process for producing a water-absorbing polymer composition, composite, process for producing a comp

专利摘要:
: PRODUCTION PROCESS OF A COMPOSITION OF WATER-ABSORBING POLYMERS, COMPOSITE, PROCESS FOR THE PRODUCTION OF A COM-POSITIVE, FOAMS, MOLDS, FIBERS, LEAVES, FILMS, CABLES, SEALING MATERIALS, ABSORBER HYGIENE ARTICLES , CARRIERS FOR THE GROWTH OF PLANTS AND REGULATORS FOR GROWTH OF FUNGI, PACKAGING MATERIALS, ADDITIVES FOR THE GROUND OR MATERIALS FOR THE CONSTRUCTION AND USE OF THE POLYMER ABSORBING WATER OR A COMPOSITE The invention refers to a process of production of a water-absorbing polymer composition comprising the steps of (i) mixing (Alpha1) 0.1 to 99.999% by weight, preferably 20 to 98.99% by weight, and even more preferably 30 to 98.95% by weight of ethylenically unsaturated polymerized monomers containing acidic groups or their ethylenically unsaturated polymerized salts or monomers containing protonated or quaternized nitrogen, or mixtures thereof, with particular preference given to mixtures containing at least monomer ethylenically unsaturated rosins containing acid groups, preferably acrylic acid, (Alfa2) at 70% by weight, preferably 1 to 60% by weight and more preferably from 1 to 40% by weight of ethylenically unsaturated polymerised monomers cup-limerized with (Alpha1), (Alpha3) 0.001 to 10% by weight, preferably 0.01 to 7% by weight and more preferably 0.05 to 5% by weight of one (...).
公开号:BR112013026998B1
申请号:R112013026998-7
申请日:2012-04-03
公开日:2020-12-01
发明作者:Laurent Wattebled；Christoph Loick；Jörg Harren；Stefan Leininger
申请人:Evonik Operations Gmbh；
IPC主号:

专利说明:

[0001] The present invention relates to a process of producing water-absorbing polymers with a high absorption rate, and their use.
[0002] The current trend in diaper production is to produce even thinner structures, with reduced content of cellulose fibers and higher superabsorbent content. The advantage of thinner structures is evidenced not only in better comfort in use, but also in reduced packaging and storage costs. With the trend towards increasingly thin diaper structures, the requirements profile of superabsorbents has changed significantly. Currently, the hydrogel's ability to transport and distribute the fluid is of crucial significance. Due to the greater amount of charge in the hygiene article (amount of superabsorbent per unit area), the polymer in the expanded state cannot form a barrier layer for the subsequent fluid (blocking gel). If the product has good transport properties, the optimal use of the entire hygiene item is ensured.
[0003] In addition to the permeability of superabsorbents (expressed in the form of "saline flow conductivity - SFC") and the absorption capacity under a compression load, the absorption rate of the superabsorbent particles (expressed as the amount of liquid absorbed by gram of superabsorbent material per second) is also a determining criterion, which allows statements about the capacity of a superabsorbent core composed of a large concentration of the superabsorbent with only a small portion of fluff pulp, in its first contact with liquids, to absorb it. them quickly ("acquisition"). In the case of absorbent cores with a high content of superabsorbents, this "acquisition" depends, among other factors, on the absorption rate of the superabsorbent material.
[0004] In the state of the art, there are several property rights that are supposed to allow for increased absorption. W096 / 17884A1 describes a water-absorbing resin for which a solid blowing agent with a particle diameter of 1 to 100μm is used in the monomer solution. In principle, preference is given to organic azo compounds, and here in particular, to acrylic acid salts containing an amino group. Pure carbonates, ammonium nitride or their mixtures can be used, optionally.
[0005] The disadvantage of this is the rapid rotation of azo compounds and the basic dispersion of the small solid particles in the monomer solution. Larger particles cannot be dispersed, without separation of the various particles in the dispersion when at rest.
[0006] US 5,118,719 describes the addition of blowing agents carbonates in the form of carbonates, bicarbonates or mixtures thereof, as well as the introduction of carbon dioxide gas in the monomer solution. The blowing agent can be present in the dispersion in solid or dissolved form, and is added shortly before or after the polymerization induction. This increases the absorption properties, such as a higher rate of expansion and stability of the gel.
[0007] A disadvantage of this is that the blowing agent has already escaped the superabsorbent hydrogel before or during gelation, or forms larger bubbles that do not ensure a microporous structure of the superabsorbent polymer.
[0008] The general use of blowing agents is also described in EP 664207, US5712316, US5399591 and US5462972. This also includes the use of inorganic blowing agents, which usually release carbon dioxide in suspension, or gaseous or solid carbon dioxide, which are added to the monomer solution. Predominantly potassium and ammonium compounds are used. An increase in absorption and absorption under pressure was observed.
[0009] Generally, the present invention aims to overcome the disadvantages resulting from the state of the art.
[0010] More particularly, it is an object of the present invention to provide a process for producing a water-absorbing polymer that has an improved expansion rate and a faster liquid absorption rate, while simultaneously maintaining overall quality. This process must also be carried out simply and without requiring the use of organic additives.
[0011] It is a particular object of the present invention to provide a process for producing a water-absorbing polymer, which ensures a high expansion rate.
[0012] Another objective of the invention is mainly to specify a water-absorbing polymer, a composite that contains such water-absorbing polymers and chemicals that contain such water-absorbing polymers or compounds, wherein such water-absorbing polymers have a high rate of absorption of aqueous solutions.
[0013] Another objective of the present invention is to provide a process for the production of water-absorbing polymers, ensuring a homogeneous distribution and a very homogeneous action of the expansion agents in the reaction space.
[0014] These objectives are achieved by means of the technical matter covered by the category-forming claims. Advantageous embodiments and other developments, which may occur alone or in combination, are the subject of the respective dependent claims.
[0015] A contribution to the achievement of the aforementioned initial objective is provided by the process of producing a water-absorbing polymer composition, comprising the steps of: (i) mixing (α1) 0.1 to 99.999% by weight preferably 20 to 98.99% by weight, and even more preferably 30 to 98.95% by weight of ethylenically unsaturated polymerized monomers containing acid groups or their ethylenically unsaturated polymerized salts or monomers containing protonated or quaternized nitrogen, or mixtures thereof, being particular preference given to mixtures containing at least ethylenically unsaturated monomers containing acid groups, preferably acrylic acid, (α2) 0 to 70% by weight, preferably 1 to 60% by weight and more preferably 1 to 40% by weight of monomers polymerized ethylenically unsaturated copolymerized with (α1), (α3) 0.001 to 10% by weight, preferably 0.01 to 7% by weight and more preferably 0.05 to 5% by weight of one or more retention agents (α4) 0 to 30% by weight, preferably from 1 to 20% by weight and more preferably from 5 to 10% by weight of water-soluble polymers, and (α5) from 0 to 20% by weight, preferably 0.01 to 7% by weight and more preferably 0.05 to 5% by weight of one or more auxiliary agents, where the sum of their weights (α1) to (α5) is 100% by weight, (ii ) polymerization of free radicals with cross-linking to form an aqueous, untreated, water-insoluble hydrogel polymer, (iii) drying of the hydrogel polymer, (iv) optionally crushing and sieving the water-absorbing polymer, (v) post-cross-linking the surface of the crushed polymer hydrogel and (vi) drying and finalizing the water-absorbing polymer, in which expansion agents with a particle diameter of 100μm to 900μm are added to the aqueous monomer solution, before the addition of the initiator and the beginning of the polymerization of free radicals.
[0016] In another embodiment of the present invention, in step (iii), optionally, the grinding can be carried out before drying the polymer hydrogel.
[0017] The blowing agents used can all be carbonates from the lithium, sodium, potassium, rubidium, cesium carbonate group, or higher valence metal ions, such as beryllium, calcium carbonate, magnesium, strontium or their mixtures. Other compounds employed can also be granular carbonates, which are produced in the form of mixed salts of a carbonate and / or percarbonate with an additional salt that functions as an outer layer, for example, a sulfate compound.
[0018] The sodium carbonate used in the process according to the invention can be prepared, for example, as described in WO 2008/012181. This is a sodium carbonate that has a particulate structure composed of several layers of sodium carbonate and sodium sulfate and / or a high temperature phase composed of a double salt of Na4 (SO4) 1 + n (CO3) 1- n where n is 0 to 0.5. This carbonate compound has a particle size distribution in the range of 100 to 900μm. Production is carried out by granulation by accumulation in a fluidized bed. This compound is used as a cleaning agent in dishwashers. In the process according to the invention, preference is given to the use of a pure granular sodium carbonate, according to WO 2008/012181.
[0019] Preference is given to a particle size of 200μm to 800μm and more preferably a particle size in the range of 300μm to 700μm. The particles can be amorphous or have a regular three-dimensional configuration.
[0020] In another embodiment, the blowing agent employed can be composed, for example, of amorphous particles with a particle size of 200μm to 800μm, preferably from 300μm to 700μm and even more preferably from 400μm to 600μm.
[0021] According to the invention, steps (i) and (ii) of the process according to the invention are performed in a mass reactor. According to the invention, a mass reactor is used which performs at least one axis co-rotation movement. Preference is given to the use of mixing reactors with at least two axes.
[0022] Advantageously, the use of the granules as a blowing agent and a mixer that has at least one axis, ensures a homogeneous distribution of the blowing agent in the resulting hydrogel. Layer-by-layer removal is caused by intensive mixing processes and energy dissipation, which is ideal for these purposes, in the mixing chamber's internal reaction chamber. This additionally allows the homogeneous release of carbon dioxide throughout the reaction. As a result, a water-absorbing polymer with a higher swelling rate is advantageously obtained.
[0023] Surprisingly, the positive effect on the swelling increase rate is observed only with the granular blowing agent in combination with the kneading polymerization process. The use of the granulated carbonate composition described above provides a layered structure for the production of the superabsorbent in polymer strip technologies does not lead to any significant effect on the swelling rate (FSR).
[0024] It is a particular object of the present invention to provide a process in which absorbent polymers can be produced, and can ensure a particularly high rate of swelling.
[0025] It is still an objective of the present invention to provide a process for the production of water-absorbing polymer that allows a homogeneous distribution of the soda ash particles.
[0026] This objective is achieved by the process according to the invention, in which steps (i) and (ii) take place in a mixing reactor with at least one axis.
[0027] The layer-by-layer removal is caused by the intense kneading process and the homogeneous dissipation of energy, which is ideal for these purposes, within the reaction.
[0028] Surprisingly, the mass reactor in continuous or batch mode, with at least one axis system demonstrates that granulated sodium carbonate is homogeneously incorporated in the monomer solution and the step (ii) of the process at a speed of 10 to 80 revolutions per minute. Preferably, the process step is carried out at rotation speeds of the mass reactor at rotation speeds of 15 to 60 revolutions per minute and, more preferably, at speeds of 20 to 35 revolutions per minute.
[0029] Surprisingly, the process according to the invention produced water-absorbing polymers with an FSR in the range of 0.3 to 0.55, preferably 0.35 to 0.45.
[0030] Surprisingly, in the case of the use of granulated sodium carbonate, it was found that the effect of the invention, at a given time, after the addition of hydrogen peroxide and before the addition of ascorbic acid to the monomer solution in the reactor masseira, resulted in higher swelling rates of the resulting superabsorbent polymer, with no side effects on the other characteristics of the water-absorbing polymer. This effect is not observed in any case with a static polymer strip process. The use of sodium carbonate of different density (low density and high density) also led to an increase in the value of the swelling rate, but the increase in the swelling rate, in the case of the massaging process is not as pronounced as that resulting from the addition of granulated sodium carbonate. In addition, the use of sodium carbonate allows such a porosity that it allows an increase in the particle surface.
[0031] Preferably, the combination of sodium carbonate and a co-rotational double axis mixer in steps i) and ii) of the process according to the invention, reduces oxygen, greatly minimizes the destruction of the granules, and ensures incorporation of carbonate and also homogeneous release of carbon dioxide.
[0032] Monoethylenically unsaturated (α1) monomers containing acid groups can be partially or totally, preferably partially, neutralized. Monoethylenically unsaturated monomers containing acid groups are preferably neutralized by at least 10 mol%, more preferably at least 25 to 50 mol% and even more preferably 50 to 90 mol%. The neutralization of the monomers (α1) can also be done after polymerization. In this case, partial neutralization is at least 10 mol%, more preferably at least 25 to 50 mol% and even more preferably 50 to 90 mol% neutralized. In addition, neutralization can be carried out with alkali metal hydroxides, alkaline earth metal hydroxides, ammonia, and carbonates and bicarbonates. In addition, any other base that forms a water-soluble salt with the acid is conceivable. Neutralization mixed with different bases is also conceivable. Preference is given to neutralization with ammonia or with alkali metal hydroxides, more preferably with sodium hydroxide, or with ammonia.
[0033] In addition, groups of free acids in a polymer can be predominant, so that this polymer has a pH in the acid 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 relation to the acidic polymer. These polymers are referred to in the literature as "mixed ion-bed absorbent polymers" (MBIEA polymers) and are described inter alia in WO 99/34843. The disclosure in WO 99/34843 is hereby incorporated by reference and is therefore , considered to be part of this disclosure. In general, MBIEA polymers constitute a composition that primarily includes basic polymers capable of exchanging anions, and secondly a polymer that is acidic in comparison to the basic polymer and capable of exchanging cations. basic polymer has basic groups and is typically obtained by polymerizing monomers that have basic groups or groups that can be converted to basic groups.These monomers are, in particular, those that have primary, secondary or tertiary amines or the corresponding phosphines, or at least least two of the mentioned functional groups. This group of monomers includes, in particular, ethyleneamine, allylamine, diallylamine, 4-aminobutene, loxycyclines, vinylformamide, 5-aminopentene, carbodiimide, formaldacin, melamine and the like, and derivatives of secondary or tertiary amines thereof.
[0034] The monoethylenically unsaturated (α1) monomers that contain acid groups are preferably acrylic acid, methacrylic acid, ethacrylic acid, α-chloroacrylic acid, α-cyanoacrylic acid, β-methylacrylic acid (crotonic acid), α acid -phenylacrylic, β-acrylooloxypropionic acid, sorbic acid, α-chlorosorbic acid, 2'-methylisocrotonic acid, cinnamic acid, p-chlorokinamic acid, β-stearyl acid, itaconic acid, citraconic acid, mesaconic acid, glutaconic acid, aconitic acid, maleic acid, fumaric acid, tricarboxyethylene and maleic anhydride, preference being given particularly to acrylic acid and methacrylic acid and, in addition to acrylic acid.
[0035] In addition to these monomers containing carboxylate groups, the monoethylenically unsaturated (α1) monomers containing preferred acid groups additionally include ethylenically unsaturated sulfonic acid monomers or ethylenically unsaturated phosphonic acid monomers.
[0036] The preferred ethylenically unsaturated sulfonic acid monomers are allylsulfonic acids or aromatic aliphatic or vinyl sulfonic acids or methacrylic or acrylic sulfonic acids. Preferred aromatic aliphatic or vinyl sulfonic acids are vinyl sulfonic acid, 4-vinyl benzyl sulfonic acid, vinyl toluenesulfonic acid and styrenes sulfonic acid. Preferred methacrylic or acrylic sulfonic acids are (meth) sulfoethyl acrylate, (meth) sulfopropyl acrylate, 2-hydroxy-3-methacryloyloxypropylsulfonic acid, and (meth) acrylamidoalkylsulfonic acids such as 2-acrylamido-2-methylpropanesulfonic acid.
[0037] The preferred ethylenically unsaturated phosphonic acid monomers are vinylphosphonic acid, allylphosphonic acid, vinylbenzylphosphonic acid, (meth) acrylamidoalkylphosphonic acids, acrylamidoalkyldiphosphonic acids, phosphonyl methylated vinylamines and derivatives of methyl (phosphonic acid).
[0038] The preferred ethylenically unsaturated (α1) monomers containing a protonated nitrogen are dialkylaminoalkyl (meth) acrylates in the protonated form, for example, dimethylaminoethyl hydrochloride (methyl) acrylate or dimethylaminoethyl (methyl) acrylate, and dialkyl acrylate, and dialkyl acrylate, and dialkyl ) acrylamides in protonated form, for example, dimethylaminoethyl (meth) acrylamide hydrochloride, dimethylaminopropyl (meth) acrylamide hydrochloride, dimethylaminopropyl (meth) acrylamide hydrochloride or dimethylaminoethyl- (meth) acrylamide hydrosulaphate.
[0039] Ethylenically unsaturated monomers (α1) containing a quaternized nitrogen atom are preferably dialkylamnioalkyl (meth) acrylates in quaternized form, for example, trimethylammonioethyl (meth) acrylate, methacrylamethylamine and methylethyl acrylate (methyl) acrylate and acrylate); quaternized form, for example, (meth) acrylamidopropyltrimethylammonium chloride, trimethylammonioethyl chloride (met) acrylate or (meth) acrylamidopropyltrimethylammonium sulfate.
[0040] The monoethylenically unsaturated (α2) monomers copolymerizable with (α1) are preferably acrylamides and methacrylamides.
[0041] Preferred (meth) acrylamides are, in addition to acrylamide and methacrylamide, substituted (meth) acrylamides of alkyl or aminoalkyl derived from (meth) acrylamide, such as N-methylol (meth) acrylamide, N, N-dimethylamino ( met) acrylamide, dimethyl (meth) acrylamide or diethyl (meth) acrylamide. Possible vinylamides are, for example, N-vinylamides, N-vinylformamides, N-vinylacetamides, N-vinyl-N-methylacetamides, N-vinyl-N-methylformamides, vinylpyrrolidone. Among these monomers, particular preference is given to acrylamide.
[0042] In addition, monoethylenically unsaturated (α2) monomers copolymerizable with (α1) preferred are water-dispersible monomers. The preferred water-dispersible monomers are acrylic esters and methacrylic esters, such as methyl (meth) acrylate, ethyl (meth) acrylate, propyl (meth) acrylate or butyl (meth) acrylate, and also vinyl acetate, styrene and isobutylene.
[0043] Preferred cross-linking agents (α3) according to the invention are compounds with at least two ethylenically unsaturated groups within a molecule (class I cross-linking agent), compounds having at least two functional groups that can react with functional groups of monomers (α1) or (α2) in a condensation reaction (= condensation crosslinking agents), in an addition reaction or ring opening reaction (class II crosslinking agent), compounds that have at least one ethylenically unsaturated group and at least least one functional group that can react with functional groups of monomers (α1) or (α2) in a condensation reaction, an addition reaction or a ring opening reaction (class III crosslinking agent), or polyvalent metal cations (crosslinking agent class IV). Class I crosslinking compounds achieve crosslinking of polymers through the polymerization of free radicals of the ethylenically unsaturated groups of the crosslinking molecule with monoethylenically unsaturated monomers (α1) or (α2), whereas class II crosslinking compounds and polyvalent metal cations of class IV crosslinking agent achieve the crosslinking of polymers through a condensation reaction of the functional groups (class II crosslinking agent) or by electrostatic interaction of the polyvalent metal cation (class IV crosslinking agent) with the functional groups of monomers (α1) or (α2). In the case of the class III crosslinking agent compounds, there is correspondingly crosslinking of the polymer both through the polymerization of free radicals of the ethylenically unsaturated group and through a condensation reaction between the functional group of the crosslinking agent and the functional groups. monomers (α1) or (α2).
[0044] The compounds of class I crosslinking agents are preferably poly (meth) acrylic esters obtained, for example, by the reaction of a polyol, for example ethylene glycol, propylene glycol, trimethylolpropane, 1,6-hexanediol, glycerol, pentaerythritol , polyethylene glycol or polypropylene glycol, an amino alcohol, a polyalkylene polyamine, for example, diethylene triamine or triethylene tetramine, or an alkoxylated polyol with acrylic acid or methacrylic acid. In addition, preferred class I crosslinking agent compounds are also polyvinyl compounds, poly (meth) ally compounds, (meth) acrylic esters, a monovinyl compound or (meth) acrylic esters, a mono (meth) ally compound , preferably of mono (meth) ally compounds of a polyol or an amino alcohol. In this context, reference is made to documents DE 195 43 366 and DE 195 43 368. Disclosures are hereby incorporated by reference and therefore form part of the disclosure.
[0045] Examples of class I crosslinking agent compounds include alkenyl di (meth) acrylates, for example, ethylene glycol di (meth) acrylate, 1,3-propylene glycol di (meth) acrylate, 1,4-butylene glycol di (met) acrylate, 1,3-butylene glycol di (met) acrylate, 1,6-hexanediol di (met) acrylate, 1,10-decanediol di (met) acrylate, 1,12-dodecanediol di (met) acrylate, 1,18-octadecanediol di (meth) acrylate, cyclopentanediol di (meth) acrylate, neopentyl glycol di (meth) acrylate, methylene di (meth) acrylate or pentaerythritol di (meth) acrylate, alkenyldi (meth) acrylamides, for example, N -methyldi (meth) acrylamide, N, N'-3-methylbutylenebis (meth) acrylamide, N, N '- (1,2-dihydroxyethylene) bis (meth) acrylamide, N, N'-hexamethylenebis (meth) acrylacrylamide or N , N'-methylenebis (meth) acrylamide, polyalkoxy di (meth) acrylates, for example, diethylene glycol di (meth) acrylate, triethylene glycol di (meth) acrylate, tetraethylene glycol di (meth) acrylate, dipropylene glycol di (met) acrylate, tripropylene glycol di (met) acrylate, tetrapropylene glycol di (m et) acrylate, bisphenol A di (meth) acrylate, bisphenol A di (meth) acrylate ethoxylated, benzylidene di (meth) acrylate, 1,3-di (meth) acryloyloxy-2-propanol, hydroquinone di (meth) acrylate, esters trimethylolpropane di (meth) acrylate that has been preferably alkoxylated, preferably ethoxylated, with 1 to 30 mol of alkylene oxide per hydroxyl group, thioethylene glycol di (meth) acrylate, thiopropylene glycol di (meth) acrylate, thiopoliethylene glycol di (methyl ) acrylate, thiopolypropylene glycol di (meth) acrylate, divinyl ethers, for example, 1,4-butanediol divinyl ether, divinyl esters, for example, divinyl adipate, alkadiene, for example, butadiene or 1,6-hexadiene, divinylbenzene, di (meth) allyl compounds, for example, di (meth) allyl phthalate, di (meth) allyl succinate, di (meth) allyldimethylammonium chloride homo- and copolymers and diethyl (meth) allyl ammonium methyl copolymers, ammonium chloride (meth) acrylate, vinyl (meth) acryloyl compounds, for example, vinyl (meth) acrylate, d and (meth) allyl (meth) acrylate, for example, (meth) allyl (meth) acrylate, (meth) allyl (meth) acrylate with 1 to 30 mol of ethylene oxide per hydroxyl group, di (meth) allyl esters , polycarboxylic acids, for example, di (meth) allyl maleate, di (meth) ally fumarate, di (meth) ally succinate, di (meth) allyl terephthalate, compounds having three or more ethylenically unsaturated free radical polymerizable groups, for example glyceryl tri (meth) acrylate, glycerol esters (meth) acrylates that have been ethoxylated with preferably 1 to 30 mol of ethylene oxide per hydroxyl group, trimethylolpropane tri (meth) acrylate, trimethylolpropane tri (meth) acrylates which has been preferably alkoxylated, preferably ethoxylated, with 1 to 30 mol of alkylene oxide per hydroxyl group, trimethacrylamide, (meth) allylidene di (meth) acrylate, 3-allyloxy-1,2-propanediol di (meth) acrylate, tri (meth) cyanurate allyl, tri (meth) allyl isocyanurate, pentaerythritol tetra (meth) acrylate, tri (me) pentaerythritol t) acrylate, (meth) acrylic esters of ethoxylated pentaerythritol with preferably 1 to 30 mol of ethylene oxide per hydroxyl group, tris (2-hydroxyethyl) isocyanurate tri (meth) acrylate, trivinyl trimellitate, tri (meth) allylamines, di (meth) allylalkylamines, for example, di (meth) allylmethylamine, tri (meth) allyl phosphate, tetra (meth) ethylethylenediamine, poly (meth) allyl esters, tetra (meth) allyloxyetane or tetra (meth) allylammon halides.
[0046] Preferred class II crosslinking compounds are compounds that have at least two functional groups that can react in a condensation reaction (= condensation crosslinking agents), in an addition reaction or in a ring opening reaction with functional groups of monomers (α1) or (α2), preferably with the acid groups of monomers (α1). These functional groups of the class II crosslinking agent compounds are preferably functions of alcohol, amine, aldehyde, glycidyl, isocyanate, carbonate or epichloro.
[0047] Examples of class II crosslinking agent compounds include polyols, for example, ethylene glycol, polyethylene glycols, such as diethylene glycol, triethylene 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-pentanediol, 2,4-pentanediol, 1,6-hexanediol, 2,5-hexanediol, glycerol, polyglycerol, trimethylolpropane, polyoxypropylene, oxyethylene block copolymers- oxypropylene, sorbitan fatty acid esters, polyoxyethylene sorbitan fatty acid esters, pentaerythritol, sorbitol and polyvinyl alcohol, amino alcohols, for example, ethanolamine, diethanolamine, triethanolamine or propanolamine, polyamine compounds, for example, ethylene diamine, diethylamine, diethylamine triethylenetetramine, tetraethylenepentamine or pentaethylenehexamine, polyglycidyl ethers compounds such as ethyl glycol diglycidyl ether, diglycidyl ether polyethylene glycol, glyceryl diglycidyl ether, glyceryl polyglycidyl ether, pentaerythrityl polyglycidyl ether, propylene glycol diglycidyl ether, polypropylene glycol diglycidyl ether, hexanediol glycol diglycidyl ether, glycidyl ether glycol, ether glycol, ether diglycidyl phthalate, adipic acid diglycidyl ether, 1,4-phenylenebis (2-oxazoline), glycidol, polyisocyanates, preferably diisocyanates, such as toluene 2,4-diisocyanate and hexamethylene diisocyanate, compounds of polyaziridine, such as 2,2-bishhydroxymethylbutanol tris- [3- (1-aziridinyl) -propionate], 1,6-hexamethylenediethyloneurea and diphenylmethanebis-4, 4'-N, N'-diethyleneurea, halogen peroxides, for example, epichloro- and epibromhydrin and α-methylpichlorohydrin, alkylene carbonates such as 1,3-dioxane-2-one (ethylene carbonate), 4-methyl-1,3-dioxolan-2-one (propylene carbonate), 4, 5-dimethyl-1,3-dioxolan-2-o na, 4,4-dimethyl-1,3-dioxolan-2-one, 4-ethyl-1,3-dioxolan-2-one, 4-hydroxymethyl-1,3-dioxolan-2-one, 1,3- dioxane-2-one, 4-methyl-1,3-dioxane-2-one, 4,6-dimethyl-1,3-dioxane-2-one, 1,3-dioxolan-2-one, poly-1, 3-dioxolan-2-one, polyquaternary amines, such as condensation products of dimethylamines and epichlorohydrin. In addition, the preferred compounds of the class II crosslinking agent are also polyoxazolines such as 1,2-ethylenebisoxazoline, crosslinking agents with silane groups, such as Y-glycidoxypropyltrimethoxysilane and Y-aminopropyltrimethoxysilane, oxazolidinones, such as 2-oxazolidinone, bi- and poly- 2-oxazolidinones and diglycol silicates.
Preferred class III compounds include hydroxyl or amino-containing (meth) acrylic acid esters, for example, 2-hydroxyethyl (meth) acrylate and 2-hydroxypropyl (meth) acrylate, and also compounds of (meth) diols acrylamides or mono (meth) allyls containing hydroxyl or amino.
[0049] The polyvalent metal cations of class IV crosslinking agent are preferably derived from mono- or polyvalent cations, the monovalent cations especially from alkali metals, such as potassium, sodium, lithium, with preference being given to lithium. Preferred divalent cations are derived from zinc, beryllium, alkaline earth metals such as magnesium, calcium, strontium, with preference given to magnesium. Other cations of higher valence, usable in accordance with the invention are the cations of aluminum, iron, chromium, manganese, titanium, zirconium, and other transition metals, and also the double salts of such cations or mixtures of the mentioned salts. Preference is given to the use of aluminum salts and alums and their different hydrates, for example, AICI3 x 6H2O, NaAl (SO4) 2 x 12 H2O, KAl (SO4) 2 x 12 H2O or Al2 (SO4) 3 x 14 -18 H2O. Particular preference is given to the use of Al2 (SO4) 3 and its hydrates as class IV crosslinking agents.
[0050] The superabsorbent particles used in the process according to the invention are preferably crosslinked by crosslinking agents from the following crosslinking classes, or crosslinking agents from the following crosslinking class combinations: I, II, III, IV, I II, I III, I IV, I II III, I II IV, I III IV, II III IV, II IV or III IV. The above combinations of crosslinking agent classes are each a preferred embodiment of crosslinking agents of a superabsorbent particle employed in the process according to the invention.
[0051] Other preferred embodiments of the superabsorbent particles used in the process according to the invention are polymers that are cross-linked by any of the classes of cross-linking agents class I. Among these, preference is given to water-soluble crosslinking agents. In this context, special preference is given to N, N'-methylenebisacrylamide, polyethylene glycol di (meth) acrylates, trialylmethylammonium chloride, tetraalkylammonium chloride, and glycol and nonaethylene allyl acrylate prepared with 9 mol of ethylene oxide per mole of acrylic acid.
[0052] The water-soluble polymers (α4) present in the superabsorbent particles can be water-soluble polymers, such as a partially or fully hydrolyzed polyvinyl alcohol, polyvinylpyrrolidone, starch or starch derivatives, polyglycols or polyacrylic acid, preferably incorporated in the form polymerized. The molecular weight of these polymers is not critical, as long as they are soluble in water. Preferred water-soluble polymers are starch or starch derivatives or polyvinyl alcohol. Water-soluble polymers, preferably synthetic water-soluble polymers such as polyvinyl alcohol, can also serve as a graft base for the monomers to be polymerized.
[0053] The auxiliaries (α5) present in polymers are organic or inorganic particles, for example, odor binders, especially zeolites or cyclodextrins, skin substances, surfactants or anti-oxidants.
[0054] Preferred organic auxiliaries include cyclodextrins or their derivatives, and polysaccharides. Also preferred are cellulose and cellulose derivatives, such as CMC, cellulose ethers. Preferred cyclodextrins or cyclodextrin derivatives are the compounds disclosed in document DE-A-25 198 486 on page 3 line 51 to page 4 line 61. The section of that published patent application is hereby incorporated by reference and is deemed to be forming part of the description of the present invention. Particularly preferred cyclodextrins are α-, β-, Y— or δ-non-derivatized cyclodextrins.
[0055] The auxiliary inorganic particles used can be any materials that are typically employed to modify the properties of water-absorbing polymers. Preferred inorganic auxiliaries include sulfates, such as Na2SO4, lactates, for example, sodium lactate, silicates, especially structure silicates, such as zeolites, or silicates that have been obtained by drying aqueous silica solutions or colloidal silica solutions , for example, commercially available products, such as precipitated silica and smoked silica, for example, Aerosils having a particle size in the range of 5 to 50 nm, preferably in the range of 8 to 20 nm, such as "Aerosil 200" from Evonik Industries AG, aluminates, titanium dioxides, zinc oxides, clay materials, and other minerals familiar to those skilled in the art, as well as inorganic carbonaceous materials.
[0056] Preferred silicates are all natural or synthetic silicates which are described as silicates in and Holeman Wiberg, Lehrbuch der Anorganischen Chemie [Inorganic Chemistri], Walter de Gruiter-Verlag, 91a-100a edition, 1985, on pages 750 to 783 The section of this book mentioned above is hereby incorporated by reference and is considered to be part of the description of the present invention.
[0057] Particularly preferred silicates are zeolites. The zeolites employed can be fully synthetic or natural zeolites known to those skilled in the art. The preferred natural zeolites are the zeolites of the natrolite group, the harmotone group, the mordenite group, the chabasite group, the faujasita group (sodalita group) or the analcite group. Examples of natural zeolites are analcime, leucite, polucite, wairaquita, belbergita, biciitaita, bogsita, brewsterita, chabasita, wilhendersonita, calesita, dachiardita, edingtonita, epistilbita, erionita, faujasita, ferrierita, amicita, garronita, gismondina, gismondina, gismondina, gismondina, gismondina, gismondina , goosecreequita, harmotona, filipsita, welsita, clinoptilolita, heulandita, laumontita, levina, mazzita, merlinoita, montesomaita, mordenita, mesolita, natrolita, scolecite, ofretita, paranatrolita, paulingita, perlialita, barrerita, estitizita, estitizita, esternita, esternita. Preferred synthetic zeolites are zeolite A, zeolite X, zeolite i, zeolite P, or the ABSCENTS product.
[0058] The zeolites used can be zeolites of the type called "intermediates", in which the SiO2 / AlO2 ratio is less than 10, with a SiO2 / AlO2 ratio in these zeolites more preferably in the range of 2 to 10. In addition to these zeolites " intermediates ", it is also possible to employ" tall "zeolites, which include, for example, the well-known" molecular sieve "zeolites of the ZSM and β-zeolite types. These "tall" zeolites are preferably characterized by a SiO2 / AlO2 ratio of at least 35, more preferably by a SiO2 / AlO2 ratio within a range of 200 to 500.
[0059] The aluminates used preferably are naturally occurring spinel, especially common spinel, zinc spinel, iron spinel or chromium spinel.
Preferred titanium dioxides are pure titanium dioxide in the forms of rutile crystal, anatase and broochite, and also, iron-containing titanium dioxides, for example ilmenite, calcium-containing titanium dioxides, such as titanite or perovskite.
[0061] Preferred clay materials are those described as clay materials in Holeman Wiberg, Lehrbuch der Anorganischen Chemie, Walter de Gruiter-Verlag, 91a-100th edition, 1985, on pages 783 to 785. In particular, the referred section of that book is incorporated herein by reference and is considered to be part of the description of the present invention. Particularly preferred clay materials are kaolinite, illite, haloisite, montmorillonite and talc.
[0062] Additional preferred inorganic particles according to the invention are the metal salts of mono-, oligo- and polyphosphoric acids. Among these, preference is given especially to hydrates, particularly with preference given to mono- to decahydrates and trihydrates. Useful metals especially include alkali metals and alkaline earth metals, with preference being given to alkaline earth metals. Among these Mg and Ca are preferred and Mg is particularly preferred. In the context of phosphates, phosphoric acids and metallic compounds, reference is made to Holeman Wiberg, Lehrbuch der Anorganischen Chemie, Walter de Gruiter-Verlag, 91th-100th edition, 1985, on pages 651 to 669. The section of this book is here incorporated by reference and is considered to be part of the description of the present invention.
[0063] Preferred non-organic assistant carbonaceous are those pure carbons that are mentioned as graphites in Holeman and Wiberg, Lehrbuch der Anorganischen Chemie, Walter de Gruiter-Verlag, edition 91a-100a 1985, on pages 705 to 708. The section of this the aforementioned book is hereby incorporated by reference and is considered to be part of the description of the present invention. Particularly preferred graphites are synthetic graphites, for example, coke, pyrography, activated carbon or black carbon.
[0064] The superabsorbent particles used in the process according to the invention are preferably obtainable by first preparing a water-absorbent polymer (P), in the form of particles from the mentioned monomers and crosslinking agents. This polymer (P), which works as a starting material for superabsorbent particles, is produced, for example, by mass polymerization, which is preferably carried out in mass reactors such as extruders, solution polymerization, spray polymerization, polymerization in reverse emulsion or reverse suspension polymerization. Preference is given to carrying out polymerization in solution in water as a solvent. Solution polymerization can be carried out continuously or in batch. The state of the art reveals a wide variety of possible variations with respect to the reaction conditions, such as temperature, type and quantity of the initiators, and the reaction solution. Typical processes are described in the following patents: US 4,286,082, DE2706135, US 4,076,663, DE3503458, DE4020780, DE4244548, DE4323 001, DE4333 056, DE44 18 818. The disclosures are hereby incorporated by reference and, therefore, form part of the disclosure.
[0065] The initiators used to initiate the polymerization can all be initiators that form free radicals under the conditions of polymerization and are typically used in the production of superabsorbents. These include thermal catalysts, redox catalysts and photoinitiators, which are activated by means of high energy radiation. The polymerization initiators can be dissolved or dispersed in a solution of inventive monomers. Preference is given to the use of water-soluble catalysts.
[0066] Useful thermal initiators include all compounds that decompose to free radicals under thermal action and are known to those skilled in the art. Particular preference is given to thermal polymerization initiators having a half-life of less than 10 seconds, even more preferably less than 5 seconds at less than 180 ° C, even more preferably at less than 140 ° C. Peroxides, hydroperoxides, hydrogen peroxide, persulfates and azo compounds are particularly preferred thermal polymerization initiators. In some cases, it is advantageous to use mixtures of different thermal polymerization initiators. Among these mixtures, preference is given to those of hydrogen peroxide and sodium peroxodisulfate or potassium peroxodisulfate, which can be used in any conceivable proportion. Suitable organic peroxides are preferably acetylacetone peroxide, methyl ethyl ketone peroxide, benzoyl peroxide, lauroyl peroxide, acetyl peroxide, capryl peroxide, isopropyl peroxydicarbonate, 2-ethylhexyl peroxydicarbonate, t-butyl hydroperoxide, cumene hydroperoxide, t-amyl perpivalate, t-butyl perpivalate, t-butyl perneohexanoate, t-butyl isobutyrate, t-butyl per-2-ethylhexanoate, t-butyl perisononanoate, t-butyl permaleate butyl, t-butyl perbenzoate, t-butyl 3,5,5-trimethylhexanoate and amyl perneodecanoate. In addition, preferred thermal polymerization initiators are: azo compounds such as azobisisobutyronitrile, azobisdimethylvaleronitrile, 2,2'-azobis (2-amidinopropane) dihydrochloride, azobisamidinopropane dihydrochloride, 2,2'-azobidine dihydrochloride (N, N-dimethylene) , 2- (carbamoylazo) isobutyronitrile and 4,4'-azobis (4-cyanovaleric acid). The mentioned compounds are used in usual amounts, preferably within a range of 0.01 to 5 mol%, preferably 0.1 to 2 mol%, based, in each case, on the amount of monomers to be polymerized .
[0067] Redox catalysts comprise, as an oxidic component, at least one of the compounds specified above per se, as a reducing component, preferably ascorbic acid, glucose, sorbose, mannose, hydrogensulfide, sulfate, thiosulfate, hyposulphite or ammonium sulfide, hydrogensulfide , sulfate, thiosulfate, hyposulfite or alkali metal sulfide, metal salts, such as iron (II) ions or silver ions, or sodium hydroxymethylsulfoxylate. The reducing component used in the redox catalyst is preferably ascorbic acid or sodium pyrosulfite. Based on the amount of monomers used in the polymerization, 1x10-5 to 1 mol% of the redox catalyst reducing component and 1x10-5 to 5 mol% of the oxidation component of the redox catalyst are used. Instead of the oxidation component of the redox catalyst, or in addition to this, it is possible to employ one or more azo compounds, preferably soluble in water.
[0068] If the polymerization is triggered by the action of high energy radiation, it is customary to employ so-called photoinitiators as the initiator. These can be, for example, so-called α-dividers, H-abstraction systems, or azides. Examples of such initiators are benzophenone derivatives, such as Micler's ketone, phenanthrene derivatives, fluorene derivatives, anthraquinone derivatives, thioxanthone derivatives, coumarin derivatives, benzoyl ethers and their derivatives, azo compounds such as radical initiators above mentioned free, substituted hexaaryl bisisimidazoles or acylphosphine oxides. Examples of azides are: 2- (N, N-dimethylamino) 4-azidocinamate, 2- (N, N-dimethylamino) ethyl acetate 4-azidonafty, 2- (N, N-dimethylamino) 4-azidobenzoate, sulfone 5-azido-1-naphthyl 2 '- (N, N-dimethylamino) -ethyl, N- (4-sulfonylazidophenyl) maleimide, N-acetyl-4-sulfonylazidoaniline, 4-sulfonylazidoaniline, 4 azidoaniline, 4-azidophenacyl bromide, p-azidobenzoic acid, 2,6-bis (p-azidobenzylidene) cyclohexanone and 2,6-bis (p-azidobenzylidene) -4-methylcyclohexanone. Photoinitiators are, if used, typically employed in amounts of 0.01 to 5% by weight, based on the monomers to be polymerized.
[0069] Preference is given, according to the invention, to the use of a redox system consisting of hydrogen peroxide, sodium peroxodisulfate and ascorbic acid. In general, polymerization is initiated with the initiators within a temperature range of 0 ° C to 90 ° C.
[0070] The polymerization reaction can be triggered by an initiator or by a plurality of interacting initiators. In addition, polymerization can be carried out in such a way that one or more redox initiators are added first. Later in the polymerization, thermal initiators or photoinitiators are then applied additionally, and the polymerization reaction in the case of photoinitiators is then initiated by the action of high energy radiation. The reverse sequence is also conceivable, that is, the initial initiation of the reaction by means of high energy radiation and photoinitiators or thermal initiators and the initiation of polymerization by means of one or more redox initiators later in the polymerization.
[0071] In order to convert the polymers (P) thus obtained into a particulate form, they can first, after having been removed from the reaction mixture, be dried at a temperature within a range of 20 to 300 ° C , preferably within a range from 50 to 250 ° C and more preferably within a range of 100 to 200 ° C, up to a water content of less than 40% by weight, preferably less than 20% by weight, and even more preferably less than 10% by weight, in each case based on the total weight of the polymer (P). Drying is preferably carried out in ovens or dryers known to those skilled in the art, for example, belt dryers, stage dryers, rotary tube ovens, fluidized bed dryers, tray dryers, paddle dryers and infrared dryers.
[0072] According to the present invention, fragmentation is preferably carried out by dry grinding, preferably by dry grinding in a hammer mill, an immobilized disc mill, a ball mill or a roller mill.
[0073] In a preferred embodiment of the process according to the invention, the superabsorbent particles employed are particles that have an inner region and a surface region bordering the inner region, the surface region having a different chemical composition from the inner region or differing from the internal region in a physical property. Physical properties in which the inner region differs from the surface region are, for example, the charge density or the degree of crosslinking.
[0074] These superabsorbent particles that have an inner region and a surface region bordering the inner region are preferably obtained by post-crosslinking reactive groups close to the surface of the superabsorbent particles, before or after they have been removed from the remaining particles of the polymer (P ) in particles. This post-crosslinking can be performed thermally, photochemically or chemically.
[0075] Preferred post-crosslinkers are the compounds of class II and IV crosslinking agents mentioned in connection with the crosslinking agents (α3).
[0076] Among these compounds, particularly preferred post-crosslinkers are diethylene glycol, triethylene glycol, polyethylene glycol, glycerol, polyglycerol, propylene glycol, diethanolamine, triethanolamine, polyoxypropylene, oxyethylene-oxypropylene block copolymers, fatty acid esters, fatty acid esters. polyoxyethylene sorbitan, trimethylolpropane, pentaerythritol polyvinyl alcohol, sorbitol, 1,3-dioxolan-2-one (ethylene carbonate), 4-methyl-1,3-dioxolan-2-one (propylene carbonate), 4,5-dimethyl -1,3-dioxolan-2-one, 4,4-dimethyl-1,3-dioxolan-2-one, 4-ethyl-1,3-dioxolan-2-one, 4-hydroxymethyl-1,3-dioxolan -2-one, 1,3-dioxane-2-one, 4-methyl-1,3-dioxane-2-one, 4,6-dimethyl-1,3-dioxane-2-one, 1,3-dioxolan -2-one, poly-1,3-dioxolan-2-one.
[0077] Particular preference is given to the use of ethylene carbonate as a post-crosslinker.
[0078] Preferred embodiments of the superabsorbent particles are those which are post-crosslinked by crosslinking agents of the following classes of crosslinking agents or by crosslinking agents of the following combinations of crosslinking classes: II, IV, and II IV.
The crosslinking agent is preferably employed in an amount within the range of 0.01 to 30% by weight, more preferably in an amount within the range of 0.1 to 20% by weight and even more preferably in an amount within a range of 0.3 to 5% by weight, based, in each case, on the weight of the superabsorbent polymers in the post-crosslinking.
[0080] It is also preferable that post-cross-linking is carried out by contacting a fluid F comprising a solvent, preferably water, organic solvents miscible with water, for example, methanol or ethanol, or mixtures of at least two of these, and the post-crosslinker with the outer region of the polymer particles at a temperature within a range of 30 to 300 ° C, more preferably within a range of 100 to 200 ° C. The contact is preferably made by spraying the fluid F on the polymer particles and then by mixing the polymer particles in contact with the fluid F. The post-crosslinker is present in fluid F preferably in an amount in the range of 0, 01 to 20% by weight, more preferably in an amount within the range of 0.1 to 10% by weight, based on the total weight of the F fluid. Additionally, it is preferable that the F fluid comes into contact with the polymer particles in an amount within a range of 0.01 to 50% by weight, and more preferably in an amount within a range of 0.1 to 30% by weight, based, in each case, on the weight of the polymer particles.
[0081] The fluid used in step (vi) of the process, in the processes according to the invention preferably comprises a solvent and the crosslinkable but non-crosslinked polymer. The solvents employed are preferably water or polar solvents, miscible with water, such as acetone, methanol, ethanol, 2-propanol, or mixtures of at least two of these. The non-crosslinked polymer can be dissolved or dispersed in the solvent.
Useful condensation reactions preferably include the formation of ester, amide, imide or urethane bonds, with preference being given to the formation of ester bonds. These ester bonds are preferably formed by reacting an OH group of the non-crosslinked polymer with an acidic group of the superabsorbent particle or with an acid group of the non-crosslinked polymer.
[0083] Monomers (β1) containing acidic groups are preferably neutralized to an extent of at least 10 mol%, more preferably to an extent of at least 20 mol%, even more preferably to an extent of at least 40 mol% mol and even more preferably in the range of 45 to 80 mol%. The monomers can be neutralized before, during or only after the preparation of the non-cross-linked crosslinkable polymer. The neutralization is preferably carried out with the same bases that have already been mentioned in connection with the neutralization of the monomers (α1) that have acid groups. In addition to the bases mentioned therein, non-cross-linked polymers are preferably neutralized using bases that contain ammonium, calcium or magnesium as cations. The preferred bases in this context are ammonium carbonate, ammonia, calcium carbonate, calcium hydroxide, magnesium hydroxide and magnesium carbonate.
[0084] The monomers (β1) and (β2) used are preferably the monomers that are also used as preferred monomers (α1) and (α2), respectively.
[0085] In principle, the useful monomers (M) or (β3) are all suitable monomers for the person skilled in the art, especially those of class III crosslinking agent. Preferred monomers (β3) are products of the reaction of saturated aliphatic, cycloaliphatic hydrocarbons, aromatic alcohols, amines or thiols with ethylenically unsaturated carboxylic acids, derivatives of reactive carboxylic acids or allyl halides. Examples in this context include: (meth) allyl alcohol, (meth) allylamines, (meth) acrylic acid esters containing hydroxyls or amines, such as hydroxyalkyl acrylates, especially aminomethyl, 2-hydroxyethyl- (meth) acrylate acrylate or 2-aminopropyl (meth) acrylate, mono (meth) ally compounds of polyols, preferably diols, for example, polyethylene glycols or polypropylene glycols and glycidylalkyl (meth) acrylates, such as (meth) acrylate glycidyl.
[0086] Particularly preferred non-crosslinkable crosslinkable polymers that are employed in the processes according to the invention are polymers based on 1 to 80% by weight, more preferably on 1 to 60% by weight, and even more preferably on 1 to 20% by weight of (meth) acrylamide and 20 to 99% by weight, more preferably 40 to 99% by weight, and even more preferably 80 to 99% by weight, based, in each case, on the total weight of the polymer non-cross-linked, in (meth) acrylic acid, the (meth) acrylic acid being preferably partially neutralized.
[0087] Additionally, it is preferable that the fluid used in the process according to the invention, in addition to the solvent and the non-cross-linked crosslinkable polymer, additionally comprises an external cross-linking agent. This is especially true when the non-crosslinkable polymers do not include any monomers (M) or (β3). Additionally preferred external cross-linking agents are those of cross-linking classes II and IV, which have already been mentioned in connection with cross-linking agents (α3). Particularly preferred are the new cross-linking agents that have been mentioned as particularly preferred cross-linking agents of classes II and IV, in relation to the monomers (α3). In this context, it is even more preferred that the fluid still comprises the external crosslinking agent in an amount within a range of 0.01 to 30% by weight, preferably within a range of 0.1 to 15% by weight, and most preferably within a range of 0.2 to 7% by weight, based on the weight of the non-crosslinked polymer.
[0088] Preferred additives are substances that reduce the fragility of the superabsorbent particles produced by the process according to the invention, for example, polyethylene glycol, polypropylene glycol, mixed polyalkoxylates, polyalkoxylates based on polyols such as glycerol, trimethylolpropane or butanediol, surfactants with an HLB greater than 10, such as alkyl polyglucosides or ethoxylated sugar esters, such as polysorbates, under the trade name Tween from ICI. Some of these additives also act simultaneously as additional crosslinking agents, for example, polyethylene glycol, polypropylene glycol, trimethylolpropane or butanediol.
[0089] Other preferred additives are agents that reduce the hardness of the superabsorbent particles produced by the process according to the invention, for example, cationic surfactants such as alkyl trimethylammonium chloride, dialkyldimethylammonium chloride, dimethilstearylammonium chloride, alkylbenzyl dimethylammonium chloride, or the corresponding methyl methysulfates of imidazolinium quaternary oil fatty acids. These additives are preferably employed in amounts within a range of 0 to 5% by weight, more preferably within a range of 0.5 to 4% by weight, based on the weight of the non-crosslinked polymer. Additives can be added before or after polymerization. They bind polycarboxylates through anion-cation interaction and thus produce the softening effect. They simultaneously produce an improvement in the ability to absorb aqueous liquids. Another advantage of the substances is their biocidal action, which prevents unwanted degradation of swelling agents. This property is particularly important for some applications.
[0090] Preferred additives are, in addition, release agents, for example, powdery organic or inorganic release agents. These release agents are preferably employed in amounts within a range of 0 to 2% by weight, more preferably within a range of 0.1 to 1.5% by weight, based on the weight of the crosslinked polymer. Preferred release agents are: wood flour, pulp fibers, powdered bark, cellulose powder, mineral fillers, such as perlite, synthetic fillers such as powdered nylon, powdered rayon, diatomaceous earth, bentonite, kaolin, zeolites, talc, chalk, ash, coal dust, magnesium silicates, fertilizers or mixtures of substances. Finely divided colloidal silica is preferred, as it is sold under the trade name Aerosil by Evonik Degussa.
[0091] In a preferred embodiment of the process according to the invention, the superabsorbent particles come into contact with the fluid comprising the non-cross-linked polymer in the presence of an effect substance based on a poly-sugar or a compound containing oxygen-silicon or a mixture of at least two of these. The effect substance can be present in the fluid, or it can be mixed with the superabsorbent particles prior to contact of the superabsorbent particles with the fluid. It is also possible for the effect substance to be dissolved or dispersed in another liquid F 'and to make contact with the superabsorbent particles in the form of this solution or dispersion together with the fluid. Fluid F 'is composed, in addition to the effect substance, preferably a liquid, particularly preferred liquids being water and organic solvents, for example, methanol or ethanol, or mixtures of at least two of these, with special preference being given to water such as liquid.
[0092] Useful poly-sugars according to the invention include all starches familiar to a person skilled in the art and their derivatives, and also celluloses and their derivatives, and cyclodextrins, the cyclodextrins employed being preferably α-cyclodextrin, β-cyclodextrin, Y— cyclodextrin or mixtures of these cyclodextrins.
[0093] The preferred compounds containing silicon and oxygen are zeolites. The zeolites employed can be all natural or synthetic zeolites known to those skilled in the art. The preferred zeolites are the natural zeolites of the natrolite group, the harmotone group, the mordenite group, the chabasite group, the faujasita group (sodalite group) or the analcite group. Examples of natural zeolites are analcima, leucite, polucite, wairaquita, belbergita, biquitaita, bogsita, brewsterita, chabazita, wilhendersonita, cowlesita, dachiardita, edingtonita, epistilbita, erionita, faujasita, ferrierita, amicita, garronita, garmondita, gismondina, gismondina, gismondina, gismondina, gismondina , goosecreequita, harmotoma, filipsita, welsita, clinoptilolita, heulandita, laumontita, levina, mazzita, merlinoita, montesomaita, mordenita, mesolita, natrolita, scolecite, offretita, paranatrolita, paulingita, perlialita, barrerita, estitizita, esternitaita, estitizita, esternita, esternita. . Preferred synthetic zeolites are zeolite A, zeolite X, zeolite Y, zeolite P, or ABSCENTS products.
[0094] The cations present in the zeolites used in the process according to the invention are preferably alkali metal cations such as Li +, Na +, K +, Rb +, Cs + or Fr + and / or alkaline earth metal cations such as Mg2 +, Ca2 +, Sr2 + or Ba2 +.
[0095] The zeolites used can be zeolites of the so-called "intermediate" type, in which the SiO2 / AlO2 ratio is less than 10; the SiO2 / AlO2 ratio of these zeolites being more preferably within a range of 2 to 10. In addition to these "intermediate" zeolites, it is also possible to employ "high" type zeolites, which include, for example, the known "molecular sieve zeolites" "type ZSM, and beta-zeolites. These "high" zeolites are preferably characterized by a SiO2 / AlO2 ratio of at least 35, more preferably by a SiO2 / AlO2 ratio within a range of 200 to 500.
[0096] Zeolites are preferably used in the form of particles with an average particle size within a range of 1 to 500 μm, more preferably within a range of 2 to 200 μm and even more preferably within a range of 5 at 100 μm.
[0097] The effect substances are used in the processes according to the invention preferably in an amount within a range of 0.1 to 50% by weight, more preferably within a range of 1 to 40% by weight, and even more preferably in an amount within a range of 5 to 30% by weight, based, in each case, on the weight of the superabsorbent particles.
[0098] Preferred microbial inhibiting substances are, in principle, all active substances against Gram-positive bacteria, for example, 4-hydroxybenzoic acid and its salts and esters, N- (4-chlorophenyl) -N '- (3, 4-dichlorophenyl) urea, 2,4,4'ether-trichloro-2'-hydroxydiphenyl (triclosan), 4-chloro-3,5-dimethylphenol, 2,2'-methylenebis (6-bromo-4-chlorophenol), 3-methyl-4- (1-methyl-ethyl) phenol, 2-benzyl-4-chlorophenol, 3- (4-chlorophenoxy) -1,2-propanediol, 3-iodo-2-propynylbutyl, chlorhexidine, 3,4 , 4'-trichlorocarbonylide (TTC), anti-bacterial fragrances, thymol, thyme oil, eugenol, clove oil, menthol, mint oil, famesol, phenoxyethanol, glyceryl monocaprinate, glyceryl monocaprilate, glyceryl monolaurate ( GML), diglyceryl monocaprinate (DMC), N-alkylsalicylamides, for example N-octylsalicylamide or N-decylsalicylamide.
[0099] Suitable enzyme inhibitors are, for example, esterase inhibitors. These are preferably trialkyl citrates, such as trimethyl citrate, tripropyl citrate, triisopropyl citrate, tributyl citrate and, especially, triethyl citrate (TM Hidagen CAT, Cognis GmbH, Dusseldorf, Germany). The substances inhibit the activity of the enzyme and, as a result, reduce the formation of odor. Substances useful as esterase inhibitors are sterol sulphates or phosphates, for example, lanosterol sulphate or phosphate, cholesterol sulphate or phosphate, campesterol sulphate or phosphate, stigmasterol sulphate or phosphate and sitosterol sulphate or phosphate, acids dicarboxylic acids and esters thereof, for example glutaric acid, monoethyl glutarate, diethyl glutarate, adipic acid, monoethyl adipate, diethyl adipate, malonic acid and diethyl malonate, hydroxycarboxylic acids and their esters, for example citric acid, malic acid, tartaric acid or diethyl tartrate, and zinc glycinate.
[0100] Suitable odor absorbers are substances that can substantially adsorb and retain odor-forming substances. They reduce the partial pressure of the individual components and thus also reduce the rate of propagation of the same components. It is important that perfumes should remain intact. Odor absorbers have no effect against bacteria. They contain, for example, as a main constituent, a complex salt of zinc or ricinoleic acid or specific fragrances substantially neutral in odor known to those skilled in the art as "fixatives", for example, extracts of labdanum or stirax or certain derivatives of abietic acid The function of odor maskers is carried out by odorants or perfume oils, which, in addition to their function as odor maskers, transmit their own particular fragrance notes to deodorants Examples of perfume oils include mixtures of natural and synthetic odors Natural odors are extracts of flowers, stems and leaves, fruits, fruit peels, roots, woods, herbs and grasses, needles and branches, as well as resins and balms.Additionally useful are raw materials of animal origin, for example, algal Typical synthetic odorant compounds are products of the ester, ether, aldehyde, ketone, alcohol and hydrocarbon type. , for example, benzyl acetate, p-tert-butylcyclohexyl acetate, linalyl acetate, phenylethyl acetate, linalyl benzoate, benzyl formate, allylcyclohexyl propionate, stiralyl propionate and benzyl salicylate. Ethers include, for example, benzyl ethyl ether; aldehydes include, for example, linear alkanes with 8 to 18 carbon atoms, citral, citronelal, citroneliloxyacetaldehyde, cyclamen aldehyde, hydroxycitronelal, lilial and bourgeonal; ketones include, for example, ionones and methyl cedryl ketone; alcohols include anethole, citronelol, eugenol, isoeugenol, geraniol, linalool, phenylethyl alcohol and terpineol; hydrocarbons mainly include terpenes and balms. However, preference is given to the use of mixtures of different odorants that together produce a pleasant fragrance note. Suitable perfume oils are also essential oils of relatively low volatility, which are generally used as aroma components, for example, sage oil, chamomile oil, clove oil, melissa oil, mint oil, cinnamon leaf oil , lemon flower oil, juniper fruit oil, vetiver oil, olibanum, galbanum oil, labdanum oil and lavender oil. Preference is given to the use of bergamot oil, dihydromyrcenol, lilial, liral, citronelol, phenylethyl alcohol, alpha-hexylcinamaldehyde, geraniol, benzylacetone, cyclamen aldehyde, linalool, Boisambrene Forte, ambroxane, indole, Hedione, Sandelice, lemon oil, oil mandarin, orange oil, allyl amyl glycolate, cyclovertal, lavender oil, sage, beta-damask, geranium oil bourbon, cyclohexyl salicylate, Vertofix Coeur, Iso-E-Super, Fixolide NP, evernil, iraldein gamma, phenylacetic acid, geranyl acetate, benzyl acetate, rose oxide, Romilat, Irotil and Floramat, alone or in mixtures.
[0101] Antiperspirants reduce the formation of sweat by influencing the activity of the sweat glands and screens, and thus prevent underarm moisture and body odor. Suitable astringent antiperspirant active ingredients are, in particular, aluminum, zirconium or zinc salts. Such anti-hydrotically suitable active ingredients are, for example, aluminum chloride, aluminum hydrochloride, aluminum dihydrochloride, aluminum sesquichlorohydrate and the complexes thereof, for example, with 1,2-propylene glycol, aluminum hydroxyalantoinate, aluminum tartrate chloride , zirconium trihydrochloride, aluminum zirconium tetrachloride, aluminum zirconium pentachlorodrate and complexes of these, for example, with amino acids, such as glycine.
[0102] Apparatus suitable for mixing or spraying are all those that allow homogeneous distribution of the fluid in or with superabsorbent particles. Examples are Lodige mixers (manufactured by Gebrüeder Lodige Maschinenbau GmbH), Gericke multi-flow mixers (manufactured by Gericke GmbH), DRAIS mixers (manufactured by Drais GmbH Spezialmaschinenfabrik Manheim), Hosokawa mixers (Hosokawa Mokron Co., Ltd.), Ruberg mixers (manufactured by Gebr. Ruberg GmbH & Co.KG Nieheim), Hüttlin coaters (manufactured by BWI Hüttlin GmbH Steinen), fluidized bed dryers or AMMAG spray granulators (manufactured by AMMAG Gunskirchen, Austria) or Heinen (manufactured by A. Heinen AG Anlagenbau Varel), Patterson-Kelly mixers, NARA paddle mixers, screw mixers, pan mixers, fluidized bed dryers, Schugi mixers or PROCESSALL.
[0103] For contacting a fluidized bed, it is possible to employ all fluidized bed processes known to those skilled in the art and which appear to be suitable. For example, it is possible to use a fluid bed coater.
[0104] In addition to achieve the objectives described at the beginning, it is made by a composite including the inventive superabsorbents or the superabsorbents that can be obtained by the process according to the invention and a substrate. It is preferable that the inventive superabsorbents and the substrate are fixedly connected to each other. Preferred substrates are polymer films, for example, polyethylene, polypropylene or polyamide, metals, fabrics, hair, fabrics, fabrics made of natural or synthetic fibers, or other foams. In addition, it is preferable according to the invention that the composite comprises at least a region comprising the superabsorbent material of the invention in an amount in the range of 15 to 100% by weight, preferably about 30 to 100% by weight, more preferably from 50 to 99.99% by weight, even more preferably from 60 to 99.99% by weight and even more preferably from 70 to 99% by weight, based, in each case, on the total weight of the composite region in question, this region preferably having a size of at least 0.01 cm3, preferably at least 0.1 cm3 and more preferably at least 0.5 cm3.
[0105] A particularly preferred embodiment of the inventive compound involves a flat compound, as described in WO 02/056812 A1 as an "absorbent material". The disclosure and content of WO 02/056812 A1, especially with respect to the exact structure of the compound, the basic weight of its components and its thickness, is incorporated herein by reference and forms part of the disclosure of the present invention.
[0106] An additional contribution to the achievement of at least one of the objectives established at the beginning is made by a process to produce a composite, in which the water-absorbing polymers of the invention or the superabsorbents that can be obtained by the process according to invention and a substrate and, optionally, an additive come into contact with each other. The substrates used are preferably those substrates that have already been mentioned above, in relation to the inventive compound.
[0107] A contribution towards the realization of at least one of the objectives indicated at the beginning is also made by a composite obtained by the process described above, this composite, preferably having the same properties as the inventive composite described above.
[0108] An additional contribution to the achievement of at least one of the objectives established at the beginning is made by chemicals, including inventive superabsorbents or an inventive compound. Preferred chemicals are especially foams, molds, fibers, sheets, films, cables, sealing materials, liquid-absorbent hygiene items, mainly diapers and hygienic towels, plant growth carriers or fungus growth regulators or active ingredients for plant protection, additives for building materials, additives for packaging materials or additives for soil.
[0109] The use of inventive superabsorbents or the inventive composite in chemical products, preferably in the aforementioned chemicals, in particular in hygiene items, such as diapers or hygienic towels, as well as the use of superabsorbent particles as carriers for the growth of plants or fungi growth regulators or active ingredients for plant protection contribute to the achievement of at least one of the objectives stated at the beginning. If used as a carrier for plant growth or fungal growth regulators or plant protection active ingredients, preference is given to plant or fungal growth regulators or plant protection active ingredients to be released over a period controlled by the carrier. Testing methods
[0110] Unless otherwise indicated hereinafter, the measurements performed here are in accordance with ERT methods. "ERT" means EDANA Recommended Test and "EDANA" means European Disposable and Non-Woven Association. Centrifugal holding capacity (CRC)
[0111] Centrifugal holding capacity is determined by test method No. 441.2-02 "centrifugal holding capacity" from EDANA (European Association of Disposables and Non-Woven Fabrics). Determination of the Free Swelling Rate (FSR)
[0112] The absorption rate was determined by measuring the free swelling rate (FSR), using the test method described in EP-A-0 443 627, on page 12. Determination of permeability
[0113] Permeability is determined by measuring the "Flow of Saline Conductivity - SFC" by the test method described in WO-A-95/26209.
[0114] The following examples serve to further illustrate the invention, but without restricting it to them. Example 1
[0115] A monomer solution consisting of 2,480g of acrylic acid, 3,124g of water, 14.92g of polyethylene glycol-300 diacrylate, 11.94g of monoalyl polyethylene glycol-450 monoacrylate is free of dissolved oxygen by means of a nitrogen purification. The acrylic acid was neutralized to an extent of 70 mol%, with a sodium hydroxide solution (in this example, with 1,927 g of 50% NaOH). Purification with nitrogen is carried out over a period of about 10 minutes. During purification with inert gas, 2.33 g of sodium peroxodisulfate in 50 g of water are added to the monomer solution. Shortly before the transfer of the monomer solution to the polymerization reactor, 0.54g of 35% hydrogen peroxide solution in 50g of water is added to the monomer solution purified with inert gas. This is followed by the transfer of the monomer solution to the polymerization reactor, which is carried out in an inert gas countercurrent. The polymerization reactor consists of a co-rotational batch mixer reactor with double axis (LIST mixer reactor 10 liters CKR). The reactor is maintained at a coating temperature of approximately 85 ° C, by coating and heating the shaft before adding the monomer solution. The reactor axes rotate at 30 revolutions per minute. Immediately after transferring the monomer solution to the reactor, 0.5% by weight of sodium carbonate (produced in a fluidized bed spray granulation process, with a particle size of 400-600 μm) is added to the monomer solution and distributed in the reaction space by the rotating axes. This is followed by the addition of 0.233 g of ascorbic acid in 50 g of water, as a polymerization initiator. An exothermic polymerization reaction occurs. The final adiabatic temperature is in the range of 105 ° C to 110 ° C and the residence time of the reaction mixture is 10 minutes. Without additional crushing steps, the resulting hydrogel is dried in a drying booth with forced laboratory air at 150 ° C for 120 minutes.
[0116] The dry polymer is crushed in a Retsch cutting mill (2mm). Sieving results in a particle size of the dry and crushed superabsorbent from 150μm to 850μm.
Surface cross-linking
[0117] Subsequent post-crosslinking of the surface is carried out with particles of dry, ground and sieved polymer (= precursor material) of Example 1. For this purpose, the post-crosslinking solution of the surface composed of, Example 1a), carbonate ethylene / water, (1 or 3% by weight, based on the mass of the superabsorbent material) or, Example 1b), ethylene carbonate / water / aluminum sulfate / aluminum lactate (1/3 / 0.3 / 0, 4% by weight, based on the mass of the superabsorbent material) is sprayed onto the precursor material using a disposable syringe and mixed in a Krupp mixer. Drying / post-crosslinking of the surface is carried out in a laboratory drying cabinet at 170 ° C / 90 minutes (i), or 180 ° C / 30 minutes (ii). The following CRC and FSR values were measured:
Example 2
[0118] A monomer solution consisting of 2,560 g of acrylic acid is made, which has been neutralized to an extent of 70 mol%, with a sodium hydroxide solution (1,989 g of 50% NaOH), 3,363 g of water, 9 , 21g polyethylene glycol-300 diacrylate, 13.31g monoalkyl polyethylene glycol-450 monoacrylate. Two kilograms of the resulting material are taken for polymerization. The 2 kg of the monomer solution taken is free of dissolved oxygen by means of nitrogen purification. Purification with nitrogen is carried out for approximately 15 minutes. During purification with inert gas, 0.60g of sodium peroxodisulfate in 10g of water are added to the monomer solution. Shortly before the transfer of the monomer solution to the polymerization reactor, 0.14g of 35% hydrogen peroxide solution in 10g of water is added to the monomer solution purified with inert gas. This is followed by the transfer of the monomer solution to the polymerization reactor in an inert gas countercurrent. The polymerization reactor consists of a coaxial batch mixer reactor with double axis (LIST mixer reactor 2.5 liters CRP). Before adding the monomer solution, the reactor is heated to a temperature of approximately 75 ° C by means of a coating and the temperature is maintained. The reactor axes are rotated at 60 revolutions per minute. Immediately after transferring the monomer solution to the reactor, 0.5% by weight of sodium carbonate (produced in a fluidized bed spray granulation process, with a particle size of 400-600μm) is added to the monomer solution and distributed in the reaction space by the rotating axes. After that, 0.03 g of ascorbic acid in 2 g of water are added as a polymerization initiator. The target temperature of the heating circuit thermostat of the reactor heating jacket is set to 100 ° C immediately after the start of the reaction. An exothermic polymerization reaction occurs. The final adiabatic temperature is in the range of 105 ° C to 110 ° C. The residence time of the reaction mixture is 10 minutes. Without additional crushing steps, the hydrogel formed is dried in a drying booth with forced laboratory air at 150 ° C for 120 minutes. The dry polymer is crushed in a Retsch cutting mill (2 mm). Sieving results in a fragmented superabsorbent particle size of 150μm to 850μm.
Post-crosslinking of the surface:
[0119] Subsequent post-crosslinking of the surface is carried out with particles of dry, ground and sieved polymer (= precursor material) from Example 2. For this purpose, the post-crosslinking solution of the surface composed of, Example 2a), carbonate ethylene / water / aluminum sulfate / aluminum lactate (1/3 / 0.3 / 0.4% by weight, based on the mass of the superabsorbent material) is sprayed onto the precursor material using a disposable syringe and mixed in a Krupp mixer. This is then followed by drying / post-crosslinking the surface in a laboratory drying cabinet at 170 ° C / 90 minutes (i), or 180 ° C / 30 minutes (ii). The following FSR values were measured:
Example 3
[0120] A monomer solution consisting of 2,560 g of acrylic acid that was neutralized to a 70% mol extent, with sodium hydroxide solution (1,989 g of 50% NaOH), 3,363 g of water, 9,21 g of polyethylene glycol-300 diacrylate, 13.31g monoalyl polyethylene glycol-450 monoacrylate is composed.
[0121] 2 kg of this is taken for polymerization. The 2 kg of monomer solution made is free of dissolved oxygen by means of nitrogen purification. The nitrogen purification is carried out for approximately 15 minutes. During purification with inert gas, 0.60 g of sodium peroxodisulfate in 10 g of water are added to the monomer solution. Shortly before transferring the monomer solution to the polymerization reactor, a solution of 0.14 g of 35% hydrogen peroxide in 10 g of water is added to the monomer solution purified with inert gas. Then, the monomer solution is transferred to the polymerization reactor in an inert gas countercurrent. The polymerization reactor consists of a dual axis corrotational batch mixer reactor (2.5 L CRP mixer reactor). Before adding the monomer solution, the reactor is heated to a temperature of approximately 75 ° C by means of a coating and the temperature is maintained. The reactor axes are rotated at 60 revolutions per minute. Immediately after transferring the monomer solution to the reactor, 1.0% by weight of sodium carbonate (produced in a fluidized bed spray granulation process, with a particle size of 400-600μm) is added to the monomer solution and distributed in the reaction space by the rotating axes. After that, 0.03g of ascorbic acid in 2g of water is added as a polymerization initiator. The target temperature of the heating circuit thermostat of the reactor heating jacket is set to 100 ° C immediately after the start of the reaction. An exothermic polymerization reaction occurs. The final adiabatic temperature is in the range of 105 ° C to 110 ° C. The residence time of the reaction mixture is 10 minutes. Without additional crushing steps, the hydrogel formed is dried in a drying booth with forced laboratory air at 150 ° C for 120 minutes. The dry polymer is crushed in a Retsch cutting mill (2 mm). Sieving results in a fragmented superabsorbent particle size of 150μm to 850μm.
Post-crosslinking of the surface:
[0122] Subsequent post-crosslinking of the surface is carried out with particles of dry, ground and sieved polymer (= precursor material) from Example 3. For this purpose, the post-crosslinking solution of the surface composed of, Example 3a), carbonate ethylene / water / aluminum sulfate / aluminum lactate (1/3 / 0.3 / 0.4% by weight, based on the mass of the superabsorbent material) is sprayed onto the precursor material using a disposable syringe and mixed in a Krupp mixer. This is then followed by drying / post-crosslinking the surface in a laboratory drying cabinet at 170 ° C / 90 minutes (i), or 180 ° C / 30 minutes (ii). The following CRC and FSR values were measured:
Example 4
[0123] A monomer solution consisting of NaOH and acrylic acid, with a degree of neutralization of 70 mol% and a WS of 32% acrylic acid are prepared. In this monomer solution, 0.2% (based on acrylic acid) of the polyethylene glycol-300 diacrylate crosslinking agent and 0.4% (based on acrylic acid) of the monoalyl polyethylene glycol-450 crosslinking agent are dissolved.
[0124] The monomer solution is purified with nitrogen in a 3-liter Becker for 30 minutes in order to remove dissolved oxygen. At a temperature of 4 ° C, 0.5% granulated sodium carbonate (400-600μm) is added and then the polymerization is started with the successive addition of 0.3 g of sodium peroxodisulfate in 10 g of water distilled, 0.07g of 35% hydrogen peroxide solution in 10g of distilled water and 0.015g of ascorbic acid in 2g of distilled water. Once the final temperature (about 100 ° C) is obtained, the gel is ground with a meat grinder and dried in a drying booth with forced laboratory air at 150 ° C for 2 hours. The dry powder is coarsely crushed, ground and sieved to achieve a particle fraction of 150μm to 850μm.
Post-crosslinking of the surface:
[0125] Subsequent post-crosslinking of the surface is carried out with particles of dry, ground and sieved polymer (= precursor material) from Example 4. For this purpose, the post-crosslinking solution of the surface composed of, Example 4a), carbonate ethylene / water / aluminum sulfate / aluminum lactate (1/3 / 0.3 / 0.4% by weight, based on the mass of the superabsorbent material) is sprayed onto the precursor material using a disposable syringe and mixed in a Krupp mixer. This is then followed by drying / post-crosslinking the surface in a laboratory drying cabinet at 170 ° C / 90 minutes (i), or 180 ° C / 30 minutes (ii). The following CRC and FSR values were measured:

[0126] Despite the addition of granulated sodium carbonate, there was no improvement in FSR when a pot mixer was used. Example 5
[0127] The batch size and the experimental procedure, including post-crosslinking are in accordance with Examples 2 and 2a). The only difference is that the addition of sodium carbonate (0.5% by weight) immediately follows the addition of ascorbic acid.

[0128] According to the invention, the timing of the addition affects the resulting FSR, and should preferably follow the addition of H2O2 and precede the addition of ascorbic acid. Example 6: Comparative example
[0129] The batch size and the experimental procedure, including post-crosslinking are in accordance with Example 2 and Example 2a). The experiment was carried out without the addition of sodium carbonate.

[0130] The comparative example shows that, without the addition of sodium carbonate, the FSR does not obtain an inventive increase after the post-cross-linking step.

权利要求:
Claims (7)
[0001]
1. Process for the production of a composition of water-absorbing polymers, the process comprising the steps of (i) mixing (α1) 0.1 to 99.999%, by weight, of polymerized, ethylenically unsaturated monomers containing acid groups or their salts or polymerised monomers, ethylenically unsaturated, containing protonated or quaternized nitrogen, or mixtures thereof, (α2) 0 to 70% by weight, of ethylenically unsaturated polymerized monomers copolymerized with (α1), (α3) 0.001 to 10% by weight of one or more cross-linking agents, (α4) 0 to 30% by weight of water-soluble polymers, and (α5) from 0 to 20% by weight of one or more auxiliary agents, where the sum of their weights (α1) to (α5) is 100%, by weight, (ii) polymerize via free radicals with crosslinking to form an aqueous, untreated, water-insoluble hydrogel polymer, (iii) dry the hydrogel polymer, ( iv) crush and sieve the water-absorbing polymer, (v) post-cross-link the surface of the crushed hydrogel polymer and ( vi) drying and finalizing the water-absorbing polymer, in which expansion agents with a particle diameter of 300μm to 700μm are added to an aqueous monomer solution, before the addition of the initiator and the beginning of the polymerization of free radicals, characterized by process steps i) and ii) be carried out in batches or continuously in a mixing reactor, in which the blowing agents consist of granules of soda ash particles, and in which the blowing agent consists of particles of carbonate sodium that have a layered structure, in which the mass reactor is operated with a system of at least one axis and granulated sodium carbonate is homogeneously incorporated into the monomer solution and process step ii).
[0002]
2. Process according to claim 1, characterized in that the mixtures of polymerized, ethylenically unsaturated monomers containing acid groups or salts thereof and polymerized, ethylenically unsaturated monomers containing protonated or quaternized nitrogen, include at least ethylenically unsaturated monomers containing groups acids.
[0003]
Process according to claim 2, characterized by the fact that the acid group is acrylic acid.
[0004]
Process according to claim 1, characterized in that, in step iii), crushing is also carried out before drying the hydrogel polymer.
[0005]
A composite characterized in that it includes a water-absorbing polymer composition obtained by the process as defined in any one of claims 1 to 4.
[0006]
6. Process for producing a composite, characterized by a composition of water-absorbing polymers obtained by the process as defined in any one of claims 1 to 4 and an auxiliary agent coming into contact with each other.
[0007]
Use of the water-absorbing polymer composition obtained by the process as defined in any one of claims 1 to 4 or of a composite comprising a water-absorbing polymer composition as defined in claim 5 in foams, molds, fibers, sheets, films , cables, sealing materials, liquid-absorbent hygiene articles, plant growth conveyors and fungus growth regulators, packaging materials, additives for the soil, characterized for being for controlled release of active ingredients or in building materials .

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同族专利:

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公开号 | 公开日

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WO2012143235A1|2012-10-26|

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KR101635257B1|2016-06-30|

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法律状态:
2018-07-17| B06F| Objections, documents and/or translations needed after an examination request according art. 34 industrial property law|

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2019-10-01| B06U| Preliminary requirement: requests with searches performed by other patent offices: suspension of the patent application procedure|

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2020-04-14| B06A| Notification to applicant to reply to the report for non-patentability or inadequacy of the application according art. 36 industrial patent law|

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2020-05-19| B25D| Requested change of name of applicant approved|Owner name: EVONIK OPERATIONS GMBH (DE) |

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2020-09-15| B09A| Decision: intention to grant|

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2020-12-01| B16A| Patent or certificate of addition of invention granted|Free format text: PRAZO DE VALIDADE: 20 (VINTE) ANOS CONTADOS A PARTIR DE 03/04/2012, OBSERVADAS AS CONDICOES LEGAIS. |

优先权:

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申请号 | 申请日 | 专利标题

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DE102011007723A|DE102011007723A1|2011-04-20|2011-04-20|Process for the preparation of water-absorbing polymers with high absorption rate|

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DE102011007723.5|2011-04-20|

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PCT/EP2012/056019|WO2012143235A1|2011-04-20|2012-04-03|Process for producing water-absorbing polymers with high absorption rate|

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