WO2004113452A1 - Water absorbent resin compostion and production method thereof - Google Patents
Water absorbent resin compostion and production method thereof Download PDFInfo
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- WO2004113452A1 WO2004113452A1 PCT/JP2004/009242 JP2004009242W WO2004113452A1 WO 2004113452 A1 WO2004113452 A1 WO 2004113452A1 JP 2004009242 W JP2004009242 W JP 2004009242W WO 2004113452 A1 WO2004113452 A1 WO 2004113452A1
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- absorbent resin
- water absorbent
- multivalent metal
- resin composition
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
- C08K3/00—Use of inorganic substances as compounding ingredients
- C08K3/10—Metal compounds
-
- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61L—METHODS OR APPARATUS FOR STERILISING MATERIALS OR OBJECTS IN GENERAL; DISINFECTION, STERILISATION OR DEODORISATION OF AIR; CHEMICAL ASPECTS OF BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES; MATERIALS FOR BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES
- A61L15/00—Chemical aspects of, or use of materials for, bandages, dressings or absorbent pads
- A61L15/16—Bandages, dressings or absorbent pads for physiological fluids such as urine or blood, e.g. sanitary towels, tampons
- A61L15/42—Use of materials characterised by their function or physical properties
- A61L15/60—Liquid-swellable gel-forming materials, e.g. super-absorbents
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L101/00—Compositions of unspecified macromolecular compounds
- C08L101/12—Compositions of unspecified macromolecular compounds characterised by physical features, e.g. anisotropy, viscosity or electrical conductivity
- C08L101/14—Compositions of unspecified macromolecular compounds characterised by physical features, e.g. anisotropy, viscosity or electrical conductivity the macromolecular compounds being water soluble or water swellable, e.g. aqueous gels
-
- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61F—FILTERS IMPLANTABLE INTO BLOOD VESSELS; PROSTHESES; DEVICES PROVIDING PATENCY TO, OR PREVENTING COLLAPSING OF, TUBULAR STRUCTURES OF THE BODY, e.g. STENTS; ORTHOPAEDIC, NURSING OR CONTRACEPTIVE DEVICES; FOMENTATION; TREATMENT OR PROTECTION OF EYES OR EARS; BANDAGES, DRESSINGS OR ABSORBENT PADS; FIRST-AID KITS
- A61F13/00—Bandages or dressings; Absorbent pads
- A61F13/15—Absorbent pads, e.g. sanitary towels, swabs or tampons for external or internal application to the body; Supporting or fastening means therefor; Tampon applicators
- A61F13/53—Absorbent pads, e.g. sanitary towels, swabs or tampons for external or internal application to the body; Supporting or fastening means therefor; Tampon applicators characterised by the absorbing medium
- A61F2013/530481—Absorbent pads, e.g. sanitary towels, swabs or tampons for external or internal application to the body; Supporting or fastening means therefor; Tampon applicators characterised by the absorbing medium having superabsorbent materials, i.e. highly absorbent polymer gel materials
- A61F2013/530671—Absorbent pads, e.g. sanitary towels, swabs or tampons for external or internal application to the body; Supporting or fastening means therefor; Tampon applicators characterised by the absorbing medium having superabsorbent materials, i.e. highly absorbent polymer gel materials being mixed with mineral or inert material, e.g. "introfying particles"
- A61F2013/530686—Absorbent pads, e.g. sanitary towels, swabs or tampons for external or internal application to the body; Supporting or fastening means therefor; Tampon applicators characterised by the absorbing medium having superabsorbent materials, i.e. highly absorbent polymer gel materials being mixed with mineral or inert material, e.g. "introfying particles" with metallic soluble salts, e.g. Na, K, Mg chloride
-
- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61F—FILTERS IMPLANTABLE INTO BLOOD VESSELS; PROSTHESES; DEVICES PROVIDING PATENCY TO, OR PREVENTING COLLAPSING OF, TUBULAR STRUCTURES OF THE BODY, e.g. STENTS; ORTHOPAEDIC, NURSING OR CONTRACEPTIVE DEVICES; FOMENTATION; TREATMENT OR PROTECTION OF EYES OR EARS; BANDAGES, DRESSINGS OR ABSORBENT PADS; FIRST-AID KITS
- A61F13/00—Bandages or dressings; Absorbent pads
- A61F13/15—Absorbent pads, e.g. sanitary towels, swabs or tampons for external or internal application to the body; Supporting or fastening means therefor; Tampon applicators
- A61F13/53—Absorbent pads, e.g. sanitary towels, swabs or tampons for external or internal application to the body; Supporting or fastening means therefor; Tampon applicators characterised by the absorbing medium
- A61F2013/530481—Absorbent pads, e.g. sanitary towels, swabs or tampons for external or internal application to the body; Supporting or fastening means therefor; Tampon applicators characterised by the absorbing medium having superabsorbent materials, i.e. highly absorbent polymer gel materials
- A61F2013/530708—Absorbent pads, e.g. sanitary towels, swabs or tampons for external or internal application to the body; Supporting or fastening means therefor; Tampon applicators characterised by the absorbing medium having superabsorbent materials, i.e. highly absorbent polymer gel materials characterized by the absorbency properties
- A61F2013/530737—Absorbent pads, e.g. sanitary towels, swabs or tampons for external or internal application to the body; Supporting or fastening means therefor; Tampon applicators characterised by the absorbing medium having superabsorbent materials, i.e. highly absorbent polymer gel materials characterized by the absorbency properties by the absorbent capacity
- A61F2013/530744—Absorbent pads, e.g. sanitary towels, swabs or tampons for external or internal application to the body; Supporting or fastening means therefor; Tampon applicators characterised by the absorbing medium having superabsorbent materials, i.e. highly absorbent polymer gel materials characterized by the absorbency properties by the absorbent capacity by the absorbency under load
Definitions
- the present invention relates to a water absorbent resin and a production method thereof. More specifically, the present invention relates to (i) a water absorbent resin composition favorably used in disposable paper diapers, pads, or women's sanitary napkins, and (ii) a production method of the water absorbent resin composition.
- a water absorbent resin is widely used as a main component of sanitary materials (absorbent articles) such as paper diapers, sanitary napkins, incontinence pads and the like, in order to absorb body fluids (e . g. urine and blood) .
- water absorbent resin are (i) cross-linked partially neutralized polyacrylic acid; (ii) a hydrolyzed starch-acrylonitrile graft polymer; (iii) a neutralized starch-acrylic graft polymer; (iv) a saponified vinyl acetate-acrylic ester copolymer; (v) cross-linked carboxymethylcellulose; . (vi) hydrolyzed acrylonitrile copolymer or hydrolyzed acrylamide copolymer, or cross-linked acrylonitrile copolymer or cross-linked acrylamide copolymer; (vii) a cross-linked cationic monomer,
- the water absorbent resin has a high absorbency with respect to an aqueous liquid. However, due to its high absorbency, the water absorbent resin absorbs also moisture in air (moisture absorption) . Thus, particles of the water absorbent resin are coagulated with each other, which results in a blocking phenomenon in which the water absorbent resin loses fluidity as powder.
- the moisture absorption blocking phenomenon raises the following problems: at the time of production of the water absorbent resin and at the time of production of a sanitary material such as a disposable paper diaper using the water absorbent resin, the blocking phenomenon occurs in a storage hopper or a transportation line, or the water absorbent resin adheres to a production apparatus, so that the blocking or adhering water absorbent resin becomes much less treatable. As a result, it is impossible to stably manufacture the product. Then, in order to prevent the blocking phenomenon occurring at the time of moisture absorption, a method in which an inorganic compound is added to the water absorbent resin is conventionally adopted.
- Examples of the method are: a method in which an inorganic powder is mixed with such a water absorbent resin that approximately 60 wt% or less polymer particles pass through a sieve of 300 ⁇ m in mesh (Published Japanese
- examples of a method in which an inorganic compound is added to the water absorbent resin in order to improve a water-absorbing ability of the water absorbent resin powder include: a method in which a multivalent metal salt such as aluminum sulfate and a water absorbent resin are dry-blended and thus obtained mixture is brought into contact with a binding agent (water or the like) so as to produce such a water absorbent resin that a gel having absorbed water has elasticity and a gel blocking phenomenon
- Patent Application No. 523287/2001 (Tokuhyo 2001 -523287)) ; a water-insoluble swelling hydrogel obtained by coating a water-insoluble swelling hydrogel, having specific absorbency under pressure and having gel strength, with a three-dimensional or electrostatic spacer (U. S. Patent No. 2002 / 0128618) ; a water absorbent resin secondarily cross-linked by an organic surface cross-linking agent aqueous solution and a cation aqueous solution (Published Japanese Translations of International Publication of Patent Application No. 538275/2002 (Tokuhyo 2002-538275)) ; and the like.
- the sanitary material such as the sanitary napkin and the like using the water absorbent resin has higher performance and a thinner size, and an amount of the water absorbent resin used for each sanitary material tends to increase, and also a weight % of the water absorbent resin tends to increase with respect to the whole absorber constituted of the water absorbent resin and a hydrophilic fiber. That is, by using (i) a smaller amount of a hydrophilic fiber whose bulk density is low and (ii) a larger amount of a water absorbent resin having a superior water absorbent property and high bulk density, a ratio of the water absorbent resin contained in the absorber is increased, thereby making the sanitary material thinner without decreasing an amount of water absorption.
- the sanitary material which includes a smaller amount of the hydrophilic fiber and a larger amount of the water absorbent resin is preferable merely in terms of liquid storage, but raises problems in terms of distribution and diffusion of liquid in actual use in diapers. That is, when a large amount of the water absorbent resin is used, the water absorbent resin becomes soft and gelatinous upon absorbing water. This causes a gel blocking phenomenon. As a result, a liquid diffusing property of the diaper significantly drops. In order to avoid such phenomenon and to keep the absorbent property of the absorber high, a ratio of the hydrophilic fiber and the water absorbent resin is limited, so that there is a limit in making the sanitary material thinner.
- a water absorbent resin is treated with a metal compound so as to improve a liquid diffusing property of water absorbent resin powder.
- the method include: a method in which multivalent metal salt such as aluminum sulfate is dry-blended with a water absorbent resin, and is brought into contact with a binding agent (water or the like) , thereby producing a water absorbent resin, having elasticity, which hardly causes the gel blocking (WO 98/ 48857 pamphlet); a method in which a water absorbent resin is secondarily cross-linked with a water-soluble organic surface cross-linking agent and water-soluble cation (Tokuhyo 2002-538275 and Tokuhyo
- a high water absorbent resin composition which includes a high water absorbent resin and fine powder made up of hydrated oxides at least partially containing two types of metals (M l and M2) so as to have a -M 1 -0-M2- bond (Japanese Unexamined Patent Publication No. 147724/ 1998 (Tokukaihei 10- 147724)) ; and the like.
- the present invention was devised in view of the foregoing conventional problems, and the obj ect of the present invention is to provide (i) a water absorbent resin composition which is free from any clump of particles even in high humidity and is superior in absorbent properties such as an absorbency and a diffusing absorbency under pressure and has particles whose surfaces are secondarily cross-linked evenly, and (ii) a production method of the water absorbent resin composition.
- the water absorbent resin composition of the present invention is a water absorbent resin composition, whose main component is a particulate water absorbent resin (A) having a cross-linking structure obtained by polymerizing an unsaturated monomer containing an acid group, said particulate water absorbent resin (A) being cross-linked in a vicinity of a surface of the water absorbent resin (A) , wherein: the water absorbent resin composition contains 95 wt % or more of particles whose particle diameter is less than 850 ⁇ m and not less than 106 . ⁇ m, and a weight average particle diameter of the particles is less than 500 ⁇ m and not less than 300 ⁇ m, and a logarithmic standard deviation ( ⁇ ) of a particle size distribution of the water absorbent resin composition is 0.45 or less, and a water-soluble component of the water absorbent composition is 35 wt % or less, and the water absorbent resin composition includes a multivalent metal component, and an extraction rate of the multivalent metal component is 5.0 wt % or
- the particulate water absorbent resin (A) is a particulate water absorbent resin in which the vicinity of the surface is further cross-linked by a surface cross-linking agent containing a polyol.
- a moisture absorption blocking ratio a is 30 % or less when the water absorbent resin composition is left at 25°C in a relative humidity of 90 % for an hour.
- a centrifuge retention capacity (CRC) at which the water absorbent resin composition absorbs 0.90 wt % of a physiological saline without load for 30 minutes is 25 g/g or more
- a diffusion absorbency under pressure (DAP) at which the water absorbent resin composition absorbs 0.90 wt % of a physiological saline at 1.9kPa for 60 minutes is 20 g/ g or more.
- the absorber of the present includes the water absorbent resin composition and a hydrophilic fiber so that an amount of the water absorbent resin composition (core concentration) is 20 wt % or more with respect to a total amount of the water absorbent resin composition and the hydrophilic fiber.
- the absorbent article of the present invention includes the absorber, a liquid-permeable surface sheet, and a liquid-impermeable back sheet.
- the method of the present invention for producing the water absorbent resin composition includes the steps of: adding a solution of an aqueous multivalent metal compound (B) to a particulate water absorbent resin (A) , having a cross-linking structure obtained by polymerizing an unsaturated monomer containing an acid group, which is cross-linked in a vicinity of a surface of the particulate water absorbent resin (A); and mixing the solution of the aqueous multivalent metal compound (B) with the particulate water absorbent resin (A), wherein: the particulate water absorbent resin (A) contains 95 wt % or more of the particles whose particle diameter is less than 850 ⁇ m and not less than 106 ⁇ m, and a weight average particle diameter of the particles is less than 500 ⁇ m and not less than 300 ⁇ m, and a logarithmic standard deviation ( ⁇ ) of a particle size distribution of the particulate water absorbent resin (A) is
- a water-soluble component of the particulate water absorbent resin (A) is 35 wt % or less
- an amount of a multivalent metal component contained in the solution of the aqueous multivalent metal compound (B) is 0.001 to 10 wt % with respect to the particulate water absorbent resin (A)
- a concentration of the aqueous multivalent metal compound (B) in the solution is 0.40 or more with respect to a saturated concentration of the aqueous multivalent metal compound (B) in the solution
- temperature of the particulate water absorbent resin (A) is 50°C or higher and lower than 100°C
- / or temperature of the solution of the aqueous multivalent metal compound (B) is 30°C or higher and lower than 100°C.
- the inventors of the present invention earnestly studied the water absorbent resin composition so as to realize (i) a superior moisture absorption blocking property which less causes particles to clump in high humidity and (ii) a superior liquid permeation/ liquid diffusing property at the same time.
- the method so as to includes the steps of: mixing a particulate water absorbent resin whose main component is a polymer having a cross-linking structure obtained by polymerizing acrylic acid and/ or its salt, a specific amount of an aqueous solution of a multivalent metal compound, and an organic surface cross-linking agent; and heating a mixture obtained in the mixing step at 150 to 300°C, so as to cross-link a vicinity of a surface of the particulate water absorbent resin, wherein the particulate water absorbent resin has a specific particle size distribution, and a concentration of a multivalent metal component contained in the aqueous solution of the multivalent metal compound (B) is
- the inventors of the present invention found that: the water absorbent resin composition treated by using a surface treatment agent whose concentration of a multivalent metal component is high has a much higher saline flow conductivity (SFC : indicative of a liquid permeation rate under pressure) than that of a water absorbent resin composition whose surface is treated with a surface treatment agent having a known concentration.
- SFC saline flow conductivity
- the precursor of the present invention is a mixture of the particulate water absorbent resin, the aqueous solution of the multivalent metal compound, and the organic surface cross-linking agent.
- the humidification of the present invention means to mix an aqueous solution of a multivalent metal compound and an organic surface cross-linking agent with a particulate water absorbent resin.
- the saline of the present invention is an aqueous solution obtained by dissolving sodium chloride in water.
- the method of the present invention for producing the water absorbent resin composition includes the steps of: mixing a particulate water absorbent resin (A) having a cross-linking structure obtained by polymerizing an unsaturated monomer containing an acid group, a solution of an aqueous multivalent metal compound (B) , and an organic surface cross-linking agent (C) ; and heating a mixture that has been obtained in the mixing step at 150 to 300°C so as to cross-link a vicinity of a surface of the particulate water absorbent resin (A) , wherein: the particulate water absorbent resin (A) contains 95 wt % or more of the particles whose particle diameter is less than 850 ⁇ m and not less than 106 ⁇ m, and a logarithmic standard deviation ( ⁇ ) of a particle size distribution of the particulate water absorbent resin (A) is 0.45 or less, and an amount of a multivalent metal component contained in the solution of the aqueous multivalent metal compound (B) is 0.001 to 10
- the method of the present invention for producing the water absorbent resin composition includes the step of heating a precursor (D) obtained by mixing a particulate water absorbent resin (A) having a cross-linking structure obtained by polymerizing an unsaturated monomer containing an acid radical, a solution of a multivalent metal compound (B) , and an organic surface cross-linking agent at 150 to 300°C so as to cross-link a vicinity of a surface of the particulate water absorbent resin (A) , wherein: the particulate water absorbent resin (A) contains 95 wt % or more of the particles whose particle diameter is less than 850 ⁇ m and not less than 106 ⁇ m, and a logarithmic standard deviation ( ⁇ ) of a particle size distribution of the particulate water absorbent resin (A) is 0.45 or less, and an amount of a multivalent metal component contained in the solution of the multivalent metal compound (B) is 0.00 1 to 10 w
- a main , component of the water absorbent resin composition is a polymer having a cross-linking structure obtained by polymerizing acrylic acid and/ or salt thereof.
- a concentration of the multivalent metal component contained in the solution of the multivalent metal compound (B) is at least 1 .80 wt %.
- the solution of the multivalent metal compound (B) and/or the organic surface cross-linking agent is heated at 30°C or higher.
- the organic surface cross-linking agent includes a multivalent alcohol.
- the multivalent metal component of the multivalent metal compound (B) includes one or more metals selected from bivalent or further multivalent typical metals and transition metals whose group numbers are 4 to 12.
- the multivalent metal component of the multivalent metal compound (B) is aluminum.
- Fig. 1 is a cross sectional view schematically showing a measuring apparatus used to measure an absorbency against pressure (AAP) of the water absorbent resin composition.
- AAP absorbency against pressure
- Fig. 2 is a cross sectional view schematically showing a measuring apparatus used to measure a saline flow conductivity (SFC) of the water absorbent resin composition.
- SFC saline flow conductivity
- a water absorbent resin composition according to the present embodiment includes a particulate water absorbent resin (A) and a multivalent metal component (B) .
- the water absorbent resin composition of the present embodiment is a composition which includes a water absorbent resin as a main component, and includes 80 to 100 wt % of the water absorbent resin, more preferably 90 to 100 wt % of the water absorbent resin.
- the water absorbent resin composition is favorably used in sanitary materials such as paper diapers, sanitary napkins, incontinence pads, medical pads, and the like. The following description will detail (I) the water absorbent resin (A) and (II) the multivalent metal component (B) .
- the "particulate water absorbent resin (A)" is constituted of spherical or amorphous particles of water-insoluble water-swelling hydrogel formation polymer (hereinafter, referred to also as a water absorbent resin) which can be obtained by polymerizing a hydrophilic monomer.
- the water-swelling property means a condition under which the water absorbent resin necessarily absorbs a large amount of water whose weight is five times as much as a weight of the water absorbent resin itself, preferably 50 to 1000 times as much as the weight of the water absorbent resin itself, in an ion exchange water.
- the water-insoluble property means a condition under which 5 wt % or more and 50 wt % or less, more preferably 5 wt % or more and 25 wt % or less, further more preferably 5 wt % or more and 20 wt % or less, particularly preferably 5 wt % or more and 15 wt % or less, most preferably 5 wt % or more and 10 wt % or less of a water-soluble component (water-soluble polymer) is contained in the water absorbent resin.
- the water-insoluble water-swelling hydrogel formation polymer has a spherical or indeterminate particulate shape.
- water-insoluble water-swelling hydrogel formation polymer includes: a partially neutralized cross-linked polyacrylic acid polymer (U.S . Patent No. 4625001 , U.S. Patent No. 4654039, U.S. Patent No. 5250640,
- the water absorbent resin of the present embodiment is constituted of a cross-linked polyacrylic acid (salt) polymer including acrylic acid and/ or salt thereof as a main component.
- the "main component" of the present embodiment is defined as follows: in case where a certain component "a" is included in “B", as long as “B” includes 30 wt % or more of the component "a” with respect to the whole amount of "B", the component
- the cross-linked polyacrylic acid (salt) polymer of the present embodiment is a cross-linked polymer in which 50 mol % or more and 100 mol % or less of acrylic acid and/or salt thereof is included in a monomer component, preferably 70 mol % or more and 100 mol % or less, more preferably 90 mol % or more and 100 mol % or less of acrylic acid and/or salt thereof is included in the monomer component. Further, it is preferable that 50 to
- the water absorbent resin for forming salt may be neutralized in a monomer phase before polymerization, or may be neutralized during and after polymerization, or these processes may be combined with each other.
- the particulate water absorbent resin (A) it is possible to use a water absorbent resin having a cross-linking structure obtained by polymerizing an unsaturated monomer containing an acid radical, in terms of the absorbent property.
- the unsaturated monomer containing an acid group used in the present embodiment includes a monomer containing an acid group in polymerization and a monomer such as acrylonitrile which becomes an acid group by being hydrolyzed after polymerization.
- water absorbent resin examples are one kind or two or more kinds of: partially neutralized polyacrylic acid polymer; hydrolyzed starch-acrylonitrile graft polymer; starch-acrylic acid graft polymer; saponified vinyl acetate-acrylic acid ester copolymer; hydrolyzed acrylonitrile copolymer or hydrolyzed acrylamide copolymer, or cross-linked acrylonitrile copolymer or cross-linked acrylamide copolymer; denaturated carboxyl-group-containing cross-linked polyvinyl alcohol; cross-linked isobutylene-maleic anhydride copolymer; and the like. It is preferable to use partially neutralized polyacrylic acid polymer obtained by polymerizing and cross-linking a monomer containing acrylic acid and/ or its salt (neutralized acrylic acid) as a main component.
- the partially neutralized polyacrylic acid polymer may be obtained by copolymerizing a monomer (acrylic acid and/ or salt thereof) used as a main component with other monomer as required.
- a monomer acrylic acid and/ or salt thereof
- other monomer include: an anionic unsaturated monomer such as methacrylic acid, fumaric acid, crotonic acid, itaconic acid, maleic acid, vinyl sulfonic acid, styrene sulfonic acid,
- 2-(meth)acryloylethane sulfonic acid 2-(meth)acryloylepropane sulfonic acid, and salt thereof; a nonionic hydrophilic-group-containing unsaturated monomer such as N-vinyl-2-pyridone, N-viniyl acetamide, methoxypolyethylene glycol(meth)acrylate, polyethylene glycol (meth)acrylate, isobutylene, lauryl(meth)acrylate, acrylamide, (meth)acrylamide, N-ethyl (meth)acrylamide, N-n-propyl (meth)acrylamide, N-isopropyl (meth)acrylamide, N,N-dimethyl
- (meth)acrylate polyethyleneglycol mono (meth)acrylate, vinylpyridine, N-vinylpyrrolidone, N-acryloylpiperidine, and
- N-acryloylpyrrolidine N-acryloylpyrrolidine; and cationic unsaturated monomer such as N,N-dimethylaminoethyl (meth)acrylate,
- an amount of the monomer other than acrylic acid is 0 to 30 mol %, preferably 0 to 10 mol %, with respect to all the monomers (contained in the water absorbent resin) , thereby further improving an absorbent property of a product water absorbent resin (composition) and producing the water absorbent resin (composition) at lower cost.
- Examples of a method for introducing a cross-linking structure into the water absorbent resin used in the present embodiment are as follows: self cross-linking is proceeded without using a cross-linking agent; not only the monomer but also an internal cross-linking agent having two or more polymerizable unsaturated groups or two or more reactive groups is copolymerized or reacted with the particulate water absorbent resin; and a. similar manner. It is preferable to copolymerize or react the internal cross-linking agent.
- Examples of the internal cross-linking agent include:
- These internal cross-linking agents may be used either independently or in a suitable combination of two or more kinds.
- the internal cross-linking agent may be added to the reaction system either at once or in separate doses.
- a cross-linking monomer including not less than two polymerizable unsaturated groups is always used for the polymerization, taking into account the absorption characteristics or other properties of the product water absorbent or the product water absorbent resin composition.
- An amount of internal cross-linking agent used is preferably 0.001 to 3 mol %, more preferably 0.001 to 2 mol %, further more preferably 0.005 to 2 mol %, still more preferably 0.005 to 0.5 mol %, further still more preferably 0.01 to 1 mol %, particularly preferably 0.01 to 0.2 mol %, more particularly preferably 0.03 to 0. 15 mol %, and most preferably 0.03 to 0.5 mol %, with respect to a total number of moles of all the unsaturated monomers (excluding the cross-linking agent) .
- the amount of the internal cross-linking agent used is less than 0.001 mol %, or in case where the internal cross-linking agent exceeds 3 mol %, it may be impossible to obtain the sufficient absorbent property.
- the internal cross-linking agent When the internal cross-linking agent is used to form a cross-linking structure inside the water absorbent resin, the internal cross-linking agent is added to the reaction system before, during, or after the polymerization of the unsaturated monomer, or after the neutralization of the unsaturated monomer or the polymer.
- polymerization it is possible to add (i) for example 0 to 30 wt % (with respect to the monomer) of hydrophilic polymers such as a mixture of starch and cellulose, a derivative of starch and cellulose, polyvinyl alcohol, polyacrylic acid (salt) , cross-linked polyacrylic acid (salt) , and the like or (ii) for example 0 to 5 wt % (with respect to the monomer) of a chain transfer agent such as hypophosphorous acid (salt) .
- a chain transfer agent such as hypophosphorous acid (salt)
- more preferable methods of polymerization are aqueous polymerization and reversed suspension polymerization that are performed under such condition that an aqueous solution of the monomer is used.
- the concentration of the monomer contained in the aqueous solution (hereinafter, referred to as monomer aqueous solution) is determined depending on temperature of the aqueous solution and a type of the monomer, and is not particularly limited. However, the concentration of the monomer is preferably 10 to 70 mass %, more preferably 20 to 60 mass %. Further, in carrying out the aqueous solution polymerization, solvent other than water may be used together as required, and a type of the solvent used together is not particularly limited.
- the reversed suspension polymerization is a polymerization method in which a monomer aqueous solution is suspended in a hydrophobic organic solvent, and is recited for example in U.S. Patent No. 4093776, U.S. Patent No. 4367323 , U. S. Patent No-. 4446261 , U. S . Patent No. 4683274, U.S. Patent No. 5244735, and the like.
- the aqueous solution polymerization is a method in which the monomer aqueous solution is polymerized without using a dispersion solvent, and is recited for example in U.S. Patent No. 4625001 , U.S. Patent No. 4873299, U.S. Patent No. 4286082, U.S.
- Patent No. 4973632 U. S . Patent No. 4985518, U. S. Patent No .
- Patent No. 081 1636 European Patent No. 0955086, European Patent No. 0922717, European Patent No. 1 178059, and the like. Monomers, initiators, and the like, that are used in these polymerization methods as examples are applicable to the present embodiment.
- a radical polymerization initiator such as potassium persulfate, ammonium persulfate, sodium persulfate, t-butylhydroperoxide, hydrogen peroxide, 2,2'-azobis
- an amount of polymerization initiators used is ordinarily 0.001 to 2 mol %, preferably 0.01 to 0.1 mol % (with respect to all the monomers) .
- redox polymerization may be carried out by using a reducer such as sodium sulfite, sodium bisulfite, ferrous sulfate, L-ascorbic acid, and the like, together.
- a reducer such as sodium sulfite, sodium bisulfite, ferrous sulfate, L-ascorbic acid, and the like.
- an amount of polymerization initiators used is ordinarily 0.001 to 2 mol %, preferably 0.01 to 0. 1 mol % (with respect to all the monomers) .
- the resultant is ordinarily a cross-linked polymer in an aqueous gel phase, and is dried as required.
- the cross-linked polymer in the aqueous gel phase is pulverized before and/ or after the drying, thereby obtaining the water absorbent resin (A) .
- the drying treatment is performed ordinarily at 60°C to 250°C, preferably at 100°C to 220°C, more preferably 120°C to 200°C.
- the drying time depends on a surface area and a moisture content of the polymer and a type of the dryer, and is set so as to realize a desired moisture content.
- the moisture content (defined by a moisture content found by measuring a drying loss after drying the water absorbent resin or the water absorbent resin composition that has been left at 180°C for three hours) of the water absorbent resin or the water absorbent resin composition, whose surface has been or has not been cross-linked, which is used in the present embodiment, is not particularly limited.
- the moisture content is preferably 0.2 to 30 wt %, more preferably 0.3 to 15 wt %, further more preferably 0.5 to 10 wt % so that the water absorbent resin is in a powder phase, in terms of properties of the obtained water absorbent resin composition.
- (A) whose surface has been or has not been cross-linked is not particularly limited such as a spherical shape or coagulum shape made up of spherical particles, a granular shape, an indeterminate shape, and the like.
- a spherical shape or coagulum shape made up of spherical particles, a granular shape, an indeterminate shape, and the like.
- an indeterminate granular shape obtained through the pulverizing step is preferable.
- its bulk density (defined by JIS K-3362) 0.40 to 0.80 g/ml, more preferably
- the water absorbent resin (A) in the present embodiment can be obtained by cross-linking a surface of a water absorbent resin, which has been subjected to the internal cross-linking process and the dry process, by using the organic surface cross-linking agent.
- the following description explains the organic surface cross-linking agent.
- (II) Organic surface cross-linking agent (C)
- cross-linking agents for cross-linking the surface.
- cross-linking agents (a) polyol compounds, (b) epoxy compounds, (c) multivalent amine compounds, (d) condensates of the multivalent amine compounds and haloepoxy compounds, (e) oxazoline compounds, (f) mono, di, or poly oxazolidine compounds, (g) alkylene carbonate compounds, (h) cyclic urea compounds, (i) trimethylene oxide compounds, (j) and the like .
- organic surface cross-linking agent used in the present embodiment, specific examples are given in U. S.
- Patent No. 6228930 U. S Patent No. 6071976, U. S Patent No .
- organic surface cross-linking agent (C) examples include : polyol compounds such as ethyleneglycol, diethyleneglycol, propyleneglycol, triethyleneglycol, tetraethyleneglycol, polyethyleneglycol, 1 ,3-propanediol, dipropyleneglycol,
- epoxy compounds such as ethyleneglycol diglycidyl ether, polyethylene glycidyl ether, glycerol polyglycidyl ether, diglycerol polyglycidyl ether, polyglycerol polyglycidyl ether, propyleneglycol diglycidyl ether, polypropyleneglycol diglycidyl ether, and glycidol; multivalent amine compounds such as ethylenediamine, diethylenetriamine, triethylenetetramine, tetraethylenepentamine, pentaethylenehexamine,
- the multivalent alcohol is preferable since it is superior in terms of safety and it improves the hydrophilic property of the particle surface of the water absorbent resin. It is preferable that the multivalent alcohol contains 2 to 10 carbon atoms, preferably
- the polyhydric alcohol reacts with the particulate water absorbent resin as the surface cross-linking agent so as to form an ester bond. Further, due to the reaction, some hydroxyl groups of the polyhydric alcohol do not react, so that the hydroxyl groups remain on the surface of the particulate water absorbent resin. Therefore, the hydroxyl groups, contained in the polyhydric alcohol, which do not react, improve the hydrophilic property on the surface of the particulate water absorbent resin.
- An amount of the organic surface cross-linking agent (C) used depends on compounds used and a combination thereof, but is preferably 0.01 weight parts to 10 weight parts, more preferably 0.001 weight parts to 5 weight parts, with respect to 100 weight parts of the water absorbent resin. When the amount of the organic surface cross-linking agent (C) is less than 0.001 weight parts, the moisture absorption blocking property and the liquid permeability/ liquid diffusing property are not sufficiently improved. When the amount of the organic surface cross-linking agent (C) is more than 10 weight parts, a centrifuge retention capacity (CRC) , a diffusing absorbency under pressure (DAP) , and an absorbency against pressure (AAP) significantly drop.
- CRC centrifuge retention capacity
- DAP diffusing absorbency under pressure
- AAP absorbency against pressure
- water it is preferable to use water as a solvent in combination with the surface cross-linking agent in performing the surface cross-linking treatment.
- an amount of the water to be used depends on how much moisture content of the water absorbent resin to be used has. In general, with respect to 100 weight parts of the water absorbent resin, the amount of the water to be used is in a range of 0.5 weight parts to 20 weight parts, and preferably 0.5 weight parts to 5 weight parts. Further, in the present embodiment, it is possible to use a hydrophilic organic solvent other than water.
- An amount of the hydrophilic organic solvent is in a range of 0 weight part to 10 weight pars, preferably in a range of 0 weight part to 5 weight parts, and more preferably in a range of 0 weight part to 3 weight parts with respect to 100 weight parts of the water absorbent resin.
- the surface cross-linking agent is mixed with water and/ or the hydrophilic organic solvent as required, and the mixture is sprayed or dropped directly to the water absorbent resin. It is more preferable to spray the mixture directly to the water absorbent resin.
- An average diameter of liquid droplets to be sprayed is preferably 300 ⁇ m or less, and more preferably 200 ⁇ m or less.
- a heating temperature is in a range of 100°C to 250°C, more preferably in a range of 150°C to 250°C; and a heating time is preferably in a range of one minute to two hours. Examples of appropriate combinations of the heating temperature and heating time are: (a) 180°C for 0. 1 to 1.5 hours, and (b) 200°C for 0. 1 to one hour.
- the water absorbent resin composition of the present embodiment is obtained by adding and mixing a solution of the water-soluble multivalent metal compound (B) to the particulate water absorbent resin (A) obtained in the foregoing manner.
- the multivalent metal compound (B) of the present embodiment is a compound having bivalent or further multivalent metal atoms.
- the multivalent metal component of the present embodiment is constituted of bivalent or further multivalent metal atoms contained in the multivalent metal compound (B) .
- aluminum sulfate (AI2 (S0 )3) is a compound including aluminum (Al) which has tervalent atoms, so that the aluminum sulfate is the multivalent metal compound (B) , and aluminum (Al) constituted of tervalent metal atoms contained in the multivalent metal compound is the multivalent metal component.
- the multivalent metal component used in the present invention includes one or more metals selected from typical metals and transition metals whose group numbers are 4 to 12.
- the multivalent metal compound (B) includes Mg, Ca, Ti, Zr, V, Cr, Mn, Fe, Co, Ni, Pd, Cu, Ag, Zn, Cd, and Al. Al is particularly preferable.
- the multivalent metal compound (B) is water-soluble.
- the "water-soluble" of the present invention means a condition under which 1 g or more, preferably 10 g or more, of a compound dissolves in 100 g of water whose temperature, is 25°C.
- Examples of the multivalent metal compound (B) which can be used in the present embodiment include: aluminum chloride, polyaluminum chloride, aluminum sulfate, aluminum nitrate, bis aluminum potassium sulfate, bis aluminum sodium sulfate, calcium chloride, calcium nitrate, magnesium chloride, magnesium sulfate, magnesium nitrate, zinc chloride, zinc sulfate, zinc nitrate, copper sulfate, cobalt chloride, zirconium chloride, zirconium sulfate, and zirconium nitrate. Further, in terms of solubility, it is preferable to use salt having these crystal waters. It is particularly preferable to use aluminum compounds.
- aluminum sulfate it is preferable to use aluminum sulfate, and it is possible to most favorably use powder of hydrated crystal such as aluminum sulfate octadecahydrate and aluminum sulfate hydrate (tetradecahydrate to octadecahydrate) .
- the water absorbent resin composition according to the present embodiment is a water absorbent resin composition, whose main component is a particulate water absorbent resin (A) having a cross-linking structure obtained by polymerizing an unsaturated monomer containing an acid radical, said particulate water absorbent resin (A) being cross-linked in a vicinity of a surface of the water absorbent resin (A) , wherein: the water absorbent resin composition contains 95 wt % or more of particles whose particle diameter is less than 850 ⁇ m and not less than 106 ⁇ m, and a weight average particle diameter of the particles is less than 500 ⁇ m and not less than 300 ⁇ m, and a logarithmic standard deviation ( ⁇ ) of a particle size distribution of the water absorbent resin composition is 0.45 or less, and a water-soluble component of the water absorbent composition is 35 wt % or less, and the water absorbent resin composition includes a multivalent metal component, and an extraction rate of the multivalent metal component is 5.0 wt % or more and
- the average particle diameter of the particulate water absorbent resin (A) of the present embodiment it is preferable that the average particle diameter is 300 ⁇ m or more and 500 ⁇ m or less. When the average particle diameter is less than
- the moisture absorption blocking ratio is raised at the time of water absorption, so that the gel blocking tends to occur. Further, when the average particle diameter exceeds 500 ⁇ m, an absorption rate (Vortex) becomes low.
- the water absorbent resin composition according to the present embodiment is used in the absorber and/ or the absorbent article such as a paper diaper, this results in problems such as liquid leakage and skin fit.
- the particulate water absorbent resin (A) contains 95 to 100 wt %, preferably 97 to 100 wt %, more preferably 99 to 100 wt % of particles whose particle diameter is less than 850 ⁇ m and not less than 106 ⁇ m, and a logarithmic standard deviation ( ⁇ ) of its particle size distribution is 0.45 or less, preferably 0.40 or less, more preferably 0.35 or less, most preferably 0.30 or less. Further, it is preferable that the logarithmic standard deviation ( ⁇ ) is
- the particle size distribution is narrower. Note that, when the amount of the particles whose particle diameter is less than 850 ⁇ m and not less than 106 ⁇ m is less than 95 wt % with respect to the whole particulate water absorbent resin (A) , a large number of particles whose particle diameter is not less than 850 ⁇ m and a large number of particles whose particle diameter is less than 106 ⁇ m are contained in the water absorbent resin.
- the particulate water absorbent resin (A) feels grainy in a sanitary material such as a diaper.
- the particulate water absorbent resin (A) may pass through a surface material (referred to also as a top sheet or liquid permeation sheet) of the sanitary material such as the diaper.
- a surface material referred to also as a top sheet or liquid permeation sheet
- the productivity significantly drops, so that it may be impossible to obtain an effect corresponding to the cost.
- the logarithmic standard deviation ( ⁇ ) of the particle size distribution exceeds 0.45, the particle size distribution is excessively widened, so that it may be impossible to obtain the desired moisture absorption blocking property and the desired liquid permeation/liquid diffusing property.
- the use of such water absorbent resin is not preferable.
- the water absorbent resin composition according to the present embodiment includes 95 to 100 wt%, preferably 97 to 100 wt%, more preferably 99 to 100 wt% of particles whose particle diameter is less than 850 ⁇ m and more than 106 ⁇ m or less, with respect to the whole water absorbent resin composition, and a logarithmic standard deviation ( ⁇ ) of a particle size distribution is 0.45 or less, preferably 0.40 or less, more preferably 0.35 or less, most preferably 0.30 or less. Further, it is preferable that the logarithmic standard deviation ( ⁇ ) of the particle size distribution is 0.20 or more. Further, the particle diameter of the water absorbent resin or the water absorbent resin composition may be adjusted by agglomeration or the like as required.
- the gel blocking and the moisture absorption blocking are influenced by the water-soluble component of the particulate water absorbent resin.
- the amount of the water-soluble component is 5 wt % or more and 35 wt % or less, preferably 5 wt % or more and 25 wt % or less, more preferably 5 wt % or more and 20 wt % or less, particularly preferably 5 wt % or more and 15 wt % or less, and most preferably 5 wt % or more and 10 wt % or less.
- the amount of the water-soluble component exceeds 35 wt %, the water-soluble component of the particulate water absorbent resin elutes at the time of water absorption.
- the water-soluble component functions like a binder between particles in the particulate water absorbent resin, so that the gel blocking tends to occur.
- the use of such water absorbent resin is not preferable .
- the productivity of the water absorbent resin composition significantly drops, and the production cost significantly rises, so that such arrangement is not preferable.
- the water-soluble component can be applied also to the water absorbent resin composition according to the present embodiment. That is, in the present embodiment, the water-soluble component of the water absorbent resin composition is 5 wt % or -more and 35 wt % or less, preferably 5 wt % or more and 25 wt % or less, more preferably 5 wt % or more and 20 wt % or less, particularly preferably 5 wt % or more and 15 wt % or less, most preferably 5 wt % or more and
- the water-soluble component exceeds 35 wt %, the water-soluble component of the particulate water absorbent resin elutes at the time of water absorption. As a result, the water-soluble component functions like a binder between particles in the particulate water absorbent resin, so that the gel blocking tends to occur. Thus, the use of such water absorbent resin is not preferable.
- An amount of the particulate water absorbent resin (A) contained in the water absorbent resin composition as a main component is 70 wt % or more and less than 100 wt %, preferably 80 wt % or more and less than 100 wt %, further more preferably 90 wt % or more and less than 100 wt %, most preferably 95 wt % or more and less than 100 wt %, with respect to the water absorbent resin composition.
- the inventors of the present invention found that: as to the water absorbent resin composition of the present embodiment, it is important that the multivalent metal component exists in a vicinity of a surface of the particulate water absorbent resin subjected to the surface treatment. Further, it is possible to specify the multivalent metal component, which exists in a vicinity of a surface of the water absorbent resin . particles, in accordance with an extraction rate of the multivalent metal component (the extraction rate will be described in Examples) .
- the extraction rate of the multivalent metal component is 5.0 wt % or more and less than 100 wt %, preferably 8.0 wt % or more and 90.0 wt % or less, more preferably 10.0 wt % or more and 70.0 wt % or less.
- the extraction rate of the multivalent metal component is 100 wt % in case where the multivalent metal component is mixed with the water absorbent resin in accordance with dry blending treatment.
- the extraction rate of the multivalent metal component is too high, it is impossible to evenly mix the multivalent metal compound with a surface of the water absorbent resin, so that the moisture absorption blocking property in high humidity cannot be improved.
- the multivalent metal component penetrates into the water absorbent resin. This drops the centrifuge retention capacity (CRC) , the diffusing absorbency under pressure (DAP) , and/or the absorbency against pressure (AAP) . Further, it is impossible to realize such improvement of the moisture absorption blocking property in high humidity that corresponds to the cost, and it is impossible to improve the liquid permeation/liquid diffusing property.
- CRC centrifuge retention capacity
- DAP diffusing absorbency under pressure
- AAP absorbency against pressure
- the moisture absorption blocking property of the water absorbent resin composition of the present embodiment is represented by the moisture absorption blocking ratio.
- the moisture absorption blocking ratio is measured by a known method.
- a specific example of the method for measuring the moisture absorption blocking ratio is as follows: as described in later Examples, a particulate water absorbent resin (or a water absorbent resin composition) is evenly dispersed on a bottom of a predetermined cup, and the water absorbent resin which has absorbed moisture at 25°C with a relative humidity of 90 % for one hour is sieved for a certain time by a sieve shaker, and the moisture absorption blocking ratio is measured on the basis of a weight W4 (g) of the water absorbent resin which remains on the sieve and a weight W5 (g) of the water absorbent resin which passed through the sieve.
- the moisture absorption blocking ratio a is 0 wt % or more and 30 wt % or less, preferably o wt % or more and 20 wt % or less, more preferably 0 wt % or more and 10 wt % or less, most preferably 0 wt % or more and 5 wt % or less, under such condition that the water absorbent resin is left at 25°C with a relative humidity of 90 % for one hour.
- the moisture absorption blocking ratio a exceeds 30 wt %, it is difficult to handle the water absorbent resin composition in high humidity.
- This condition may cause such problem that: in a production plant, the water absorbent resin composition and/ or the water absorbent resin particle are coagulated and jammed in a transportation pipe, and it is impossible to evenly mix them with a hydrophilic fiber, at the time of production of a thin absorber used in a sanitary material described later.
- the moisture absorption blocking ratio a is 0 wt % or more and 40 wt % or less, preferably 0 wt % or more and 30 wt % or less, more preferably 0 wt % or more and 20 wt % or less, most preferably 0 wt % or more and 10 wt % or less, under such condition that the water absorbent resin is left at 25°C with a relative humidity of 90 % for one hour.
- the moisture absorption blocking ratio a exceeds 40 wt %, it is difficult to handle the water absorbent resin composition in high humidity.
- This condition may cause such problem that: in a production plant, the water absorbent resin composition and/ or the water absorbent resin particle are coagulated and jammed in a transportation pipe, and it is impossible to evenly mix them with a hydrophilic fiber, at the time of production of a thin absorber used in a sanitary material described later.
- liquid permeability and the liquid diffusing property of the water absorbent resin composition of the present embodiment are represented by a saline flow conductivity (SFC: a barometer indicative of a liquid permeation rate under • pressure) mentioned in Published Japanese Translations of International Publication of Patent
- the saline flow conductivity (SFC) is preferably 30 ⁇ 10- 7 cm 3 -s/g or more, more preferably 70* 10 _7 cm 3 -s/g, further more preferably 100* 10" 7 cm 3 -s/ g, particularly preferably
- its centrifuge retention capacity (CRC) at which 0.90 wt % of saline is absorbed for 30 minutes without any load is preferably 25 g/g or more and 50 g/ g or less, more preferably 27 g/g or more and 45 g/ g or less, further more preferably 28 g/g or more and 40 g/g or less, particularly preferably 29 g/ g or more and 38 g/ g or less, most preferably 30 g/g or more and 35 g/ g or less.
- CRC centrifuge retention capacity
- the water absorbent resin composition according to the present embodiment when used in the absorber and/ or the absorbent article such as a paper diaper, this results in problems such as a liquid leakage and a skin rash.
- the use of such water absorbent resin composition is not preferable.
- a load such as a weight of a wearer of a paper diaper is exerted to the absorber and/ or the absorbent article in practically using the water absorbent resin composition in the paper diaper or the like.
- CRC exceeds 50 g/ g, an amount of the water-soluble component of the particulate water absorbent resin is large.
- the particulate water absorbent resin causes the gel blocking, so that it may be impossible to obtain the desired liquid permeation/liquid diffusing property.
- the use of such water absorbent resin is not preferable.
- 0.7 psi (4.83 kPa) is preferably 20 g/g or more, more preferably 21 g/ g or more and 50 g/g or less, further more preferably 23 g/ g or more and 40 g/ g or less, particularly preferably 25 g/g and 30 g/g or less.
- AAP absorbent against pressure
- a diffusing absorbency under pressure (DAP) at which 0.90 mass % of physiological saline is absorbed for 60 minutes under pressure of 1.9 kPa is 20 g/ g or more and 50 g/g or less, preferably 24 g/ g or more and 45 g/ g or less, more preferably 28 g/g or more, most preferably 32 g/g or more and 40 g/ g or less.
- DAP diffusing absorbency under pressure
- the liquid is not diffused in the absorber and/ or the absorbent article and a blocking phenomenon occurs in the liquid. Under such condition, the liquid does not spread over the water absorbent resin composition used. This may result in problems such as a liquid leakage and a skin rash in practically using the water absorbent resin composition in the paper diaper. The use of such water absorbent resin is not preferable.
- the shape, the solid content (moisture content) , and the water-soluble component of the water absorbent resin composition of the present embodiment are in the aforementioned ranges, and the amount of the water-soluble component is preferably 25 wt % or less, more preferably 20 wt % or less, further more preferably 15 wt % or less. Further, the concentration of the remaining monomer is 0 to 400 ppm, and more preferably 0 to 300 ppm.
- the water absorbent resin composition of the present embodiment is used in .
- sanitary materials such as sanitary napkins, incontinence pads, medical pads, and the like.
- sanitary material that includes (a) a liquid permeable top sheet disposed adjacent to a body of the user, (b) a liquid impermeable back sheet disposed adjacent to a clothe of the user so as to be away from the body of the user, and (c) an absorber disposed between the top sheet and the back sheet.
- the absorber may be arranged so as to be two-or-more-layered, or may be used with a pulp layer.
- the absorber is an absorbent layer in which a fiber base material or the like is included as required.
- the water absorbent resin composition of the present embodiment is free from any coagulation of particles even in high humidity, and exhibits a superior liquid permeation/liquid diffusing property.
- the water absorbent resin composition exhibits a superior moisture absorption blocking property.
- the water absorbent resin composition is superior also in the liquid permeation/liquid diffusing property.
- the absorber of the present embodiment includes a large amount (high core concentration) of the water absorbent resin composition with respect to a total weight of the water absorbent resin composition and the hydrophilic fiber. As a result, it is possible to produce an extremely thin sanitary material.
- An amount (core concentration) of the contained water absorbent resin composition with respect to a total amount of the water absorbent resin composition and the hydrophilic fiber is preferably 20 to 100 mass %, more preferably 30 to 90 mass %, most preferably 40 to 80 mass %. In this manner, when the water absorbent resin composition of the present embodiment is used, it is possible to produce a thin absorber superior in the absorbent property without any trouble at the time of production.
- the thin absorber is sandwiched by a liquid-permeable base material (surface sheet) and a liquid-impermeable base material (back sheet) , and is provided with an elastic member, a diffusion layer, an adhesive tape, and the like, thereby obtaining an absorbent article (product for consumers) , particularly an adult paper diaper and a sanitary napkin.
- the absorber is pressed so that its density is 0.06 to 0.50 g/ cc and its basic weight is 0.01 to 0.20 g/ cm 2 .
- the fiber base material used is a hydrophilic fiber, for example, crushed wood pulp, a cotton linter, a cross-linked cellulose fiber, rayon, cotton, wool, acetate, or vinylon. These fiber base materials are preferably aerated.
- the water absorbent resin composition of the present embodiment is obtained by (i) adding an aqueous solution of a water-soluble multivalent metal compound having a specific solution concentration to the particulate water absorbent resin (A), having a specific particle size distribution, whose surface vicinity has been cross-linked, and (ii) mixing them with each other.
- the extraction rate of the multivalent metal component is substantially 100 %, and the multivalent metal salt is dry-blended, so that it is impossible to evenly mix the multivalent metal component with a surface of the water absorbent resin. As a result, the moisture absorption blocking property is not improved.
- the method (2) as in the method ( 1) , it is impossible to evenly coat the surface of the water absorbent resin at the time of dry-blending of the multivalent metal salt, and water is added under such condition, so that the water is quickly absorbed by a part of the water absorbent resin particles.
- the multivalent metal salt may permeate the water absorbent resin.
- the moisture absorption blocking property is not improved, and the centrifuge retention capacity (CRC) , the diffusing absorbency under pressure (DAP) , and the absorbency against pressure (AAP) may drop.
- the moisture absorption blocking property is not improved. This may be based on the following reason: according to such a method that the surface cross-linking agent and the aqueous solution of the multivalent metal salt are simultaneously added, mixed, and heated, a ratio of the multivalent metal component which exists in a vicinity of the surface of the water absorbent resin so as to improve the moisture absorption blocking property becomes smaller.
- a surface of the water absorbent resin composition of the present embodiment is evenly coated with the multivalent metal component while preventing the multivalent metal component from permeating the water absorbent resin.
- a vicinity of the surface of the particulate water absorbent resin is cross-linked and its particle size distribution is specified as described above. The inventors of the present invention found this, thereby devising the present invention.
- the inventors found it possible to evenly provide the multivalent metal component in the vicinity of the surface of the water absorbent resin while preventing the multivalent metal component from permeating the water absorbent resin by adjusting the solution concentration of the multivalent metal compound (B) to the aforementioned specific range, thereby devising the present invention. That is, it is possible to obtain the water absorbent resin composition according to the present embodiment by adding a solution of the aqueous multivalent metal compound (B) to the particulate water absorbent resin (A) and mixing them with each other.
- the solution is regarded as a solution of the aqueous multivalent metal compound (B) as long as the multivalent metal compound (B) dissolves even though the concentration of the multivalent metal compound (B) exceeds a saturation concentration and a part of the multivalent metal compound (B) is precipitated or dispersed. Further, an amount of the multivalent metal compound
- the amount of the multivalent metal compound (B) added as the multivalent metal component is preferably 0.001 to 10 weight parts, more preferably 0.01 to 5 weight parts, particularly preferably 0.05 to 1 weight parts, with respect to 100 weight parts of a solid content.
- the multivalent metal component is less than 0.001 weight parts, the moisture absorption blocking property and the liquid permeation/liquid diffusing property are not sufficiently improved.
- the centrifuge retention capacity (CRC) the diffusing absorbency under pressure (DAP) , and the absorbency against pressure
- the solution of the multivalent metal compound (B) it is possible to use a solution obtained by dissolving the multivalent metal compound (B) in water and/or aqueous solution or various kinds of hydrophilic organic solvent, but it • is preferable to use an aqueous solution.
- a suitable amount of a solvent, i.e., water, vapor, or an aqueous liquid constituted of water and hydrophilic organic solvent, with respect to solid contents of the water absorbent resin varies depending on a type and a particle size of the water absorbent resin.
- the suitable amount thereof is more than 0 to 10 weight parts or less, preferably 1 to 5 weight parts, with respect to 100 weight parts of solid contents.
- an amount of the hydrophilic organic solvent used is generally 0 to 10 weight parts or less, preferably 0. 1 to 5 weight parts, with respect to 100 weight parts of the solid contents.
- the solution concentration of the multivalent metal compound (B) used is adjusted so that a ratio of the aqueous solution concentration and the saturation concentration at
- 25°C is 0.40 or more, preferably 0.50 or more, more preferably 0.60, most preferably 0.70 or more, so that it is possible to improve the moisture absorption blocking property in high humidity and to prevent the centrifuge retention capacity (CRC), the diffusing absorbency under pressure
- the concentration of the aqueous solution added may exceed the saturation . concentration at 25°C. That is, generally, an upper limit of a ratio of the concentration of the added aqueous solution with respect to the saturation concentration is preferably 1.50 or less, more preferably 1.00 or less.
- the multivalent metal component permeates the water absorbent resin, so that the centrifuge retention capacity (CRC) , the diffusing absorbency under pressure (DAP) , and the absorbency against pressure (AAP) drop, and the multivalent metal component influence the improvement of the moisture absorption blocking property in high humidity.
- CRC centrifuge retention capacity
- DAP diffusing absorbency under pressure
- AAP absorbency against pressure
- the multivalent metal component influence the improvement of the moisture absorption blocking property in high humidity.
- an amount of the multivalent metal component existing in a vicinity of a surface of the water absorbent resin becomes smaller. This may be a reason for which it is impossible to realize such improvement of the moisture absorption blocking property that corresponds to the amount of the solution of the multivalent metal component.
- temperature of the particulate water absorbent resin (A) is preferably 50°C or higher and lower than 100°C, more preferably 50°C or higher and lower than 80°C, further preferably 50°C or higher and lower than 70°C.
- moisture of the solution of the multivalent metal compound less vaporizes after the solution of the multivalent metal compound is added to the particulate water absorbent resin (A) .
- the multivalent metal component permeates the particulate water absorbent resin (A) .
- Such arrangement is not preferable.
- the particulate water absorbent resin (A) exceeds 100°C, the particulate water absorbent resin (A) and the multivalent metal component are unevenly mixed, or the particulate water absorbent resin deteriorates. Thus, such arrangement is not preferable.
- Temperature of the aqueous solution of the multivalent metal compound is preferably 30°C or higher and lower than 100°C, more preferably 50°C or higher and lower than 100°C, further more preferably 70°C or higher and lower than 100°C. When the temperature of the aqueous solution of the multivalent metal compound is lower than
- the concentration of the multivalent metal component of the solution of the multivalent metal compound becomes lower, so that the multivalent metal component permeates the particulate water absorbent resin.
- the temperature of the aqueous solution of the multivalent metal compound exceeds 100°C, the particulate water absorbent resin (A) deteriorates, so that it is impossible to realize such sufficient improvement of the moisture absorption blocking property that corresponds to the amount of the multivalent metal component added.
- such arrangement is not preferable.
- examples of a device which adds and mixes the aqueous solution of the multivalent metal compound (B) with the particulate water absorbent resin (A) are as follows: a cylindrical mixer, a screw mixer, a screw extruder, a turbulizer, a nauta mixer, a V-shaped mixer, a ribbon blender, a double-arm kneader, a flow mixer, an air current mixer, a rotary disc mixer, a roll mixer, a convolution mixer, and a L ⁇ dige mixer.
- a mixing speed is not particularly limited to a high speed or a low speed.
- a heating process and classification may be performed as required. Further, it may be so arranged that: temperature thereof is adjusted during or after addition/mixing of the multivalent metal compound (B) , thereby controlling the precipitation and dispersion of the multivalent metal component.
- the water absorbent resin and the water absorbent resin composition according to the present embodiment may be, where necessary, subjected to another step of adding various additives.
- the additives include: deodorant; antibacterial agent; perfume; foaming agent; pigment; dye; plasticizer; adhesive; surfactant; fertilizer; oxidizing agent; reducing agent; water, salt; chelating agent; bactericide; hydrophilic polymer, such as polyethylene glycol, and polyethyleneimine; hydrophobic polymer, such as paraffin; thermoplastic resins, such as polyethylene and polypropylene; and thermosetting resins, such as a polyester resin and urea resin.
- the additives are added at quantities from 0 to 20 wt %, preferably from 0 to 5 wt %, more preferably 0 to 1 wt %, with respect to the water absorbent resin composition.
- a water absorbent resin composition according to the present embodiment includes a particulate water absorbent resin (A) and a multivalent metal component (B) that are similar to those of Embodiment 1 .
- a particulate water absorbent resin (A) having a cross-linking structure obtained by polymerizing an unsaturated monomer containing an acid group, a solution of an aqueous multivalent metal compound (B), and an organic surface cross-linking agent (C) are mixed with each other, thereby obtaining the water absorbent resin composition.
- the following description explains a method according to the present embodiment for producing the water absorbent resin composition.
- the water absorbent resin composition of the present embodiment can be obtained by heating a mixture of the particulate water absorbent resin (A) , the solution of the multivalent metal compound (B) , and the organic surface cross-linking agent (C) , at 150 to 300°C.
- a method for mixing the particulate water absorbent resin (A) , the solution of the multivalent metal compound (B) , and the organic surface cross-linking agent (C) with each other is not particularly limited.
- the solution of the multivalent metal compound (B) and the organic surface cross-linking agent (C) are separately or simultaneously mixed with the particulate water absorbent resin (A) , or it may be so arranged that a mixture solution obtained by mixing the solution of the multivalent metal compound (B) with the organic surface cross-linking agent (C) is mixed with the particulate water absorbent resin (A) . It is preferable to adopt the method in which a mixture solution obtained by mixing the solution of the multivalent metal compound (B) with the organic surface cross-linking agent (C) is mixed with the particulate water absorbent resin (A) . Note that, in the present embodiment, any solution is used as the
- inorganic acids, organic acids, polyamino acids that are mentioned in European Patent No . 0668080 may be introduced as a mixing coadjuvant.
- the mixing coadjuvant may function as a surface cross-linking agent.
- volatile alcohols whose boiling point is lower than 150°C since the volatile alcohols vaporize so that there is no residue at the time of the surface cross-linking treatment.
- non-cross-linking water-soluble inorganic bases preferably, alkali metal salt, ammonium salt, alkaline metal hydroxide, and ammonia or hydroxide thereof
- a non-reducing alkali metal salt pH buffer preferably, hydrogen carbonate, dihydrogen salt phosphate, hydrogen salt phosphate, and the like
- An amount of them varies depending on a kind and a particle size of the water absorbent resin particles, but is preferably 0.005 to 10 weight parts, more preferably 0.05 to 5 weight parts, with respect to 100 weight parts of the solid contents of the water absorbent resin particles.
- a total amount of the organic surface cross-linking agent (C) and the multivalent metal compound (B) varies depending on respective amounts of the organic surface cross-linking agent (C) and the multivalent metal compound (B) , but is preferably 0.001 weight parts to 10 weight parts, more preferably 0.01 weight parts to 5 weight parts, with respect to 100 weight parts of the water absorbent resin.
- the total amount of the organic surface cross-linking agent (C) and the multivalent metal compound (B) is less than 0.001 weight parts, the moisture absorption blocking property and the liquid permeability/ liquid diffusing property are not sufficiently improved.
- (B) is not less than 10 weight parts, the centrifuge retention capacity (CRC), the diffusing absorbency under pressure
- DAP absorbency against pressure
- the water absorbent resin compound of the present embodiment realizes both the superior moisture absorption blocking property and the superior liquid permeability/liquid diffusing property under a condition of high humidity, it is necessary that: concentration of the multivalent metal component in the aqueous solution in mixing the particulate water absorbent resin (A) with the solution of the multivalent metal compound (B) is at least 1.80 wt %, and the mixture of the particulate water absorbent resin (A) , the organic surface cross-linking agent (C) , and the solution of the multivalent metal compound (B) is heated at 150°C to 300°C. This was found by the inventors of the present invention for the first time. As a result, the present invention was devised.
- a saline flow conductivity (SFC: a barometer indicative of a liquid permeation rate under pressure) of a water absorbent resin subjected to surface treatment with a surface treatment agent having a highly concentrated multivalent metal component is much higher than that of a water absorbent resin subjected to surface treatment with a surface treatment agent having a known concentration.
- the solution of the highly concentrated multivalent metal compound (B) (at least 1.80 wt % of the multivalent metal component is contained in the aqueous solution) is mixed with the particulate water absorbent resin, so that the multivalent metal component exists around a surface layer of the water absorbent resin after preparing the mixture.
- the moisture absorption blocking property and the liquid permeation/liquid diffusing property are remarkably improved.
- neither the solution prepared by mixing the particulate water absorbent resin (A) with the multivalent metal compound (B) nor the mixing method of the solution and the organic surface cross-linking agent (C) are particularly limited.
- concentration (S/T - [M]) of the multivalent metal component contained in the solution of the multivalent metal compound (B)" in the methods (i) and (ii) is calculated in accordance with the following equations.
- the concentration of the multivalent metal component contained in the solution of the multivalent metal compound (B) used in the present embodiment is preferably 1.80 wt % or more, more preferably 2.00 wt % or more, further more preferably 2.50 wt % or more, most preferably 2.90 wt % or more.
- an upper limit of the concentration of the multivalent metal component included in the solution of the multivalent metal compound (B) is not particularly limited, but is preferably 20 wt % or less, more preferably 10 wt % or less.
- An amount of the multivalent metal compound (B) used varies depending on the desired moisture absorption blocking property and the desired liquid permeation/ liquid diffusing property, but is preferably 0.001 weight parts to 10 weight parts, more preferably 0.01 weight parts to 5 weight parts, particularly preferably 0.05 to 1 weight parts, with respect to 100 weight parts of the water absorbent resin.
- the amount of the multivalent metal compound (B) is less than 0.001 weight parts, the moisture absorption blocking property and the liquid permeability/liquid diffusing property are not sufficiently improved.
- a centrifuge retention capacity (CRC) a diffusing absorbency under pressure (AAP) , and the absorbency against pressure (AAP) significantly drop.
- the aqueous solution of the multivalent metal compound (B) and/ or the organic surface cross-linking agent (C) that can be used in the present invention are heated preferably at 30°C or higher, more preferably at 50°C or higher, particularly preferably at 70°C or higher. This is based on the following reason: when a temperature of the solution is higher, it is possible to raise the concentration of the multivalent metal component contained in the solution, so that a larger amount of the multivalent metal component can exist on the surface of the water absorbent resin.
- a condition under which a precursor (D) constituted of the mixture of the particulate water absorbent resin (A), the organic surface cross-linking agent (C) , and the solution of the multivalent metal compound (B) is heated is as follows.
- a heating temperature is preferably 150 to 300°C, more preferably 160 to 250°C, further more preferably 170 to 230°C.
- a heating time is preferably one minute to two hours, more preferably 15 minutes to 1.5 hours.
- a favorable example of a combination of the heating temperature and the heating time is as follows: The heating temperature is 180°C, and the heating time is 15 minutes to 1.5 hours; The heating temperature is 200°C, and the heating time is 15 minutes to one hour.
- a functional group of the organic surface cross-linking agent (C) insufficiently reacts with an acid group (for example, a carboxyl group) of the particulate water absorbent resin (A) .
- the heating temperature exceeds 300°C
- the water absorbent resin is damaged while performing the heating treatment.
- the moisture absorption blocking property and the liquid permeation/ liquid diffusing property are not sufficiently improved.
- the water absorbent resin composition of the present embodiment has a superior moisture absorption blocking property in high humidity and a superior liquid permeation/liquid diffusing property at the same time, it is necessary that a particle surface of the water absorbent resin composition is evenly subjected to the surface treatment.
- the inventors first found that: in order to achieve this object, it is important that a humidification blocking ratio (wt %) of a precursor (D) is 0 wt % or more and 80 wt % or less.
- the humidification blocking ratio (wt %) of the precursor (D) exceeds 80 wt % and is less than 100 wt %, a large amount of coagulum are contained in the precursor (D) .
- the precursor (D) is heated, heat is not sufficiently conducted into the coagulum, so that the particle surfaces of the water absorbent resin composition are not secondarily cross-linked evenly.
- a blocking phenomenon is caused by coagulum of portions that are not secondarily cross-linked to each other.
- this condition may bring about such problem that: the water absorbent resin is jammed in a production apparatus due to the blocking phenomenon, so that it is impossible to stably produce the water absorbent resin composition.
- a method for obtaining the precursor (D) whose humidification blocking ratio is 80 wt % or less is not particularly limited. However, it is preferable that the concentration of the multivalent metal component contained in the aqueous solution is at least 1.80 wt % in mixing the particulate water absorbent resin (A) with the multivalent metal compound (B) .
- the solution of the highly concentrated multivalent metal compound (B) (the concentration of the multivalent metal component is at least 1.80 wt %) is mixed, so that the multivalent metal component exists around a surface layer of the water absorbent resin after mixing them. As a result, the humidification blocking property is further improved.
- the concentration of the multivalent metal component contained in the solution of the multivalent metal compound (B) in obtaining the precursor (D) having a humidification blocking ratio of 80 wt % or less is preferably 1.80 wt % or more, more preferably 2.00 wt % or more, further more preferably 2.50 wt % or more, most preferably 2.90 wt % or more.
- the concentration of the multivalent metal component contained in the solution of the multivalent metal compound (B) is less than 1.80 wt %, the multivalent metal component permeates the water absorbent resin, so that a smaller amount of the multivalent metal component exists in a vicinity of a surface of the water absorbent resin. Thus, it is impossible to realize such sufficient improvement of the moisture absorption blocking property and the liquid permeation/liquid diffusing property that corresponds to an amount of the multivalent metal component added.
- an amount of the multivalent metal compound (B) used varies depending on the desired moisture absorption blocking property and the desired liquid permeation/liquid diffusing property.
- the amount of the multivalent metal compound (B) added as the multivalent metal component is preferably 0.001 to 10 weight parts, more preferably 0.01 to 5 weight parts, particularly preferably 0.05 to 1 weight parts, with respect to 100 weight parts of solid contents.
- the multivalent metal component is less than 0.001 weight parts, the moisture absorption blocking property and the liquid permeation/liquid diffusing property are not sufficiently improved.
- the centrifuge retention capacity (CRC) , the diffusing absorbency under pressure (AAP), and the absorbency against pressure (AAP) significantly drop.
- the solution of the multivalent metal compound (B) and/ or the organic surface cross-linking agent (C) that can be used in the present embodiment are heated preferably at 30°C or higher, more preferably at 50°C or higher, particularly preferably at 70°C or higher. This is based on the following reason: when a temperature of the solution is higher, it is possible to raise the concentration of the multivalent metal component contained in the solution, so that a larger amount of the multivalent metal component can exist on the surface of the water absorbent resin. Further, it is preferable that the upper limit temperature is less than 100°C.
- a condition under which the precursor (D) whose humidification blocking ratio is 80 wt % or less is heated is as follows.
- a heating temperature is preferably 150 to 300°C, more preferably 160 to 250°C, further more preferably 170 to 230°C.
- a heating time is preferably one minute to two hours, more preferably 15 minutes to 1.5 hours.
- a favorable example of a combination of the heating temperature and the heating time is as follows: The heating temperature is 180°C, and the heating time is 15 minutes to 1.5 hours; The heating temperature is 200°C, and the heating time is 15 minutes to one hour.
- the water absorbent resin composition of the present embodiment it is important that: specific amounts of the organic surface cross-linking agent and the multivalent metal compound (B) are added, and the organic surface cross-linking agent evenly reacts with a carboxyl group of the particulate water absorbent resin (A) , and the multivalent metal component exists in a vicinity of a surface of the water absorbent resin without permeating the water absorbent resin, and the humidification blocking ratio (wt %) of the precursor (D) is 0 wt % or more and 80 wt % or less.
- the present invention is not limited to them.
- properties of the water absorbent resin and the water absorbent resin composition were measured in accordance with the following method. Further, when a specific condition is not described, this means that all the operations were performed at room temperature (23 ⁇ 2°C) and at humidity of 50RH%.
- the centrifuge retention capacity represents an absorbency at which 0.90 wt % of saline is absorbed for 30 minutes without any pressure.
- a water absorbent resin or a water absorbent resin composition
- a bag 60 mm ⁇ 60 mm
- a nonwoven fabric Heatron Paper made by Nangoku Pulp Kogyo Co. , Ltd. : model type is GSP-22
- the bag was heat-sealed. Thereafter, the bag was soaked in an excessively large amount (generally, about 500 m) of 0.90 wt % sodium chloride solution (physiological saline) whose temperature had been adjusted to room temperature, and was withdrawn 30 minutes later.
- an excessively large amount generally, about 500 m
- 0.90 wt % sodium chloride solution physiological saline
- centrifugal machine made by KOKUSAN Corporation: model type is H- 122 the bag was drained for three minutes at a centrifugal force (250G) recited in edana ABSORBENCY II 441 , 1 -99, and a weight W2 (g) of the bag was measured. Further, the same operation was performed without using the water absorbent resin, and a weight W I (g) was measured.
- Centrifuge retention capacity (g/ g) ((weight W2 (g) - weight W I (g)) / weight (g) of water absorbent resin) - 1
- DAP Diffusing absorbency under pressure
- the diffusion absorbency of the water absorbent resin was calculated as follows .
- a weight W3 (g) of a physiological saline absorbed by the water absorbent resin composition under a pressure of 1.9 kPa (0.3 psi) for 60 minutes was measured.
- the diffusing absorbency (g/ g) in 60 minutes after the beginning of the absorption was calculated in accordance with the following equation.
- the absorbency against pressure (AAP) represents an absorbency at which 0.90 wt % of saline is absorbed for 60 minutes at 4.83 kPa.
- AAP absorbency against pressure
- a glass filter 106 (product of Sougo Rikagaku Glass Seisakusho
- JIS P3801 No. 2; thickness: 0.26 mm; diameter of retained particles: 5 ⁇ m) having a 90 mm diameter was placed thereon, so that an entire surface of the filter paper 107 was wetted. An excess of the 0.90 wt % saline 108 was removed.
- the measuring apparatus set was placed on the wet filter paper 107. Then, the water absorbent resin composition was made to absorb the 0.90 wt % saline 108 for one hour under the load of 4.83 kPa (0.7 psi) . At this time, the water absorbent resin composition absorbed the 0.90 wt % saline
- the measuring apparatus set having absorbed the 0.90 wt % saline 108 was lifted, and a weight Wb (g) thereof was measured. From the weights Wa and Wb, the absorbency against pressure AAP (g/g) was calculated according to the following equation.
- a flow rate F s (t) of the solution passing through the swollen gel 44 was determined in terms of g/ s by dividing an increasing weight (g) by an increasing time (s) .
- Lo a height of the gel layer that is represented by "cm”
- p a density ( 1.003 g/ cm 3 ) of NaCl solution
- A an area (28.27 cm 2 ) on the upper side of the gel layer of the cell 41
- ⁇ P a hydrostatic pressure (4920 dyne/cm 2 ) exerted to the gel layer.
- a unit of the saline flow conductivity (SFC) is ( 10- 7 ⁇ cm 3 ⁇ s ⁇ g-i) .
- a glass tube 32 was inserted into the tank 31 , and a lower end of the glass tube
- a hole 47 which allowed liquid to pass through was provided on a lower portion of a piston 46, and a glass filter 45 having high permeability was provided on the bottom thereof so that the water absorbent resin composition or the swelling gel did not enter into the hole 47.
- the cell 41 was placed on a table for the cell, and the table's surface which is in contact with the cell was positioned on the stainless metal gauze 43 which did not prevent the liquid from passing through.
- the synthesized urine ( 1) was prepared by mixing 0.25 g of calcium chloride dihydrate, 2.0 g of potassium chloride,
- the moisture absorption blocking ratio (wt %) was calculated in accordance with the following equation. As the moisture absorption blocking ratio is lower, the water absorbent resin is superior in terms of the moisture absorption blocking property.
- Moisture absorption blocking ratio (wt %) weight W4 (g) / (weight W4 (g) + weight W5 (g)) x 100
- the moisture absorption blocking ratio (wt %) was calculated by setting the predetermined cup and the sieving time of the sieve shaker under the following two conditions.
- TESTING SIEVE diameter is 8cm) respectively having mesh sizes of 850 ⁇ m, 710 ⁇ m, 600 ⁇ m, 500 ⁇ m, 425 ⁇ m, 300 ⁇ m,
- An amount of the multivalent metal component contained in the water absorbent resin was determined as follows. 1.0 g of the water absorbent resin composition was measured and placed in a polypropylene beaker of 260 ml, and 190.0 g of physiological saline (0.9 wt % NaCl aqueous solution) and 10.0 g of 2N hydrochloric acid were added thereto, and thus obtained mixture was stirred for 30 minutes at room temperature. After stirring them, supernatant liquid thereof was filtered by using a chromatodisc (GL Chromatodisc 25A, product of GL Science Inc.) , and was analyzed by plasma emission spectrochemical analysis (by using ULTIMA, product of HORIBA, Ltd.), thereby calculating the multivalent metal component concentration. Note that, an analytical curve was made in accordance with physiological saline containing a known amount of the multivalent metal component. On the basis of the calculated multivalent metal component concentration, the multivalent metal component concentration in the water absorbent resin composition is represented by the following equation.
- Multivalent metal component concentration (wt %) in the water absorbent resin composition (multivalent metal component concentration (wt %) in solution) * 200 •
- the multivalent metal component extraction rate was measured as follows.
- Solution A was prepared by mixing 95 g of methanol solution of 1.0 wt % 8-quinolinol (product of Wako Pure Chemical Industries, Ltd.) with 5 g of pure water
- solution B was prepared by mixing 95 g of methanol with 5 g of pure water.
- a teflon (registered trademark) rotor whose diameter was 35 mm was placed in a 260 ml polypropylene container, and 5 g of the water absorbent resin composition and 25 g of the solution A were measured and poured therein.
- the container was tightly closed, and the content was stirred by using a magnetic stirrer for 20 hours at room temperature.
- 5 ml of supernatant liquid thereof was picked up by using a polypropylene syringe, and a chromatodisc (GL chromatodisc 25A, product of GL Scienpe Inc.) was provided on the syringe, and the filtered liquid was placed in a polypropylene container. Part of the filtered liquid was moved to a 1 cm cell
- 8-quinolinol absorbs light of specific wavelength was measured by using a spectrophotometer (Hitachi spectrophotometer U- 1 100) .
- the specific wavelength was 380 nm.
- the specific wavelength is explained on the assumption that the multivalent metal component is aluminum.
- the light absorbance at the time of extraction of 100 wt % multivalent metal component measurement was performed with respect also to a light absorbance at which light of 380 nm wavelength was absorbed by a solution obtained by dissolving the multivalent metal component in the solution A so that there is the same amount of the multivalent metal component as at the time of extraction of 100 wt % multivalent metal component (the concentration of the multivalent metal component in the water absorbent resin composition was separately measured in the foregoing manner) .
- the extraction rate of the multivalent metal component was calculated in accordance with the following equation.
- Extraction rate (wt %) of the multivalent metal component ((filtered liquid's light absorbance with respect to light of 380 nm wavelength) - (solution A's light absorbance with respect to light of 380 nm wavelength)) / (light absorbance with respect to light of 380nm wavelength at the time of extraction of 100 wt % multivalent metal component) x 100 (H) Humidification Blocking ratio (wt %)
- the humidification blocking ratio calculated by the following measurement method is regarded as an index of a humidification blocking property of the precursor (D) .
- 10 g of the precursor (D) constituted of the mixture of the particulate water absorbent resin (A) , aqueous solution of the multivalent metal compound (B) , and/ or the organic surface cross-linking agent (C) was moved onto a JIS standard sieve (diameter is 7.5 cm, mesh size is 1000 ⁇ m) , and was sieved by using a sieve shaker (IIDA SIEVE SHAKER, TYPE: ES-65, SER.
- the humidification blocking ratio was calculated in accordance with the following equation. As the humidification blocking ratio is lower, the precursor (D) is superior in terms of the humidification blocking property.
- Humidification blocking ratio (wt %) weight W6 (g) / (weight W6 (g) + weight W7 (g)) 100
- a water absorbent resin composition includes a known amount of acrylic acid and its sodium chloride
- an amount of soluble component in the water absorbent resin composition in accordance with the following, from an average molecular mass of the monomer and the titration amounts ([bNaOH]ml, [bHCl]ml, [NaOH]ml, and [HCl]ml) obtained by the foregoing operation.
- Amount of soluble component (weight %) 0. 1 (average molecular mass) ⁇ l84.3 ⁇ l 00 ⁇
- Neutralization ratio (mol %) ( l -([NaOH]ml-[bNaOH]ml) / ([HCl]ml-[bHCl]ml)) x 100
- a time (second) since the water-absorbent resin had been added to the test solution until the stirrer was surrounded by the test solution was measured, and the time (second) was regarded as the absorption rate. Note that, in the present embodiment, the time until the stirrer was surrounded by the test solution was a period until the rotating stirrer that had been seen was hidden by the protuberant swirl that had almost disappeared.
- the blue physiological saline is composed of: 991 mass parts of deionized water, 9 mass parts of sodium chloride, and 0.02 mass parts of food additive • edible Brilliant Blue, (food additive • edible brilliant blue: benzyl- ethyl-[4'-(4"-benzyl ethyl amino) -diphenyl methylene)-2', 5-cyclohexa dienylidene]-ammonium-2'",3,3'"-disodium trisulfonic acid; brilliant blue FCF; CI No. 42090; CI Food blue 2) ⁇ Referential Example 1 >
- water-containing gelled polymer had been fragmented so that its diameter was approximately 5 mm.
- the water-containing gelled polymer fragmented was spread out on a wire mesh of 50 mesh (mesh size is 300 ⁇ m), and was dried by hot air at 150°C for 90 minutes.
- a dry polymer thus obtained was crushed by using a vibrating mill, and then classified by using a wire mesh of 20 meshes (mesh size is 850 ⁇ m) then blended.
- water absorbent resin powder (a) having a crushed indeterminate form was obtained.
- water absorbent resin powder (a) a surface cross-linking solvent including 0.5 weight parts of propyleneglycol, 0.03 weight parts of ethyleneglycol diglycidyl ether, 0.3 weight parts of 1 ,4-butanediol, and three weight parts of water, was mixed. The mixture was then thermally processed at 200°C for 55 minutes, thereby obtaining a water absorbent resin ( 1) .
- Table 1 shows a particle size distribution of the water absorbent resin ( 1)
- Table 2 shows other properties of the water absorbent resin ( 1) .
- water absorbent resin powder (b) having a crushed indeterminate form was obtained.
- a surface cross-linking solvent including 0.5 weight parts of propyleneglycol, 0.03 weight parts of ethyleneglycol diglycidyl ether, 0.3 weight parts of 1 ,4-butanediol, and three weight parts of water, was mixed. The mixture was then thermally processed at 200°C for 55 minutes, thereby obtaining a water absorbent resin (2) .
- Table 1 shows a particle size distribution of the water absorbent resin (2)
- Table 2 shows other properties of the water absorbent resin (2) .
- the dry polymer was crushed by using a pin mill instead of the vibrating mill, and then classified by using a wire mesh of 20 meshes (mesh size is 850 ⁇ m) then blended.
- water absorbent resin powder (C) having a crushed indeterminate form was obtained.
- water absorbent resin powder (C) was subjected to the same treatment as in the Referential Example 1 , thereby obtaining a water absorbent resin (3) .
- Table 1 shows a particle size distribution of the water absorbent resin (3)
- Table 2 shows other properties of the water absorbent resin (3) .
- water-containing gelled polymer had been fragmented so that its diameter was approximately 5 mm.
- the water-containing gelled polymer fragmented was spread out on a wire mesh of 50 mesh (mesh size is 300 ⁇ m) , and was dried by hot air at 150°C for 90 minutes.
- a dry polymer thus obtained was crushed by using a vibrating mill, and then classified by using a wire mesh of 30 meshes (mesh size is
- water absorbent resin powder (D) having a crushed indeterminate form was obtained.
- a surface cross-linking solvent including 0.5 weight parts of propyleneglycol, 0.03 weight parts of ethyleneglycol diglycidyl ether, 0.3 weight parts of 1 ,4-butanediol, and three weight parts of water was mixed. The mixture was then thermally processed at 200°C for 55 minutes, thereby obtaining a water absorbent resin (4) .
- Table 1 shows a particle size distribution of the water absorbent resin (4)
- Table 2 shows other properties of the water absorbent resin (4) .
- Table 2 shows other properties of the water absorbent resin composition (8) .
- Table 1 shows a particle size distribution of the water absorbent resin composition (5)
- Table 2 shows other properties of the water absorbent resin composition (5) .
- a surface cross-linking solvent constituted of 0.5 weight parts of propyleneclycol, 0.03 weight parts of ethyleneglycol diglycidyl ether, 0.3 weight parts of 1 ,4-butanediol, and three weight parts of water was mixed with 100 weight parts of the water absorbent resin powder (a) of the Referential Example 1 , and 9.0 weight parts of 30.8 mass % aluminum sulfate (tetradecahydrate to octadecahydrate) hydrate was added and mixed therewith. Then, thus obtained mixture was thermally processed at 200°C for 55 minutes, thereby obtaining a water absorbent resin (6) .
- Table 1 shows a particle size distribution of the water absorbent resin composition (6)
- Table 2 shows other properties of the water absorbent resin composition (6) .
- Table 1 shows a particle size distribution of the water absorbent resin composition (7)
- Table 2 shows other properties of the water absorbent resin composition (7) .
- water-containing gel cross-linking polymer had been fragmented so that its diameter was approximately 5 mm.
- the water-containing gel cross-linking polymer fragmented was spread out on a wire mesh of 50 mesh (mesh size is 300 ⁇ m) , and was dried by hot air at 175°C for 50 minutes, thereby obtaining a water absorbent resin (A) , constituted of particulate or powdery dried substances, which had an indeterminate form and was easily crushed.
- water absorbent resin (A) was crushed by using a roll mill, and then classified by using a JIS standard sieve (mesh size is 850 ⁇ m) .
- particles having passed through the mesh of 850 ⁇ m were classified by using a JIS standard sieve (mesh size is 150 ⁇ m) , so that the water absorbent resin passing through the mesh of 150 ⁇ m were removed, thereby obtaining a particulate water absorbent resin (Al) .
- the water absorbent resin (A) obtained in the same manner was crushed by using a roll mill, and then classified by using a JIS standard sieve (mesh size is 710 ⁇ m) .
- the water absorbent resin (A) obtained in the same manner was crushed by using a roll mill, and then classified by using a JIS standard sieve (mesh size is 600 ⁇ m) .
- particles having passed through the mesh of 600 ⁇ m were classified by using a JIS standard sieve (mesh size is 150 ⁇ m) , so that the water absorbent resin passing through the mesh of 150 ⁇ m were removed, thereby obtaining a particulate water absorbent resin (A3) .
- the water absorbent resin (A) obtained in the same manner was crushed by using a roll mill, and then classified by using a JIS standard sieve (mesh size is 710 ⁇ m) .
- Example 6 thereby obtaining a precursor ( 1) .
- precursor ( 1) was thermally processed at 180°C for 30 minutes. Further, particles thereof were fragmented so as to pass through a JIS standard sieve (mesh size is 850 ⁇ m) , thereby obtaining a water absorbent resin composition ( 1) .
- JIS standard sieve mesh size is 850 ⁇ m
- Table 4 shows a result obtained by measuring properties of the water absorbent resin composition ( 1) .
- a surface treatment agent constituted of a mixture solution obtained by mixing 1.0 g of ethyleneglycol, 2.0 g of pure water, and 0.8 g of aluminum chloride 6 hydrate was evenly mixed with 100 g of the water absorbent resin (Al) obtained in the Referential Example 6. Thereafter, thus obtained mixture was thermally processed at 200°C for 25 minutes. Further, particles thereof were fragmented so as to pass through a JIS standard sieve (mesh size is 850 ⁇ m) , thereby obtaining a water absorbent resin composition (2) .
- Table 4 shows a result obtained by measuring properties of the water absorbent resin composition (2) .
- Example 6 Thereafter, thus obtained mixture was heated at 180°C for 30 minutes. Further, particles thereof were fragmented so as to pass through a JIS standard sieve (mesh size is 850 ⁇ m) , thereby obtaining a comparative water absorbent resin composition ( 1) .
- Table 4 shows a result obtained by measuring properties of the comparative water absorbent resin composition ( 1) .
- a surface treatment agent constituted of a mixture solution obtained by mixing 1.0 g of ethyleneglycol, 3.0 g of pure water, and 0.5 g of aluminum sulfate tetradecahydrate was evenly mixed with 100 g of the water absorbent resin (A l) obtained in the Referential Example 6, thereby obtaining a comparative precursor (2) .
- comparative precursor (2) was thermally processed at 180°C for 30 minutes. Further, particles thereof were fragmented so as to pass through a JIS standard sieve (mesh size is 850 ⁇ m) , thereby obtaining a comparative water absorbent resin composition (2) .
- Table 4 shows a result obtained by measuring properties of the comparative water absorbent resin composition (2) .
- Table 4 shows that: the water absorbent resin composition ( 1) , obtained in Example 5, whose multivalent metal component (aluminum) concentration in the surface treatment agent is high, has much higher SFC and AAP than those of the comparative water absorbent resin composition
- the multivalent metal component concentration in the surface treatment agent is raised, thereby obtaining the water absorbent resin composition having much higher saline flow conductivity (SFC) and moisture absorption blocking property than those of a water absorbent resin composition obtained by a conventional technique, while keeping the same centrifuge retention capacity (CRC) as that of the conventional water absorbent resin composition.
- SFC saline flow conductivity
- CRC centrifuge retention capacity
- the comparative water absorbent resin composition (3) obtained in the Comparative Example 9 it is impossible to obtain the sufficient property by using mere the organic secondary cross-linking agent. That is, the comparative water absorbent resin composition (3) has the same CRC as that of the conventional water absorbent resin composition, but has extremely low SFC and moisture absorption blocking property.
- the comparative water absorbent resin composition (3) does not have a sufficient performance .
- Table 5 shows a result obtained by measuring properties of the water absorbent resin composition (3) .
- a surface treatment agent constituted of a mixture solution obtained by dissolving 0.7 g of ethylenecarbonate and 1 .5 g of aluminum sulfate octadecahydrate in 2.2 g of pure water heated to 80°C was evenly mixed with 100 g of the water absorbent resin (A2) obtained in the Referential
- Example 6 thereby obtaining a precursor (4) .
- precursor (4) was thermally processed at 180°C for 30 minutes. Further, particles thereof were fragmented so as to pass through a JIS standard sieve (mesh size is 710 ⁇ m) , thereby obtaining a water absorbent resin composition (4) .
- Table 5 shows a result obtained by measuring properties of the water absorbent resin composition (4) .
- Thus obtained comparative precursor (4) was thermally processed at 180°C for 30 minutes.
- a surface treatment agent constituted of a mixture solution obtained by mixing 0.7 g of ethylenecarbonate, 2.2 g of pure water, and 0.8 g of aluminum sulfate 18 hydrate was evenly mixed with 100 g of the water absorbent resin (A2) obtained in the Referential Example 6. Thereafter, thus obtained mixture was thermally processed at 180°C for 30 minutes. Further, particles thereof were fragmented so as to pass through a JIS standard sieve (mesh size is 710 ⁇ m) , thereby obtaining a comparative water absorbent resin composition (5) .
- Table 5 shows a result obtained by measuring properties of the comparative water absorbent resin composition (5) .
- Table 5 shows a result obtained by comparing the Example 8 with the Comparative Example 10 under such condition that ethylene carbonate was used as the organic secondary cross-linking agent and the multivalent metal component concentration in the surface treatment agent was varied.
- the solution is at ordinary temperature, it is difficult to prepare the treatment agent having a composition shown in the Example 8 due to the solubility of aluminum sulfate .
- temperature of the treatment agent was raised to 80°C, thereby preparing the treatment agent whose multivalent metal component concentration was high.
- the water absorbent resin composition (4) obtained in this manner was much superior to the comparative water absorbent resin composition (5) obtained in the Comparative Example 10 in terms of the saline flow conductivity (SFC) and the moisture absorption fluidity.
- SFC saline flow conductivity
- precursor (5) was thermally processed at 180°C for 30 minutes.
- Table 6 shows a result obtained by measuring properties of the water absorbent resin composition (6) .
- a surface treatment agent constituted of a mixture solution obtained by mixing 1.0 g of ethyleneglycol, 2.0 g of pure water, and 0.8 g of aluminum chloride 6 hydrate was evenly mixed with 100 g of the water absorbent resin (A3) obtained in the Referential Example 6. Thereafter, thus obtained mixture was thermally processed at 2 10°C for 20 minutes . Further, particles thereof were fragmented so as to pass through a JIS standard sieve (mesh size is 600 ⁇ m) , thereby obtaining a water absorbent resin composition (7) .
- Table 6 shows a result obtained by measuring properties of the water absorbent resin composition (7) .
- a surface treatment agent constituted of a solution obtained by dissolving 0.7 g of ethylenecarbonate and 1.2 g of aluminum sulfate 18 hydrate in 2.2 g of pure water heated to 60°C was evenly mixed with 100 g of the water absorbent resin (A2) obtained in the Referential Example 6. Thereafter, thus obtained mixture was thermally processed at 180°C for 30 minutes. Further, particles thereof were fragmented so as to pass through a JIS standard sieve (mesh size is 710 ⁇ m), thereby obtaining a water absorbent resin composition (8) .
- Table 5 shows a result obtained by measuring properties of the water absorbent resin composition (8) .
- Thus obtained comparative precursor (7) was thermally processed at 180°C for 30 minutes.
- Table 6 shows a result obtained by measuring properties of the comparative water absorbent resin composition (8) .
- a surface treatment agent constituted of a mixture solution obtained by mixing 0.32 g of 1 ,4-butanediol, 0.5 g of propyleneglycol, and 2.73 g of pure water was evenly mixed with 100 g of the water absorbent resin (A3) obtained in the Referential Example 6,. thereby obtaining a comparative precursor (9) .
- Thus obtained comparative precursor (9) was thermally processed at 180°C for 35 minutes. Further, particles thereof were fragmented so as to pass through a JIS standard sieve (mesh size is 600 ⁇ m) , thereby obtaining a comparative water absorbent resin composition (9) .
- Table 6 shows a result obtained by measuring properties of the comparative water absorbent resin composition (9) .
- a surface treatment agent constituted of a mixture solution obtained by mixing 0.32 g of 1 ,4-butanediol, 0.5 g of propyleneglycol, 0.5 g of isopropyl alcohol, and 2.73 g of pure water was evenly mixed with 100 g of the water absorbent resin (A3) obtained in the Referential Example 6, thereby obtaining a comparative precursor ( 10) .
- comparative precursor ( 10) was thermally processed at 190°C for 30 minutes. Further, particles thereof were fragmented so as to pass through a JIS standard sieve (mesh size is 600 ⁇ m) , thereby obtaining a comparative water absorbent resin composition ( 10) .
- Table 6 shows a result obtained by measuring properties of the comparative water absorbent resin composition ( 10) .
- Table 6 shows that: according to the present invention, the multivalent metal component concentration in the surface treatment agent is raised, thereby obtaining the water absorbent resin composition having much higher saline flow conductivity (SFC) and much higher moisture absorption blocking property than those of a water absorbent resin composition obtained by a conventional technique, while keeping the same centrifuge retention capacity (CRC) as that of the conventional water absorbent resin composition.
- SFC saline flow conductivity
- CRC centrifuge retention capacity
- Table 7 shows a result obtained by measuring a moisture absorption blocking ratio (wt %) of each comparative precursor, and also shows properties of each corresponding water absorbent resin composition. Table 7 shows that: as the humidification blocking ratio is smaller, both the SFC and the moisture absorption fluidity of the water absorbent resin composition are higher. On the basis of such characteristic, the inventors of the present invention succeeded in obtaining the water absorbent resin composition, having extremely high saline flow conductivity
- (A ⁇ m or more) represents a water absorbent resin remaining on a sieve whose mesh size is A ⁇ m after performing the classification.
- (B ⁇ m or more) represents a water absorbent passing through a sieve whose mesh size is B ⁇ m after performing the classification.
- (C to D ⁇ m) represents a water absorbent resin which passes through a sieve whose mesh size is C ⁇ m and remains on a sieve whose mesh size is D ⁇ m after performing the classification.
- EGDGE Ethyleneglycol diglycidyl ether
- ASH 14- 18W Aluminum sulfate hydrate (tetradecahydrate to octadecahydrate)
- AICI3-6W Aluminum chloride hexahydrate
- the water absorbent resin of the present invention is favorably used in sanitary materials such as paper diapers, sanitary napkins, incontinence pads, medical pads, and the like.
Abstract
Description
Claims
Priority Applications (5)
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BRPI0411370-5A BRPI0411370B1 (en) | 2003-06-24 | 2004-06-23 | ABSORBENT WATER RESIN COMPOSITION, ABSORBENT, ABSORBENT ARTICLE, METHOD FOR PRODUCING A WATER ABSORBENT RESIN COMPOSITION |
CN2004800177650A CN1813033B (en) | 2003-06-24 | 2004-06-23 | Water-absorptive resin composition and its production process |
EP04746711A EP1641883B1 (en) | 2003-06-24 | 2004-06-23 | Water absorbent resin compostion and production method thereof |
US10/562,140 US7960469B2 (en) | 2003-06-24 | 2004-06-23 | Water absorbent resin composition and production method thereof |
MXPA05013945 MX285679B (en) | 2003-06-24 | 2004-06-23 | COMPOSITION OF ABSORBENT WATER RESIN AND PRODUCTION METHOD OF THE SAME. |
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US (1) | US7960469B2 (en) |
EP (1) | EP1641883B1 (en) |
JP (1) | JP4683405B2 (en) |
KR (1) | KR100709911B1 (en) |
CN (1) | CN1813033B (en) |
BR (1) | BRPI0411370B1 (en) |
IN (1) | IN2006CH00111A (en) |
MX (1) | MX285679B (en) |
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Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH11240959A (en) * | 1998-02-24 | 1999-09-07 | Nippon Shokubai Co Ltd | Water absorptive polymer composition and its production |
JPH11315147A (en) * | 1998-03-03 | 1999-11-16 | Nippon Shokubai Co Ltd | Production of water absorbing agent |
JP2000302876A (en) * | 1999-02-15 | 2000-10-31 | Nippon Shokubai Co Ltd | Production of water absorptive resin powder, water absorptive resin powder and its use |
JP2001098170A (en) * | 1999-07-26 | 2001-04-10 | Nippon Shokubai Co Ltd | Water absorbent composition and its usage |
JP2001096151A (en) | 1999-10-01 | 2001-04-10 | Nippon Shokubai Co Ltd | Water absorbent and its preparing method |
JP2003105092A (en) * | 2001-06-08 | 2003-04-09 | Nippon Shokubai Co Ltd | Water-absorbing agent and its manufacturing method, and hygienic material |
JP2003165883A (en) * | 2001-09-18 | 2003-06-10 | San-Dia Polymer Ltd | Water-absorbing polymer and absorbing article using the same |
Family Cites Families (79)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3959569A (en) * | 1970-07-27 | 1976-05-25 | The Dow Chemical Company | Preparation of water-absorbent articles |
US3935099A (en) * | 1974-04-03 | 1976-01-27 | The United States Of America As Represented By The Secretary Of Agriculture | Method of reducing water content of emulsions, suspensions, and dispersions with highly absorbent starch-containing polymeric compositions |
JPS51125468A (en) * | 1975-03-27 | 1976-11-01 | Sanyo Chem Ind Ltd | Method of preparing resins of high water absorbency |
US4043952A (en) * | 1975-05-09 | 1977-08-23 | National Starch And Chemical Corporation | Surface treatment process for improving dispersibility of an absorbent composition, and product thereof |
JPS5265597A (en) * | 1975-11-27 | 1977-05-31 | Sumitomo Chem Co Ltd | Preparation of high polimeric materials with improved water absorption |
JPS5346389A (en) * | 1976-10-07 | 1978-04-25 | Kao Corp | Preparation of self-crosslinking polymer of acrylic alkali metal salt |
US4286082A (en) * | 1979-04-06 | 1981-08-25 | Nippon Shokubai Kagaku Kogyo & Co., Ltd. | Absorbent resin composition and process for producing same |
JPS6056724B2 (en) * | 1980-10-22 | 1985-12-11 | 株式会社クラレ | Manufacturing method of water absorbent resin |
GB2088392B (en) * | 1980-12-03 | 1984-05-02 | Sumitomo Chemical Co | Production of hydrogels |
JPS57158209A (en) * | 1981-03-25 | 1982-09-30 | Kao Corp | Production of bead-form highly water-absorbing polymer |
US4985518A (en) * | 1981-10-26 | 1991-01-15 | American Colloid Company | Process for preparing water-absorbing resins |
US4558091A (en) * | 1983-05-13 | 1985-12-10 | Grain Processing Corporation | Method for preparing aluminum and polyhydric alcohol modified liquid absorbing composition |
JPS60163956A (en) | 1984-02-04 | 1985-08-26 | Arakawa Chem Ind Co Ltd | Production of water-absorptive resin |
JP2509087B2 (en) | 1984-08-11 | 1996-06-19 | 三洋化成工業株式会社 | Water absorbent resin, manufacturing method and water absorbent, water retention agent |
US4625001A (en) * | 1984-09-25 | 1986-11-25 | Nippon Shokubai Kagaku Kogyo Co., Ltd. | Method for continuous production of cross-linked polymer |
JPS6187702A (en) * | 1984-10-05 | 1986-05-06 | Seitetsu Kagaku Co Ltd | Production of water-absorptive resin |
US4654039A (en) * | 1985-06-18 | 1987-03-31 | The Proctor & Gamble Company | Hydrogel-forming polymer compositions for use in absorbent structures |
JPS627745A (en) | 1985-07-03 | 1987-01-14 | Sanyo Chem Ind Ltd | Water-absorptive resin composition its production and water-absorptive and retentive agent |
CA1280398C (en) * | 1986-02-05 | 1991-02-19 | Hideharu Shirai | Water-absorbent resin and process for producing the same |
JPS63270741A (en) | 1986-02-05 | 1988-11-08 | Sekisui Plastics Co Ltd | Production of water-absorptive polyacrylic acid resin |
DE3609545A1 (en) * | 1986-03-21 | 1987-09-24 | Basf Ag | METHOD FOR THE DISCONTINUOUS PRODUCTION OF CROSSLINKED, FINE-PARTICLE POLYMERISATS |
JPH0615574B2 (en) | 1987-08-26 | 1994-03-02 | 積水化成品工業株式会社 | Method for producing water absorbent resin |
CA1333439C (en) * | 1988-05-23 | 1994-12-06 | Akito Yano | Method for production of hydrophilic polymer |
US6087002A (en) * | 1988-06-28 | 2000-07-11 | Nippon Shokubai Kagaku Kogyo Co. Ltd. | Water absorbent resin |
US5244735A (en) * | 1988-06-28 | 1993-09-14 | Nippon Shokubai Kagaku Kabushiki Kaisha | Water-absorbent resin and production process |
TW201758B (en) * | 1988-06-28 | 1993-03-11 | Catalyst co ltd | |
KR930007272B1 (en) * | 1988-06-28 | 1993-08-04 | 닙본 쇼쿠바이 가브시기 가이샤 | Water-absorbent resin and production process |
JP2930555B2 (en) | 1988-07-04 | 1999-08-03 | 株式会社日本触媒 | Method for producing water absorbent resin |
US5145906A (en) * | 1989-09-28 | 1992-09-08 | Hoechst Celanese Corporation | Super-absorbent polymer having improved absorbency properties |
JP2877255B2 (en) | 1989-12-08 | 1999-03-31 | 株式会社日本触媒 | Manufacturing method of water absorbent resin with excellent durability |
EP0454497B1 (en) * | 1990-04-27 | 1997-02-26 | Nippon Shokubai Co., Ltd. | Method for production of salt-resistant absorbent resin |
US5241009A (en) | 1990-05-07 | 1993-08-31 | Kimberly-Clark Corporation | Polymeric composition containing carboxy nueutralized with lithium or potassium |
DE69108804T2 (en) * | 1990-07-17 | 1995-08-24 | Sanyo Chemical Ind Ltd | Process for the production of water-absorbent resins. |
TW241279B (en) * | 1991-02-01 | 1995-02-21 | Catalyst co ltd | |
US5250640A (en) * | 1991-04-10 | 1993-10-05 | Nippon Shokubai Co., Ltd. | Method for production of particulate hydrogel polymer and absorbent resin |
JPH0540780A (en) | 1991-08-07 | 1993-02-19 | Nec Software Ltd | Vectorizing processing system |
JP3205422B2 (en) | 1992-04-17 | 2001-09-04 | 花王株式会社 | Super absorbent polymer |
JP3121934B2 (en) | 1992-09-25 | 2001-01-09 | 株式会社日本触媒 | Water-absorbing resin composition |
US5849405A (en) * | 1994-08-31 | 1998-12-15 | The Procter & Gamble Company | Absorbent materials having improved absorbent property and methods for making the same |
EP0744965A1 (en) * | 1994-02-17 | 1996-12-04 | The Procter & Gamble Company | Absorbent materials having modified surface characteristics and methods for making the same |
JPH09509591A (en) | 1994-02-17 | 1997-09-30 | ザ、プロクター、エンド、ギャンブル、カンパニー | Absorbent material with improved absorbent properties and method of making same |
US5610208A (en) | 1994-02-17 | 1997-03-11 | Nippon Shokubai Co., Ltd. | Water-absorbent agent, method for production thereof, and water-absorbent composition |
US5843575A (en) * | 1994-02-17 | 1998-12-01 | The Procter & Gamble Company | Absorbent members comprising absorbent material having improved absorbent property |
KR0183511B1 (en) * | 1994-06-13 | 1999-04-15 | 다나카 쇼소 | Water absorbent process for producing the same and absorbent article containing the same |
JP2918808B2 (en) | 1994-06-13 | 1999-07-12 | 株式会社日本触媒 | Absorber and absorbent article |
USRE38444E1 (en) * | 1994-06-13 | 2004-02-24 | Nippon Shokubai Co., Ltd. | Absorbing agent, process of manufacturing same, and absorbent product containing same |
KR100371649B1 (en) * | 1994-08-12 | 2003-05-22 | 가오가부시끼가이샤 | Process for producing improved super absorbent polymer |
JP2938775B2 (en) | 1994-12-27 | 1999-08-25 | 花王株式会社 | Method for producing improved superabsorbent resin |
JP3103754B2 (en) | 1995-10-31 | 2000-10-30 | 三洋化成工業株式会社 | Modified water-absorbing resin particles and method for producing the same |
DE19646484C2 (en) * | 1995-11-21 | 2000-10-19 | Stockhausen Chem Fab Gmbh | Liquid absorbing polymers, processes for their production and their use |
EP0812873B2 (en) * | 1995-12-27 | 2018-10-24 | Nippon Shokubai Co., Ltd. | Water absorbent and process and equipment for the production thereof |
US6194531B1 (en) | 1996-06-05 | 2001-02-27 | Nippon Shokubai Co., Ltd. | Method for production of cross-linked polymer |
JPH10147724A (en) | 1996-11-19 | 1998-06-02 | Kao Corp | Resin composition of high water absorption |
US6951895B1 (en) * | 1996-12-02 | 2005-10-04 | Kimberly-Clark Worldwide, Inc. | Absorbent composition |
US6232520B1 (en) | 1997-02-19 | 2001-05-15 | The Procter & Gamble Company | Absorbent polymer compositions having high sorption capacities under an applied pressure |
KR100639053B1 (en) | 1997-04-29 | 2006-10-27 | 다우 글로벌 테크놀로지스 인크. | Superabsorbent polymers having improved processability |
JP2001523289A (en) | 1997-04-29 | 2001-11-20 | ザ・ダウ・ケミカル・カンパニー | Resilient superabsorbent composition |
US6228930B1 (en) * | 1997-06-18 | 2001-05-08 | Nippon Shokubai Co., Ltd. | Water-absorbent resin granule-containing composition and production process for water-absorbent resin granule |
TW473485B (en) | 1997-12-10 | 2002-01-21 | Nippon Catalytic Chem Ind | The production process of a water-absorbent resin |
US6254990B1 (en) * | 1998-02-18 | 2001-07-03 | Nippon Shokubai Co., Ltd. | Surface-crosslinking process for water-absorbent resin |
US6599989B2 (en) * | 1998-03-03 | 2003-07-29 | Nippon Skokubai Co., Ltd. | Water-absorbent agents containing polycarboxylic amine chelating agents |
KR100476170B1 (en) | 1998-04-28 | 2005-03-10 | 니폰 쇼쿠바이 컴파니 리미티드 | Method for preparing gel state material containing water from water absorbing resin |
US6124391A (en) * | 1998-08-18 | 2000-09-26 | Stockhausen Gmbh & Co. Kg | Superabsorbent polymers having anti-caking characteristics |
US6562743B1 (en) | 1998-12-24 | 2003-05-13 | Bki Holding Corporation | Absorbent structures of chemically treated cellulose fibers |
US6562879B1 (en) | 1999-02-15 | 2003-05-13 | Nippon Shokubai Co., Ltd. | Water-absorbent resin powder and its production process and use |
US6232510B1 (en) * | 1999-02-26 | 2001-05-15 | General Electric Company | Method and composition for hydroxylation of aromatic substrates |
DE19909653A1 (en) * | 1999-03-05 | 2000-09-07 | Stockhausen Chem Fab Gmbh | Powdery, crosslinked, aqueous liquids and blood-absorbing polymers, processes for their preparation and their use |
DE19909838A1 (en) * | 1999-03-05 | 2000-09-07 | Stockhausen Chem Fab Gmbh | Powdery, crosslinked, aqueous liquids and blood-absorbing polymers, processes for their preparation and their use |
EP1072630B1 (en) * | 1999-07-26 | 2004-12-01 | Nippon Shokubai Co., Ltd. | Water-absorbing composition and its use |
JP2001252307A (en) | 2000-03-13 | 2001-09-18 | Oji Paper Co Ltd | Absorptive article |
DE10016041A1 (en) | 2000-03-31 | 2001-10-04 | Stockhausen Chem Fab Gmbh | Powdery surface crosslinked polymers |
DE50102334D1 (en) * | 2000-03-31 | 2004-06-24 | Stockhausen Chem Fab Gmbh | POWDERED POLYMERISATE CROSSLINED ON THE SURFACE |
US6906159B2 (en) | 2000-08-03 | 2005-06-14 | Nippon Shokubai Co., Ltd. | Water-absorbent resin, hydropolymer, process for producing them, and uses of them |
DE10043706A1 (en) * | 2000-09-04 | 2002-04-25 | Stockhausen Chem Fab Gmbh | Powdery, crosslinked, aqueous liquids and blood-absorbing polymers, processes for their preparation and their use |
DE10043710B4 (en) | 2000-09-04 | 2015-01-15 | Evonik Degussa Gmbh | Use of powdery postcrosslinked polymers and hygiene articles |
EP1347790A1 (en) * | 2000-12-29 | 2003-10-01 | Basf Aktiengesellschaft | Absorbent compositions |
BR0205523A (en) | 2001-06-08 | 2003-07-08 | Nippon Catalytic Chem Ind | Water absorbing agent and process for its production, and sanitary material |
MX251840B (en) | 2003-02-10 | 2007-11-26 | Nippon Catalytic Chem Ind | Particulate water-absorbing agent. |
US8247491B2 (en) | 2003-02-10 | 2012-08-21 | Nippon Shokubai Co., Ltd. | Water-absorbent resin composition and its production process |
-
2004
- 2004-06-23 EP EP04746711A patent/EP1641883B1/en not_active Revoked
- 2004-06-23 BR BRPI0411370-5A patent/BRPI0411370B1/en active IP Right Grant
- 2004-06-23 MX MXPA05013945 patent/MX285679B/en active IP Right Grant
- 2004-06-23 WO PCT/JP2004/009242 patent/WO2004113452A1/en active Application Filing
- 2004-06-23 JP JP2004185608A patent/JP4683405B2/en active Active
- 2004-06-23 KR KR1020057024740A patent/KR100709911B1/en active IP Right Grant
- 2004-06-23 CN CN2004800177650A patent/CN1813033B/en active Active
- 2004-06-23 RU RU2005140797/04A patent/RU2333229C2/en not_active IP Right Cessation
- 2004-06-23 US US10/562,140 patent/US7960469B2/en active Active
- 2004-06-24 TW TW093118328A patent/TWI332021B/en active
-
2006
- 2006-01-10 IN IN111CH2006 patent/IN2006CH00111A/en unknown
Patent Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH11240959A (en) * | 1998-02-24 | 1999-09-07 | Nippon Shokubai Co Ltd | Water absorptive polymer composition and its production |
JPH11315147A (en) * | 1998-03-03 | 1999-11-16 | Nippon Shokubai Co Ltd | Production of water absorbing agent |
JP2000302876A (en) * | 1999-02-15 | 2000-10-31 | Nippon Shokubai Co Ltd | Production of water absorptive resin powder, water absorptive resin powder and its use |
JP2001098170A (en) * | 1999-07-26 | 2001-04-10 | Nippon Shokubai Co Ltd | Water absorbent composition and its usage |
JP2001096151A (en) | 1999-10-01 | 2001-04-10 | Nippon Shokubai Co Ltd | Water absorbent and its preparing method |
JP2003105092A (en) * | 2001-06-08 | 2003-04-09 | Nippon Shokubai Co Ltd | Water-absorbing agent and its manufacturing method, and hygienic material |
JP2003165883A (en) * | 2001-09-18 | 2003-06-10 | San-Dia Polymer Ltd | Water-absorbing polymer and absorbing article using the same |
Non-Patent Citations (1)
Title |
---|
See also references of EP1641883A4 |
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Also Published As
Publication number | Publication date |
---|---|
RU2005140797A (en) | 2006-07-10 |
KR20060027360A (en) | 2006-03-27 |
EP1641883A1 (en) | 2006-04-05 |
MX285679B (en) | 2011-04-14 |
IN2006CH00111A (en) | 2007-03-02 |
TW200514583A (en) | 2005-05-01 |
CN1813033A (en) | 2006-08-02 |
RU2333229C2 (en) | 2008-09-10 |
MXPA05013945A (en) | 2006-02-24 |
BRPI0411370B1 (en) | 2018-04-10 |
CN1813033B (en) | 2010-06-16 |
EP1641883A4 (en) | 2008-04-09 |
EP1641883B1 (en) | 2012-02-08 |
US20070106013A1 (en) | 2007-05-10 |
US7960469B2 (en) | 2011-06-14 |
BRPI0411370A (en) | 2006-08-01 |
KR100709911B1 (en) | 2007-04-24 |
JP4683405B2 (en) | 2011-05-18 |
JP2005113117A (en) | 2005-04-28 |
TWI332021B (en) | 2010-10-21 |
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