradation). be able to. Examples of the chelating agent include those exemplified in US Pat. No. 6,599,989 and International Publication No. 2008/090961, and among them, aminocarboxylic acid metal chelating agents and polyvalent phosphorus Acid compounds are preferred.

  When acrylic acid (salt) is used as a main component, it may contain a hydrophilic or hydrophobic unsaturated monomer other than acrylic acid (salt) (hereinafter also referred to as “other monomer”). . Examples of such other monomers include methacrylic acid, (anhydrous) maleic acid, (meth) acryloxyalkanesulfonic acid, N-vinyl-2-pyrrolidone, N-vinylacetamide, (meth) acrylamide, N -Isopropyl (meth) acrylamide, N, N-dimethyl (meth) acrylamide, 2-hydroxyethyl (meth) acrylate, methoxypolyethylene glycol (meth) acrylate, polyethylene glycol (meth) acrylate, stearyl acrylate and their salts It is done. Although the addition amount of this monomer changes with desired performance, Preferably it is 50 mass% or less with respect to the mass of all the monomers, More preferably, it is 0-20 mass%.

When acrylic acid (salt) is the main component, the total amount is 50 to 100 mol%, further 70 to 100 mol%, particularly 90 to 100 mol% in all monomers (excluding the crosslinking agent). means.
(A) -2. Water absorbent resin B
The water-absorbent resin B according to the present invention is preferably composed of a sulfonic acid group-containing monomer (particularly a sulfonic acid group-containing monomer acrylamide monomer) and acrylic acid (salt) as a raw material (monomer). Copolymers, typically 2-acrylamido-2-methylpropanesulfonic acid (salt) (hereinafter referred to as AMPS (salt)) and acrylic acid (salt), or 2-sulfoethyl-methacrylate (salt) (Hereinafter referred to as SEMS (salt)) and acrylamide and acrylic acid (salt), or 2-sulfoethyl-methacrylate (salt) (hereinafter referred to as SEMS (salt)) are used as main components. (The total of both is 50 to 100 mol%, and other monomers are 0 to 50 mol%, more preferably 0 to 30 mol%, and 0 to 10 mol% in all monomers) The acid group of the monomer is It is preferable that at least a part is neutralized, and from the viewpoint of water absorption performance of the water-absorbent resin, monovalent salts selected from alkali metal salts, ammonium salts, and amine salts are preferable, alkali metal salts are more preferable, sodium salts Further, a salt selected from lithium salt and potassium salt is more preferable, and sodium salt is particularly preferable.

  Examples of the basic substance for preparing the monomer salt include alkali metal hydroxides such as sodium hydroxide, potassium hydroxide and lithium hydroxide, sodium carbonate (hydrogen), potassium carbonate (hydrogen) and the like. Basic carbonates such as carbonic acid (hydrogen) salts are preferred, and sodium hydroxide is particularly preferred.

  The neutralization rate of the monomer (or the polymer when post-neutralized after polymerization) is preferably 10 to 100 mol%, more preferably 30 to 100 mol%, still more preferably 40 to 100 mol%, Most preferably, it is 50-100 mol%. Moreover, it does not restrict | limit especially as temperature at the time of neutralization (neutralization temperature), Preferably it is 10-100 degreeC, More preferably, it determines suitably at 30-90 degreeC. In addition, preferable conditions for the neutralization treatment are exemplified in EP 574260, and the conditions described in the publication can also be applied to the present invention.

  The above-described monomers (including the following crosslinking agent) are usually polymerized in an aqueous solution, and the solid content concentration after neutralization is usually 10 to 90% by mass, preferably 20 to 80% by mass, and more preferably 30. It is -70 mass%, Most preferably, it is 35-60 mass%.

  In order to improve various physical properties of the water-absorbing resin obtained, water-soluble resins such as starch, polyacrylic acid (salt), polyethyleneimine, water-absorbing resins, and various foaming agents (carbonates, azo Compounds, bubbles, etc.), surfactants, and additives described below may be added as optional components. As the addition amount, the water-soluble resin or water-absorbent resin is preferably 0 to 50% by mass, more preferably 0 to 20% by mass, and particularly preferably 0 to 10% by mass with respect to the total amount of monomers. 0 to 3% by mass is most preferable. Moreover, 0-5 mass% is preferable and, as for the said foaming agent, surfactant, etc., 0-1 mass% is more preferable.

  Moreover, when adding a chelating agent, hydroxycarboxylic acid, and a reducing inorganic salt to monomer aqueous solution, the addition amount is preferable 10-5000 mass ppm with respect to a water absorbing resin, and 10-1000 mass ppm is more. Preferably, 50 to 1000 ppm by mass is more preferable, and 100 to 1000 ppm by mass is particularly preferable.

  In particular, by adding a chelating agent, the resulting water-absorbent resin can be improved in color stability (color stability when stored for a long time under high temperature and high humidity conditions) and urine resistance (preventing gel degradation). be able to. Examples of the chelating agent include those exemplified in US Pat. No. 6,599,989 and International Publication No. 2008/090961, and among them, aminocarboxylic acid metal chelating agents and polyvalent phosphorus Acid compounds are preferred.

  Further, when AMPS and acrylic acid (salt) are used as main components, a hydrophilic or hydrophobic unsaturated monomer other than acrylic acid (salt) (hereinafter also referred to as “other monomer”) is included. Also good. Examples of such other monomers include methacrylic acid, (anhydrous) maleic acid, (meth) acryloxyalkanesulfonic acid, N-vinyl-2-pyrrolidone, N-vinylacetamide, (meth) acrylamide, N -Isopropyl (meth) acrylamide, N, N-dimethyl (meth) acrylamide, 2-hydroxyethyl (meth) acrylate, methoxypolyethylene glycol (meth) acrylate, polyethylene glycol (meth) acrylate, stearyl acrylate and their salts It is done. Although the addition amount of this monomer changes with desired performance, Preferably it is 50 mass% or less with respect to the mass of all the monomers, More preferably, it is 0-20 mass%.

  It should be noted that, when AMPS and acrylic acid (salt) are the main components, the total amount is 50 to 100 mol%, more preferably 70 to 100 mol%, particularly 90 to 100 mol in all monomers (excluding the crosslinking agent). Means%. In addition, AMPS and acrylic acid (salt) may be used alone, and when used in combination, the molar ratio of AMPS: acrylic acid (salt) is 0 to 100: 100 to 0, preferably 10 to 90:10. 90, more preferably 20-80: 80-20.

(B) Cross-linking agent (internal cross-linking agent)
In the present invention, it is particularly preferable to use a crosslinking agent (hereinafter sometimes referred to as “internal crosslinking agent”) from the viewpoint of water absorption characteristics. The amount of the internal crosslinking agent used is preferably from 0.001 to 5 mol%, more preferably from 0.005 to 2 mol%, more preferably from 0.01 to 1 with respect to all monomers excluding the crosslinking agent, from the viewpoint of physical properties. The mol% is more preferable, and 0.03 to 0.5 mol% is particularly preferable.

  Examples of the internal crosslinking agent that can be used include a polymerizable crosslinking agent with acrylic acid, a reactive crosslinking agent with a carboxyl group, and a crosslinking agent having both of them. Specifically, N, N′-methylenebisacrylamide, (poly) ethylene glycol di (meth) acrylate, (polyoxyethylene) trimethylolpropane tri (meth) acrylate, poly (meth) are used as the polymerizable crosslinking agent. Examples include compounds having at least two polymerizable double bonds in the molecule, such as allyloxyalkanes. Examples of reactive cross-linking agents include covalent cross-linking agents such as polyglycidyl ether (ethylene glycol diglycidyl ether, etc.), polyhydric alcohols (propanediol, glycerin, sorbitol, etc.), and ionic bonds that are polyvalent metal compounds such as aluminum. An example of the functional cross-linking agent. Among these, from the viewpoint of water absorption properties, a polymerizable crosslinking agent with acrylic acid is preferable, and acrylate-based, allyl-based, and acrylamide-based polymerizable crosslinking agents are particularly preferably used. These internal crosslinking agents may be used alone or in combination of two or more.

(C) Polymerization initiator As a polymerization initiator used by this invention, it selects suitably by the form of superposition | polymerization, A photodecomposition type polymerization initiator, a thermal decomposition type polymerization initiator, a redox type polymerization initiator etc. can be illustrated. The amount of the polymerization initiator used is preferably 0.0001 to 1 mol%, more preferably 0.001 to 0.5 mol%, based on all monomers.

  Examples of the photodegradable polymerization initiator include benzoin derivatives, benzyl derivatives, acetophenone derivatives, benzophenone derivatives, azo compounds, and the like.

  Thermal decomposition polymerization initiators include persulfates (sodium persulfate, potassium persulfate, ammonium persulfate), peroxides (hydrogen peroxide, t-butyl peroxide, methyl ethyl ketone peroxide), azo compounds (2, 2 '-Azobis (2-amidinopropane) dihydrochloride, 2,2'-azobis [2- (2-imidazolin-2-yl) propane] dihydrochloride, etc.) can be exemplified.

  Examples of the redox polymerization initiator include a system in which a reducing compound such as L-ascorbic acid or sodium bisulfite is used in combination with the persulfate or peroxide, and both are combined. Moreover, it can also be mentioned as a preferable aspect to use the said photodegradable initiator and a thermal decomposable polymerization initiator together.

(D) Polymerization method The polymerization method according to the embodiment of the present invention is usually carried out by aqueous solution polymerization or reverse phase suspension polymerization from the viewpoint of the properties of the water-absorbent resin such as liquid permeability and water absorption speed and ease of polymerization control. Is called. Among these polymerization methods, aqueous solution polymerization, which has heretofore been difficult to control polymerization or improve coloring, is preferable, continuous aqueous solution polymerization is more preferable, and high concentration / high temperature starting continuous aqueous solution polymerization is particularly preferable.

  Preferable forms of the above-mentioned continuous aqueous solution polymerization include, for example, continuous kneader polymerization (described in US Pat. Nos. 6,987,151 and 6,710,141), continuous belt polymerization (US Pat. Nos. 4,893,999 and 6,241,928, and published US patent applications). No. 2005/215734 etc.).

  These polymerizations can be carried out in an air atmosphere, but from the viewpoint of color improvement, it is preferably carried out in an inert gas atmosphere (for example, an oxygen concentration of 1% by volume or less) such as nitrogen or argon. Moreover, it is preferable to use it for superposition | polymerization, after the oxygen in the solution containing a monomer or a monomer is fully substituted with an inert gas (for example, less than 1 mg / L of oxygen). Thus, even if it deaerates, it is excellent in the stability of a monomer, gelatinization before superposition | polymerization does not occur, and it can provide a water absorbing resin with higher physical properties and high whiteness.

(2) Gel refinement step The hydrogel crosslinked polymer (hydrogel) obtained in the above polymerization step may be dried as it is, but from the viewpoint of water absorption speed and liquid permeability, at the time of polymerization or polymerization Then, if necessary, the gel is crushed using a crusher (kneader, meat chopper, etc.) to form particles. That is, the weight average particle size (specified by sieve classification) of the particulate hydrogel after the gel crushing is preferably in the range of 0.1 to 10 mm, more preferably 0.5 to 5 mm, and still more preferably 1 to 3 mm. It is.

  The temperature of the hydrogel at the time of gel crushing is preferably 40 to 95 ° C., more preferably 50 to 80 ° C., from the viewpoint of physical properties. The resin solid content of the hydrous gel is not particularly limited, but is preferably 20 to 80% by weight, more preferably 30 to 70% by weight, and still more preferably 40 to 60% by weight from the viewpoint of physical properties.

(3) Drying step The hydrogel crosslinked polymer is dried to form a dry polymer. The resin solid content determined from the loss on drying (1 g of powder or particles is heated at 180 ° C. for 3 hours) is preferably 80% by weight or more, more preferably 85 to 99% by weight, still more preferably 90 to 98% by weight, particularly Preferably, it is adjusted to the range of 92 to 97% by weight to obtain a dry polymer.

  The drying temperature is not particularly limited, but is preferably in the range of 100 to 300 ° C, more preferably in the range of 150 to 250 ° C. There are various drying methods such as heat drying, hot air drying, vacuum drying, infrared drying, microwave drying, drum dryer drying, azeotropic dehydration with hydrophobic organic solvents, and high humidity drying using high temperature steam. Although it can employ | adopt, Preferably it is a hot-air drying by a gas with a dew point of 40-100 degreeC, More preferably, a dew point of 50-90 degreeC, Especially a ventilation band type dryer.

  The shape of the dry polymer is usually in the form of particles or aggregates thereof (eg, block-like product; see Patent Document 1) or a mixture of both, and is not particularly limited.

(4) Pulverization step and classification step The dried polymer obtained in the drying step may be supplied to the pulverization step as it is, but when aggregates are contained (especially, it is dried with a ventilation band dryer). In the case of a block-like product), the dried polymer (particularly block-like aggregate) is crushed into particles having a particle size of 0.1 to 10 mm, preferably 0.5 to 5 mm, more preferably 1 to 3 mm. (Agglomeration is loosened) and it is preferably supplied to the pulverization step. (Hereinafter, coarsely pulverizing the block-shaped aggregates after drying (pulverization to a degree of partial aggregation) is also referred to as coarse pulverization, which corresponds to the zero-order pulverization step in the present application.

(Arbitrary zero-order grinding)
In addition to the first pulverization step and the second pulverization step using at least two types of impact pulverizers, which will be described later, a zero-order pulverization step is preferably provided before the one-hour pulverization. In the zero-order pulverization step, the particles or aggregates thereof are coarsely pulverized (pulverized to the extent that they are partially agglomerated) to form a fluidized powder or fluidized agglomerate. Preferably, the weight average is 0.1 to 100 mm by sieve classification. Coarsely pulverized to a degree (1 to 100 mm, more preferably 1 to 10 mm).

  When supplying to the pulverization step (zero-order pulverization step), the temperature of the particulate material, the aggregate thereof, the crushed aggregate, or a mixture thereof is preferably 100 ° C. or less, and 95 ° C or lower is more preferable, 90 ° C or lower is further preferable, 85 ° C or lower is further preferable, and 80 ° C or lower is particularly preferable. The lower limit may be any temperature that does not cause condensation, and is usually preferably 0 ° C. or higher, more preferably 20 ° C., still more preferably 30 ° C., and particularly preferably 35 ° C. or higher. The said temperature range is the same also in the said dry polymer supplied to the said crushing. Outside the above temperature range, the grinding efficiency (processing capacity and particle size distribution) may decrease, and aggregation and adhesion may occur.

  The method for adjusting to the temperature range is not particularly limited, and can be carried out by allowing the dry polymer at a high temperature to stand for a predetermined time or contacting a gas such as air in the temperature range.

  Usually, in order to obtain a pulverized product with uniform particle size in a high yield, it is common to repeat pulverization and classification. For example, when a granular material of 0.1 to 100 mm (preferably by zero-order pulverization) is pulverized to 150 to 850 μm, if pulverized under the condition that all are 850 μm or less at a time, there are many finely pulverized products of 150 μm or less. And the yield decreases. Therefore, after pulverizing under the condition that a certain amount of large particles of 850 μm or more are generated and classifying the obtained pulverized product, the large particles are returned to the original pulverization process or sent to another pulverization process. Is called. In addition, the generation ratio of large particles is appropriately set in consideration of processing efficiency and yield. As the zero-order pulverization, a pulverizer described later, particularly an impact-type pulverizer, is used. In particular, a pulverizer different from the primary pulverization and the secondary pulverization, for example, a horizontal pulverizer installed in parallel with the outlet during belt drying ( A crusher with rotating teeth) is used.

(Primary grinding and secondary grinding)
The pulverization method of the present invention is a method in which a plurality of pulverizers of a specific type are combined, that is, a method having a plurality of pulverization steps (primary pulverization and secondary pulverization, preferably further the above-described zeroth pulverization). As a result, a pulverized product having a uniform particle size can be obtained in a high yield without repeating the classification for achieving the target particle size and the pulverization of the large particles, which have been conventionally performed.

  The pulverizer used in the present invention is pulverized by at least two types of impact pulverizers (primary pulverization and secondary pulverization), and further, the third dry pulverizer (zero pulverization, primary pulverization and subsequent tertiary pulverization). ), A pulverizer selected from compression, bending, shearing, impact, and friction may be used, and an impact pulverizer is particularly preferable. Moreover, any of a continuous type and a batch type may be sufficient, and specifically, a ball mill, a hammer mill, a pin mill, a flash mill, a fluidized bed type grinder (jet mill), etc. are mentioned. In addition, the said ball mill is not limited to the type which uses only a spherical shape, It is a broad concept including a rod mill and a compound mill. A preferable pulverizer is a pulverizer of a type in which an object to be pulverized floating or falling in the air is broken by impact and the parts of the pulverizer do not contact each other, specifically, a pin mill, a flash mill, a fluidized bed type pulverizer. Machine (jet mill). The preferable three types of pulverizers have little increase in temperature of the material to be pulverized at the time of pulverization, so that the quality of the water-absorbent resin is suppressed, and the pulverizer itself is hardly worn or damaged. There is an advantage that there is little foreign matter contamination.

  The combination of pulverizers varies depending on the particle size before pulverization and the target particle size, but the pulverizer used in the first pulverization step is preferably a hammer mill or a pin mill, and more preferably a pin mill. The pulverizer used in the second pulverization step is preferably a flash mill or a fluidized bed pulverizer (jet mill). In order to obtain particles having an average particle size of 50 μm or less, a flash mill is used in the second pulverization step. It is preferable to use a fluidized bed pulverizer (jet mill) in the pulverization step.

  In each of the pulverizers, when the water-absorbing resin absorbs moisture, the pulverization efficiency is lowered, and it causes adhesion and accumulation in the apparatus. Therefore, it is desirable not to cool the pulverization indoor wall temperature to a temperature lower than the ambient temperature. If the pulverization indoor wall temperature is 150 ° C. or lower, there is no need to cool it.

  From the viewpoint of pulverization efficiency, it is preferable to adjust the pulverization inner wall temperature, preferably 30 to 150 ° C, more preferably 35 to 120 ° C, and particularly preferably 40 to 100 ° C.

  Further, the relative humidity in the grinding chamber is preferably 70 RH% or less, more preferably 50 RH% or less, and further preferably 30 RH% or less. In a pulverizer that supplies gas to the pulverization chamber such as a jet mill, the dew point of the gas is preferably 0 ° C. or less, more preferably −5 to −80 ° C., and particularly preferably −10 to −50 ° C. . Other operating conditions may be appropriately set in consideration of the particle size and processing amount of the material to be crushed, the size of the pulverizer, and the like.

In addition, it is preferable to classify the pulverized material obtained by the first-stage pulverizer because the particle sizes can be more uniform. In the classification step, large particles having an average particle diameter of 10 times or more, more preferably 15 times or more of the final target average particle diameter may be removed, and the removed large particles are returned to the first-stage pulverizer and re-pulverized. You may do it. That is, embodiments including the first of the first milling step by an impact grinder, classifying step, the second milling step in the form of different second impact mill is preferred.

Furthermore, in order to obtain fine particles having a volume average particle diameter of 1 to 100 μm, the volume average particle diameter of the first pulverized product is preferably 1000 μm or less, and more preferably in the range of 150 to 1000 μm. Preferably, it is in the range of 150 to 700 μm. Then, the first pulverized step treated product pulverized to the volume average particle size, optionally including a classification step after pulverization, and more preferably the classified step treated product has a volume average particle size of less than 150 μm in the second pulverizing step. It is obtained by crushing and crushing to a volume average particle size of 100 μm or less in the third crushing step (particle size)
The final volume average particle diameter is adjusted to 1 to 150 μm, preferably 1 to 100 μm, more preferably 1 to 80 μm, still more preferably 5 to 50 μm, and particularly preferably 5 to 30 μm. The particle size distribution is preferably as small as the coefficient of variation (standard deviation σ ÷ volume average particle diameter), and is usually adjusted to 0.8 or less, preferably 0.7 or less, and particularly preferably 0.6 or less. About these measuring methods, it measures using the light-scattering particle size distribution measuring apparatus (LA-920 by the HORIBA company) etc. It has been found that by controlling the volume average particle size to be small and narrow to a specific range, not only the water absorption rate but also the fine particle size water absorption magnification is improved.

(5) Transport process and circulation process In the present invention, the pulverization process-classification process and its front and back are connected by a transport device. As a transport device used, as a transport machine used in the transport process, for example, Examples thereof include a belt conveyor, a screw conveyor, a chain conveyor, a vibration conveyor, a pneumatic conveyor, and the like, which are provided with means for heating and / or keeping the inner wall surface from the outside. In these transport processes, the pressure is reduced or increased.

  Of these transport aircraft, pneumatic transport is preferred. Pneumatic transportation of the water-absorbent resin is exemplified in International Publication Nos. 2007/104657, 2007/104674, and 2007/104676. Among pneumatic transportation, it is preferably transported at a dew point of 0 ° C. or less. . The pneumatic transportation of the present invention may be pressurized transportation or reduced pressure transportation. The pressure to be used is appropriately determined and is, for example, in the range of −0.8 bar to 10 bar.

(Classification device)
The classifying apparatus used in the present invention is not particularly limited as long as it has a sieve mesh surface, and examples thereof include those classified as a vibratory screen or a shifter. Vibrating screens include tilted, low-head, Hum-mer, Rheum, Ty-Rock, Gyrex, and elliptical vibration (Eliptex), etc. The shifter includes a reciprocating type, Exonon-grader, Traversator-sieb, Sauer-meyer, a gyratory shifter (Gyratory), a gyroshifter, and a rotex screen (Ro-tex).

(6) Other steps In addition to the above, an evaporation monomer recycling step, a granulation step, and the like may be provided as necessary. Furthermore, additives described later may be used for the monomer or a polymer thereof for the purpose of color stability with time and prevention of gel deterioration.

[3] Physical properties of water-absorbing resin The water-absorbing resin obtained by the production method according to the present invention preferably has an absorption rate (Vortex) of 10 seconds or less. When used as a rubber, in addition to the above physical properties, at least one of the following (a) to (d), preferably two or more including the absorption rate (Vortex), more preferably three or more It is desirable to control the physical properties within a desired range. When these physical properties do not satisfy the following ranges, the effects of the present invention are not sufficiently obtained, and the absorption of an aqueous liquid containing a polyvalent metal salt at a high concentration does not exhibit sufficient performance. There exists a possibility that the effect using the manufacturing method of invention may become small.

(A) Artificial Sea Water-Free Swell Capacity (ASW-FSC) (also known as micro-particle water absorption capacity)
The artificial seawater absorption capacity (ASW-FSC) of the water-absorbent resin of the present invention is defined by the below-mentioned fine particle size water absorption capacity, preferably 10 (g / g) or more, more preferably 15 (g / g) or more, 20 (G / g) or more is more preferable, and 25 (g / g) or more is particularly preferable. Although an upper limit is not specifically limited, From a balance with other physical properties, 50 (g / g) or less is preferable, 45 (g / g) or less is more preferable, and 40 (g / g) or less is still more preferable. ASW-FSC can be controlled by a crosslinking density (for example, ASW-FSC improvement by suppressing the addition amount of the crosslinking agent) and an additive (for example, ASW-FSC improvement by adding inorganic fine particles).

(B) Artificial Sea Water-Free Swell Vortex (ASW-Vortex) (Also Known as Artificial Sea Water Absorption Rate)
The artificial seawater absorption rate (ASW-Vortex) of the water-absorbent resin of the present invention is defined by the below-mentioned fine particle size water absorption rate, preferably 30 seconds or less, more preferably 20 seconds or less, still more preferably 15 seconds or less, and more preferably 10 seconds. The following are particularly preferred:

  Further, the physiological saline absorption rate (Saline-Vortex) of the water-absorbent resin of the present invention is preferably 30 seconds or less, more preferably 20 seconds or less, still more preferably 15 seconds or less, and particularly preferably 10 seconds or less. The lower limit exceeds 0, and is usually about 0.1 second, and further about 1 second. ASW-Vortex can be controlled by the absorption ratio (increase), the narrow particle size control of the present invention, the surface area Up due to foaming, the neutralization rate increase, and additives (particularly water-insoluble inorganic fine powder).

(C) Water content The water content of the water-absorbent resin of the present invention (3 hours at 180 ° C.) is preferably more than 1% by weight and 15% by weight or less, more preferably 1 to 13% by weight, and more preferably 2 to 10% by weight. Is more preferable, and 1 to 9% by weight is particularly preferable. By controlling the water content within the above range, it is possible to obtain a water-absorbent resin excellent in powder characteristics (for example, fluidity, transportability, damage resistance, etc.). The water content can be controlled by the degree of drying (temperature, time), water addition after drying, and heat treatment.

(D) Particle diameter The water-absorbent resin particles of the present invention are crushed indeterminate and have a volume average particle diameter of 1 to 150 μm, preferably 1 to 100 μm, more preferably 1 to 80 μm, still more preferably 5 to 50 μm, particularly Preferably, the fine particles are 5 to 30 μm.

  Particles with a volume-based particle diameter of less than 1 μm are more cohesive and more likely to generate secondary particles, making it difficult to combine with rubber, water-stopping tape, etc. If it is, the effect of the present invention may not be sufficiently exerted, for example, primary particles may fall off. In the case of exceeding 100 μm, there is almost no effect of improving the water absorption magnification found in the present invention, and further, the water absorption performance in the presence of high-concentration metal ions such as seawater is insufficient, which is not preferable. The critical effect of such particle size is shown in Table 1 of the Examples and FIG.

  Accordingly, the coefficient of variation (standard deviation σ ÷ volume average particle diameter) is preferably small, and may be 1.0 or less, preferably 0.8 or less, more preferably 0.7 or less, and even more preferably 0.6 or less. . If the coefficient of variation is 1 or more, the effect of the present invention may be insufficient because particles of less than 1 μm or 200 μm are contained on a number basis by 10% or more. The critical effect of such particle size is shown in Table 1 of the Examples and FIG.

  Furthermore, it is preferable that the volume average particle size−standard deviation ≦ 1 to 200 μm ≦ volume average particle size + standard deviation, and the volume average particle size−standard deviation × 2 ≦ 1 to 200 μm ≦ volume average particle size + standard deviation × 2. More preferably, the volume average particle size-standard deviation × 3 ≦ 1 to 200 μm ≦ volume average particle size + standard deviation × 3. And the range of 1-200 micrometers is more preferable in it being 1-150 micrometers, it is still more preferable in it being 1-100 micrometers, and it is especially preferable in it being 1-50 micrometers.

  About the measuring method of said volume average particle diameter, a volume reference | standard particle diameter, and a standard deviation, it measures wet with methanol as a dispersion | distribution solvent using the light-scattering particle size distribution measuring apparatus (LA-920 by HORIBA).

Water-absorbent resin particles of the present invention having the characteristics related to the particle size, high absorption rate and absorption capacity at high concentrations in the presence of metal ions such as seawater, is suitable for such conjugation with rubber.

  And if the grinding | pulverization method of this invention is used, the water-absorbing-resin particle | grains which have the characteristic regarding the said particle size can be manufactured efficiently and simply, without performing the particle size adjustment by sieving.

[3] Other additives Furthermore, depending on the purpose, the water-absorbing resin may be an oxidizing agent, an antioxidant, water, a polyvalent metal compound, water-insoluble inorganic powder such as silica or metal soap, or organic such as polyacrylic acid fine particles. Powder, deodorant, antibacterial agent, polymer polyamine, pulp, thermoplastic fiber and the like may be added to the water absorbent resin in an amount of 0 to 3% by mass, preferably 0 to 1% by mass.

[4] Measuring method for water absorption performance with fine particle size Water-absorbing resin powder having an average particle size of 100 μm or less has high self-aggregation property, and thus cannot be correctly evaluated by the conventional measuring method. Therefore, a new evaluation method for fine particle water-absorbing resin was developed.

  By mixing the water-absorbing resin powder and the inorganic compound powder, self-aggregation is suppressed, so that the water absorption ratio and the water absorption speed can be measured. The inorganic oxide powder to be used is preferably an inorganic oxide powder that does not exhibit swelling and ion dissociation by the measurement liquid. Specific examples include silicon dioxide, aluminum oxide, titanium oxide, zirconium dioxide, zinc dioxide, silicon carbide, silicon nitride, silica-alumina, zeolite, etc., and silicon dioxide, aluminum oxide, titanium oxide, zirconium dioxide, Zinc, silicon carbide and silicon nitride are preferred, silicon dioxide, aluminum oxide, titanium oxide, zirconium dioxide and zinc dioxide are more preferred, silicon dioxide and aluminum oxide are further preferred, and silicon dioxide, particularly hydrophilic silica is particularly preferred. Hydrophilic silica is commercially available from Nippon Aerosil Co., Ltd., Degussa, Tokuyama Co., Ltd., etc., and typically, Toroyama's Leolosil-QS20 or its equivalent (same composition, particle size, specific surface area, etc.) is used.

  The average particle size of the inorganic powder compound varies depending on the average particle size and particle size distribution of the water absorbent resin powder to be measured, but is preferably the same or smaller than the average particle size of the water absorbent resin powder. It is preferably smaller than D10 on the particle size side. The lower limit value of the average particle size of the inorganic powder compound may be determined in consideration of the measurement method using the mixed sample, and is usually 1 / 1,000,000 or more of the average particle size of the water absorbent resin powder. is there. Specifically, the thickness is 1 nm to 100 μm, preferably 1 nm to 1 μm, more preferably 1 nm to 100 nm, and still more preferably 2 nm to 50 nm.

  The mixing ratio may be appropriately set depending on the water-absorbent resin powder to be measured, the inorganic compound to be used, and the measured physical properties, and is usually 20 to 80% by mass as the inorganic compound content in the mixed sample for measurement. 70 mass% is more preferable, 20-60 mass% is still more preferable, 30-60 mass% is still more preferable, 40-60 mass% is especially preferable. If the content of the inorganic compound is small, the effect of suppressing the self-aggregation property may be insufficient. If the content is too large, the influence of the inorganic compound on the measurement result may be increased.

(Mixed sample for measurement)
30 g of 5 g of water-absorbing resin and 5 g of hydrophilic silica (manufactured by Tokuyama; Leolo Seal-QS20) in a paint shaker (Toyo Seiki Seisakusho Co., Ltd., AC 100 V, single phase 60 Hz, reference standard JIS K 5101-1-2: 2004) Get mixed for minutes.

(Fine particle water absorption rate (also known as artificial seawater absorption rate))
This is a method for measuring the artificial seawater absorption rate of the present invention, and the basic measurement method is in accordance with the Vortex method, but the sample to be used for measurement is used by weighing 0.8 g of the measurement mixed sample.

  The water absorption speed is preferably 30 seconds or less and 20 seconds or less, more preferably 15 seconds or less, and particularly preferably 10 seconds or less with respect to artificial seawater.

(Fine particle size water absorption ratio: FGA (also known as artificial water absorption ratio))
This is a method for measuring the artificial seawater absorption magnification of the present invention. The basic measurement method is the AAP method defined in 442.2-02 (2002) or the equivalent WSP 442.3 (2010), without using weights. Measure the absorption capacity under load. The detailed measurement method is as shown in the examples. The sample to be used for measurement is the mixed sample for measurement (0.2 g).

  In order to eliminate the influence of the inorganic compound powder (hydrophilic silica: Leolosil-QS20) or its equivalent added to the water-absorbent resin at the time of measurement, a value obtained by subtracting the value obtained by performing blank measurement in advance is obtained. .

[5] Uses The use of the water-absorbent resin of the present invention is not particularly limited, but is preferably used for industrial uses such as water-stopping materials for civil engineering, inter-segment water-stopping materials for tunnel construction, and water-proof tapes for optical cables. Can be done. In particular, even when in contact with an aqueous liquid containing a polyvalent metal ion such as hard water or seawater such as water-swellable rubber, the water absorption speed is extremely fast, and particularly excellent water absorption performance is exhibited over a long period of time.

  EXAMPLES Hereinafter, although an invention is demonstrated according to an Example, this invention is limited to an Example and is not interpreted. The physical properties described in the claims and examples of the present invention were determined according to the EDANA method and the following measurement methods.

(Fine-grain water absorption speed by artificial seawater) (Also known as artificial seawater absorption speed)
5 g of water-absorbing resin and 5 g of hydrophilic silica (manufactured by Tokuyama; Leoroseal-QS20) are charged into a 225 ml mayonnaise bottle, and paint shaker (Toyo Seiki Seisakusho, AC100V, single phase 60 Hz, reference standard JIS K 5101-1-2: 2004). ) For 30 minutes to obtain a mixed sample for measurement (about 10 g). In addition, even when 5 g of the water absorbent resin used for the measurement contains other additives (for example, silica, chelating agent, water, etc.) in advance, 5 g is measured as it is.

  Next, 0.8 g of the measurement mixed sample is weighed and prepared on a medicine wrapping paper. A cylindrical stirrer bar coated with 50 g of artificial seawater (30 ° C.) and 40 mm fluororesin coated in blue No. 2 in advance in a 100 ml beaker. A beaker is set on a magnetic stirrer, and while stirring at 500 rpm, 0.8 g of the water absorbent resin / silica mixed sample prepared earlier is charged. The end point is the point where the stirrer bar is hidden behind the gel and cannot be seen.

(Small particle size water absorption rate by physiological saline) (Also known as physiological saline water absorption rate)
In the measurement of the fine particle size water absorption rate by the artificial seawater, the same measurement was performed except that the artificial seawater was changed to 30 ° C. physiological saline (0.9 mass% NaCl aqueous solution).

(Fine-grain water absorption ratio (FGA) by artificial seawater) (Also known as artificial seawater magnification)
FGA1 described below is an artificial seawater absorption ratio (30 minutes value) of 1/1 (weight ratio) of water absorbent resin powder / silica, and FGA is a water absorbent resin corrected by subtracting the water absorption amount derived from silica from FGA1. It is the artificial seawater absorption ratio (30 minutes value) in the powder state.

  That is, in the measurement method (measurement principle and measuring apparatus) of the absorption capacity under pressure of ERT442.2-02 (2002) to the corresponding WSP442.3 (2010) without using a weight according to the following, under no load on artificial seawater The water absorption rate (g / g) was measured and used as the fine particle size water absorption rate (FGA1, FGA).

  A glass filter (diameter 120 mm, hole diameter JIS standard No. 0, height 5 mm) is placed in the center of the tray (SUS square D20 cm × L20 cm × H10 mm), and 200 g of artificial seawater is added. A filter paper (No. 2 110 mm manufactured by ADVANTEC) is placed on the glass filter, and then a cylinder (C-207431-D-2 with screen (400 mesh) manufactured by Machintek) is placed thereon.

  The mixed sample for measurement (WS 0.2 g) is uniformly spread in a cylinder. After soaking for 30 minutes, the cylinder is gently lifted, and the total mass (WS1) of the cylinder with the sample after measurement is measured. As a blank measurement, a sample charged with only hydrophilic silica (WBS 0.1 g) is measured.

  Using the above measurement results, the absorption capacity (g / g) of the water-absorbent resin was calculated by the following formula.

WBC: Cylinder empty cylinder mass (g)
WBS: Mass of silica used for blank test (g)
WBS1: Total mass of cylinder after immersion for 30 minutes in blank test (g)
WBS2: Water absorption in blank test (g)
= WBS1-WBC
FGAB: Silica water absorption capacity (g / g) required from blank test
= WBS2 / WBS
WSS1: Silica mass used for preparation of mixed sample for measurement (g)
WSA1: Water-absorbing resin mass (g) used for preparation of mixed sample for measurement
RSS1: Silica mass ratio (-) in the mixed sample for measurement
= WSS1 ÷ (WSS1 + WSA1)
RSA1: Mass ratio of water absorbent resin in the mixed sample for measurement (-)
= WSA1 ÷ (WSS1 + WSA1)
WS: Measurement mixed sample mass (g) used for measurement
WSS: Silica mass (g) in the mixed sample for measurement used for measurement
= WS1 x RSS1
WSA: Mass of water absorbent resin (g) in the mixed sample for measurement used for measurement
= WS1 x RSA1
WS1: Total cylinder mass (g) after 30 minutes of immersion
WS2: Water absorption (g)
= WS1- (WBC + WS)
FGA1: fine particle size water absorption ratio (g / g) of mixed sample for measurement
= WS2 ÷ WS
FGA: Fine particle size water absorption ratio (g / g)
= (WS1-WBC-WSS × FGAB) / WSA
(Particle size measurement method)
Using LA-920, a laser diffraction particle size distribution device manufactured by HORIBA, set the distribution form: standard, particle size standard: volume, graph form: bar graph, and then add methanol to the sample bath to remove air and adjust the optical axis. I do. Next, the sample is placed in the sample bath, and at the same time as the sample is loaded, after applying ultrasonic waves for 2 minutes, the sample concentration is adjusted so that the transmittance is 81 to 88%. The measurement is carried out after adjusting the sample concentration and again performing ultrasonic treatment for 2 minutes.

[Example 1]
Each device of the polymerization process (stationary polymerization on the belt), gel granulation (pulverization) process, drying process, pulverization process, classification process, and transport process between each process is connected, and each process is continued. An apparatus for continuously producing a water-absorbing resin that can be carried out is used. The production capacity is about 3500 kg per hour. Using this continuous manufacturing apparatus, water-absorbing resin powder was continuously manufactured.

  First, a monomer aqueous solution (1) having the following composition was prepared.

Monomer aqueous solution (1) Composition: acrylic acid: 193.3 parts by mass, 48% by mass sodium hydroxide aqueous solution: 64.4 parts by mass, methylenebisacrylamide: 1.26 parts by mass, 0.1% by mass ethylenediaminetetra ( Methylenephosphonic acid) 5-sodium aqueous solution: 52 parts by mass, deionized water: 134 parts by mass Next, the above monomer aqueous solution (1) was adjusted to 40 ° C., continuously fed with a metering pump, and 48% by mass water 97.1 parts by mass of an aqueous sodium oxide solution and then 8.05 parts by mass of a 4% by mass aqueous sodium persulfate solution were continuously mixed by line mixing. The continuous mixture obtained by this line mixing was supplied to a flat belt having weirs at both ends in a thickness of about 7.5 mm, and polymerized continuously for 3 minutes to obtain a hydrogel crosslinked polymer (1). .

  The obtained hydrogel crosslinked polymer (1) was continuously cut at approximately equal intervals in the direction perpendicular to the belt traveling direction. Next, it was subdivided into about 1.5 mm with a meat chopper having a hole diameter of 22 mm. This finely divided gel was spread and placed on a perforated plate moving with a continuous ventilation band dryer in a thickness of about 7 cm, dried at 185 ° C. for 30 minutes, and a dry polymer (1) of 246 mass with a moisture content of 4%. Part (total amount of water-absorbent resin discharged in the drying step) was obtained.

  The dried polymer (1) is in the form of a block (one plate on the drying belt) in which the dried product of the finely divided gel is aggregated, and after cooling to 60 ° C., crushing at the outlet of the dryer (zero-order pulverization) The dried polymer (1) at about 60 ° C. was continuously fed to a pin mill and pulverized (primary pulverization) to obtain a pulverized product (1) at about 60 ° C. The pulverized product (1) is continuously classified into particles (1J) that did not pass through the 250 μm sieve and particles (1K) that passed through the 250 μm sieve using a sieving device having a metal sieve mesh with an opening of 250 μm. did. The particles (1J) of the substantially unmilled sieve-on product were supplied again to the pin mill and pulverized (primary pulverization).

  The particles (1K) were subsequently sent to the second pulverization step by pneumatic transportation and further refined by a flash mill. After being finely divided by a flash mill, it was pneumatically transported to the jet mill in the third pulverization step, and pulverization was performed by collision between objects to be pulverized using a jet stream. The air pressure of the device at this time was 0.35 Mpa.

  Thus, a water-absorbent resin powder (1) having a volume average particle diameter of 50 μm and a water content of 4% was obtained through four different pulverization steps. The obtained water-absorbent resin powder (1) was measured according to the measurement method of the fine particle size water absorption rate and fine particle size water absorption rate. The measurement results are shown in Table 1.

[Example 2]
Sodium 2-acrylamido-2-methylpropanesulfonate (AMPS) 50% aqueous solution 235.4 parts by mass, acrylic acid 43.2 parts by mass, sodium acrylate 37% aqueous solution 152.3 parts by mass and deionized water 58.6 parts by mass 15.0 parts by mass of a 1.5% aqueous solution of methylenebisacrylamide was dissolved in the mixed liquid to prepare a reaction solution.

  Next, the reaction solution was degassed by bubbling with nitrogen gas (10 L / min) for 40 minutes, and then the reaction solution was supplied to a jacketed stainless steel double-arm kneader having two sigma-type blades and heated to 30 ° C. The system was purged with nitrogen gas while maintaining. Subsequently, while stirring the reactor, 2.0 parts by mass of a 21% by mass aqueous solution of sodium persulfate and 2.1 parts by mass of a 2% by mass aqueous solution of L-ascorbic acid were added, and polymerization started about 1 minute later. The maximum temperature during the polymerization was 80 ° C., 60 minutes after the start of the polymerization, the stirring was once stopped, 41.3 parts by mass of a 5% by mass aqueous sodium hydrogen sulfite solution was added, and the mixture was mixed for 10 minutes. The coalescence was taken out.

  The obtained polymer was subdivided into about 5 mm in diameter. This finely divided hydrogel polymer was spread on a 50 mesh (mesh size 300 μm) wire mesh and dried at 160 ° C. for 130 minutes to obtain a dry polymer (2) having a moisture content of 4%.

  The dry polymer (2) at about 60 ° C. was similarly subjected to zero-order pulverization at the outlet of the dryer and further pulverized (primary pulverization) by continuously supplying it to a pin mill to obtain a pulverized product (2) at about 60 ° C. . The pulverized product (2) is continuously classified into particles (2J) that did not pass through the 250 μm sieve and particles (2K) that passed through the 250 μm sieve using a sieving device having a metal sieve mesh with an opening of 250 μm. did. The particles (2J) were again supplied to the pin mill and pulverized (primary pulverization).

  The particles (2K) were subsequently sent to the second pulverization step by pneumatic transportation and further refined by a flash mill. After being finely divided by a flash mill, it was pneumatically transported to the jet mill in the third pulverization step, and pulverization was performed by collision between objects to be pulverized using a jet stream. The air pressure of the device at this time was 0.60 Mpa.

  Thus, a water-absorbent resin powder (2) having a volume average particle size of 15.5 μm, a standard deviation of 8.6 μm, a minimum particle size of 1.510 μm, a maximum particle size of 58.953 μm and a water content of 4% was obtained. The obtained water-absorbing resin powder (2) was measured according to the measurement method of the fine particle size water absorption rate and fine particle size water absorption rate. The measurement results are shown in Table 1.

[Example 3]
276.7 parts by mass of a 40% by mass aqueous solution of acrylamide, 169.7 parts by mass of a 37% by mass aqueous solution of sodium acrylate, 11.2 parts by mass of an aqueous solution of 43% by mass of 2-sulfoethyl sodium methacrylate and 33.2 parts by mass of deionized water In the mixed solution, 22.9 parts by mass of a 1.5% by mass aqueous solution of methylenebisacrylamide was dissolved to obtain a reaction solution.

  Next, this reaction solution was deaerated by bubbling with nitrogen gas (10 L / min) for 40 minutes. Next, the reaction solution was supplied to a stainless steel double-arm kneader with a jacket having two sigma type blades, and the inside of the system was replaced with nitrogen gas while maintaining the temperature at 30 ° C. Subsequently, while stirring the reactor, 3.8 parts by mass of a 21% by mass aqueous solution of sodium persulfate and 3.9 parts by mass of a 2% by mass aqueous solution of L-ascorbic acid were added, and polymerization started about 1 minute later. The maximum temperature during the polymerization was 110 ° C., 60 minutes after the start of the polymerization, the stirring was once stopped, 28.7 parts by mass of a 5% by mass aqueous sodium hydrogen sulfite solution was added, and the mixture was mixed for 10 minutes. The coalescence was taken out.

  The obtained polymer was subdivided into about 5 mm in diameter. This finely divided hydrogel polymer was spread on a 50 mesh (mesh size 300 μm) wire mesh and dried at 160 ° C. for 130 minutes to obtain a dry polymer (3) having a moisture content of 4%.

  The dry polymer (3) at about 60 ° C. is similarly subjected to zero-order pulverization at the outlet of the dryer and further pulverized (primary pulverization) by continuously supplying it to a pin mill to obtain a pulverized product (3) at about 60 ° C. It was. The pulverized product (3) is continuously classified into particles (3J) that did not pass through the 250 μm sieve and particles (3K) that passed through the 250 μm sieve using a sieving device having a metal sieve mesh with an opening of 250 μm. did. The particles (3J) were again supplied to the pin mill and pulverized.

  The particles (3K) that passed through the 250 μm sieve were subsequently sent to the second grinding step by pneumatic transport and further refined by a flash mill. After being finely divided by a flash mill, it was pneumatically transported to the jet mill in the third pulverization step, and pulverization was performed by collision between objects to be pulverized using a jet stream. The air pressure of the device at this time was 0.60 Mpa.

  Thus, a water absorbent resin powder (3) having a volume average particle size of 15.3 μm, a standard deviation of 6.7 μm, a minimum particle size of 1.510 μm, a maximum particle size of 44.938 μm and a water content of 4% was obtained. The obtained water-absorbent resin powder (3) was measured according to the measurement method of the fine particle size water absorption rate and fine particle size water absorption rate. The measurement results are shown in Table 1.

[Comparative Example 1]
In Example 1, the same operation as in Example 1 was carried out except that after pulverization (primary pulverization) by a pin mill and pulverization was completed without being sent to the second pulverization step, the volume average particle diameter was continuously obtained. A comparative water absorbent resin powder (1) of 186 μm was obtained.

  The obtained comparative water-absorbent resin powder (1) was measured according to the measurement method of the fine particle size water absorption rate and fine particle size water absorption rate. The measurement results are shown in Table 1.

[Comparative Example 2]
In Example 2, the same operation as in Example 3 was carried out except that the pulverization was terminated without being sent to the second pulverization step after being finely divided (primary pulverization) by a pin mill, and the volume average particle diameter was continuously obtained. A comparative water absorbent resin powder (2) of 181 μm was obtained.

  The obtained comparative water-absorbent resin powder (2) was measured according to the measurement method of the fine particle size water absorption rate and the fine particle size water absorption rate. The measurement results are shown in Table 1.

[Example 4]
In Example 3, after finely pulverizing (secondary pulverization) with a flash mill, the air was transported to the jet mill in the third pulverization step, and the air pressure was changed to 0.25 MPa to make the particle size 50 μm. Were the same as in Example 3 to obtain a water absorbent resin powder (4) having a volume average particle size of 44.8 μm, a standard deviation of 30.78 μm, a minimum particle size of 1.981 μm, and a maximum particle size of 133.103 μm. Obtained. The obtained water-absorbent resin powder (4) was measured according to the measurement method of the fine particle size water absorption rate and fine particle size water absorption rate. The measurement results are shown in Table 1.

[Example 5]
In Example 3, after finely pulverizing (secondary pulverization) by a flash mill, the air is transported to the jet mill in the third pulverization step, and pulverization is performed by collision between objects to be pulverized using a jet stream. The same operation as in Example 3 was performed except that the air pressure was changed to 0.15 MPa in order to obtain a particle size of 75 μm, and a water absorbent resin powder (5) having a volume average particle size of 75 μm was continuously obtained. Obtained. The obtained water-absorbent resin powder (5) was measured according to the method for measuring the fine particle size water absorption rate and fine particle size water absorption rate. The measurement results are shown in Table 1.

[Example 6]
In Example 3, the same operation as in Example 3 was carried out except that the pulverization was terminated without being sent to the third pulverization step after being finely divided by the flash mill (secondary pulverization), and the volume average was continuously obtained. Water-absorbing resin powder (6) having a particle diameter of 109 μm was obtained. The obtained water-absorbent resin powder (6) was measured according to the measurement method of the fine particle size water absorption rate and fine particle size water absorption rate. The measurement results are shown in Table 1.

[Comparative Example 3]
In Example 3, the same operation as in Example 3 was carried out except that the pulverization was completed without being sent to the second pulverization step after being finely divided (primary pulverization) by a pin mill, and the volume average particle diameter was continuously obtained. A comparative water absorbent resin powder (3) of 191 μm was obtained.

  The obtained comparative water-absorbent resin powder (3) was measured according to the measurement method of the fine particle size water absorption rate and fine particle size water absorption rate. The measurement results are shown in Table 1.

  Note 1) In the water absorption rate in Table 1, × indicates that no end point is observed even after 10 minutes.

Note 2) FGA1 is water absorption resin powder / silica 1/1 (weight ratio) artificial seawater absorption ratio (30 minutes value), FGA absorbs silica-derived water absorption from FGA1 (water absorption ratio of 16.8 g / g) Artificial seawater absorption ratio of the water-absorbent resin powder itself corrected by subtracting (30 minutes value)
(Figure 1)

  FIG. 1 is a diagram comparing the volume average particle size and the fine particle size water absorption ratio of the same polymer (Examples 3 to 6 and Comparative Example 3).

(Summary)
As shown in Table 1 and FIG. 1, a comparison between Example 1 (FGA = 21.9 g / g) and Comparative Example 1 (12.4 g / g), Example 2 (FGA = 39.2 g / g) Comparison with Comparative Example 2 (33.0 g / g), Examples 3 to 6 (FGA = 32.6 to 37.0 g / g) and Comparative Example 3 (21.2 g / g) also shown in FIG. As is clear from the comparison, it can be seen that even with the same water-absorbing resin, when the volume average particle diameter after pulverization is critically 1 to 150 μm, both the water absorption speed and the water absorption ratio (FGA) are greatly improved. It is well known that the water absorption speed is improved with a finer particle diameter (Non-patent Document 1), but it is not known that the artificial seawater absorption magnification (FGA) is improved with a volume average particle diameter of 1 to 150 μm.

  In the present invention, by finely pulverizing to a specific particle size, in particular, by pulverizing a polysulfonic acid-based (or AMPS water-absorbing resin) to a specific particle size, the water absorption speed and the water absorption ratio are improved, and it is combined with rubber. A suitable water absorbent resin can be obtained.

Claims (11)

A method of pulverizing a dry polymer of a water absorbent resin using a dry pulverizer, wherein at least two different types of impact pulverizers are used, the first pulverization step and the impact different from the first pulverization step. and possess a second milling step using equation pulverizer, the volume average particle diameter of the particles obtained by the pulverizing method is 1-150 [mu] m,
A method for pulverizing a water-absorbing resin, further comprising a classification step of removing large particles from the processed product in the first pulverization step, and re-pulverizing the removed large particles in the first pulverization step . After the first milling step treated product was treated with the classification step, the second milling step process, grinding method according to claim 1. The pulverization method according to claim 1 or 2, wherein the volume average particle size of the first pulverized step processed product is 1000 µm or less, and the volume average particle size of the second pulverized step processed product is 150 µm or less.   It has a 3rd crushing process which grinds the 2nd crushing process processed goods using an impact type crusher of a form different from a crusher used in the 1st crushing process and the 2nd crushing process. 4. The grinding method according to any one of 3 above. Wherein the fluidized-bed pulverizer is used one of the impact mill, grinding method according to any one of claims 1 to 4. The pulverization method according to any one of claims 3 to 5, wherein a gas having a dew point of 0 ° C or lower is supplied into the pulverization chamber in at least one of the first pulverization step to the third pulverization step. The dried polymer is supplied to the first milling step after crushing, grinding method according to any one of claims 1-6.   The pulverization method according to any one of claims 1 to 7, wherein a temperature of a supply to the first pulverization step is 100 ° C or lower. Dry polymer of the water-absorbing resin is dried at flow band dryer, and formed by coarse grinding process of a block-like dry product (0-order pulverization) is provided in front of the first grinding step, of the preceding claims The grinding method according to any one of the above. Method for producing a water-absorbent resin particles having a grinding method according to any one of claims 1-9. The manufacturing method according to claim 10, wherein the water absorbent resin includes the following water absorbent resin A and / or water absorbent resin B.
Water-absorbing resin A: Water-absorbing water containing 80% by mass or more of polyacrylic acid (salt) -based crosslinked polymer having a neutralization rate of 50% by mol or more (repeating units other than acrylic acid are 0 to 50% by mol of the whole) Resin Water-absorbing resin B: Monomer containing 20 to 90 mol% of sulfonic acid group-containing acrylamide monomer and salt thereof and 80 to 10 mol% of one or more of acrylic acid and acrylate (other monomers are all A water-absorbent resin containing 80% by mass or more of a crosslinked polymer obtained by copolymerization of 0 to 50 mol% in the monomer.