WO2004037903A2 - Absorbierende polymergebilde mit verbesserter retentionskapazität und permeabilität - Google Patents
Absorbierende polymergebilde mit verbesserter retentionskapazität und permeabilität Download PDFInfo
- Publication number
- WO2004037903A2 WO2004037903A2 PCT/EP2003/011828 EP0311828W WO2004037903A2 WO 2004037903 A2 WO2004037903 A2 WO 2004037903A2 EP 0311828 W EP0311828 W EP 0311828W WO 2004037903 A2 WO2004037903 A2 WO 2004037903A2
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- absorbent polymer
- polymer structure
- aqueous solution
- pul
- inorganic compound
- Prior art date
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/18—Stationary reactors having moving elements inside
- B01J19/1806—Stationary reactors having moving elements inside resulting in a turbulent flow of the reactants, such as in centrifugal-type reactors, or having a high Reynolds-number
-
- 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
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
- B01F23/50—Mixing liquids with solids
- B01F23/51—Methods thereof
- B01F23/511—Methods thereof characterised by the composition of the liquids or solids
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
- B01F23/50—Mixing liquids with solids
- B01F23/53—Mixing liquids with solids using driven stirrers
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F33/00—Other mixers; Mixing plants; Combinations of mixers
- B01F33/80—Mixing plants; Combinations of mixers
- B01F33/82—Combinations of dissimilar mixers
- B01F33/821—Combinations of dissimilar mixers with consecutive receptacles
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B7/00—Mixing; Kneading
- B29B7/002—Methods
- B29B7/005—Methods for mixing in batches
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F8/00—Chemical modification by after-treatment
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F27/00—Mixers with rotary stirring devices in fixed receptacles; Kneaders
- B01F27/05—Stirrers
- B01F27/11—Stirrers characterised by the configuration of the stirrers
- B01F27/114—Helically shaped stirrers, i.e. stirrers comprising a helically shaped band or helically shaped band sections
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F29/00—Mixers with rotating receptacles
- B01F29/40—Parts or components, e.g. receptacles, feeding or discharging means
- B01F29/401—Receptacles, e.g. provided with liners
- B01F29/402—Receptacles, e.g. provided with liners characterised by the relative disposition or configuration of the interior of the receptacles
- B01F29/4022—Configuration of the interior
- B01F29/40221—Configuration of the interior provided with baffles, plates or bars on the wall or the bottom
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
- Y10T428/00—Stock material or miscellaneous articles
- Y10T428/24—Structurally defined web or sheet [e.g., overall dimension, etc.]
- Y10T428/24942—Structurally defined web or sheet [e.g., overall dimension, etc.] including components having same physical characteristic in differing degree
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
- Y10T428/00—Stock material or miscellaneous articles
- Y10T428/29—Coated or structually defined flake, particle, cell, strand, strand portion, rod, filament, macroscopic fiber or mass thereof
- Y10T428/2982—Particulate matter [e.g., sphere, flake, etc.]
- Y10T428/2991—Coated
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
- Y10T428/00—Stock material or miscellaneous articles
- Y10T428/29—Coated or structually defined flake, particle, cell, strand, strand portion, rod, filament, macroscopic fiber or mass thereof
- Y10T428/2982—Particulate matter [e.g., sphere, flake, etc.]
- Y10T428/2991—Coated
- Y10T428/2993—Silicic or refractory material containing [e.g., tungsten oxide, glass, cement, etc.]
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
- Y10T428/00—Stock material or miscellaneous articles
- Y10T428/29—Coated or structually defined flake, particle, cell, strand, strand portion, rod, filament, macroscopic fiber or mass thereof
- Y10T428/2982—Particulate matter [e.g., sphere, flake, etc.]
- Y10T428/2991—Coated
- Y10T428/2993—Silicic or refractory material containing [e.g., tungsten oxide, glass, cement, etc.]
- Y10T428/2995—Silane, siloxane or silicone coating
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
- Y10T428/00—Stock material or miscellaneous articles
- Y10T428/29—Coated or structually defined flake, particle, cell, strand, strand portion, rod, filament, macroscopic fiber or mass thereof
- Y10T428/2982—Particulate matter [e.g., sphere, flake, etc.]
- Y10T428/2991—Coated
- Y10T428/2993—Silicic or refractory material containing [e.g., tungsten oxide, glass, cement, etc.]
- Y10T428/2996—Glass particles or spheres
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
- Y10T428/00—Stock material or miscellaneous articles
- Y10T428/29—Coated or structually defined flake, particle, cell, strand, strand portion, rod, filament, macroscopic fiber or mass thereof
- Y10T428/2982—Particulate matter [e.g., sphere, flake, etc.]
- Y10T428/2991—Coated
- Y10T428/2998—Coated including synthetic resin or polymer
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
- Y10T428/00—Stock material or miscellaneous articles
- Y10T428/31504—Composite [nonstructural laminate]
Definitions
- the invention relates to a method for producing an absorbent polymer structure, an absorbent polymer structure obtainable by this method, an absorbent polymer structure, a composite, a method for producing a composite, a composite obtainable from this method, chemical products containing the absorbent polymer structure or the composite, the use of the absorbent polymer structure or the composite in chemical products, an aqueous solution, a method for producing the aqueous solution, an aqueous solution obtainable by the method and the use of the aqueous solution for treating the outside of an absorbent polymer structure.
- Superabsorbers are water-insoluble, crosslinked polymers which are able to absorb large amounts of aqueous liquids, in particular body fluids, preferably urine or blood, with the swelling and formation of hydrogels and to retain them under a certain pressure. Due to these characteristic properties, these polymers are mainly used for incorporation into sanitary articles, such as baby diapers, incontinence products or sanitary napkins.
- the superabsorbers currently commercially available are essentially crosslinked polyacrylic acids or crosslinked starch-acrylic acid graft polymers in which the carboxyl groups are partially neutralized with sodium hydroxide solution or potassium hydroxide solution.
- the superabsorbent has further tasks with regard to the transport and distribution of liquid, which can be summarized as permeability properties.
- permeability means the ability to transport added liquids in the swollen state and to distribute them three-dimensionally. This process takes place in the swollen superabsorbent gel via capillary transport through spaces between the gel particles. Liquid transport by swollen superabsorbent particles themselves follows the laws of diffusion and is a very slow process, which plays no role in the distribution of the liquid in the use situation of the sanitary article.
- superabsorbent materials which cannot achieve capillary transport due to a lack of gel stability, embedding these materials in a fiber matrix ensured separation of the particles from one another while avoiding the gel blocking phenomenon.
- the superabsorbers used here must therefore have a sufficiently high stability in the swollen state so that the swollen gel still has a sufficient amount of capillary spaces through which liquid can be transported.
- EP-A-0 450 923, EP-A-0 450 922, DE-A-35 23 617, US 5,140,076 and US 4,734,478 describe the treatment of the surface of absorbent polymers by bringing the surface into contact with inorganic compounds, such as, for example, with finely divided silica, during or after the post-crosslinking of the surface.
- inorganic compounds such as, for example, with finely divided silica
- this type of surface treatment also increases the permeability of the absorbent polymers.
- DE 35 03 458 describes a process for producing an improved absorbent resin, in which a water-absorbent resin, which contains units of a monomer with a carboxyl group in the form of the free acid or a salt as a constituent component thereof, in the presence of a powder of a finely divided metal oxide allows a crosslinking agent and water to be absorbed and the resulting mixture is heated with stirring to effect crosslinking of the resin and removal of water.
- absorbent resins with a good water absorption capacity are obtained, which at the same time have a good absorption rate.
- No. 4,535,098 describes a process for increasing the gel strength of non-post-crosslinked superabsorbers by swelling absorbent polymers in the presence of a colloidally disperse, inorganic compound, such as a silica sol, or by producing an absorbent polymer in the presence of a colloidally disperse, inorganic compound.
- DE 198 05 447 discloses a process for the post-crosslinking of polyacrylonitrile hydrolyzates with bifunctional compounds and a simultaneous immobilization of silica in the surface structure of the superabsorbent polymer. The silica was brought into contact with the surface together with the crosslinking agent in a water / alcohol mixture. Immobilization of the silica is said to improve absorption under load and reduce gel blocking.
- No. 5,147,921 discloses the addition of a silica sol as an inert filler that can be dispersed in the monomer solution to be polymerized.
- JP 1994-16822 describes the aftertreatment of the surface of absorbent polymers with an inorganic sol.
- an organic solvent component is additionally added.
- Mono- and dimethyl ethers of diols or diols themselves are mentioned as organic solvent components.
- the absorbent polymers should have a higher gel stability, a lower tendency to gel blocking and an improved permeability for water in simple tests without pressure loading of the superabsorbers.
- the invention is based on the object of overcoming the disadvantages arising from the prior art.
- a further object of the invention is superabsorbent
- these polymers should contain the smallest possible amounts of toxic monomers, such as acrylamide or acrylonitrile, which wash out when the superabsorbent polymers come into contact with body fluids and, for example when the superabsorbent polymers are used in diapers, in this way in contact with the skin of the diaper wearer can kick.
- toxic monomers such as acrylamide or acrylonitrile
- a further object on which the present invention is based was to provide hygiene articles, such as, for example, diapers, which, in comparison with the hygiene articles known from the prior art, are better able to retain absorbed body fluids, absorb liquids under pressure and when absorbing liquids distribute them as quickly and evenly as possible in the hygiene article.
- Another object of the invention is to provide a method with which such absorbent polymers can be produced in a simple, continuous manner as small as possible amounts of organic solvents.
- added inorganic auxiliaries should detach from the superabsorbent polymer in small amounts at most, which do not adversely affect the polymer properties.
- the solution used in this process for treating the surface of the absorbent polymer should be able to be handled like a single-phase system and should be able to be metered uniformly.
- the coated superabsorbent should only form agglomerates to a minor extent in the course of the process and should be able to be fed to a continuously operating annealing step in a simple manner.
- Steps bringing the outer area of the untreated absorbent polymer structure (Pul) into contact with an aqueous solution containing at least one chemical crosslinker and at least one inorganic compound in colloidally dispersed form;
- Inner area is more crosslinked and the inorganic compound is at least partially immobilized in the outer area of the absorbent polymer structure.
- Absorbent polymer structures (Pa) according to the invention are fibers, foams or particles, fibers and particles being preferred and particles being particularly preferred. Absorbent polymer structures (Pa) in these forms are obtained by using fibers, foams or particles in a corresponding manner as the absorbent polymer structures (Pul) or (Pu2).
- Absorbent polymer fibers preferred according to the invention are dimensioned such that they can be incorporated in or as a game for textiles and also directly in textiles. It is preferred according to the invention that the absorbent polymer fibers have a length in the range from 1 to 500, preferably 2 to 500 and particularly preferably 5 to 100 mm and a diameter in the range from 1 to 200, preferably 3 to 100 and particularly preferably 5 to 60 denier have.
- Absorbent polymer particles which are particularly preferred according to the invention are dimensioned such that they have an average particle size according to ERT 420.1-99 in the range from 10 to 3000, preferably 20 to 2000 and particularly preferably 150 to 850 ⁇ m.
- the absorbent polymer structure (Pul) or (Pu2) used in the process according to the invention is preferably a polymer structure which is based on ( ⁇ l) 20-99.999% by weight, preferably 55 to 98.99% by weight and particularly preferably 70 to 98, 79% by weight of polymerized, ethylenically unsaturated, acid group-containing monomers or their salts or polymerized, ethylenically unsaturated monomers containing a protonated or quaternized nitrogen, or mixtures thereof, mixtures containing at least ethylenically unsaturated, acid group-containing monomers, preferably acrylic acid, being particularly preferred, ( ⁇ 2) 0-80% by weight, preferably 0-44.99% by weight and particularly preferably 0.1-44.89% by weight of polymerized, monoethylenically unsaturated monomers copolymerizable with ( ⁇ l), ( ⁇ 3) 0.001-5% by weight, preferably 0.01-3% by weight and particularly preferred
- crosslinkers 0.01-2.5% by weight of one or more crosslinkers, ( ⁇ 4) 0-30% by weight, preferably 0-5% by weight and particularly preferably 0.1-5
- Wt .-% of a water-soluble polymer and ( ⁇ 5) 0-20 wt .-%, preferably 0 to 10 wt .-% and particularly preferably 0.1-
- Amounts by weight ( ⁇ l) to ( ⁇ 5) is 100% by weight.
- the monoethylenically unsaturated monomers ( ⁇ l) containing acid groups can be partially or completely, preferably partially, neutralized.
- the monoethylenically unsaturated monomers containing acid groups are preferably neutralized to at least 25 mol%, particularly preferably to at least 50 mol% and moreover preferably to 50-80 mol%.
- Some or all of the neutralization can also be carried out after the polymerization. Neutralization with alkali metal hydroxides,
- Alkaline earth metal hydroxides, ammonia and carbonates and bicarbonates any other base is conceivable that forms a water-soluble salt with the acid.
- Mixed neutralization with different bases is also conceivable. Neutralization with ammonia and
- Alkali metal hydroxides particularly preferably with sodium hydroxide and with
- the free acid groups can also predominate in a polymer, so that this polymer has a pH value in the acidic range.
- This acidic water-absorbing polymer can be at least partially neutralized by a polymer with free basic groups, preferably amine groups, which is basic in comparison to the acidic polymer.
- MIEA polymers Glassed Bed Ion Exchange Absorbent Polymers
- WO 99/34843 The disclosure of WO 99/34843 is hereby introduced as a reference and applies thus as part of the revelation.
- MBIEA polymers are a composition which contains, on the one hand, basic polymers which are able to exchange anions and, on the other hand, a polymer which is acidic in comparison with the basic polymer and which is able to exchange cations.
- the basic polymer has basic groups and is typically obtained by polymerizing monomers that carry basic groups or groups that can be converted to basic groups. These monomers are, above all, those which have primary, secondary or tertiary amines or the corresponding phosphines or at least two of the above functional groups.
- This group of monomers includes in particular ethylene amine, allylamine, diallylamine, 4-aminobutene, alkyloxycyclines, vinylformamide, 5-aminopentene, carbodiimide, formaldacin, melamine and the like, and also their secondary or tertiary amine derivatives.
- the monoethylenically unsaturated monomers ( ⁇ l) containing acid groups can be partially or completely, preferably partially, neutralized.
- the monoethylenically unsaturated monomers containing acid groups are preferably neutralized to at least 25 mol%, particularly preferably to at least 50 mol% and moreover preferably to 50-90 mol%.
- the monomers ( ⁇ l) can also be neutralized before the polymerization.
- Neutralization can also be carried out using alkali metal hydroxides, alkaline earth metal hydroxides, ammonia and carbonates and bicarbonates. In addition, any other base is conceivable that forms a water-soluble salt with the acid. Mixed neutralization with different bases is also conceivable. Neutralization with ammonia or with alkali metal hydroxides is preferred, particularly preferably with sodium hydroxide or with ammonia.
- Preferred monoethylenically unsaturated monomers ( ⁇ l) containing acid groups are acrylic acid, methacrylic acid, ethacrylic acid, ⁇ -chloroacrylic acid, ⁇ -
- Cyanoacrylic acid ß-methyl acrylic acid (crotonic acid), ⁇ -phenylacrylic acid, ß- Acryloxypropionic acid, sorbic acid, ⁇ -chlorosorbic acid, 2'-
- ethylenically unsaturated sulfonic acid monomers or ethylenically unsaturated phosphonic acid monomers are also preferred as monoethylenically unsaturated, acid group-containing monomers ( ⁇ l).
- Ethylenically unsaturated sulfonic acid monomers are preferred allylsulfonic acid or aliphatic or aromatic vinylsulfonic acids or acrylic or methacrylic sulfonic acids.
- Vinyl sulfonic acid, 4-vinylbenzyl sulfonic acid, vinyl toluenesulfonic acid and styrene sulfonic acid are preferred as aliphatic or aromatic vinyl sulfonic acids.
- Preferred acrylic or methacrylic sulfonic acids are sulfoethyl (meth) acrylate, sulfopropyl (meth) acrylate, 2-hydroxy-3-methacryloxypropyl sulfonic acid and 2-acrylamido-2-methylpropane sulfonic acid.
- ethylenically unsaturated phosphonic acid monomers such as vinylphosphonic acid, allylphosphonic acid, vinylbenzylphosphonic acid,
- Preferred ethylenically unsaturated monomers ( ⁇ l) containing a protonated nitrogen are dialkylaminoalkyl (meth) acrylates in protonated form, for example dimethylaminoethyl (meth) acrylate hydrochloride or dimethylaminoethyl (meth) acrylate hydrosulfate, and dialkylaminoalkyl (meth) acrylamides in protonated form Form, for example dimethylaminoethyl (meth) acrylamide hydrochloride or dimethylaminoethyl (meth) acrylamide hydrosulfate is preferred.
- Dialkylammoniumalkyl (meth) acrylates in quaternized form for example trimethylammoniumethyl (meth) acrylate methosulfate or dimethylethylammoniumethyl (meth) acrylate ethosulfate and (meth) acrylamidoalkyl dialkylamines in quaternized form are dialkylammonium alkyl (meth) acrylates as ethylenically unsaturated monomers ( ⁇ l) containing a quaternized nitrogen , for example
- component ( ⁇ l) consists of at least 50% by weight, preferably at least 70% by weight and moreover preferably at least 90% by weight of monomers containing carboxylate groups. It is particularly preferred according to the invention that component ( ⁇ l) consists of at least 50% by weight, preferably at least 70% by weight, of acrylic acid, which preferably neutralizes at least 20 mol%, particularly preferably at least 50 mol% is.
- Acrylamides and methacrylamides are preferred as monoethylenically unsaturated monomers ( ⁇ 2) copolymerizable with ( ⁇ l).
- (meth) acrylamides are alkyl-substituted (meth) acrylamides or aminoalkyl-substituted derivatives of (meth) acrylamide, such as N-methylol (meth) acrylamide, N, N-dimethylamino (meth) acrylamide, dimethyl (meth ) acrylamide or diethyl (meth) acrylamide.
- Possible vinylamides are, for example, N-vinylamides, N-vinylformamides, N-vinyl acetamides, N-vinyl-N-methylacetamides, N-vinyl-N-methylformamides, vinyl pyrrolidone.
- Acrylamide is particularly preferred among these monomers.
- preferred monoethylenically unsaturated monomers ( ⁇ 2) which are copolymerizable with ( ⁇ 1) are water-dispersible monomers.
- water-dispersible monomers are acrylic acid esters and methacrylic acid esters, such as thyl (meth) acrylate, ethyl (meth) acrylate, propyl (meth) acrylate or butyl (meth) acrylate, as well as methyl polyethylene glycol (meth) acrylate,
- Methyl polyethylene glycol allyl ether, vinyl acetate, styrene and isobutylene are preferred.
- the compounds of crosslinking class I crosslink the polymers by radical polymerization of the ethylenically unsaturated groups of the crosslinking molecule with the monoethylenically unsaturated monomers ( ⁇ l) or ( ⁇ 2), while in the case of compounds of crosslinking class II and the polyvalent metal cations of crosslinking class IV crosslinking of the polymers is achieved by the condensation reaction of the functional groups (crosslinking class II) or by electrostatic interaction of the polyvalent metal cation (crosslinking class IV) with the functional groups of the monomers ( ⁇ l) or ( ⁇ 2).
- the polymer is accordingly crosslinked both by radical polymerization of the ethylenically unsaturated group and by a condensation reaction between the functional group of the crosslinking agent and the functional groups of the monomers ( ⁇ l) or ( ⁇ 2).
- Preferred compounds of crosslinking class I are poly (meth) acrylic esters or poly (meth) acrylamides, which, for example, by the reaction of a polyol, such as ethylene glycol, propylene glycol, trimethylol propane, 1,6-hexanediol, glycerol, pentaerythritol, polyethylene glycol or polypropylene glycol, of an amino alcohol , a polyalkylene polyamine, such as diethylenetriamine or triethylenetetraamine, or an alkoxylated polyol with acrylic acid or methacrylic acid.
- a polyol such as ethylene glycol, propylene glycol, trimethylol propane, 1,6-hexanediol, glycerol, pentaerythritol, polyethylene glycol or polypropylene glycol
- a polyalkylene polyamine such as diethylenetriamine or triethylenetetraamine
- Polyvinyl compounds, poly (mefh) allyl compounds, (meth) acrylic acid esters of a monovinyl compound or (meth) acrylic acid esters of a mono (meth) allyl compound, preferably the mono (meth) allyl compounds of a polyol or an amino alcohol, are further preferred as compounds of crosslinking class I.
- alkylene di (mefh) acrylates for example ethylene glycol di (meth) acrylate, 1,3-propylene glycol di (meth) acrylate, 1,4-butylene glycol di (meth) acrylate, 1,3- Butylene glycol di (mefh) acrylate, 1, 6-hexanediol di (meth) acrylate, 1, 10-decanediol di (meth) acrylate, 1, 12-dodecanediol di (meth) acrylate, 1, 18-octadecanediol di (meth) acrylate, cyclopen tandiol di (meth) acrylate, neopentyl glycol di (meth) acrylate, methylene di (meth) acrylate or pentaerythritol di (meth) acrylate, alkenyldi (meth) acrylamides,
- Di (meth) allyl compounds for example di (meth) allyl phthalate or di (meth) allyl succinate, homo- and copolymers of
- These functional groups of the compounds of crosslinker class II are preferably alcohol, amine, aldehyde, glycidyl, isocyanate, carbonate or epichloride functions.
- Examples of compounds of crosslinking class II include polyols, for example ethylene glycol, polyethylene glycols such as diethylene glycol, triefylene glycol and tetraethylene glycol, propylene glycol, polypropylene glycols such as dipropylene glycol, tripropylene glycol or tetrapropylene glycol, 1,3-butanediol, 1,4-butanediol, 1,5-butanediol Pentanediol, 2,4-pentanediol, 1,6-hexanediol, 2,5-hexanediol, glycerin, polyglycerin, trimethylolpropane, polyoxypropylene, oxyethylene-oxypropylene block copolymers, sorbitan fatty acid esters, polyoxyethylene sorbitan fatty acid esters, pentaerythritol, polyvinyl alcohol and sorbitol, for example,
- Hexamethylene diisocyanate polyaziridine compounds such as 2,2-bishydroxy-methylbutanol-tris [3- (l-aziridinyl) propionate], 1,6-hexamethylenediefhylene urea and diphenylmethane-bis-4,4'-N, N'-diethylene urea, Halogenepoxides, for example epichlorohydric and epibromohydrin and ⁇ -methylepichlorohydrin, alkylene carbonates such as 1,3-dioxolan-2-one (ethylene carbonate), 4-methyl-1,3-dioxolan-2-one (propylene carbonate), 4,5-dimethyl -l, 3-dioxolan-2-one, 4,4-dimethyl-l, 3- dioxolan-2-one, 4-ethyl-l, 3-dioxolan-2-one, 4-hydroxymethyl-l, 3-dioxolan-2-one, l, 3-dio
- crosslinker class II Other compounds of crosslinker class II are polyoxazolines such as 1,2-ethylenebisoxazoline, crosslinkers with silane groups such as ⁇ -glycidoxypropyltrimethoxysilane and ⁇ -aminopropyltrimethoxysilane, oxazolidinones such as 2-oxazolidinone, bis- and poly-2-oxazolidinones and digly preferred ,
- Class III compounds include hydroxyl- or amino group-containing esters of (meth) acrylic acid, such as 2-hydroxyethyl (meth) acrylate, as well as hydroxyl- or amino group-containing (meth) acrylamides, or
- the polyvalent metal cations of crosslinking class IV are preferably derived from mono- or polyvalent cations, the monovalent in particular from alkali metals such as potassium, sodium, lithium, lithium being preferred.
- Preferred divalent cations are derived from zinc, beryllium, alkaline earth metals, such as magnesium, calcium, strontium, magnesium being preferred.
- Other higher-value cations which can be used according to the invention are cations of aluminum, iron, chromium, manganese, titanium, zirconium and other transition metals, and also double salts of such cations or mixtures of the salts mentioned.
- Aluminum salts and alums and their different hydrates such as, for. B.
- Al 2 (SO 4 ) 3 and its hydrates are particularly preferably used as crosslinking agents of crosslinking class IV.
- Preferred absorbent polymer structures are polymer structures which are crosslinked by crosslinkers of the following crosslinking classes or by crosslinkers of the following combinations of crosslinking classes: I, II, III, IV, I II, I III, I IN, I II III, I II IV, I III IV, II III IV, II IV or III IN.
- the above combinations of crosslinking classes each represent a preferred embodiment of crosslinking a polymer.
- absorbent polymer structures are polymer structures which are crosslinked by any of the aforementioned crosslinkers of crosslinking classes I.
- crosslinkers of crosslinking classes I.
- water-soluble crosslinkers are preferred.
- ⁇ , ⁇ '-mefhylenebisacrylamide, polyethylene glycol di (meth) acrylates, triallylmethylammonium chloride, tetraallylammonium chloride and allylnonaethylene glycol acrylate prepared with 9 moles of ethylene oxide per mole of acrylic acid are particularly preferred.
- water-soluble polymers such as partially or fully hydrolyzed polyvinyl alcohol, polyvinylpyrrolidone, starch or starch derivatives, polyglycols or polyacrylic acid can preferably be copolymerized in the absorbent polymer structures (Pul) or (Pu2) according to the invention.
- the molecular weight of these polymers is not critical as long as they are water soluble.
- Preferred water-soluble polymers are starch or starch derivatives or polyvinyl alcohol.
- the water-soluble polymers, preferably synthetic such as polyvinyl alcohol can also serve as a graft base for the monomers to be polymerized.
- Auxiliaries ( ⁇ 5) in the absorbent polymer structures (Pul) or (Pu2) used in the process according to the invention may preferably contain adjusting agents, surface-active agents, odor binders, fillers or antioxidants.
- the absorbent polymer structure (Pul) or (Pu2) is a crosslinked polyacrylate in particulate form, which by polymerizing an acrylic acid and optionally one of the The aforementioned crosslinking agent in aqueous solution, comprising the acrylic acid in an amount in a range from 5 to 80% by weight, preferably 10 to 70% by weight and particularly preferably 20 to 50% by weight, based on the weight of the aqueous Solution, and then comminuting the polymer gel obtained, drying the comminuted gel and optionally further grinding the dried polymer gel was obtained.
- the absorbent polymer structures obtained in this way are preferably characterized by a water content of 0.5 to 25% by weight, preferably 1 to 10% by weight.
- the absorbent polymer structures (Pul) or (Pu2) are based on acrylic acid, which is at least 50% by weight, preferably at least 75% by weight and moreover preferably at least 90% by weight is preferably neutralized to at least 20 mol%, particularly preferably to at least 50 mol%.
- the absorbent polymer structure (Pul) or (Pu2) is not based on polyacrylonitrile emulsions. It is preferred that the absorbent polymer structures (Pul) or (Pu2) less than 37 mol%, particularly preferably less than 20 mol%, more preferably less than 10 mol% and furthermore even more preferably less than 5 mol% based on acrylamide and / or acrylonitrile monomers.
- the absorbent polymer structure (Pul) or (Pu2) has a proportion of soluble monomers or polymers based on acrylonitrile and / or acrylamide monomers of less than 1,000 ppm, particularly preferably less than 500 ppm, moreover preferably have less than 100 ppm and, moreover, more preferably less than 10 ppm.
- the absorbent polymer structure (Pul) or (Pu2) can be obtained from the aforementioned monomers and crosslinkers by various polymerization methods produce.
- bulk polymerization which preferably takes place in kneading reactors such as extruders, solution polymerization, spray polymerization, inverse emulsion polymerization and inverse suspension polymerization.
- the solution polymerization is preferably carried out in water as the solvent.
- the solution polymerization can be carried out continuously or batchwise.
- reaction conditions such as temperatures, type and amount of the initiators and also of the reaction solution can be found in the prior art.
- absorbent polymer structures Pul or (Pu2)
- Another possibility for producing the absorbent polymer structures (Pul) or (Pu2) is to first produce uncrosslinked, in particular linear, polymers, preferably by radical means, from the aforementioned monoethylenically unsaturated monomers ( ⁇ l) or ( ⁇ 2) and then crosslinking them Reagents ( ⁇ 3), preferably those of classes II and IV to implement.
- This variant is preferably used when the polymer structures are first to be processed in shaping processes, for example into fibers, foils or other flat structures, such as woven fabrics, knitted fabrics, spunbond or nonwovens, and are to be crosslinked in this form.
- the polymerization is initiated as usual by an initiator. All initiators which form free radicals under the polymerization conditions and are customarily used in the production of superabsorbents can be used as initiators for initiating the polymerization. It is also possible to initiate the polymerization by the action of electron beams on the polymerizable, aqueous mixture. However, the polymerization can also be carried out in the absence of initiators of the type mentioned above Exposure to high-energy radiation can be triggered in the presence of photoinitiators. Polymerization initiators can be dissolved or dispersed in a solution of monomers according to the invention. All radical-decomposing compounds known to those skilled in the art are suitable as initiators.
- Suitable organic peroxides are preferably acetylacetone peroxide,
- azo compounds such as 2,2'-azobis- (2-amidinopropane) dihydrochloride, azo-bis-amidinopropane dihydrochloride, 2,2'-azobis- (N, N-dimethylene) isobutyramidine dihydrochloride , 2- (carbamoylazo) isobutyronitrile and 4,4'-azobis (4-cyanovaleric acid).
- the compounds mentioned are used in customary amounts, preferably in a range from 0.01 to 5, preferably from 0.1 to 2 mol%, in each case based on the amount of the monomers to be polymerized.
- the redox catalysts contain at least one of the above-mentioned per compounds as the oxidic component and preferably ascorbic acid, glucose, sorbose, mannose, ammonium or alkali metal hydrogen sulfite, sulfate, thiosulfate, hyposulfite or sulfide, metal salts such as iron II as the reducing component -ions or silver ions or sodium hydroxymethyl sulfoxylate. Ascorbic acid or sodium pyrosulfite is preferred as the reducing component of the redox catalyst used.
- Relative to the employed in the polymerization amount of monomers is l lO "5 and 1 mol% of the reducing component of the redox catalyst and lxlO" used 5 to 5 mol% of the oxidizing component of the redox catalyst.
- l lO 5 and 1 mol% of the reducing component of the redox catalyst
- lxlO used 5 to 5 mol% of the oxidizing component of the redox catalyst.
- one or more, preferably water-soluble, azo compounds can be used.
- photoinitiators are usually used as initiators. These can be, for example, so-called ⁇ -splitters, H-abstracting systems or also azides.
- initiators are benzophenone derivatives such as Michler's ketone, phenanthrene derivatives, fluorene derivatives, anthraquinone derivatives, thioxanone derivatives, coumarin derivatives, benzoin ethers and their derivatives, azo compounds such as the radical formers mentioned above, substituted Hexaarylbisimidazole or acylphosphine oxides.
- azides examples include: 2- (N, N-dimethylamino) ethyl 4-azidocinnamate, 2- (N, N-dimethylamino) ethyl-4-azidonaphthyl ketone, 2- (N, N-dimethylamino) ethyl-4 -azidobenzoate, 5-azido-1-naphthyl-2 '- (N, N-dimethylamino) ethylsulfone, N- (4-sulfonylazidophenyl) maleinimide, N-acetyl-4-sulfonylazidoaniline, 4-sulfonylazidoaniline, 4-azido aniline, 4-azidophenacyl bromide, p-azidobenzoic acid, 2,6-bis (p-azidobenzylidene) cyclohexanone and 2,6-bis (p-azi
- a redox system consisting of hydrogen peroxide, sodium peroxodisulfate and ascorbic acid is preferably used according to the invention.
- azo compounds according to the invention are preferred as initiators, with azo-bis-amidinopropane dihydrochloride being particularly preferred.
- the polymerization is initiated with the initiators in a temperature range from 30 to 90 ° C.
- the polymer gel is dried up to a water content of 0.5 to 25% by weight, preferably 1 to 10% by weight, at temperatures which are usually in the range from 100 to 200.degree.
- 440.1-99 is in a range from at least 10 to 1000, preferably from
- the proportion extractable according to ERT 470.1-99 with 0.9% by weight of aqueous NaCl solution is less than 30, preferably less than 20 and particularly preferably less than 10% by weight, based on the absorbent polymer structure ( Pul) or (Pu2),
- the bulk density according to ERT 460.1-99 is in the range from 300 to 1000, preferably 310 to 800 and particularly preferably 320 to 700 g / 1,
- the CRC value according to ERT 441.1-99 is in the range from 10 to 100, preferably 15 to 80 and particularly preferably 20 to 60 g / g.
- the contacting of the absorbent polymer structure (Pul) or (Pu2) with the aqueous solution is preferably carried out in the process according to the invention by thorough mixing of the aqueous solution with the absorbent polymer structure (Pul) or (Pu2).
- the aqueous solution is preferably essentially free of organic solvents, in particular free of polyhydric alcohols and polyalkylene glycol ethers, particularly preferably free of diethylene glycol monomethyl ether and 1,3-butanediol.
- an aqueous solution is understood to mean a solution which is at least 50% by weight, particularly preferably at least 60% by weight, moreover preferably at least 70% by weight and beyond more preferably at least 90% by weight, based on the total amount of all components present in the aqueous solution which are liquid at room temperature, based on water.
- the chemical crosslinker can be contained in the aqueous solution containing the inorganic compound in colloidal form from the outset.
- the chemical crosslinker and the colloidally disperse, inorganic compound can be separated, but preferably brought into contact with the absorbent polymer structure (Pul) or (Pu2) at the same time.
- two separate solutions one of which contains the chemical crosslinker and the other the inorganic compound in a colloidally disperse form, are preferably mixed simultaneously with the absorbent polymer structure (Pul) or (Pu2), but with a homogeneous distribution of the chemical crosslinker and the inorganic compound must be guaranteed in colloidal form.
- Suitable mixing units for applying the components are e.g. B. the Patterson-Kelley mixer, DRAIS turbulence mixer, Lödigem mixer, Ruberg Mixers, screw mixers, plate mixers and fluidized bed mixers as well as continuously operating vertical mixers, in which the polymer structure is mixed at high frequency by means of rotating knives (Schugi mixer).
- the absorbent polymer structure (Pul) or (Pu2) is preferably in the process according to the invention preferably at most 20% by weight, particularly preferably at most 15% by weight, more preferably at most 10% by weight, and even more preferably brought into contact with at most 5% by weight of water and most preferably with less than 3% by weight, in each case based on the weight of the absorbent polymer structure (Pul) or (Pu2).
- absorbent polymer structures (Pul) or (Pu2) are used in the form of preferably spherical particles, it is further preferred according to the invention that this is brought into contact in such a way that only the outer area, but not the inner area, of the particle-shaped absorbent polymer structure with the inorganic compound in colloidal dispersed form are brought into contact.
- the outer region of the polymer structures is preferably understood to be that region which is characterized in that the distance of each spatial point lying in this region from the center of the particle is at least 50%, particularly preferably at least 75%, more preferably at least 90% and above more preferably at least 95% of the radius of the particulate absorbent polymer structures.
- the inhomogeneous immobilization of the colloidally disperse inorganic compound on the polymer structures achieved in this way is achieved according to the invention in that dry polymer structures are brought into contact with the aqueous solution and, in addition, only small amounts of water are used such that it is only in the outer region of the absorbent polymer structures absorption of the aqueous liquid. It is further preferred in the process according to the invention that at least 30% by weight, particularly preferably at least 60% by weight and moreover preferably at least 90% by weight of the colloidally disperse inorganic compound have a particle size in the range from 1 to 100, preferably from 5 to 80 and more preferably from 6 to 50 nm.
- the inorganic compound is preferably used in an amount of 0.001 to 10% by weight, particularly preferably 0.01 to 5% by weight and moreover preferably 0.05 to 1.5% by weight, based on the absorbent polymer structure (Pul) or (Pu2), brought into contact with the absorbent polymer structure (Pul) or (Pu2).
- All inorganic compounds which are insoluble in water and from which stable, colloidally disperse, preferably single-phase, aqueous solutions can be obtained which can be obtained at 20 ° C. and normal pressure over a period of at least 6h, preferably at least 24h and particularly preferably at least 72h to can be used as the inorganic compound show no phase separation for 6 months, such as the settling of a solid, inorganic precipitate.
- a colloidally disperse solution is preferably understood to mean a solution which contains particles with a particle diameter in a range from 100-1000 A (10 " to 10 " cm). These solutions have the property of scattering a light beam sent through the solution in all directions so that the path of the light beam through the colloidally dispersed solution can be followed (Tyndall effect, see also Hollemann-Wiberg, Textbook of inorganic chemistry, 91.-100 Edition, de Gruyter Verlag, page 765).
- Particles containing polysilicic acid are used as a particularly preferred colloidally disperse inorganic compound.
- a colloidally disperse solution containing such particles can be obtained, for example, by careful acidification of sodium silicate solutions which react alkaline as a result of hydrolysis, or by dissolving molecular silica in water and possibly subsequently stabilizing the resulting colloidally disperse solution.
- the exact production of such silica sols is known to the person skilled in the art and is described, for example, in Jander-Blasius,, Yearbook of Analytical and Preparative Inorganic Chemistry,, S. Hirzel Verlag, Stuttgart.
- iron (III) oxide hydrate brine In addition to the colloidally disperse silicic acid, iron (III) oxide hydrate brine, tin (IV) oxide hydrate brine or on are also according to the invention.
- Silver halides, in particular silver chloride, based sols are particularly preferred as colloidally disperse inorganic compounds.
- Chemical crosslinkers which are contained in the aqueous solution in the process according to the invention are preferably understood to mean compounds which have at least two functional groups which have functional groups
- Ring opening reaction can react or polyvalent metal cations by electrostatic interaction between the polyvalent
- Post-crosslinking agents are preferred in the process according to the invention to those which, in connection with the crosslinking agents ( ⁇ 3), are the crosslinking agents
- post-crosslinking agents are particularly preferred
- Condensation crosslinking agents such as, for example, diethylene glycol, triethylene glycol, polyethylene glycol, glycerin, polyglycerol, propylene glycol, diethanolamine,
- Ethylene carbonate is particularly preferably used as postcrosslinker.
- the postcrosslinker is preferably used in the process according to the invention in an amount in the range from 0.01 to 30, particularly preferably 0.1 to 20 and moreover preferably from 0.3 to 5% by weight, based on the absorbent polymer structure (pul) or (Pu2) used.
- the post-crosslinking reaction takes place in the process according to the invention by heating the absorbent polymer structure to temperatures in the range from 40 to 300 ° C. preferably from 80 to 250 ° C and particularly preferably from 150 to 220 ° C.
- the optimal duration of the reheating can easily be determined for the individual types of crosslinkers and colloidally disperse inorganic compounds. It is limited when the desired property profile of the super absorber is destroyed again as a result of heat damage.
- the thermal treatment can be carried out in conventional dryers or ovens, examples being rotary tube ovens, fluidized bed dryers, plate dryers, paddle dryers or infrared dryers.
- the outer region of the absorbent polymer structure is more cross-linked than that
- the inorganic External connection is at least partially immobilized.
- the radius of the outer region is smaller than three times the value of the radius of the inner region.
- the outer region of the absorbent polymer structures is brought into contact with a compound containing Al 3+ ions before or after, preferably after, contacting the aqueous solution containing the chemical crosslinker and the inorganic compound in colloidally disperse form brought.
- the compound containing Al ions in an amount in a range from 0.01 to 30 wt .-%, particularly preferably in an amount in a range from 0.1 to 20 wt .-% and beyond preferably in an amount in a range from 0.3 to 5% by weight, in each case based on the weight of the absorbent polymer structures, is brought into contact with the polymer structures.
- the contacting of the outer region of the absorbent polymer structure with the compound containing Al ions preferably takes place by mixing the absorbent polymer structure (Pa) with the compound under dry conditions or by comprising the absorbent polymer structure (Pa) with a fluid a solvent, preferably water, water-miscible organic solvents such as methanol or ethanol or mixtures of at least two of them, and the compound containing Al 3+ ions are brought into contact, the contacting preferably by spraying the polymer particles with the fluid and mixing takes place.
- a solvent preferably water, water-miscible organic solvents such as methanol or ethanol or mixtures of at least two of them
- the compound containing Al 3+ ions are brought into contact
- the contacting preferably by spraying the polymer particles with the fluid and mixing takes place.
- the contacting of the absorbent polymer structure (Pa) with the fluid containing the Al 3+ ion-containing compound takes place in a two-stage process.
- the two-stage process comprises a first mixing process, in which a multiplicity of absorbent polymer structures are mixed with the fluid, and a second mixing process, in which the fluid is homogenized inside the polymer particles, the polymer particles being mixed in the first mixing process at a rate such that the kinetic energy of the individual polymer particles is on average greater than the adhesive energy between the individual polymer particles, and the polymer particles in the second mixing process are at a lower rate than mixed in the first mixing process.
- absorbent polymer structures (Pa) By treating the absorbent polymer structures (Pa) with the fluid containing the Al 3+ ion-containing compound by the two-step process described above, absorbent polymer structures with improved absorption properties can be obtained.
- the compound containing Al 3+ ions is preferably in each case without consideration of water of crystallization in an amount in a range from 0.1 to 50% by weight, particularly preferably in an amount in a range from 1 to 30% by weight based on the total weight of the fluid contained in the fluid. It is further preferred that the fluid in an amount in a range from 0.01 to 15 wt .-%, particularly preferably in an amount in a range from 0.05 to 6 wt .-%, each based on the weight of the absorbent polymer structure (Pa), is brought into contact with the absorbent polymer structure (Pa).
- the present invention further relates to absorbent polymer structures (Pa) which can be obtained by the inventive method described above.
- the invention also relates to an absorbent polymer structure (Pa) comprising an inner region and an outer region surrounding the inner region, wherein the outer area is more cross-linked than the inner area, in the outer area, preferably only in the outer area and not in the inner area, an inorganic compound is at least partially immobilized and wherein the absorbent polymer structure (Pa) has at least one of the following properties:
- Embodiments of the absorbent polymer structure (Pa) according to the invention are preferred in each case Embodiments of the absorbent polymer structure (Pa) according to the invention. Also particularly preferred as embodiments according to the invention is an absorbent polymer structure (Pa) which shows the properties or combinations of properties shown below as letters or combinations of letters: ⁇ 1, ⁇ 2, ⁇ 3, ⁇ 4, ⁇ 5, ⁇ 6, ⁇ 7 , with ⁇ 2, ⁇ 3, ⁇ 4, ⁇ 5 and ⁇ 6 being particularly preferred.
- the absorbent polymer structure (Pa) has an absorbance against pressure (AAP) according to ERT 442.1-99 at a pressure of 50 g / cm of at least 18 g / g, particularly preferably at least 20 g / g and beyond particularly preferably of at least 22 g / g.
- AAP absorbance against pressure
- the radius of the outer region is smaller than twice the value of the radius of the inner region.
- the outer region of the polymer structures is preferably understood to be that region which is characterized in that the distance of each spatial point in this region from the center of the particle is at least 50%, particularly preferably at least 75% , moreover preferably at least 90% and even more preferably at least 95% of the radius of the particulate absorbent polymer structures.
- the inorganic compound, which is at least partially immobilized in the outer region of the absorbent polymer structure (Pa) according to the invention can be any water-insoluble, inorganic compound from which stable, colloidally disperse aqueous solutions can be obtained.
- a particularly preferred inorganic compound which is at least partially immobilized in the outer region of the absorbent polymer structure (Pa) according to the invention is a condensate of polysilicic acids.
- the values of features according to the invention given only with a lower limit have an upper limit which is 20 times, preferably 10 times and particularly preferably 5th -fold the most preferred value of the lower limit.
- the invention further relates to a composite comprising a previously defined absorbent polymer structure (Pa) and a substrate.
- the polymer structure (Pa) according to the invention and the substrate are preferably firmly connected to one another.
- Films made of polymers, such as polyethylene, polypropylene or polyamide, metals, nonwovens, fluff, tissues, fabrics, natural or synthetic fibers, or other foams, are preferred as substrates.
- sealing materials, cables, absorbent cores and diapers and hygiene articles containing them are preferred as the composite.
- the sealing materials are preferably water-absorbent films, in which the absorbent polymer structure (Pa) is incorporated as a substrate in a polymer matrix or fiber matrix. This is preferably done in that the absorbent polymer structure (Pa) is mixed with a polymer (Pm) forming the polymer or fiber matrix and then connected by optionally thermal treatment.
- the absorbent structure is used as a fiber, games can be obtained from it, which are spun with other fibers made of a different material as a substrate and then connected to one another, for example, by weaving or knitting, or directly, ie without being spun with other fibers , Typical procedures for this are in H.
- the absorbent polymer structure (Pa) can be used as particles directly, preferably under the insulation of the cable.
- the absorbent polymer structure (Pa) can be used in the form of swellable, tensile strength games.
- the absorbent polymer structure (Pa) can be used as a swellable film.
- the absorbent can be used as a swellable film.
- Polymer structures (Pa) can be used as a moisture-absorbing core in the middle of the cable.
- the substrate forms all components of the cable which do not contain an absorbent polymer structure (Pa).
- the absorbent polymer structure (Pa) is incorporated into a substrate.
- This substrate is preferably fiber materials.
- Fiber materials in the present Invention can be used include naturally occurring fibers (modified or unmodified) as well as synthetic fibers. Examples of suitable unmodified and modified naturally occurring fibers include cotton, esparto grass, sugar cane, awn hair, flax, silk, wool, pulp, chemically modified pulp, jute, rayon, ethyl cellulose and cellulose acetate.
- Suitable synthetic fibers can be made from polyvinyl chloride, polyvinyl fluoride, polytetrafluoroethylene, polyvinylidene chloride, polyacrylate such as Orion ®, polyvinyl acetate, polyethylvinyl acetate, non-soluble or soluble polyvinyl alcohol, polyolefins such as polyethylene (e.g., PULPEX ®) and polypropylene, polyamides such as nylon, polyesters such as DACRON ® or Kodel, polyurethanes, polystyrene and the like can be produced.
- the fibers used can include only naturally occurring fibers, only synthetic fibers, or any compatible combination of naturally occurring and synthetic fibers.
- the fibers used in the present invention can be hydrophilic or hydrophobic, or they can consist of a combination of hydrophilic and hydrophobic fibers.
- hydrophilic as used herein describes fibers or surfaces of fibers that are wettable by aqueous liquids (e.g. aqueous body fluids) deposited on these fibers. Hydrophilicity and wettability are typically defined in terms of the contact angle and surface tension of the liquids and solids involved. This is discussed in detail in a publication by the American Chemical Society entitled “Contact Angle, Wettability and Adhesion", published by Robert F. Gould (Copyright 1964). A fiber or the surface of a fiber is wetted by a liquid (i.e.
- a fiber or the surface of a fiber is considered to be hydrophobic if the Contact angle is greater than 90 ° and the liquid does not spontaneously spread on the surface of the fiber.
- Fibers preferred according to the invention are hydrophilic fibers.
- Suitable hydrophilic fibers include cellulose fibers, modified cellulose fibers, rayon, polyester fibers such as polyethylene terephthalate (e.g. DACRON ® ), hydrophilic nylon (HYDROFIL ® ) and the like.
- Suitable hydrophilic fibers can also be obtained by hydrophilizing hydrophobic fibers, such as surface-treated or silica-treated thermoplastic fibers based, for example, on polyolefins such as polyethylene or polypropylene or on polyacrylates, polyamides, polystyrene, polyurethanes and the like.
- Cellulose fibers, particularly cellulose fibers are preferred for use in the present invention for reasons of availability and cost.
- hydrophilic fibers for use in the present invention are chemically stiffened cellulose fibers.
- the term "chemically stiffened cellulose fibers” here means cellulose fibers which are stiffened by means of chemical agents in order to increase the stiffness of the fibers under both dry and aqueous conditions.
- Such agents can be chemical stiffeners which, for example, cover and / or impregnate the fibers
- they can also be those chemical stiffeners which stiffen by changing the chemical structure of the fibers, for example caused by the crosslinking of polymer chains
- polymer stiffeners which can cover or impregnate the cellulose fibers include: cationic starches which are nitrogen containing Grappen (for example, amino groups) such as they, NJ, USA are available from the National Starch and Chemical Corp., Bridgewater, latexes, wet strength resins such as polyamide epichlorohydrin resin (eg, Kymene ® 557H, Hercules, Inc., Wilmington, Delaware, USA ), Polya crylamide resins, as described, for example, in US Pat.
- polyacrylamides such as Parez® 631 NZ from American Cyanamid Co., Stanfort, CT, USA, urea formaldehydes and melamine formaldehyde resins.
- Fibers that have been stiffened by crosslinking bonds in individual forms are described, for example, in US Pat. Nos. 3,224,926, 3,440,135, 3,932,209 and 4,035,147.
- Preferred crosslinking agents are glutaraldehyde, glyoxal, formaldehyde, glyoxalic acid, oxydisuccinic acid and citric acid.
- the stiffened cellulose fibers obtained by crosslinking or coating, impregnation or crosslinking can be twisted or crimped, preferably the fibers are twisted and additionally crimped.
- the core can also contain thermoplastic materials.
- thermoplastic materials typically caused by the capillary gradients, travels between the fibers to the intersections of the fibers. These crossings become connection points for the thermoplastic material.
- the thermoplastic material solidifies at these intersections to form junctions that hold the matrix or fabric of the fibers together in each of the respective layers.
- the thermoplastic materials can be in various forms, such as particles, fibers or combinations of particles and fibers.
- thermoplastic polymers selected from polyolefins, such as polyethylene (for example PULPEX®) and polypropylene, polyester, copolyester, polyvinyl acetate, polyethyl vinyl acetate, polyvinyl chloride, polyvinylidene chloride, polyacrylate, polyamide, copolyamide, polystyrene, polyurethane and copolymers of the preceding substances.
- polyolefins such as polyethylene (for example PULPEX®) and polypropylene
- polyester, copolyester polyvinyl acetate, polyethyl vinyl acetate, polyvinyl chloride, polyvinylidene chloride, polyacrylate, polyamide, copolyamide, polystyrene, polyurethane and copolymers of the preceding substances.
- vinyl chloride / vinyl acetate and the like preferably fibrous materials consisting predominantly of cellulose come into consideration as the substrate.
- the core in addition to the substrate and the absorbent polymer structure (Pa), it comprises further powdery substances, such as, for example, odor-binding substances such as cyclodextrins, zeolites, inorganic or organic salts and similar materials.
- powdery substances such as, for example, odor-binding substances such as cyclodextrins, zeolites, inorganic or organic salts and similar materials.
- the absorbent polymer structure (Pa) is incorporated in an amount in the range from 10 to 90, preferably from 20 to 80 and particularly preferably from 40 to 70,% by weight, based on the core.
- the absorbent polymer structure (Pa) is incorporated into the core as particles.
- the absorbent polymer structures (Pa) can be homogeneously distributed in the fiber materials, they can be inserted in layers between the fiber material or the concentration of the absorbent polymer structures (Pa) can have a gradient within the fiber material.
- the absorbent polymer structure (Pa) is incorporated into the core as a fiber.
- absorbent polymer particles which differ, for example, in the suction speed, permeability, storage capacity, absorption against pressure, grain distribution or also the chemical composition, can also be used simultaneously.
- These different polymer particles can be mixed into the suction pad or placed locally differentiated in the core. Such a differentiated placement can take place in the direction of the thickness of the core or the length or width of the core.
- the core can be produced by conventional processes known to the person skilled in the art, as are known to the person skilled in the art in general under the term "drum forming", for example with the aid of shaped wheels, pockets and product forms and correspondingly adapted metering devices for the raw materials.
- established processes such as the so-called airlaid process (e.g. EP 850 615, US 4,640,810) with all forms of metering, depositing the fibers and consolidation such as hydrogen bonding (e.g. DE 197 50 890), thermobonding, latex bonding (e.g. EP 850 615) and hybrid bonding, the so-called wetlaid Processes (e.g.
- this in addition to the substrate and the absorbent polymer structure (Pa) incorporated into the substrate, which together serve as a storage layer for the body fluids, this includes a receiving layer, which is preferably used for the rapid absorption and distribution of the liquid in the core.
- the receiving layer can be arranged directly above the storage layer, but it is also possible for the receiving layer to be separated from the storage layer by a preferably liquid-stable intermediate layer.
- This intermediate layer then primarily serves as a support substrate for the receiving layer and the storage layer.
- Preferred materials for this intermediate layer are polyester spunbonded nonwovens or nonwovens made of polypropylene, polyethylene or nylon.
- the receiving layer is free of the absorbent polymer.
- the receiving layer can be of any suitable size and does not have to extend over the entire length or width of the storage layer.
- the receiving layer can, for example, be in the form of a strip or stain.
- the entire receiving layer is preferably hydrophilic, but it can also have hydrophobic components.
- the receiving layer can be a woven material, a non-woven material or one other suitable type of material.
- the receiving layer is preferably based on hydrophobic polyethylene terephthalate fibers (PET fibers), chemically stiffened cellulose fibers or from mixtures of these fibers.
- PET fibers polyethylene terephthalate fibers
- Other suitable materials are polypropylene, polyethylene, nylon or biological fibers.
- the receiving layer comprises a nonwoven material
- it can be made by a variety of different methods. These include wet laying, airflow application, melt application, spunbond formation, carding (this includes thermal bonding, solvent bonding, or melt spinning bonding).
- the latter processes are preferred when it is desired to align the fibers in the take-up layer because in such processes it is easier to align the fibers in a single direction.
- a particularly preferred material for the receiving layer is a PET spunbond.
- the constituents of the diaper which differ from the absorbent polymer structure (Pa), constitute the substrate of the composite.
- the diaper contains a previously described core.
- the constituent parts of the diaper, which are different from the core constitute the substrate of the composite.
- a composite used as a diaper comprises a water-impermeable lower layer, a water-permeable, preferably hydrophobic, upper layer and a layer containing the absorbent polymer structure (Pa), between the lower layer and the upper layer is arranged.
- This layer containing the absorbent polymer structure (Pa) is preferably a previously described core.
- the lower layer can have all the materials known to the person skilled in the art, with polyethylene or polypropylene being preferred.
- the top layer can likewise contain all suitable materials known to the person skilled in the art, polyester, polyolefins, viscose and the like being preferred which result in a layer which is so porous that there is sufficient liquid passage of the top layer is ensured.
- the invention relates to a method for producing a composite, an absorbent polymer structure according to the invention and a substrate and possibly a suitable auxiliary being brought into contact with one another.
- the contacting is preferably carried out by wetlaid and airlaid processes, compacting, extruding or mixing.
- the invention relates to a composite that can be obtained by the above method.
- the invention further relates to chemical products, in particular foams, moldings, fibers, foils, films, cables, sealing materials, liquid-absorbing hygiene articles, carriers for plant or fungal growth regulators or crop protection agents, additives for building materials, packaging materials or soil additives which comprise the absorbent polymer structure according to the invention (Pa ) or the substrate described above.
- the invention relates to the use of the absorbent polymer structure (Pa) according to the invention or the substrate described above in chemical products, in particular in foams, moldings, fibers, foils, films, cables, sealing materials, and liquid-absorbing materials
- Hygiene articles carriers for plant or fungal growth regulators or crop protection agents, additives for building materials, packaging materials or soil additives.
- a carrier for plant or fungal growth regulating agents or crop protection agents it is preferred that the plant or fungal growth regulating agents or crop protection agents can be released over a period controlled by the carrier.
- the invention further relates to an aqueous solution containing at least one chemical crosslinker and at least one inorganic compound in colloidally dispersed form, the chemical crosslinker and the inorganic compound corresponding to those chemical crosslinkers or inorganic compounds which have already been described in connection with the inventive method described at the outset Production of absorbent polymer structures (Pa) were called.
- the chemical crosslinking agent in the aqueous solution according to the invention is preferably in an amount of 5 to 70% by weight, particularly preferably 20 to 60% by weight and moreover preferably 30 to 50% by weight, based on the amount of Water, in the aqueous solution.
- the inorganic compound in the aqueous solution according to the invention is preferably present in an amount of from 1 to 40% by weight, particularly preferably from 1.5 to 35% by weight and moreover preferably from 2.5 to 32% by weight on the amount of water in the aqueous solution.
- the present invention also relates to a method for producing this aqueous solution, an aqueous solution comprising at least one inorganic compound in colloidally disperse form being mixed with at least one chemical crosslinker.
- the chemical crosslinker as such or in the form of an aqueous solution can be mixed with the aqueous solution containing the inorganic compound in colloidally dispersed form.
- the invention also relates to an aqueous solution which can be obtained by the above process.
- the invention further relates to the use of an aqueous solution containing at least one chemical crosslinker and at least one inorganic compound in colloidally dispersed form or the use of an aqueous solution which can be obtained by the above process for the preparation of an aqueous solution for treating the outer region of an absorbent polymer structure (Pul) or (Pu2).
- the treatment is carried out in the manner already described at the beginning in connection with the method according to the invention for treating the outer area of an absorbent polymer structure (Pul) or (Pu2).
- the absorbent polymer structure (Pul) or (Pu2) corresponds to that absorbent polymer structure (Pul) or (Pu2), which has also already been described in connection with the method according to the invention for treating the outer region of an absorbent polymer structure (Pul) or (Pu2).
- the invention relates to the use of an aqueous solution containing at least one chemical crosslinker and at least one inorganic compound in colloidally disperse form or the use of an aqueous solution which is obtainable by the above process for the preparation of an aqueous solution for adjusting at least one of the following properties in one absorbent polymer structures (Pul) or (Pu2): ( ⁇ l) Saline Flow Conductivity (SFC), ( ⁇ 2) Centrifugation Retention Capacity (CRC) or
- Combinations of properties of two or more of these properties each represent preferred forms of use of the aqueous solution according to the invention. Furthermore, as inventive Embodiments are particularly preferred to use the aqueous solution to adjust the following properties or
- a monomer solution consisting of 280 g of acrylic acid, 70 mol% of which was neutralized with sodium hydroxide solution, 466.8 g of water, 1.4 g of polyethylene glycol 300 diacrylate and 1.68 g of allyloxypolyethylene glycol acrylic acid ester is freed from the dissolved oxygen by flushing with nitrogen and dissolved the start temperature cooled from 4 ° C.
- the initiator solution (0.1 g of 2,2'-azobis-2-amidinepropane dihydrochloride in 10 g of H 2 O, 0.3 g of sodium peroxydisulfate in 10 g of H 2 O, 0.07 g of 30% ge Hydrogen peroxide solution in 1 g H 2 O and 0.015 g ascorbic acid in 2 g HO) added.
- the resulting gel was crushed and dried at 150 ° C for 90 minutes. The dried polymer was roughly crushed, ground and sieved onto a powder with a particle size of 150 to 850 ⁇ m.
- Powder A has a retention capacity of 28.8 g / g.
- a monomer solution consisting of 280 g of acrylic acid, 70% of which was neutralized with sodium hydroxide solution, 467.6 g of water, 0.98 g of polyethylene glycol 300 diacrylate and 1.26 g of allyloxypolyethylene glycol acrylic acid ester is freed from the dissolved oxygen by flushing with nitrogen and dissolved the start temperature cooled from 4 ° C.
- the initiator solution (0.1 g of 2,2'-azobis-2-amidinepropane dihydrochloride in 10 g of H 2 O, 0.3 g of sodium peroxydi sulfate in 10 g H 2 O, 0.07 g 30% ge hydrogen peroxide solution in 1 g H 2 O and 0.015 g ascorbic acid in 2 g H 2 O) added.
- the resulting gel was crushed and dried at 150 ° C for 90 minutes. The dried polymer was roughly crushed, ground and sieved onto a powder with a particle size of 150 to 850 ⁇ m.
- Powder B has a retention capacity of 31.2 g / g.
- a monomer solution consisting of 280 g of acrylic acid, 70 mol% of which was neutralized with sodium hydroxide solution, 468.6 g of water, 0.42 g of polyethylene glycol 300 diacrylate and 0.84 g of allyloxypolyethylene glycol acrylic acid ester is freed from the dissolved oxygen by flushing with nitrogen and dissolved the start temperature cooled from 4 ° C.
- the initiator solution (0.1 g of 2,2'-azobis-2-amidinepropane dihydrochloride in 10 g of H 2 O, 0.3 g of sodium peroxydisulfate in 10 g of H 2 O, 0.07 g of 30 % ge hydrogen peroxide solution in 1 g H 2 O and 0.015 g ascorbic acid in 2 g H 2 O) added.
- the resulting gel was crushed and dried at 150 ° C for 90 minutes. The dried polymer was roughly crushed, ground and sieved onto a powder with a particle size of 150 to 850 ⁇ m.
- Powder C has a retention capacity of 37.1 g / g.
- 50 g of powder A is below by means of a Krups cake mixer with a solution of 0.5 g of ethylene carbonate, 0.84 g silica sol (Levasil ® 200 product of Bayer AG, solids content: about 30 wt .-%) and 0.66 g of water mixed vigorously and then for 30 min. heated in an oven heated to 180 ° C.
- Example 3
- 50 g powder B is mixed with a solution of 0.5 g using a Krups kitchen mixer
- 50 g powder B is mixed with a Krups kitchen mixer with a solution of 0.5 g ethylene carbonate, 0.84 g silica sol (product Levasil ® 200 from Bayer AG, solids content approx. 30% by weight) and 0.66 g water mixed vigorously and then for 30 min. heated in an oven heated to 180 ° C.
- 50 g powder A is mixed using a Krups kitchen mixer with a solution of 0.5 g ethylene carbonate and 1.5 g water with vigorous stirring and then for 30 min. heated in an oven heated to 180 ° C.
- 50 g powder B is mixed with a Kraps kitchen mixer with a solution of 0.5 g ethylene carbonate and 1.5 g water with vigorous stirring and then for 30 min. heated in an oven heated to 180 ° C.
- 50 g powder B is mixed using a Krups kitchen mixer with a solution of 0.5 g ethylene carbonate, 0.125 g Aerosil ® (pyrogenic silica sol from Degussa AG) and 2 g water with vigorous stirring and then for 30 min. heated in an oven heated to 180 ° C. Increased amounts of water were required to produce the suspension of Aerosil ® in water. However, no easily metered suspension could be obtained, since the aerosil introduced settled back very quickly and homogeneous metering onto powder B was not possible. The coated polymer tends to form lumps and is inhomogeneous.
- 50 g powder B is mixed with a Kraps kitchen mixer with a solution of 0.25 g 1,3-butanediol, 0.25 g silica sol (product Levasil ® 200 from Bayer AG, solids content approx. 30% by weight) and 1. 25 g of water mixed with vigorous stirring and then for 3 min. heated in an oven heated to 120 ° C.
- This treatment corresponds to the treatment according to Example 2 of JP 1994/16822.
- the absorbent polymer structures produced according to the invention show a significant increase in permeability (SFC) with constant or even increased retention compared to products whose outer region has been crosslinked in the absence of a silica sol (Examples 1 to 4, Comparative Examples 1 and 2). Aftertreatment of the already crosslinked polymer structures with silica sol does not lead to the desired result regardless of the subsequent thermal treatment (comparative examples 3, 4 and 6).
- Aerosil 200 ® in the post-crosslinking does not lead to comparably good superabsorber characteristics (comparative example 5). Furthermore, increased amounts of Aerosil 200 can no longer be dispersed in an acceptable amount of water and are therefore no longer dispersible.
- Comparative examples 7 and 8 show that in the examples according to the invention of the unexamined JP 1994/16822 it is not possible to achieve good performance of the polymers with regard to their permeability and retention.
- Table 1 INFLUENCE OF THE TREATMENT OF THE EXTERIOR OF THE UNTREATED ABSORBENT POLYMER FABRICS (Pul) ON THE AGGLOMERATION TENDENCY OF THE POLYMER FIELDS.
- 50 g powder B is mixed with a solution of 0.5 g ethylene carbonate and 1.5 g water with vigorous stirring using a Kraps kitchen mixer. A pressure is then produced from the absorbent polymer structure brought into contact with the aqueous solution and its density and the pressure to be used to destroy the compact are determined.
- the swollen gel layer is covered during the measurement with a special sieve cylinder, which ensures an even distribution of the 0.118 M NaCl solution above the gel and constant conditions (measuring temperature 20-25 ° C) during the measurement with regard to the gel bed properties.
- the pressure acting on the swollen superabsorbent is still 20 g / cm.
- the SFC value (K) was given in cm 3 -sg " 'and calculated as follows:
- L 0 is the thickness of the gel layer in cm
- r the density of the NaCl solution (1,003 g / cm 3 )
- A is the area of the top of the gel layer in the measuring cylinder
- the tendency of liquid-coated superabsorbents to form agglomerates is determined using an indicator from J.R. Johanson Inc.
- the superabsorbent is coated with the postcrosslinker solution to be investigated and then 50 g of the powder are fed to the investigation.
- the device produces a compact with a height of approximately 2 cm with a defined pressure of 160,000 pascals using a press ram in a hollow metal cylinder with an inner diameter of 5.23 cm. This compact is then destroyed again by passing a second cylinder, which has a diameter of 4.2 cm, the force being used for this being measured.
Abstract
Description
Claims
Priority Applications (6)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
AU2003296558A AU2003296558A1 (en) | 2002-10-25 | 2003-10-24 | Absorbent polymer structure provided with an improved retention capacity and permeability |
EP03809325.8A EP1563002B2 (de) | 2002-10-25 | 2003-10-24 | Absorbierende polymergebilde mit verbesserter retentionskapazität und permeabilität |
CN200380101982.3A CN1708542B (zh) | 2002-10-25 | 2003-10-24 | 具有提高的保持容量和渗透性的吸收性聚合物结构 |
BR0315653-2A BR0315653A (pt) | 2002-10-25 | 2003-10-24 | "processo para produzir uma estrutura de polìmero absorvente com aperfeiçoadas capacidade de retenção e permeabilidade, polìmeros e compósito obtido e seus usos" |
JP2004545982A JP4806191B2 (ja) | 2002-10-25 | 2003-10-24 | 吸水性ポリマー構造体及び吸水性ポリマー構造体の製造方法、複合体及び複合体の製造方法、化学製品、並びにその使用 |
US10/532,280 US7833624B2 (en) | 2002-10-25 | 2003-10-24 | Absorbent polymer structure with improved retention capacity and permeability |
Applications Claiming Priority (4)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE2002149821 DE10249821A1 (de) | 2002-10-25 | 2002-10-25 | Absorbierende Polymergebilde mit verbesserter Rententionskapazität und Permeabilität |
DE2002149822 DE10249822A1 (de) | 2002-10-25 | 2002-10-25 | Zweistufiges Mischverfahren zur Herstellung eines absorbierenden Polymers |
DE10249822.9 | 2002-10-25 | ||
DE10249821.0 | 2002-10-25 |
Publications (2)
Publication Number | Publication Date |
---|---|
WO2004037903A2 true WO2004037903A2 (de) | 2004-05-06 |
WO2004037903A3 WO2004037903A3 (de) | 2004-06-03 |
Family
ID=32178279
Family Applications (2)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/EP2003/011830 WO2004037900A1 (de) | 2002-10-25 | 2003-10-24 | Zweistufiges mischverfahren zur herstellung eines absorbierenden polymers |
PCT/EP2003/011828 WO2004037903A2 (de) | 2002-10-25 | 2003-10-24 | Absorbierende polymergebilde mit verbesserter retentionskapazität und permeabilität |
Family Applications Before (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/EP2003/011830 WO2004037900A1 (de) | 2002-10-25 | 2003-10-24 | Zweistufiges mischverfahren zur herstellung eines absorbierenden polymers |
Country Status (6)
Country | Link |
---|---|
US (2) | US7833624B2 (de) |
EP (1) | EP1563002B2 (de) |
AU (2) | AU2003296558A1 (de) |
BR (1) | BR0315632A (de) |
TW (2) | TWI378955B (de) |
WO (2) | WO2004037900A1 (de) |
Cited By (24)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE102005018924A1 (de) * | 2005-04-22 | 2006-10-26 | Stockhausen Gmbh | Wasserabsorbierende Polymergebilde mit verbesserten Absorptionseigenschaften |
DE102005018923A1 (de) * | 2005-04-22 | 2006-10-26 | Stockhausen Gmbh | Wasserabsorbierende Polymergebilde mit verbesserten Absorptionseigenschaften |
WO2006111404A2 (de) * | 2005-04-22 | 2006-10-26 | Evonik Stockhausen Gmbh | Oberflächennachvernetzte superabsorber behandelt mit metallsalz und metalloxid |
WO2006092271A3 (de) * | 2005-02-28 | 2007-04-05 | Stockhausen Chem Fab Gmbh | Verfahren zur herstellung eines absorbierenden polymergebildes basierend auf acrylsäure, wobei das substrat für die acrylsäuresynthese teilweise durch enzymatische verfahren gewonnen wurde |
WO2007121941A2 (de) * | 2006-04-21 | 2007-11-01 | Evonik Stockhausen Gmbh | Oberflächennachvernetzte superabsorber behandelt mit organischen und anorganischen feinstteilchen |
CN100348648C (zh) * | 2005-06-14 | 2007-11-14 | 济南昊月树脂有限公司 | 聚丙烯酸钠吸水树脂表面改性方法 |
DE102007007203A1 (de) | 2007-02-09 | 2008-08-14 | Evonik Stockhausen Gmbh | Wasserabsorbierendes Polymergebilde mit hoher Ammoniak-Bindekapazität |
DE102007024080A1 (de) | 2007-05-22 | 2008-11-27 | Evonik Stockhausen Gmbh | Verfahren zum schonenden Mischen und Beschichten von Superabsorbern |
WO2007121937A3 (de) * | 2006-04-21 | 2009-02-26 | Evonik Stockhausen Gmbh | Oberflächennachvernetzte superabsorber behandelt mit aluminiumlactat und optional aluminiumsulfat |
DE102007045724A1 (de) | 2007-09-24 | 2009-04-02 | Evonik Stockhausen Gmbh | Superabsorbierende Zusammensetzung mit Tanninen zur Geruchskontrolle |
DE102007053619A1 (de) | 2007-11-08 | 2009-05-20 | Evonik Stockhausen Gmbh | Wasserabsorbierende Polymergebilde mit verbesserter Farbstabilität |
WO2010115671A1 (de) | 2009-04-07 | 2010-10-14 | Evonik Stockhausen Gmbh | Verwendung von hohlkörpern zur herstellung wasserabsorbierender polymergebilde |
WO2011029704A1 (de) | 2009-09-11 | 2011-03-17 | Evonik Stockhausen Gmbh | Plasmamodifizierung wasserabsorbierender polymergebilde |
DE102010008163A1 (de) | 2010-02-16 | 2011-08-18 | Evonik Stockhausen GmbH, 47805 | Verfahren zur Rückführung von Polymerfeinteilchen |
US8063118B2 (en) | 2007-07-16 | 2011-11-22 | Evonik Stockhausen, Llc | Superabsorbent polymer compositions having color stability |
US8252873B1 (en) | 2010-03-30 | 2012-08-28 | Evonik Stockhausen Gmbh | Process for the production of a superabsorbent polymer |
DE102011086522A1 (de) | 2011-11-17 | 2013-05-23 | Evonik Degussa Gmbh | Superabsorbierende Polymere für hochgefüllte oder faserfreie Hygieneartikel |
TWI405776B (zh) * | 2005-04-22 | 2013-08-21 | Evonik Stockhausen Gmbh | 以聚陽離子表面處理之水份吸收聚合物結構 |
US8653320B2 (en) | 2005-11-18 | 2014-02-18 | Evonik Degussa Gmbh | Deodorizing super-absorbent composition |
US8686216B2 (en) | 2008-03-05 | 2014-04-01 | Evonik Degussa Gmbh | Superabsorbent composition with metal salicylate for odor control |
WO2014072130A1 (de) | 2012-11-09 | 2014-05-15 | Evonik Industries Ag | Superabsorber für kabelanwendungen |
US8829107B2 (en) | 2006-02-28 | 2014-09-09 | Evonik Degussa Gmbh | Biodegradable superabsorbent polymer composition with good absorption and retention properties |
US8906824B2 (en) | 2006-12-18 | 2014-12-09 | Evonik Degussa Gmbh | Water-absorbing polymer structures produced using polymer dispersions |
US10807067B2 (en) | 2016-06-27 | 2020-10-20 | Lg Chem, Ltd. | Method for producing super absorbent polymer and super absorbent polymer |
Families Citing this family (53)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP1541568A1 (de) * | 2003-12-09 | 2005-06-15 | Deutsches Wollforschungsinstitut an der Rheinisch-Westfälischen Technischen Hochschule Aachen e.V. | Reaktive cyclische Carbonate und Harnstoffe zur Modifizierung von Biomolekülen, Polymeren und Oberflächen |
CA2456482A1 (en) * | 2004-02-03 | 2005-08-03 | Bayer Inc. | Method and apparatus for controlling a polymerization reaction |
DE102004019264B4 (de) * | 2004-04-21 | 2008-04-10 | Stockhausen Gmbh | Verfahren zur Herstellung eines absorbierenden Polymers mittels Spreittrocknung |
DE102005010198A1 (de) * | 2005-03-05 | 2006-09-07 | Degussa Ag | Hydrolysestabile, nachvernetzte Superabsorber |
TW200720347A (en) * | 2005-09-30 | 2007-06-01 | Nippon Catalytic Chem Ind | Water-absorbent agent composition and method for manufacturing the same |
WO2007065840A1 (de) * | 2005-12-07 | 2007-06-14 | Basf Se | Verfahren zum kontinuierlichen mischen von polymerpartikeln |
US20070220856A1 (en) * | 2006-03-23 | 2007-09-27 | Fiber Tech Co., Ltd. | Metal fiber media, filter for exhaust gas purifier using the same as filter member, and method for manufacturing the filter |
DE102006039205A1 (de) * | 2006-08-22 | 2008-03-20 | Stockhausen Gmbh | Auf nachwachsenden Rohstoffen basierende Acrylsäure und wasserabsorbierende Polymergebilde sowie Verfahren zu deren Herstellung mittels Dehydratisierung |
US8734559B2 (en) | 2006-09-07 | 2014-05-27 | Biolargo Life Technologies, Inc. | Moderation of animal environments |
US8757253B2 (en) | 2006-09-07 | 2014-06-24 | Biolargo Life Technologies, Inc. | Moderation of oil extraction waste environments |
EP1967258A1 (de) * | 2007-03-06 | 2008-09-10 | Interglass Technology AG | Verfahren zum Mischen einer Flüssigkeit mit mindestens einer weiteren Substanz und Entgasen des Gemisches und für die Abgabe des Gemisches |
SA08290556B1 (ar) | 2007-09-07 | 2012-05-16 | نيبون شوكوباي كو. ، ليمتد | طريقة لربط راتنجات ممتصة للماء |
ATE500883T1 (de) * | 2007-09-07 | 2011-03-15 | Merck Patent Gmbh | Verfahren zur herstellung einer homogenen flüssigen mischung |
US20100063180A1 (en) * | 2008-09-05 | 2010-03-11 | Seungkoo Kang | Fire protection and/or fire fighting additives, associated compositions, and associated methods |
US8357766B2 (en) | 2008-10-08 | 2013-01-22 | Evonik Stockhausen Gmbh | Continuous process for the production of a superabsorbent polymer |
US8048942B2 (en) * | 2008-10-08 | 2011-11-01 | Evonik Stockhausen Gmbh | Process for the production of a superabsorbent polymer |
US8063121B2 (en) * | 2008-10-08 | 2011-11-22 | Evonik Stockhausen Gmbh | Process for the production of a superabsorbent polymer |
EP2404954B1 (de) | 2009-03-04 | 2015-04-22 | Nippon Shokubai Co., Ltd. | Herstellungsverfahren für wasserabsorbierendes harz |
WO2010133460A1 (de) | 2009-05-18 | 2010-11-25 | Basf Se | Beschichtungsverfahren für wasserabsorbierende polymerpartikel |
US9023951B2 (en) | 2009-08-27 | 2015-05-05 | Nippon Shokubai Co., Ltd. | Polyacrylic acid (salt)-type water absorbent resin and method for producing of same |
US8292863B2 (en) | 2009-10-21 | 2012-10-23 | Donoho Christopher D | Disposable diaper with pouches |
US9901128B2 (en) * | 2009-12-24 | 2018-02-27 | David A. Gray | Antimicrobial apparel and fabric and coverings |
US10182946B2 (en) | 2009-12-24 | 2019-01-22 | Liberman Distributing And Manufacturing Co. | Advanced fabric technology and filters |
US9976001B2 (en) | 2010-02-10 | 2018-05-22 | Nippon Shokubai Co., Ltd. | Process for producing water-absorbing resin powder |
WO2011111855A1 (ja) | 2010-03-12 | 2011-09-15 | 株式会社日本触媒 | 吸水性樹脂の製造方法 |
EP2550316B2 (de) * | 2010-03-25 | 2018-11-14 | Basf Se | Verfahren zur herstellung wasserabsorbierender polymerpartikel |
WO2012003435A2 (en) | 2010-07-02 | 2012-01-05 | Liberman Distributing And Manufacturing Co. | Method and structure for nasal dilator |
WO2012040024A1 (en) * | 2010-09-22 | 2012-03-29 | Dow Global Technologies Llc | Treatment of polysaccarides with dialdehydes |
DE102010043113A1 (de) | 2010-10-29 | 2012-05-03 | Evonik Stockhausen Gmbh | Verfahren zur Herstellung von verbesserten absorbierenden Polymeren mittels kryogenem Mahlen |
CN103347548B (zh) | 2011-02-07 | 2017-09-19 | 巴斯夫欧洲公司 | 具有高溶胀速度的吸水性聚合物颗粒的制备方法 |
US9833769B2 (en) | 2011-02-07 | 2017-12-05 | Basf Se | Process for producing water-absorbing polymer particles with high free swell rate |
DE102011007723A1 (de) | 2011-04-20 | 2012-10-25 | Evonik Stockhausen Gmbh | Verfahren zur Herstellung von wasserabsorbierenden Polymeren mit hoher Absorptionsgeschwindigkeit |
US9265855B2 (en) * | 2011-05-18 | 2016-02-23 | The Procter & Gamble Company | Feminine hygiene absorbent article comprising a superabsorbent foam of high swell rate |
DE102011086516A1 (de) | 2011-11-17 | 2013-05-23 | Evonik Degussa Gmbh | Superabsorbierende Polymere mit schnellen Absorptionseigenschaften sowieVerfahren zu dessen Herstellung |
US9427945B2 (en) | 2011-12-30 | 2016-08-30 | Liberman Distributing And Manufacturing Co. | Extendable self-supporting material composites and manufacture thereof |
USH2276H1 (en) | 2012-01-09 | 2013-06-04 | The United States Of America, As Represented By The Secretary Of The Navy | Branched amide polymeric superabsorbents |
EP2615120B2 (de) | 2012-01-12 | 2022-12-21 | Evonik Superabsorber GmbH | Verfahren zur kontinuierlichen Herstellung von wasserabsorbierenden Polymeren |
WO2014064176A1 (de) | 2012-10-24 | 2014-05-01 | Evonik Degussa Gmbh | Geruchs- und farbstabile wasserabsorbierende zusammensetzung |
US9302248B2 (en) | 2013-04-10 | 2016-04-05 | Evonik Corporation | Particulate superabsorbent polymer composition having improved stability |
CN104684969B (zh) | 2013-04-30 | 2016-03-23 | 株式会社Lg化学 | 高吸水树脂 |
EP3009474B1 (de) | 2014-10-16 | 2017-09-13 | Evonik Degussa GmbH | Herstellverfahren für wasserlösliche Polymere |
AT516414B1 (de) * | 2014-10-28 | 2017-07-15 | Chemiefaser Lenzing Ag | Flüssigkeitsgetränkter Vliesstoff, enthaltend Zinkoxid-haltige Cellulosefasern |
KR101857702B1 (ko) * | 2015-12-23 | 2018-05-14 | 주식회사 엘지화학 | 고흡수성 수지의 제조 방법 |
KR101750013B1 (ko) * | 2016-02-19 | 2017-06-22 | 주식회사 엘지화학 | 고흡수성 수지 |
KR102075738B1 (ko) * | 2016-03-11 | 2020-02-10 | 주식회사 엘지화학 | 고흡수성 수지 |
US11198768B2 (en) | 2016-03-11 | 2021-12-14 | Lg Chem, Ltd. | Preparation method of super absorbent polymer |
KR102075737B1 (ko) | 2016-03-11 | 2020-02-10 | 주식회사 엘지화학 | 고흡수성 수지의 제조 방법, 및 고흡수성 수지 |
KR101863350B1 (ko) | 2016-03-31 | 2018-06-01 | 주식회사 엘지화학 | 고흡수성 수지 및 이의 제조 방법 |
KR102093352B1 (ko) | 2016-12-19 | 2020-03-25 | 주식회사 엘지화학 | 고흡수성 수지의 제조 방법 |
KR102157785B1 (ko) * | 2017-02-10 | 2020-09-18 | 주식회사 엘지화학 | 고흡수성 수지 및 이의 제조 방법 |
KR102568226B1 (ko) | 2017-12-11 | 2023-08-18 | 주식회사 엘지화학 | 고흡수성 수지 및 이의 제조 방법 |
EP3779048A4 (de) * | 2018-03-27 | 2022-01-12 | Sumitomo Seika Chemicals Co., Ltd. | Sandsack und verfahren zur herstellung davon |
KR102418591B1 (ko) | 2018-11-13 | 2022-07-07 | 주식회사 엘지화학 | 고흡수성 수지 및 이의 제조 방법 |
Citations (24)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4076663A (en) | 1975-03-27 | 1978-02-28 | Sanyo Chemical Industries, Ltd. | Water absorbing starch resins |
DE2706135A1 (de) | 1977-02-14 | 1978-08-17 | Stockhausen & Cie Chem Fab | Verdickungsmittel fuer ausgeschiedenen darminhalt und harn |
US4286082A (en) | 1979-04-06 | 1981-08-25 | Nippon Shokubai Kagaku Kogyo & Co., Ltd. | Absorbent resin composition and process for producing same |
DE3503458A1 (de) | 1984-02-04 | 1985-08-08 | Arakawa Kagaku Kogyo K.K., Osaka | Verfahren zur herstellung verbesserter wasser absorbierender harze |
US4535098A (en) | 1984-03-12 | 1985-08-13 | The Dow Chemical Company | Material for absorbing aqueous fluids |
DE3523617A1 (de) | 1984-07-02 | 1986-01-23 | Nippon Shokubai Kagaku Kogyo Co. Ltd., Osaka | Wasserabsorbierendes mittel |
DE4020780C1 (de) | 1990-06-29 | 1991-08-29 | Chemische Fabrik Stockhausen Gmbh, 4150 Krefeld, De | |
EP0450922A2 (de) | 1990-04-02 | 1991-10-09 | Nippon Shokubai Kagaku Kogyo Co. Ltd. | Verfahren zur Herstellung von flüssigkeitsstabilem Aggregat |
EP0450923A2 (de) | 1990-04-02 | 1991-10-09 | Nippon Shokubai Co., Ltd. | Verfahren zur Oberflächenbehandlung absorbierender Harze |
US5147921A (en) | 1990-08-14 | 1992-09-15 | Societe Francaise Hoechst | Powdered superabsorbents, containing silica, their preparation process and their use |
JPH0616822A (ja) | 1992-06-30 | 1994-01-25 | Sekisui Plastics Co Ltd | 吸水性樹脂粒子の製造方法 |
DE4244548A1 (de) | 1992-12-30 | 1994-07-07 | Stockhausen Chem Fab Gmbh | Pulverförmige, unter Belastung wäßrige Flüssigkeiten sowie Blut absorbierende Polymere, Verfahren zu ihrer Herstellung und ihre Verwendung in textilen Konstruktionen für die Körperhygiene |
DE4418818A1 (de) | 1993-07-09 | 1995-01-12 | Stockhausen Chem Fab Gmbh | Pulverförmige, vernetzte, wäßrige Flüssigkeiten sowie Körperflüssigkeiten absorbierende Polymere, Verfahren zu ihrer Herstellung und ihre Anwendung |
DE4333056A1 (de) | 1993-09-29 | 1995-03-30 | Stockhausen Chem Fab Gmbh | Pulverförmige, wäßrige Flüssigkeiten absorbierende Polymere, Verfahren zu ihrer Herstellung und ihre Verwendung als Absorptionsmittel |
WO1995022356A1 (en) | 1994-02-17 | 1995-08-24 | The Procter & Gamble Company | Absorbent materials having improved absorbent property and methods for making the same |
DE19529348A1 (de) | 1995-08-09 | 1997-02-13 | Stockhausen Chem Fab Gmbh | Absorptionsmittel für Wasser und wässrige Flüssigkeiten sowie Verfahren zu ihrer Herstellung und Verwendung |
DE19543366A1 (de) | 1995-11-21 | 1997-05-22 | Stockhausen Chem Fab Gmbh | Mit ungesättigten Aminoalkoholen vernetzte, wasserquellbare Polymerisate, deren Herstellung und Verwendung |
DE19646484A1 (de) | 1995-11-21 | 1997-05-22 | Stockhausen Chem Fab Gmbh | Flüssigkeitsabsorbierende Polymere, Verfahren zu deren Herstellung und deren Verwendung |
DE19543368A1 (de) | 1995-11-21 | 1997-05-22 | Stockhausen Chem Fab Gmbh | Wasserabsorbierende Polymere mit verbesserten Eigenschaften, Verfahren zu deren Herstellung und deren Verwendung |
WO1999034843A1 (en) | 1998-01-07 | 1999-07-15 | The Procter & Gamble Company | Absorbent polymer compositions having high sorption capacities under an applied pressure |
DE19805447A1 (de) | 1998-02-11 | 1999-08-12 | Bayer Ag | Modifizierte Superabsorber auf Basis von Polyacrylnitril-Emulsionen |
DE19854575A1 (de) | 1998-11-26 | 2000-05-31 | Basf Ag | Vernetzte quellfähige Polymere |
WO2001013841A1 (de) | 1999-08-20 | 2001-03-01 | Stockhausen Gmbh & Co. Kg | Wasserabsorbierende polymere mit hohlraumverbindungen, verfahren zu deren herstellung und deren verwendung |
EP1211266A1 (de) | 2000-11-30 | 2002-06-05 | Bayer Ag | Verfahren zur Herstellung von Superabsorbern aus Polyacrylnitril-Emulsionen unter adiabatischen Reaktionsbedingungen |
Family Cites Families (61)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4703132A (en) * | 1986-05-16 | 1987-10-27 | Pirelli Cable Corporation | Filling compound for multi-wire conductor of an electrical cable and cables including such compound |
US4985251A (en) * | 1987-04-01 | 1991-01-15 | Lee County Mosquito Control District | Flowable insecticidal delivery compositions and methods for controlling insect populations in an aquatic environment |
US4983390A (en) * | 1987-04-01 | 1991-01-08 | Lee County Mosquito Control District | Terrestrial delivery compositions and methods for controlling insect and habitat-associated pest populations in terrestrial environments |
US4818534A (en) * | 1987-04-01 | 1989-04-04 | Lee County Mosquito Control District | Insecticidal delivery compositions and methods for controlling a population of insects in an aquatic environment |
US4983389A (en) | 1987-04-01 | 1991-01-08 | Lee County Mosquito Control District | Herbicidal delivery compositions and methods for controlling plant populations in aquatic and wetland environments |
EP0320594B2 (de) † | 1987-12-14 | 1998-04-15 | Nippon Shokubai Co., Ltd. | Wässrige härtbare Harzdispersionen, Verfahren zu deren Herstellung und deren Verwendung |
US5326819A (en) * | 1988-04-16 | 1994-07-05 | Oosaka Yuuki Kagaku Kogyo Kabushiki Kaisha | Water absorbent polymer keeping absorbed water therein in the form of independent grains |
US5164428A (en) * | 1988-04-16 | 1992-11-17 | Mitsui Kensetsu Kabushiki Kaisha | Method for the production of fine grain ice and dry clathrate water for manufacturing of concrete/mortar, a method for the production of concrete/mortar by using fine grain ice or dry clathrate water and concrete/mortar products manufactured thereby |
JPH01264803A (ja) | 1988-04-16 | 1989-10-23 | Mitsui Constr Co Ltd | コンクリート・モルタル製造用微粒状氷及びドライ状包接水の製造方法及び、それ等微粒状氷又はドライ状包接水を用いたコンクリート・モルタルの製造方法 |
CA1333439C (en) | 1988-05-23 | 1994-12-06 | Akito Yano | Method for production of hydrophilic polymer |
US5002986A (en) * | 1989-02-28 | 1991-03-26 | Hoechst Celanese Corporation | Fluid absorbent compositions and process for their preparation |
DE69030971T2 (de) * | 1989-09-04 | 1997-12-11 | Nippon Catalytic Chem Ind | Verfahren zur herstellung eines wasserabsorbierenden harzes |
JP2704311B2 (ja) † | 1989-10-03 | 1998-01-26 | 富士写真フイルム株式会社 | 写真印画紙用支持体 |
US5164459A (en) † | 1990-04-02 | 1992-11-17 | Nippon Shokubai Kagaku Kogyo Co., Ltd. | Method for treating the surface of an absorbent resin |
US5369148A (en) † | 1990-04-27 | 1994-11-29 | Nippon Shokubai Co., Ltd. | Method for continuous agglomeration of an absorbent resin powder and apparatus therefor |
DE4015085C2 (de) * | 1990-05-11 | 1995-06-08 | Stockhausen Chem Fab Gmbh | Vernetztes, wasserabsorbierendes Polymer und Verwendung zur Herstellung von Hygieneartikeln, zur Bodenverbesserung und in Kabelummantelungen |
JP2862357B2 (ja) | 1990-09-11 | 1999-03-03 | 日本化薬株式会社 | 吸水剤及びその製造方法 |
US5416174A (en) † | 1992-05-22 | 1995-05-16 | Shin-Etsu Chemical Co., Ltd. | Scale preventive coating of pyrogallol-acetone resin and water soluble polymer |
GB9322119D0 (en) † | 1993-10-27 | 1993-12-15 | Allied Colloids Ltd | Superabsorbent polymers and products containing them |
DE4402187A1 (de) | 1994-01-26 | 1995-07-27 | Bayer Ag | Trägervliese aus synthetischen Fasern und deren Herstellung |
US5843575A (en) * | 1994-02-17 | 1998-12-01 | The Procter & Gamble Company | Absorbent members comprising absorbent material having improved absorbent property |
CN1141005A (zh) * | 1994-02-17 | 1997-01-22 | 普罗克特和甘保尔公司 | 具有改性表面性能的吸收性材料及其制备方法 |
US5849405A (en) * | 1994-08-31 | 1998-12-15 | The Procter & Gamble Company | Absorbent materials having improved absorbent property and methods for making the same |
US5599335A (en) † | 1994-03-29 | 1997-02-04 | The Procter & Gamble Company | Absorbent members for body fluids having good wet integrity and relatively high concentrations of hydrogel-forming absorbent polymer |
JP3776480B2 (ja) † | 1995-06-01 | 2006-05-17 | 大日本印刷株式会社 | 保護層熱転写フィルム及び印画物 |
JP3103754B2 (ja) | 1995-10-31 | 2000-10-30 | 三洋化成工業株式会社 | 改質された吸水性樹脂粒子およびその製法 |
JP3688418B2 (ja) | 1995-12-27 | 2005-08-31 | 株式会社日本触媒 | 吸水剤並びに衛生材料 |
US6071976A (en) * | 1995-12-27 | 2000-06-06 | Nippon Shokubai Co., Ltd. | Water absorbing agent, manufacturing method thereof, and manufacturing machine thereof |
JPH09194598A (ja) | 1996-01-18 | 1997-07-29 | Mitsubishi Chem Corp | 高吸水性樹脂の造粒法 |
CA2259476A1 (en) * | 1996-07-06 | 1998-01-15 | Stockhausen Gmbh & Co. Kg | Absorbent inserts, method of producing them and their use |
DE19645240A1 (de) | 1996-07-06 | 1998-01-08 | Stockhausen Chem Fab Gmbh | Saugfähige Einlagen, Verfahren zu ihrer Herstellung und ihre Verwendung |
US6232520B1 (en) * | 1997-02-19 | 2001-05-15 | The Procter & Gamble Company | Absorbent polymer compositions having high sorption capacities under an applied pressure |
KR20010012132A (ko) † | 1997-04-29 | 2001-02-15 | 그래햄 이. 테일러 | 레질리언스성의 초흡수성 조성물 |
EP0979250B1 (de) * | 1997-04-29 | 2004-04-14 | Dow Global Technologies Inc. | Superabsorbierende polymere mit verbesserter verarbeitbarkeit |
DE19748153A1 (de) | 1997-10-31 | 1999-05-06 | Stockhausen Chem Fab Gmbh | Verfahren zur Herstellung kationischer Polyelektrolyte |
JPH11349979A (ja) † | 1998-01-09 | 1999-12-21 | Nof Corp | 水性切削液、水性切削剤及びそれを用いる硬脆材料の切断方法 |
DE19813443A1 (de) | 1998-03-26 | 1998-10-08 | Stockhausen Chem Fab Gmbh | Wasser- und wäßrige Flüssigkeiten absorbierende Polymerisatteilchen, Verfahren zu ihrer Herstellung und ihre Verwendung |
US6056854A (en) | 1998-03-27 | 2000-05-02 | Basf Corporation | Process to make a wet-laid absorbent structure |
JPH11349625A (ja) † | 1998-06-10 | 1999-12-21 | Sanyo Chem Ind Ltd | 吸水剤の製造法および吸水剤 |
DE19846412A1 (de) † | 1998-10-08 | 2000-04-13 | Basf Ag | Hydrophile hochquellfähige Hydrogele sowie Verfahren zu ihrer Herstellung und Verwendung |
JP4380873B2 (ja) | 1999-02-15 | 2009-12-09 | 株式会社日本触媒 | 吸水性樹脂粉末およびその用途 |
US6562879B1 (en) * | 1999-02-15 | 2003-05-13 | Nippon Shokubai Co., Ltd. | Water-absorbent resin powder and its production process and use |
DE19909653A1 (de) | 1999-03-05 | 2000-09-07 | Stockhausen Chem Fab Gmbh | Pulverförmige, vernetzte, wässrige Flüssigkeiten sowie Blut absorbierende Polymere, Verfahren zu ihrer Herstellung und ihre Verwendung |
DE19909838A1 (de) | 1999-03-05 | 2000-09-07 | Stockhausen Chem Fab Gmbh | Pulverförmige, vernetzte, wässrige Flüssigkeiten sowie Blut absorbierende Polymere, Verfahren zu ihrer Herstellung und ihre Verwendung |
JP3648125B2 (ja) † | 1999-06-25 | 2005-05-18 | 株式会社日本触媒 | 有機ハロゲン化合物の除去用触媒および有機ハロゲン化合物の除去方法 |
DE19941423A1 (de) | 1999-08-30 | 2001-03-01 | Stockhausen Chem Fab Gmbh | Polymerzusammensetzung und ein Verfahren zu dessen Herstellung |
DE19941072A1 (de) | 1999-08-30 | 2001-03-01 | Stockhausen Chem Fab Gmbh | Polymerisatzusammensetzung und ein Verfahren zu dessen Herstellung |
US6414214B1 (en) * | 1999-10-04 | 2002-07-02 | Basf Aktiengesellschaft | Mechanically stable hydrogel-forming polymers |
JP2001137704A (ja) | 1999-11-18 | 2001-05-22 | Toagosei Co Ltd | 改質された高吸水性樹脂の製造方法 |
EP1265571A1 (de) | 2000-03-06 | 2002-12-18 | The Procter & Gamble Company | Verfahren zur herstellung von absorbierenden strukturen mit einem absorbierenden polymer und einem agens zur erhaltung der permeabilität |
DE10016041A1 (de) † | 2000-03-31 | 2001-10-04 | Stockhausen Chem Fab Gmbh | Pulverförmige an der Oberfläche vernetzte Polymerisate |
DE10025304A1 (de) † | 2000-05-22 | 2001-11-29 | Bayer Ag | Mischungen wässriger Bindemittel |
DE60143706D1 (de) * | 2000-07-18 | 2011-02-03 | Sanyo Chemical Ind Ltd | Absorbens und verfahren zu dessen herstellung, absorbierbare artikel und syntheseprodukte |
DE10043710B4 (de) † | 2000-09-04 | 2015-01-15 | Evonik Degussa Gmbh | Verwendung pulverförmiger an der Oberfläche nachvernetzter Polymerisate und Hygieneartikel |
DE10043706A1 (de) † | 2000-09-04 | 2002-04-25 | Stockhausen Chem Fab Gmbh | Pulverförmige, vernetzte, wässrige Flüssigkeiten sowie Blut absorbierende Polymere, Verfahren zu ihrer Herstellung und ihre Verwendung |
US6800353B1 (en) † | 2000-09-08 | 2004-10-05 | Ecolab Inc. | Scratch-resistant strippable finish |
DE10052966A1 (de) | 2000-10-25 | 2002-05-02 | Stockhausen Chem Fab Gmbh | Hochquellbare Absorptionsmittel mit einer verminderten Tendenz zum Verbacken |
JP4315680B2 (ja) † | 2000-12-29 | 2009-08-19 | ビーエーエスエフ ソシエタス・ヨーロピア | 吸収性組成物 |
DE50208214D1 (de) † | 2001-06-28 | 2006-11-02 | Basf Ag | Saure hochquellfähige hydrogele |
US7101946B2 (en) * | 2002-02-14 | 2006-09-05 | Stockhausen Gmbh | Water-absorbing polymers having interstitial compounds, a process for their production, and their use |
WO2006033477A1 (en) † | 2004-09-24 | 2006-03-30 | Nippon Shokubai Co., Ltd. | Particulate water-absorbing agent containing water-absorbent resin as a main component |
-
2003
- 2003-10-24 TW TW92129542A patent/TWI378955B/zh not_active IP Right Cessation
- 2003-10-24 EP EP03809325.8A patent/EP1563002B2/de not_active Expired - Lifetime
- 2003-10-24 BR BR0315632A patent/BR0315632A/pt not_active IP Right Cessation
- 2003-10-24 AU AU2003296558A patent/AU2003296558A1/en not_active Abandoned
- 2003-10-24 WO PCT/EP2003/011830 patent/WO2004037900A1/de active Application Filing
- 2003-10-24 WO PCT/EP2003/011828 patent/WO2004037903A2/de active Application Filing
- 2003-10-24 US US10/532,280 patent/US7833624B2/en active Active
- 2003-10-24 US US10/532,401 patent/US7541395B2/en not_active Expired - Fee Related
- 2003-10-24 TW TW92129545A patent/TWI327062B/zh not_active IP Right Cessation
- 2003-10-24 AU AU2003274077A patent/AU2003274077A1/en not_active Abandoned
Patent Citations (26)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4076663A (en) | 1975-03-27 | 1978-02-28 | Sanyo Chemical Industries, Ltd. | Water absorbing starch resins |
DE2706135A1 (de) | 1977-02-14 | 1978-08-17 | Stockhausen & Cie Chem Fab | Verdickungsmittel fuer ausgeschiedenen darminhalt und harn |
US4286082A (en) | 1979-04-06 | 1981-08-25 | Nippon Shokubai Kagaku Kogyo & Co., Ltd. | Absorbent resin composition and process for producing same |
DE3503458A1 (de) | 1984-02-04 | 1985-08-08 | Arakawa Kagaku Kogyo K.K., Osaka | Verfahren zur herstellung verbesserter wasser absorbierender harze |
US4535098A (en) | 1984-03-12 | 1985-08-13 | The Dow Chemical Company | Material for absorbing aqueous fluids |
DE3523617A1 (de) | 1984-07-02 | 1986-01-23 | Nippon Shokubai Kagaku Kogyo Co. Ltd., Osaka | Wasserabsorbierendes mittel |
US4734478A (en) | 1984-07-02 | 1988-03-29 | Nippon Shokubai Kagaku Kogyo Co., Ltd. | Water absorbing agent |
EP0450922A2 (de) | 1990-04-02 | 1991-10-09 | Nippon Shokubai Kagaku Kogyo Co. Ltd. | Verfahren zur Herstellung von flüssigkeitsstabilem Aggregat |
EP0450923A2 (de) | 1990-04-02 | 1991-10-09 | Nippon Shokubai Co., Ltd. | Verfahren zur Oberflächenbehandlung absorbierender Harze |
US5140076A (en) | 1990-04-02 | 1992-08-18 | Nippon Shokubai Kagaku Kogyo Co., Ltd. | Method of treating the surface of an absorbent resin |
DE4020780C1 (de) | 1990-06-29 | 1991-08-29 | Chemische Fabrik Stockhausen Gmbh, 4150 Krefeld, De | |
US5147921A (en) | 1990-08-14 | 1992-09-15 | Societe Francaise Hoechst | Powdered superabsorbents, containing silica, their preparation process and their use |
JPH0616822A (ja) | 1992-06-30 | 1994-01-25 | Sekisui Plastics Co Ltd | 吸水性樹脂粒子の製造方法 |
DE4244548A1 (de) | 1992-12-30 | 1994-07-07 | Stockhausen Chem Fab Gmbh | Pulverförmige, unter Belastung wäßrige Flüssigkeiten sowie Blut absorbierende Polymere, Verfahren zu ihrer Herstellung und ihre Verwendung in textilen Konstruktionen für die Körperhygiene |
DE4418818A1 (de) | 1993-07-09 | 1995-01-12 | Stockhausen Chem Fab Gmbh | Pulverförmige, vernetzte, wäßrige Flüssigkeiten sowie Körperflüssigkeiten absorbierende Polymere, Verfahren zu ihrer Herstellung und ihre Anwendung |
DE4333056A1 (de) | 1993-09-29 | 1995-03-30 | Stockhausen Chem Fab Gmbh | Pulverförmige, wäßrige Flüssigkeiten absorbierende Polymere, Verfahren zu ihrer Herstellung und ihre Verwendung als Absorptionsmittel |
WO1995022356A1 (en) | 1994-02-17 | 1995-08-24 | The Procter & Gamble Company | Absorbent materials having improved absorbent property and methods for making the same |
DE19529348A1 (de) | 1995-08-09 | 1997-02-13 | Stockhausen Chem Fab Gmbh | Absorptionsmittel für Wasser und wässrige Flüssigkeiten sowie Verfahren zu ihrer Herstellung und Verwendung |
DE19543366A1 (de) | 1995-11-21 | 1997-05-22 | Stockhausen Chem Fab Gmbh | Mit ungesättigten Aminoalkoholen vernetzte, wasserquellbare Polymerisate, deren Herstellung und Verwendung |
DE19646484A1 (de) | 1995-11-21 | 1997-05-22 | Stockhausen Chem Fab Gmbh | Flüssigkeitsabsorbierende Polymere, Verfahren zu deren Herstellung und deren Verwendung |
DE19543368A1 (de) | 1995-11-21 | 1997-05-22 | Stockhausen Chem Fab Gmbh | Wasserabsorbierende Polymere mit verbesserten Eigenschaften, Verfahren zu deren Herstellung und deren Verwendung |
WO1999034843A1 (en) | 1998-01-07 | 1999-07-15 | The Procter & Gamble Company | Absorbent polymer compositions having high sorption capacities under an applied pressure |
DE19805447A1 (de) | 1998-02-11 | 1999-08-12 | Bayer Ag | Modifizierte Superabsorber auf Basis von Polyacrylnitril-Emulsionen |
DE19854575A1 (de) | 1998-11-26 | 2000-05-31 | Basf Ag | Vernetzte quellfähige Polymere |
WO2001013841A1 (de) | 1999-08-20 | 2001-03-01 | Stockhausen Gmbh & Co. Kg | Wasserabsorbierende polymere mit hohlraumverbindungen, verfahren zu deren herstellung und deren verwendung |
EP1211266A1 (de) | 2000-11-30 | 2002-06-05 | Bayer Ag | Verfahren zur Herstellung von Superabsorbern aus Polyacrylnitril-Emulsionen unter adiabatischen Reaktionsbedingungen |
Non-Patent Citations (3)
Title |
---|
HOLLEMANN-WIBERG: "Lehrbuch der anorganischen Chemie", DE GRUYTER-VERLAG, pages: 765 |
JANDER-BLASIUS: "lehrbuch der analytischen und präparativen anorganischen Chemie", S. HIRZEL VERLAG |
See also references of EP1563002A2 |
Cited By (50)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2006092271A3 (de) * | 2005-02-28 | 2007-04-05 | Stockhausen Chem Fab Gmbh | Verfahren zur herstellung eines absorbierenden polymergebildes basierend auf acrylsäure, wobei das substrat für die acrylsäuresynthese teilweise durch enzymatische verfahren gewonnen wurde |
US8703450B2 (en) | 2005-02-28 | 2014-04-22 | Evonik Degussa Gmbh | Water-absorbent polymer structures based on renewable resources and method for producing said structures |
WO2006111404A2 (de) * | 2005-04-22 | 2006-10-26 | Evonik Stockhausen Gmbh | Oberflächennachvernetzte superabsorber behandelt mit metallsalz und metalloxid |
DE102005018924A1 (de) * | 2005-04-22 | 2006-10-26 | Stockhausen Gmbh | Wasserabsorbierende Polymergebilde mit verbesserten Absorptionseigenschaften |
WO2006111402A2 (de) | 2005-04-22 | 2006-10-26 | Evonik Stockhausen Gmbh | Oberflächennachvernetzte superabsorber behandelt mit metallsalz und metalloxid |
WO2006111404A3 (de) * | 2005-04-22 | 2007-05-10 | Stockhausen Chem Fab Gmbh | Oberflächennachvernetzte superabsorber behandelt mit metallsalz und metalloxid |
WO2006111402A3 (de) * | 2005-04-22 | 2007-06-14 | Stockhausen Chem Fab Gmbh | Oberflächennachvernetzte superabsorber behandelt mit metallsalz und metalloxid |
US8247499B2 (en) | 2005-04-22 | 2012-08-21 | Evonik Stockhausen Gmbh | Water-absorbing polymer structure with improved absorption properties |
US8071202B2 (en) | 2005-04-22 | 2011-12-06 | Evonik Stockhausen Gmbh | Water-absorbing polymer structures with improved absorption properties |
DE102005018923A1 (de) * | 2005-04-22 | 2006-10-26 | Stockhausen Gmbh | Wasserabsorbierende Polymergebilde mit verbesserten Absorptionseigenschaften |
JP2008536987A (ja) * | 2005-04-22 | 2008-09-11 | エフォニック ストックハウゼン ゲーエムベーハー | 高吸収性を有する吸水性ポリマー構造体 |
CN101175511B (zh) * | 2005-04-22 | 2014-03-26 | 赢创德固赛有限公司 | 用金属盐和金属氧化物处理并在其表面后交联的超吸收体 |
TWI405776B (zh) * | 2005-04-22 | 2013-08-21 | Evonik Stockhausen Gmbh | 以聚陽離子表面處理之水份吸收聚合物結構 |
CN100348648C (zh) * | 2005-06-14 | 2007-11-14 | 济南昊月树脂有限公司 | 聚丙烯酸钠吸水树脂表面改性方法 |
US8653320B2 (en) | 2005-11-18 | 2014-02-18 | Evonik Degussa Gmbh | Deodorizing super-absorbent composition |
US8829107B2 (en) | 2006-02-28 | 2014-09-09 | Evonik Degussa Gmbh | Biodegradable superabsorbent polymer composition with good absorption and retention properties |
WO2007121937A3 (de) * | 2006-04-21 | 2009-02-26 | Evonik Stockhausen Gmbh | Oberflächennachvernetzte superabsorber behandelt mit aluminiumlactat und optional aluminiumsulfat |
WO2007121941A3 (de) * | 2006-04-21 | 2009-01-15 | Evonik Stockhausen Gmbh | Oberflächennachvernetzte superabsorber behandelt mit organischen und anorganischen feinstteilchen |
US9534095B2 (en) | 2006-04-21 | 2017-01-03 | Evonik Degussa Gmbh | Water-absorbing polymer structure having improved permeability and absorption under pressure |
US9133342B2 (en) | 2006-04-21 | 2015-09-15 | Evonik Degussa Gmbh | Preparation of highly permeable, superabsorbent polymer structures |
US8907017B2 (en) | 2006-04-21 | 2014-12-09 | Evonik Degussa Gmbh | Water-absorbing polymer structure having improved permeability and absorption under pressure |
WO2007121941A2 (de) * | 2006-04-21 | 2007-11-01 | Evonik Stockhausen Gmbh | Oberflächennachvernetzte superabsorber behandelt mit organischen und anorganischen feinstteilchen |
KR101407176B1 (ko) | 2006-04-21 | 2014-06-12 | 에보니크 데구사 게엠베하 | 압력하에서 향상된 투과성과 흡수성을 가지는 수분-흡수성 중합체 구조 |
KR101389190B1 (ko) | 2006-04-21 | 2014-04-25 | 에보니크 데구사 게엠베하 | 높은 투과성을 가지는 초흡수성 중합체 구조의 제조 |
US8906824B2 (en) | 2006-12-18 | 2014-12-09 | Evonik Degussa Gmbh | Water-absorbing polymer structures produced using polymer dispersions |
EP2114469B1 (de) | 2007-02-09 | 2017-03-29 | Evonik Degussa GmbH | Wasserabsorbierendes polymergebilde mit hoher ammoniak-bindekapazität |
DE102007007203A1 (de) | 2007-02-09 | 2008-08-14 | Evonik Stockhausen Gmbh | Wasserabsorbierendes Polymergebilde mit hoher Ammoniak-Bindekapazität |
DE102007024080A1 (de) | 2007-05-22 | 2008-11-27 | Evonik Stockhausen Gmbh | Verfahren zum schonenden Mischen und Beschichten von Superabsorbern |
US8349913B2 (en) | 2007-05-22 | 2013-01-08 | Evonik Stockhausen Gmbh | Process for gentle mixing and coating of superabsorbers |
US8236876B2 (en) | 2007-07-16 | 2012-08-07 | Evonik Stockhausen, Llc | Superabsorbent polymer compositions having color stability |
US8063118B2 (en) | 2007-07-16 | 2011-11-22 | Evonik Stockhausen, Llc | Superabsorbent polymer compositions having color stability |
EP2176325B1 (de) | 2007-09-24 | 2021-12-08 | Evonik Operations GmbH | Superabsorbierende zusammensetzung mit tanninen zur geruchskontrolle |
DE102007045724A1 (de) | 2007-09-24 | 2009-04-02 | Evonik Stockhausen Gmbh | Superabsorbierende Zusammensetzung mit Tanninen zur Geruchskontrolle |
US8658146B2 (en) | 2007-09-24 | 2014-02-25 | Evonik Degussa Gmbh | Superabsorbent composition with tannins for odor control |
USRE47104E1 (en) | 2007-09-24 | 2018-10-30 | Evonik Degussa Gmbh | Superabsorbent composition with tannins for odor control |
US8372920B2 (en) | 2007-11-08 | 2013-02-12 | Evonik Stockhausen Gmbh | Water-absorbing polymer structure with improved color stability |
DE102007053619A1 (de) | 2007-11-08 | 2009-05-20 | Evonik Stockhausen Gmbh | Wasserabsorbierende Polymergebilde mit verbesserter Farbstabilität |
US8686216B2 (en) | 2008-03-05 | 2014-04-01 | Evonik Degussa Gmbh | Superabsorbent composition with metal salicylate for odor control |
WO2010115671A1 (de) | 2009-04-07 | 2010-10-14 | Evonik Stockhausen Gmbh | Verwendung von hohlkörpern zur herstellung wasserabsorbierender polymergebilde |
DE102009016404A1 (de) | 2009-04-07 | 2010-10-21 | Evonik Stockhausen Gmbh | Verwendung von Hohlkörpern zur Herstellung wasserabsorbierender Polymergebilde |
DE102009040949A1 (de) | 2009-09-11 | 2011-03-31 | Evonik Stockhausen Gmbh | Plasmamodifizierung wasserabsorbierender Polymergebilde |
WO2011029704A1 (de) | 2009-09-11 | 2011-03-17 | Evonik Stockhausen Gmbh | Plasmamodifizierung wasserabsorbierender polymergebilde |
DE102010008163A1 (de) | 2010-02-16 | 2011-08-18 | Evonik Stockhausen GmbH, 47805 | Verfahren zur Rückführung von Polymerfeinteilchen |
WO2011101188A1 (de) | 2010-02-16 | 2011-08-25 | Evonik Stockhausen Gmbh | Verfahren zur rückführung von polymerfeinteilchen |
US8252873B1 (en) | 2010-03-30 | 2012-08-28 | Evonik Stockhausen Gmbh | Process for the production of a superabsorbent polymer |
US10391195B2 (en) | 2011-11-17 | 2019-08-27 | Evonik Degussa Gmbh | Super-absorbing polymers with rapid absorption properties and method for producing the same |
DE102011086522A1 (de) | 2011-11-17 | 2013-05-23 | Evonik Degussa Gmbh | Superabsorbierende Polymere für hochgefüllte oder faserfreie Hygieneartikel |
DE102012220400A1 (de) | 2012-11-09 | 2014-05-15 | Evonik Industries Ag | Superabsorber für Kabelanwendungen |
WO2014072130A1 (de) | 2012-11-09 | 2014-05-15 | Evonik Industries Ag | Superabsorber für kabelanwendungen |
US10807067B2 (en) | 2016-06-27 | 2020-10-20 | Lg Chem, Ltd. | Method for producing super absorbent polymer and super absorbent polymer |
Also Published As
Publication number | Publication date |
---|---|
AU2003296558A8 (en) | 2004-05-13 |
TWI378955B (en) | 2012-12-11 |
EP1563002B1 (de) | 2014-07-16 |
TW200412905A (en) | 2004-08-01 |
US20060057389A1 (en) | 2006-03-16 |
TW200422330A (en) | 2004-11-01 |
BR0315632A (pt) | 2005-08-23 |
EP1563002A2 (de) | 2005-08-17 |
WO2004037903A3 (de) | 2004-06-03 |
WO2004037900A1 (de) | 2004-05-06 |
AU2003274077A1 (en) | 2004-05-13 |
EP1563002B2 (de) | 2017-12-13 |
AU2003296558A1 (en) | 2004-05-13 |
TWI327062B (en) | 2010-07-11 |
US7541395B2 (en) | 2009-06-02 |
US20060029782A1 (en) | 2006-02-09 |
US7833624B2 (en) | 2010-11-16 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
WO2004037903A2 (de) | Absorbierende polymergebilde mit verbesserter retentionskapazität und permeabilität | |
WO2002036663A1 (de) | Absorbierendes gebilde mit verbesserten blockingeigenschaften | |
DE10043710B4 (de) | Verwendung pulverförmiger an der Oberfläche nachvernetzter Polymerisate und Hygieneartikel | |
EP1537177B1 (de) | Wasserabsorbierendes mittel und verfahren zu seiner herstellung | |
EP1888132B1 (de) | Oberflächennachvernetzte superabsorber behandelt mit wasserlöslichem aluminiumsalz und zinkoxid | |
WO2007121941A2 (de) | Oberflächennachvernetzte superabsorber behandelt mit organischen und anorganischen feinstteilchen | |
WO2006111403A1 (de) | Mit polykationen oberflächenbehandeltes wasserabsorbierende polymergebilde | |
DE102005010198A1 (de) | Hydrolysestabile, nachvernetzte Superabsorber | |
WO2007121937A2 (de) | Oberflächennachvernetzte superabsorber behandelt mit aluminiumlactat und optional aluminiumsulfat | |
EP1335756B1 (de) | Hochquellbare absorptionsmittel mit einer verminderten tendenz zum verbacken | |
WO2002020068A1 (de) | Pulverförmige, vernetzte, wässrige flüssigkeiten sowie blut absorbierende polymere | |
WO2010115671A1 (de) | Verwendung von hohlkörpern zur herstellung wasserabsorbierender polymergebilde | |
DE10204938A1 (de) | Verfahren zur Nachvernetzung im Bereich der Oberfläche von wasserabsorbierenden Polymeren mit beta-Hydroxyalkylamiden | |
DE10204937A1 (de) | Verfahren zur Nachvernetzung im Bereich der Oberfläche von wasserabsorbierenden Polymeren mit Harnstoffderivaten | |
EP1572782A1 (de) | Zweistufiges mischverfahren zur herstellung eines absorbierenden polymers | |
DE10249821A1 (de) | Absorbierende Polymergebilde mit verbesserter Rententionskapazität und Permeabilität | |
WO2004006971A2 (de) | Wasserabsorbierende, schaumförmige polymergebilde | |
EP2475708A1 (de) | Plasmamodifizierung wasserabsorbierender polymergebilde | |
DE60026764T2 (de) | Wasserquellbares vernetztes Polymer, dessen Zusammensetzung, Verfahren zu dessen Herstellung und Anwendung | |
EP1453891A1 (de) | Kompaktierte absorbierende polymere, deren herstellung und verwendung | |
EP1565599A1 (de) | Gezogene absorbierende polymerfasern | |
EP1453454A1 (de) | Absorbierende hygieneartikel mit einnäss-indikator | |
EP1487882B1 (de) | Durch hydrierung gewonnenes basisches polymer | |
DE102005018923A1 (de) | Wasserabsorbierende Polymergebilde mit verbesserten Absorptionseigenschaften | |
EP2012843A2 (de) | Wasserabsorbierendes polymergebilde mit verbesserter permeabilität und absorption unter druck |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
AK | Designated states |
Kind code of ref document: A2 Designated state(s): AE AG AL AM AT AU AZ BA BB BG BR BY BZ CA CH CN CO CR CU CZ DE DK DM DZ EC EE EG ES FI GB GD GE GH GM HR HU ID IL IN IS JP KE KG KP KR KZ LC LK LR LS LT LU LV MA MD MG MK MN MW MX MZ NI NO NZ OM PG PH PL PT RO RU SC SD SE SG SK SL SY TJ TM TN TR TT TZ UA UG US UZ VC VN YU ZA ZM ZW |
|
AL | Designated countries for regional patents |
Kind code of ref document: A2 Designated state(s): GH GM KE LS MW MZ SD SL SZ TZ UG ZM ZW AM AZ BY KG KZ MD RU TJ TM AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HU IE IT LU MC NL PT RO SE SI SK TR BF BJ CF CG CI CM GA GN GQ GW ML MR NE SN TD TG |
|
121 | Ep: the epo has been informed by wipo that ep was designated in this application | ||
WWE | Wipo information: entry into national phase |
Ref document number: 2004545982 Country of ref document: JP |
|
WWE | Wipo information: entry into national phase |
Ref document number: 20038A19823 Country of ref document: CN |
|
WWE | Wipo information: entry into national phase |
Ref document number: 2003809325 Country of ref document: EP |
|
WWP | Wipo information: published in national office |
Ref document number: 2003809325 Country of ref document: EP |
|
ENP | Entry into the national phase |
Ref document number: 2006029782 Country of ref document: US Kind code of ref document: A1 |
|
WWE | Wipo information: entry into national phase |
Ref document number: 10532280 Country of ref document: US |
|
WWP | Wipo information: published in national office |
Ref document number: 10532280 Country of ref document: US |