METHOD OF MANUFACTURING ABSORBENT WATER RESIN, WATER ABSORBING RESIN, WATER ABSORBING AGENT AND ABSO

专利摘要:
With respect to water-absorbing resins, a method of making a water-absorbent resin is provided which has an appropriate specific BET surface and a water-absorbing rate and a water-absorbing agent and an absorbent article which are formed using the water-absorbing resin. In a first aspect of the present invention, when the reverse phase suspension polymerization of two or more steps is carried out in an ethylenically unsaturated water-soluble monomer in a hydrocarbon dispersion medium in the presence of at least one azo compound, a peroxide and an internal cross-linking agent, the amount of internal cross-linking agent used at the time of first stage polymerization is adjusted to fall in the range of 0.015 to 0.150 mmol per mol of the water soluble ethylenically unsaturated monomer used at the time of the first polymerization step and polymerization is carried out in such a way that the specific BET surface area of the secondary particles formed by agglomeration of obtained primary particles is controlled.
公开号:BR112017000530B1
申请号:R112017000530-1
申请日:2014-11-04
公开日:2020-11-17
发明作者:Masahiro Murakami；Tetsuhiro Hinayama；Hiroki Yabuguchi；Hideki Yokoyama
申请人:Sumitomo Seika Chemicals Co. Ltd.；
IPC主号:

专利说明:

TECHNICAL FIELD
[001] The present invention relates to a method of making a water-absorbent resin, with the formation of an absorbent material suitably used for hygiene materials, such as disposable diapers and sanitary articles, a water-absorbent resin and an agent water-absorbent material and an absorbent article using such water-absorbent resin. TECHNICAL BACKGROUND
[002] In recent years, water-absorbent resins have been widely used in the fields of hygiene materials, such as sanitary ware and disposable diapers.
[003] For water absorbing resins as described above, cross-linked products of partially neutralized acrylic acid polymers are preferred because they have many advantages, including the following: they have excellent water absorption performance; its raw materials, such as acrylic acid, have easy industrial availability, and therefore, they can be manufactured with stable quality and low cost; and they show no deficiencies in which, for example, decomposition and degradation are likely to occur.
[004] Examples of the desirable property of a water-absorbent resin in hygiene materials, such as sanitary articles and disposable diapers, include a high water absorption capacity and an excellent water absorption rate. However, for example, since a water holding capacity and a water absorption rate have a conflicting relationship, it is difficult to satisfy the balance between these properties.
[005] As technologies to improve the properties of water-absorbent resin suitably used for hygiene materials, for example, the following technologies are known: a method of carrying out reverse phase suspension polymerization using specific amounts of specific polymer protective colloid surfactant (see Patent Document 1); a method of performing reverse phase suspension polymerization in multiple stages of two or more stages (see Patent Document 2); a method of carrying out reverse phase suspension polymerization under the coexistence of β-1,3-glucans to obtain a water-absorbing resin, and, in addition, the addition of a cross-linking agent to the water-absorbing resin obtained for carry out a crosslinking reaction (see Patent Document 3); a method of carrying out reverse phase suspension polymerization using a specific amount of persulfate using as a polymerization initiator (see Patent Document 4); and a method of carrying out polymerization in aqueous solution in the presence of a phosphorus acid and / or a salt thereof to obtain a water-absorbing resin precursor, then mixing the water-absorbing resin precursor and a cross-linking agent surface and heating them (see Patent Document 5).
[006] However, the water-absorbing resins obtained in these methods do not necessarily satisfy the high water absorption capacity and the excellent water absorption rate described above, and there are still improvements to be made.
[007] In an absorbent material containing a water-absorbent resin, when the water-absorbent resin in which the diffusion property of a member to be absorbed is low is used, in the vicinity of the supply position of a liquid to be absorbed, the water-absorbent resin absorbs the liquid to be absorbed locally, and the swollen water-absorbent resin becomes dense, with the result that liquid blockage occurs frequently. In this case, since the gelled water absorbent resin still inhibits the diffusion property, the amount of rewetting of the liquid to be absorbed tends to be increased. TECHNICAL STATE DOCUMENT
[008] Patent Documents
[009] Patent Document 1: Unexamined Japanese Patent Application, Publication No. H06-345819
[010] Patent Document 2: Unexamined Japanese Patent Application, Publication No. H03-227301
[011] Patent Document 3: Unexamined Japanese Patent Application, Publication No. H08-120013
[012] Patent Document 4: Unexamined Japanese Patent Application, Publication No. H06-287233
[013] Patent Document 5: Unexamined Japanese Patent Application, Publication No. H09-124710 DESCRIPTION OF THE INVENTION Problems to be solved by the invention
[014] The present invention is proposed taking into account the previous situations, and has the objective of providing a method of manufacturing a water-absorbent resin that is used in a hygienic material, that has an appropriate BET specific surface area and that is used as an absorbent material to improve the performance of the absorbent material, a water-absorbent resin, a water-absorbent agent containing the resin thereof, and an absorbent article which uses an absorbent material containing the resin thereof. Means to Solve Problems
[015] The present inventors have carried out exhaustive studies to solve the problems described above. As a result, they found that when reverse phase suspension polymerization of two or more steps is carried out on a water soluble ethylenically unsaturated monomer in a hydrocarbon dispersion medium in the presence of an azo compound and a peroxide, the surface area Specific BET of the secondary particles formed by the agglomeration of the primary particles obtained by carrying out, at the time of the first stage polymerization, the polymerization by adjusting the amount of internal cross-linking agent used in a specific range is controlled to be within a range with the result that the performance of an absorbent material using water-absorbent resin is improved. Thus, the present invention has been completed. Specifically, the present invention provides the following. (1) The present invention provides a method of making a water-absorbent resin, in which when the two-phase or more reverse phase suspension polymerization is carried out in an ethylenically unsaturated monomer soluble in water in a hydrocarbon dispersion medium in the presence of at least one azo compound, a peroxide and an internal cross-linking agent, the amount of internal cross-linking agent used at the time of the first step polymerization for 1 mol of the soluble ethylenically unsaturated monomer in water used at the time of polymerization of the first stage is adjusted to fall in the range of 0.015 to 0.150 mmol and the polymerization is carried out in such a way that a specific BET surface area of secondary particles formed by agglomeration of primary particles obtained is controlled. (2 ) According to the present invention, in the invention of item (1) above, in the method of manufacturing a resin water absorber, the amount used (in moles) of the internal crosslinking agent at the time of polymerization of the second and subsequent stages for 1 mole of the water soluble ethylenically unsaturated monomer of the second stage and later, is 90% or less of an amount used (in moles) of the internal cross-linking agent used at the time of polymerization of the first step to 1 mol of the water-soluble ethylenically unsaturated monomer used at the time of the polymerization of the first step. (3) According to the present invention, in the invention of item (1) or (2) above, in the method of manufacturing a water-absorbent resin, the specific BET surface area of the secondary particles that are formed by agglomeration of the primary particles and that are classified at 300 to 400 pm is controlled for be less than 0.03 mVg. (4) The present invention provides a water-absorbing resin that is obtained by polymerizing an ethylenically unsaturated water-soluble monomer in the presence of an internal crosslinking agent, in which the water absorption rate of a physiological saline solution in the water-absorbent resin is 40 to 80 seconds, a mass ratio of particles of 150 to 850 pm in all the water-absorbing resin is 85% by mass or more, and a particle mass ratio of 300 to 400 pm is 20% by mass or more and a specific BET surface area of particles classified at 300 to 400 pm is less than 0.03 rrP / g- (5) In accordance with the present invention, in the invention of item (4) above, in the water-absorbent resin, an average particle diameter of the water-absorbent resin is 200 to 600 pm. (6) The present invention provides a water-absorbent agent that is obtained by mixing the water-absorbing resin according to item (4) or (5) above with a fine inorganic powder. (7) The present invention provides an absorbent article that is formed using a absorbent material containing the water-absorbent resin according to item (4) or (5) above. (8 ) The present invention provides an absorbent article which is formed by means of an absorbent material containing the water absorbing agent according to item (6) above. Effects of the Invention
[016] By the method of making a water-absorbent resin in accordance with the present invention, it is possible to obtain a water-absorbent resin that has a specific BET surface area of an appropriate range.
[017] In the water-absorbent resin according to the present invention, without increasing its particle diameter, a water absorption rate that is one of the factors for the diffusion and re-wetting of a liquid to be absorbed falls within an appropriate range, and the specific BET surface area of the same also falls within an appropriate range. BRIEF DESCRIPTION OF THE DRAWINGS
[018] FIG. 1 is a pattern diagram showing the schematic arrangement of an apparatus for measuring the water-absorbing capacity of a physiological saline solution under a load of 4.14 kPa. PREFERRED MODE FOR CARRYING OUT THE INVENTION
[019] The present invention will be described in detail below. 1. Method of manufacturing water-absorbent resin
[020] A method of making a water-absorbent resin according to the present invention will be described.
[021] The method of making a water-absorbent resin according to the present invention includes a step of carrying out, in a method of making a water-absorbing resin by carrying out reverse phase suspension polymerization of an ethylenically monomer unsaturated water-soluble in a hydrocarbon dispersion medium, reverse phase suspension polymerization, in the presence of an internal cross-linking agent, and in the presence of an azo-based compound and a peroxide. A more detailed description will be given below. [Water soluble ethylenically unsaturated monomer]
[022] Ethylenically unsaturated water-soluble monomers include, for example, (meth) acrylic acid ("(meth) acry" used herein refers to both "acri" and "metachri". The same applies hereinafter) and their salts; 2- (meth) acrylamide-2-methylpropanesulfonic acid and its salts; nonionic monomers such as (meth) acrylamide, N, N-dimethyl (meth) acrylamide, 2-hydroxyethyl (meth) acrylate, N-methylol (meth) acrylamide, polyethylene glycol mono (meth) acrylate; amino group containing unsaturated monomers, such as N, N-diethylaminoethyl (meth) acrylate, N, N-diethylaminopropyl (meth) acrylate, diethylaminopropyl (meth) acrylamide and quaternary compounds thereof. Among these ethylenically unsaturated monomers soluble in water, (meth) acrylic acid or its salts, (meth) acrylamide, N, N-dimethylacrylamide are preferred in view of the easy industrial availability, and (meth) acrylic acid and its salts, are most preferred. Note that these water-soluble ethylenically unsaturated monomers can be used alone or in combination of two or more.
[023] Among these, acrylic acid and its salts are widely used as raw materials for water-absorbing resins, and can also be used in a case in which the aforementioned ethylenically unsaturated water-soluble monomers are copolymerized with these partially neutralized acrylates. In this case, a partially neutralized acrylate is preferably used as the main water-soluble ethylenically unsaturated monomer in an amount of 70 to 100 mol% relative to the total amount of water-soluble ethylenically unsaturated monomers.
[024] Preferably, an ethylenically unsaturated water-soluble monomer is dispersed in a hydrocarbon dispersion medium in the form of an aqueous solution, and subjected to reverse phase suspension polymerization. A water soluble ethylenically unsaturated monomer in the form of an aqueous solution can increase the efficiency of dispersion in a hydrocarbon dispersion medium. For the concentration of an ethylenically unsaturated monomer soluble in water in the aqueous solution, it is preferably in a range of 20% by mass for the saturation concentration. As will be described later, in polymerization in the presence of an azo compound, a polymerization rate tends to be increased, in order to avoid excessive heat storage and easily obtain the performance of the water-absorbing resin according to the present invention, the concentration of the water soluble ethylenically unsaturated monomer is more preferably 55% by weight or less, more preferably 50% by weight or less and even more preferably 45% by weight or less. On the other hand, in order to maintain productivity at a satisfactory level, the concentration of the water soluble ethylenically unsaturated monomer is more preferably 25% by weight or more, and even more preferably 28% by weight or more and even more preferably 30% by mass or more.
[025] When an ethylenically unsaturated water-soluble monomer has an acid group such as (meth) acrylic acid, 2- (meth) acrylamide-2-methylpropanesulfonic acid, those that have the pre-neutralized acid group with an alkaline neutralizer can be used if wanted. Such alkaline neutralizers include alkali metal salts, such as sodium hydroxide, sodium carbonate, sodium hydrogen carbonate, potassium hydroxide, potassium carbonate; ammonia and the like. In addition, these alkaline neutralizers can be used in the form of an aqueous solution, in order to simplify the neutralization procedures. It is noted that the alkaline neutralizers mentioned above can be used alone or in combination of two or more.
[026] For the degree of neutralization of a water-soluble ethylenically unsaturated monomer with an alkaline neutralizer, the degree of neutralization of all acid groups in the water-soluble ethylenically unsaturated monomer is preferably 10 to 100 mol%, more preferably 30 at 90 mol%, even more preferably from 40 to 85 mol% and even more preferably more than 50 to 80 mol%. [Hydrocarbon medium and dispersion]
[027] Hydrocarbon dispersion media include, for example, aliphatic hydrocarbons having 6 to 8 carbon atoms, such as n-hexane, n-heptane, 2-methylhexane, 3-methylhexane, 2,3-dimethylpentane , 3-ethylpentane, n-octane; alicyclic hydrocarbons such as cyclohexane, methylcyclohexane, cyclopentane, methylcyclopentane, trans-1,2-dimethylcyclopentane, cis-1,3-dimethylcyclopentane, trans-1,3-dimethylcyclopentane; aromatic hydrocarbons such as benzene, toluene, xylene and the like. Among these hydrocarbon dispersion media, in particular, n-hexane, n-heptane, cyclohexane are suitably used, in view of easy industrial availability, stable quality and low cost. These hydrocarbon dispersion means can be used alone or in combination of two or more. Note that examples of a mixture of hydrocarbon dispersion media include commercially available products such as Exxsol heptane (manufactured by Exxon Mobil Corporation: 75 to 85 mass% of heptane and its isomeric hydrocarbons are contained), which can also produce an adequate result.
[028] For the amount of hydrocarbon dispersion medium used, which is preferably 100 to 1500 parts by weight in relation to 100 parts by weight of a first stage of water-soluble ethylenically unsaturated monomer, and more preferably 200 to 1400 parts per mass, forms the view that the water-soluble ethylenically unsaturated monomer can be dispersed evenly to allow easy control over the polymerization temperature. It is noted that, as described below, the polymerization in reverse phase suspension is carried out in several steps, such as two or more steps, and the polymerization of the first step described above means a polymerization reaction of the first step in multiple polymerization steps. (The same applies from now on). [Dispersion stabilizer] (Surfactant)
[029] In reverse phase suspension polymerization, in order that the stability of the dispersion in the dispersion medium of the water-soluble ethylenically unsaturated monomer hydrocarbon to be reinforced, a dispersion stabilizer can also be used. A surfactant can be used as the dispersion stabilizer.
[030] As surfactants, the following may be used: for example, sucrose fatty acid esters, polyglycerin fatty acids, sorbitan fatty acid esters, polyoxyethylene sorbitan fatty acid esters, polyoxyethylene-fatty acid esters glycerin, sorbitol fatty acid esters, polyoxyethylene-sorbitol fatty acid esters, polyoxyethylene alkyl ethers, phenoxy alkyl polyoxyethylene ethers, polyoxyethylene castor oil, polyoxyethylene-hydrogenated castor oil, polyoxyethylene ethylene formaldehyde esters. , polyoxyethylene polyoxypropylene block copolymers, polyoxyethylene polyoxypropyl alkyl ethers, polyethylene glycol fatty acid esters, alkyl glycosides, N-alkyl gluconamides, polyoxyethylene fatty acid amides, polyoxyethylene alkyl amines and phosphate ester ethers, phosphate ester esters polyoxyethylene alkyl aryl ether phosphate esters and the like. Among these surfactants, in particular sorbitan fatty acid esters, polyglycerin fatty acid esters, and sucrose fatty acid esters are preferably used in terms of the stability of the monomer dispersion. These surfactants can be used alone or in combination of two or more of these.
[031] For the amount of surfactants used, it is preferably 0.1 to 30 parts by weight relative to 100 parts by weight of a first stage of ethylenically unsaturated water-soluble monomer, and more preferably 0.3 to 20 parts by weight. (Polymeric dispersing agent)
[032] A polymeric dispersion agent, can also be used, together with a surfactant described above, as a dispersion stabilizer used in reverse phase suspension polymerization.
[033] Polymeric dispersing agents include, for example, polyethylene modified with maleic anhydride, polypropylene modified with maleic anhydride, ethylene-propylene copolymer modified with maleic anhydride, (ethylene-propylene-diene terpolymer) EPDM modified with maleic anhydride, polybutadiene modified with maleic anhydride, ethylene maleic anhydride copolymer, maleic-propylene anhydride copolymer, maleic-ethylene-propylene copolymer, maleic-butadiene anhydride copolymers, polyethylene, polypropylene, ethylene-propylene copolymer, oxidized polyethylene, oxidized polyethylene, polypropylene oxidized ethylene-propylene copolymer, ethylene-acrylate copolymer, ethyl cellulose, ethyl hydroxyethyl cellulose and the like. Among these polymeric dispersing agents, particularly preferred from the point of view of the dispersion stability of the maleic anhydride modified polyethylene monomer, maleic anhydride modified polypropylene, ethylene-propylene copolymer modified with maleic anhydride, ethylene maleic anhydride copolymer, propylene copolymer maleic anhydride, maleic anhydride-ethylene-propylene copolymer, polyethylene, polypropylene, ethylene-propylene copolymer, oxidized polyethylene, oxidized polypropylene, and oxidized ethylene-propylene copolymer are preferably used. These polymeric dispersing agents can be used alone or in combination of two or more of these.
[034] For the amount of polymeric dispersing agents used, it is preferable 0.1 to 30 parts by weight relative to 100 parts by mass of a first stage water-soluble ethylenically unsaturated monomer, and more preferably 0.3 to 20 parts by weight. pasta. [Internal crosslinking agent]
[035] The method of making a water-absorbent resin according to the present invention is characterized by the fact that in the presence of internal cross-linking agent, the amount of internal cross-linking agent used at the time of the polymerization of the first step is adjusted to fall within a specific range, and reverse phase suspension polymerization is carried out on a water soluble ethylenically unsaturated monomer.
[036] Examples of the internal cross-linking agent include internal cross-linking agents that can cross-link the water-soluble ethylenically unsaturated monomer polymer to be used. They include, for example, unsaturated polyesters obtained by reacting a polyol including a diol and a triol such as (poly) ethylene glycol ("(poly)" refers to a case where a prefix "poly" exists and a case where the prefix does not exist. The same applies hereinafter), (poly) propylene glycol, 1,4-butanediol, trimethylolpropane and (poly) glycerin, with an unsaturated acid such as (meth) acrylic acid, maleic acid and fumaric acid; bisacrylamides such as N, N-methylenebisacrylamide; esters of di (meth) acrylic acid or esters of tri (meth) acrylic acids obtained by allowing polyepoxide to react with (meth) acrylic acid; carbamyl esters of di (meth) acrylic acid obtained by leaving polyisocyanate such as tolylene diisocyanate, hexamethylene diisocyanate to react with (meth) acrylic acid; hydroxyethyl, compounds having two or more polymerizable unsaturated groups, for example, allylated starch, allylated cellulose, diallyl phthalate, N, N ,, N "-triallylisocyanate, divinylbenzene and the like; polyglycidyl compounds, for example, diglycidyl compounds such diglycidyl (poly) ethylene glycol ether, diglycidyl (poly) propylene glycol ether, diglycidyl (poly) glycerin ether, triglycidyl compounds and the like; epihalohydrin compounds, such as epidorhydrin, epibromhydrin, a-methyl epidorhydrin; compounds that have two or more functional and functional groups, for example, isocyanate compounds such as 2,4-tolylene diisocyanate, hexamethylene diisocyanate; oxetane compounds such as 3-methyl-3-oxethane methanol, 3-ethyl-3-oxethane methanol, 3-butyl-3-oxethane methanol, 3-methyl-3-oxethane ethanol, 3-ethyl-3-oxethane ethanol, 3-butyl-3-oxethane ethanol Among these internal cross-linking agents, polyglycidyl compounds are preferably used, anddiglycidyl compounds such as diglycidyl (poly) ethylene glycol ether, diglycidyl (poly) propylene glycol ether, diglycidyl (poly) glycerin ether are particularly preferably used. These internal crosslinking agents can be used alone or in combination of two or more.
[037] In order for the polymer obtained to indicate an excellent water absorption performance by adequate crosslinking, the amount of internal crosslinking agent used at the time of polymerization of the first step per 1 mol of the water-soluble ethylenically unsaturated monomer used at the time of polymerization of the first step is 0.015 mmol or more, preferably 0.020 mmol or more and more preferably 0.025 mmol or more. The amount of internal cross-linking agent used at the time of polymerization of the first step for 1 mol of water-soluble ethylenically unsaturated monomer used at the time of polymerization of the first stage is 0.150 mmol or less, preferably 0.120 mmol or less and more preferably 0.100 mmol or less. Thus, the amount of internal cross-linking agent used at the time of polymerization of the first step for 1 mol of the water-soluble ethylenically unsaturated monomer used at the time of the polymerization of the first step is 0.015 to 0.150 mmol, preferably 0.020 to 0.120 mmol and more preferably 0.025 to 0.100 mmol.
[038] When in the polymerization of the second and step and later, the internal crosslinking agent is used more than necessary, there may be a possibility that the water-absorbent resin having an adequate water absorption rate will not be obtained. Thus, in the second and subsequent stages, the amount used (in moles) of internal cross-linking agent per 1 mol of the water soluble ethylenically unsaturated monomer in the second and subsequent stages is preferably 90% or less of the used (mol) amount of the cross-linking agent internal used at the time of polymerization of the first stage for 1 mol of the water-soluble ethylenically unsaturated monomer used at the time of the polymerization of the first stage, and more preferably 10 to 85% of the quantity used (mol). [Compound based on azo and peroxide]
[039] The method of making a water-absorbent resin according to the present invention is characterized by the fact that reverse phase suspension polymerization is carried out on the water soluble ethylenically unsaturated monomer in the presence of an azo-based compound. and a peroxide.
[040] In the polymerization step above, the phrase "in the presence of an azo-based compound and a peroxide" does not necessarily mean that the azo-based compound and peroxide are coexisting at the start of a polymerization reaction, but it does that the other compound is present before a monomer conversion rate by radical cleavage due to a compound becoming less than 10%. However, the two are preferably present in an aqueous solution containing a water-soluble ethylenically unsaturated monomer before the polymerization reaction begins. In addition, an azo-based compound and a peroxide can be added to a polymerization reaction system through different flow channels or can be sequentially added to the polymerization reaction system through the same flow channel.
[041] It is noted that an azo-based compound and a peroxide to be used can be in the form of a powder or an aqueous solution. (Azo-based compound)
[042] Specifically, azo-based compounds include, for example, azo-based compounds, such as l - {(l-cyano-l-methylethyl) azo} formamide, 2,2'-azobis [2 - (N-phenyl amidino) propane] dihydrate, 2,2'-azo-bis- {2- [N- (4-dorophenyl) amidino] propane} dihydrate, 2,2'-azobis {2- [N- (4-hydroxyphenyl) amidino] propane} dihydrochloride, 2,2'azobis [2- (N-benzyl amidino) propane] dihydrochloride, 2,2, -azobis [2- (N-allyl-amidino) propane] dihydrochloride, 2,2'-azobis (2-amidinopropane) dihydrochloride, 2,2'-azobis {2- [N- (2-hydroxyethyl) amidino] propane} dihydrate, 2,2 ' -azobis [2- (5-methyl-2-imidazoline-2-yl) propane] dihydrochloride, 2,2, azobis [2- (2-imidazoline-2-yl) propane] dihydrochloride, 2,2 '- azobis [2- (4,5,6,7-tetrahydro-1H-1,3-diazepine-2-yl) propane] dihydrochloride, 2,2'-azobis [2- (5-hydroxy -3,4,5,6-tetrahydro-pyrimidine-2-yl) propane] dihydrate, 2,2'-azobis {2- [l- (2-hydroxyethyl) -2-imidazoline-2-yl ] propane} dihydrochloride, 2,2'-azobis [2- (2-imidazolin-2-yl) propane], 2,2'-azobis {2-methyl-N- [1,1-bis (hydroxymethyl) -2-hydro xiethyl] propionamide}, 2,2'-azobi {2-methyl-N- [1,1-bis (hydroxymethyl) ethyl] propionamide}, 2,2'-azobis [2-methyl-N- (2-hydroxyethyl) propionamide], 2,2'-azobis [2-methylpropionamide) dihydrate, 4,4'-azobis-4-cyanovaleinic acid, 2,2, -azobis [2- (hydroxymethyl) propionitrile], 2,2'- azobis [2- (2-imidazoline-2-yl) propane] di-disulfate dihydrate, 2,2'-azobis- [N- (2-carboxyethyl) -2-methylpropionamidine] tetrahydrate, 2,2 ' -azobis [2-methyl-N- (2-hydroxyethyl) propionamide]. Among these compounds, 2,2, -azobis (2-amidinopropane) didhydrate, 2,2'-azo-bis- {2- [1- (2-hydroxyethyl) -2-imidazoline-2-yl] propane} didhydrate, and 2,2'-azo-bis- [N- (2-carboxyethyl) -2-methylpropionamidine] tetrahydrate are particularly preferred because they easily adjust to the polymerization reaction such as a polymerization temperature and it is possible to obtain a resin water absorbent having excellent water absorption performance. These azo compounds can be used alone or in combination of two or more. (Peroxide)
[043] Peroxides include, for example, persulfates such as potassium persulfate, ammonium persulfate, sodium persulfate; peroxides, such as methyl ethyl ketone peroxide, methyl isobutyl ketone peroxide, di-t-butyl peroxide, cumyl t-butyl peroxide, t-butyl peroxyacetate, t-butyl peroxy isobutyrate, t-butyl pivalate peroxy , hydrogen peroxide. Among these peroxides, potassium persulfate, ammonium persulfate, sodium persulfate, and hydrogen peroxide are preferably used; and potassium persulfate, ammonium persulfate, and sodium persulfate are used most preferably. These peroxides can be used alone or in combination of two or more. (Amount used and Proportion Used of Compound Based on Azo and Peroxide)
[044] For the amount used of an azo-based compound and a peroxide, in order to reduce the polymerization reaction time, it is preferably 0.00005 mol or more relative to 1 mol of a water-soluble ethylenically unsaturated monomer , more preferably 0.0001 mol or more. In addition, in order to prevent a rapid polymerization reaction, the amount used is preferably 0.005 moles or less relative to 1 mole of a water-soluble ethylenically unsaturated monomer, and more preferably 0.001 moles or less.
[045] For the proportion of an azo-based compound used and a peroxide, the proportion of an azo-based compound is preferably 40% by weight or more in the total amount used of an azo-based compound and a peroxide, more preferably 50% by weight or more, even more preferably 60% by weight or more and even more preferably 70% by weight or more. On the other hand, the proportion of an azo-based compound is preferably 95% by weight or less in the total amount used of an azo-based compound and peroxide, more preferably 90% by weight or less, more preferably 85% by weight. mass and even more preferably 80% by mass or less. The mass ratio range (azo-based compound: peroxide) is preferably 8:12 to 19: 1. [Other components]
[046] In the method of making a water-absorbent resin according to the present invention, other components can be added to an aqueous solution containing a water-soluble ethylenically unsaturated monomer to effect reverse phase suspension polymerization, if desired. Like other components, chain transfer agents, thickeners, various other additives and the like can be added. (Chain transfer agent)
[047] In the method of making a water-absorbent resin in accordance with the present invention, in order to control the water-absorbing performance of the water-absorbing resin, polymerization can be carried out on the ethylenically unsaturated water-soluble monomer in the presence of a chain transfer agent.
[048] Specific examples of the chain transfer agent include: thiols, such as ethane thiol, propane thiol and dodecanethiol; thiol acids such as thioglycolic acid, thiomolic acid, dimethyl dithiocarbamate, diethyl dithiocarbamate and their salts; secondary alcohols such as isopropanol; phosphorous acid compounds, such as normal phosphorous acid salts (for example, as phosphorous acid, disodium phosphoric acid, dipotassium phosphite and diaphonium phosphorous acid, etc.), and such as acidic phosphoric acid salts (for example, as sodium hydrogen phosphite, potassium hydrogen phosphite and phosphorous acid ammonium hydrogen phosphate, etc.); phosphoric acid compounds, such as normal phosphoric acid salts (for example, as phosphoric acid, sodium phosphate, potassium phosphate and ammonium phosphate, etc.), and as salts of phosphoric acid acids (for example, as di -sodium hydrogen phosphate, potassium dihydrogen phosphate, ammonium dihydrogen phosphate, disodium hydrogen phosphate, dibasic potassium hydrogen phosphate and diamonium hydrogen phosphate, etc.); hypophosphorous acid compounds, such as hypophosphorous acid salts (for example, as hypophosphorous acid, sodium hypophosphite, potassium hypophosphite and ammonium hypophosphite, etc.); pyrophosphoric acid, tripolyphosphate, polyphosphoric acid and its salts; and trimethyl phosphate, nitrilotrimethylene triphosphonic acid and the like. These chain transfer agents can be used alone or in combination of two or more. As the chain transfer agent, its hydrate can be used.
[049] For one mol of the water soluble ethylenically unsaturated monomer, the amount of chain transfer agent used is preferably 0.00001 to 0.0005 mol, and is more preferably 0.000025 to 0.00012 mol. (Thickener)
[050] In the method of making a water-absorbent resin according to the present invention, a thickener can be added to an aqueous solution containing a water-soluble ethylenically unsaturated monomer to effect reverse phase suspension polymerization. By adding a thickener to adjust the viscosity of an aqueous solution, the average particle diameter obtained by reverse phase suspension polymerization can also be controlled.
[051] Specifically, as a thickening agent, for example, hydroxyethyl cellulose, hydroxypropyl cellulose, methyl cellulose, carboxymethyl cellulose, polyacrylic acid, (partially) neutralized polyacrylic acid, polyethylene glycol, polyacrylamide, polyethyleneimine, dextrin, sodium alginate, poly alcohol polyvinyl pyrrolidone, polyethylene oxide and the like can be used. Note that in a case where the stirring speeds at the time of polymerization are the same, there is a tendency that the higher the viscosity of an aqueous solution of an ethylenically unsaturated water-soluble monomer, the larger the average particle diameter of the resulting particles. [Reverse phase suspension polymerization]
[052] When carrying out reverse phase suspension polymerization, for example, an ethylenically unsaturated water-soluble monomer is dispersed in a hydrocarbon dispersion medium in the presence of a surfactant and / or a polymeric dispersion agent. In doing so, a surfactant and a polymeric dispersing agent can be added before or after the aqueous monomer solution is dispersed, as long as they are added before starting a polymerization reaction.
[053] In particular, in view of the easy reduction of the amount of a residual hydrocarbon dispersion medium in the resulting water-absorbing resin, it is preferred that the polymerization be carried out after a water-soluble ethylenically unsaturated monomer is added and then dispersed in a hydrocarbon dispersion medium in which a polymeric dispersing agent has been dispersed, and then a surfactant is subsequently dispersed.
[054] In the present invention, reverse phase suspension polymerization is carried out in several stages of two or more stages. In the method of making a water-absorbent resin according to the present invention, the polymerization of two or more steps, as described above, is carried out and, therefore, a water-absorbent resin containing secondary particles in which the primary particles are agglomerated is manufactured. Furthermore, taking into account the increase in productivity, it is most preferably carried out in 2 or 3 stages.
[055] In a case where reverse phase suspension polymerization is carried out in several steps, such as two or more steps, after a first reverse phase suspension polymerization step is carried out, a water-soluble ethylenically unsaturated monomer it can be added to the reaction mixture obtained in the polymerization reaction step, and mixed to carry out a second reverse phase suspension polymerization step as in the first step. Preferably, in a reverse phase suspension polymerization process at each stage of the second and subsequent stages, the reverse phase suspension polymerization can be carried out by adding, in addition to a water soluble ethylenically unsaturated monomer, an internal crosslinking, an azo compound and a peroxide described above within the range of the molar ratio of each component to the water soluble ethylenically unsaturated monomer based on the amount of water soluble ethylenically unsaturated monomer mentioned above to be added in the suspension polymerization of reverse phase at each stage of the second and subsequent stages. In the method of making a water-absorbent resin according to the present invention, in the polymerization of the second step and the subsequent steps, the polymerization is carried out in the presence of an azo compound and a peroxide.
[056] For the reaction temperature for a polymerization reaction, it is preferably 20 to 110 ° C, more preferably 40 to 90 ° C from the point of view that profitability can be improved, allowing rapid progress of a polymerization to reduce a polymerization time, and the heat of polymerization can be easily removed to effect a smooth reaction. In addition, the reaction time is preferably 0.5 to 4 hours.
[057] A stirring operation of the aqueous monomer solution can be performed with several known stirring paddles. Specifically, such as the stirring blade, for example, a propeller blade, a paddle blade, an anchor blade, a turbine blade, a Pfaudler blade, a strip blade, a FULLZONE blade (produced by Shinko Pantec Co. , Ltd.), a MAXBLEND blade (manufactured by Sumitomo Heavy Industries, Ltd.), a Super-Mix blade (Satake Chemical Machinery Co., Ltd.) or the like can be used. In the present invention, a stirring speed at the time of the polymerization reaction of the water-soluble ethylenically unsaturated monomer, for example, the number of stirring revolutions, is adjusted, and therefore the average particle diameter of the primary particles obtained by the polymerization in reverse phase suspension of the first stage is controlled, with the result that it is possible to efficiently control the specific BET surface area of the second particles formed by the agglomeration of the primary particles. With the same type of blade stirring, the average particle diameter of the primary particles got more as the stirring speed is increased tends to be decreased.
[058] In the method of making a water-absorbent resin according to the present invention, it is possible to obtain a water-containing gel in the form of particles of moderate size, therefore it is possible to easily obtain a water-absorbent resin of fine grain in the form of moderately sized particles suitable for the preparation of an absorbent article. Post-cross-linking step
[059] Next, in the water-absorbent resin according to the present invention, post-crosslinking (post-crosslinking reaction) is preferably carried out with a post-crosslinking agent of a hydrated gel-like material having a structure cross-linked internal obtained by carrying out reverse phase suspension polymerization in the water-soluble ethylenically unsaturated monomer, as described above, in the presence of the internal cross-linking agent, and in the presence of an azo compound and a peroxide. Thus, after polymerization, the post-crosslinking reaction is carried out on the hydrogel which has an internal crosslinking structure, and thus it is possible to obtain a water-absorbent resin suitable particularly for applications of hygiene materials, in which a density of crosslinking in the vicinity of the water-absorbent resin surface is increased to improve various types of performance, such as a water-absorbing capacity under load, an absorption rate and a gel strength.
[060] Specifically, post-crosslinking agents can include, those compounds that have two or more reactive functional groups. They include, for example, polyols, such as ethylene glycol, propylene glycol, 1,4-butanediol, trimethylolpropane, glycerin, polyoxyethylene glycol, polyoxypropylene glycol, polyglycerin; polyglycidyl compounds, such as diglycidyl (poly) ethylene glycol ether, diglycidyl (poly) glycerin ether, triglycidyl (poly) glycerin ether, triglycidyl trimethylolpropane ether, polyglycidyl (poly) propylene glycol ether, (poly) glycerol ether polyglycidyl; haloepoxy compounds, such as epidorhydrin, epibromhydrin, o-methyl epidorhydrin; isocyanate compounds such as 2,4-tolylene diisocyanate, hexamethylene diisocyanate; oxetane compounds such as 3-methyl-3-oxethane methanol, 3-ethyl-3-oxethane methanol, 3-butyl-3-oxethane methanol, 3-methyl-3-oxethane ethanol, 3-ethyl-3-oxethane ethanol, 3-butyl-3-oxethane ethanol; oxazoline compounds, such as 1,2-ethylenebisoxazoline; carbonate compounds such as ethylene carbonate; hydroxyalkylamide compounds such as bis [N, N-di (β-hydroxyethyl)] - adipamide. Among these post-crosslinking agents, polyglycidyl compounds such as diglycidyl (poly) ethylene glycol ether, diglycidyl (poly) glycerol ether, triglycidyl (poly) glycerol ether, triglycidyl ether, trimethylolpropane ether, ( polyglycidyl poly) propylene glycol, polyglycidyl (poly) glycerol ether. These post-crosslinking agents can be used alone or in combination of two or more.
[061] The amount used of a post-crosslinking agent is preferably 0.00001 to 0.01 mol relative to 1 mol of the total amount of a water-soluble ethylenically unsaturated monomer used for the polymerization, more preferably 0.00005 to 0.005 mol and more preferably 0.0001 to 0.002 mol.
[062] As a method of adding a post-crosslinking agent, the post-crosslinking agent can be added as such or as an aqueous solution. A post-crosslinking agent can also be added as a solution in which a hydrophilic organic solvent is used as a solvent, if desired. Hydrophilic organic solvents include, for example, lower alcohols, such as methyl alcohol, ethyl alcohol, n-propyl alcohol, isopropyl alcohol; ketones, such as methyl acetone ethyl ketone; ethers, such as diethyl ether, dioxane, tetrahydrofuran; amides, such as N, N-dimethylformamide; sulfoxides, such as dimethyl sulfoxide. These hydrophilic organic solvents can be used alone or in combination of two or more, or they can be used as a solvent mixed with water.
[063] As for the time when a post-crosslinking agent is added, it can be added as long as the polymerization reaction of the water-soluble ethylenically unsaturated monomers has almost been completed, but it is preferably added in the presence of water in the range of 1 to 400 parts by weight with respect to 100 parts by weight of a water-soluble ethylenically unsaturated monomer, more preferably added in the presence of water in the range of 5 to 200 parts by mass, even more preferably added in the presence of water in the range 10 to 100 parts by mass and even more preferably added in the presence of water in the range of 20 to 60 parts by mass. Note that the amount of water means the total amount of water content in a polymerization system and a water content used, if desired, when adding a post-crosslinking agent.
[064] For the reaction temperature in the post-crosslinking reaction, which is preferably 50 to 250 ° C, more preferably 60 to 180 ° C, even more preferably 60 to 140 ° C and even more preferably 70 at 120 ° C. In addition, the reaction time of the post-crosslinking reaction is preferably 1 to 300 minutes, and more preferably 5 to 200 minutes. Drying step
[065] In the method of making a water-absorbent resin according to the present invention, a drying step of removing water, a means of dispersing hydrocarbons and the like using distillation by applying energy such as heat from the exterior after carrying out the aforementioned reverse phase suspension polymerization can be included. When dehydrating a hydrated gel after reverse phase suspension polymerization, a system in which the hydrated gel is dispersed in a hydrocarbon dispersion medium is heated to evaporate the water and temporarily the hydrocarbon dispersion medium of the system by azeotropic distillation medium. At this point, only the evaporated hydrocarbon dispersion medium is allowed to return to the system, allowing continuous azeotropic distillation. In that case, the temperature in the system during the drying treatment is maintained at, or below, the azeotropic temperature of the hydrocarbon dispersion medium. Therefore, this is preferred from the point of view that, for example, the resin is less susceptible to deterioration. Subsequently, the water and the hydrocarbon dispersion medium are removed by evaporation to obtain particles of a water-absorbent resin. By controlling the processing conditions of this drying step after polymerization to adjust the amount of dehydrated water, various properties of the resulting water-absorbent resin can be controlled.
[066] In the drying step, the drying treatment can be carried out by distillation under normal pressure or under reduced pressure. In addition, the drying treatment can be carried out under a flow of nitrogen gas and the like, in order to increase the drying efficiency. When carrying out the drying treatment under normal pressure, a drying temperature is preferably 70 to 250 ° C, more preferably 80 to 180 ° C, even more preferably 80 to 140 ° C and particularly preferably 90 to 130 ° C. In addition, when the drying treatment is carried out under reduced pressure, a drying temperature is preferably 40 to 160 ° C, more preferably 50 to 110 ° C.
[067] Note that in a case in which the post-crosslinking step is carried out with a post-crosslinking amount after monomers are polymerized by reverse phase suspension polymerization as described above, the drying step is carried out by means of distillation process, as described above, after completion of the post-cross-linking step. Alternatively, the post-crosslinking step and the drying step can be carried out simultaneously.
[068] In addition, if desired, various additives, such as chelating agents, reducing agents, oxidizing agents, antibacterial agents, deodorizing agents can be added to a water-absorbing resin after the polymerization step during or after the drying step. 2. Water absorbent resin
[069] The water-absorbent resin according to the present invention will now be described. For example, the water-absorbent resin according to the present invention can be obtained by the method described above. Specifically, it can be obtained by carrying out the polymerization while adjusting the amount of internal cross-linking agent used at the time of the first stage polymerization, its specific BET surface area is controlled to fall within a suitable range and an absorbent article using the resin water absorber has excellent water absorption capacity.
[070] Specifically, the water-absorbent resin according to the present invention is a water-absorbent resin that can be obtained by polymerizing an ethylenically unsaturated water-soluble monomer in the presence of an internal cross-linking agent, the absorption rate of water in the physiological saline solution is 40 to 80 seconds, the mass percentage of the particles of 150-850 pm in all the water absorbent resin is 85% by mass or more, the mass proportion of the particles of 300-400 pm is 20% by mass or more and the specific BET surface area of the particles that are classified as 300 to 400 pm and that is measured is less than 0.03 m2 / g.
[071] The "water absorption rate" of the water-absorbent resin is a property that affects the properties required for such an absorbent material, when the absorbent material is formed by the combination of water-absorbent resin and a hydrophilic fiber, and, for example, there is a tendency that the water absorption rate is suitably decreased to have an excellent diffusion property over the entire absorbent material of a liquid to be absorbed. The water absorption rate of the water-absorbent resin can be measured based on the following method as the water absorption rate of a physiological saline solution.
[072] Specifically, the measurement of the water absorption rate is performed as follows. As described later in the Examples, in a room conditioned at 25 ± 1 ° C, 50 ± 0.1 g of saline adjusted to a temperature of 25 ± 0.2 ° C in a constant temperature water tank is stirred with a magnetic stir bar (8 mm ψ x 30 mm without a ring) at 600 rpm to produce vortex products, 2.0 ± 0.002 g of a water absorbent resin which is a measurement of the sample is added to the saline solution physiological at the same time and the time (in seconds) during which after the addition of water-absorbing resin, the vortex is made to disappear and the liquid's surface becomes flat is measured, with the result that time can be assumed to be the water absorption rate of the water absorbent resin.
[073] In the water-absorbent resin according to the present invention, the water absorption rate of a physiological saline solution is 40 to 80 seconds. The water absorption rate of a physiological saline solution is preferably 42 seconds or more and is more preferably 45 seconds or more, because when the water-absorbent resin is used for an absorbent material, the absorbent material has a satisfactory property diffusion.
[074] In the water-absorbent resin according to the present invention, the mass proportion of the particles of 150-850 pm in the entire water-absorbent resin is 85% or more, and such a particle size distribution is provided that the particle mass ratio of 300 to 400 pm is 20% or more.
[075] Regarding the particle size distribution of the water-absorbent resin, the mass proportion of the particles of 150-850 pm in the entire water-absorbent resin is 85% by mass or more, and more preferably 90% in bulk or more. In addition, the weight ratio of the particles from 300 to 400 pm in all the water-absorbent resin is 20% by weight or more, more preferably 25% by weight or more and even more preferably 30% by weight or more.
[076] In the water-absorbent resin according to the present invention, the average particle diameter is preferably 200 to 600 pm, more preferably 200 to 500 pm and even more preferably 250-450 pm.
[077] The water-absorbent resin is not limited to a water-absorbent resin formed with secondary particles only in which the primary particles are agglomerated and the water-absorbent resin can contain individual particles (primary particles). Examples of the primary particle shape include a substantially spherical shape, a pulverized irregular shape and a plate shape. When primary particles are manufactured by reverse phase suspension polymerization, a single substantially spherical particle shape that has a smooth surface shape, such as a spherical shape or an oval spherical shape is present, and in which the primary particles of such shape, the shape of the surface is smooth, so the fluidity in powder form is improved and the agglomerated particles are not susceptible to breaking, even when a shock is received because the agglomerated particles are densely packed with primary particles, with the result of that water-absorbent resin that has a high particle resistance is achieved.
[078] In the water-absorbent resin according to the present invention, the specific BET surface area of the particles that are classified in 300 to 400 pm and that is measured is less than 0.03 m2 / g. The specific BET surface area is preferably 0.028 m2 / g or less, and more preferably 0.026 rrP / g or less. The BET specific surface area is preferably 0.010 rrf / g or more. The specific BET surface area is made to fall within such a range, and thus, it is possible to improve its water absorption performance when it is used for an absorbent article.
[079] As described later in the Examples, in the measurement of the specific BET surface area, the specific BET surface area can be determined as follows. The water-absorbent resin that is passed through a 400 pm opening sieve that is adjusted to particle diameters maintained in a 300 pm opening sieve is used, this sample is dried under conditions of exhaust from thermal vacuum degassing at 100 ° C for 16 hours, followed by a method in which a specific surface area measuring device (manufactured by Quantachrome Co. Ltd., Autosorb-1) is used and the krypton gas is used as an adsorption gas, an isothermal of adsorption is measured at a temperature of 77 K and specific BET surface area can be determined from a multipoint BET graph.
[080] When the specific BET surface area of a water-absorbing agent obtained by mixing an additive, such as a fine powder inorganic to the water-absorbing resin is measured, if the specific BET surface area of the additive adhered to the resin surface water absorber is extremely large, it may therefore be likely to obtain such a measured value that the water absorbent agent has a large specific surface area. Thus, in order to measure <the specific BET surface area of the water-absorbing resin> described in the present specification, it is desirable to measure the water-absorbent resin before adding the additive or to measure, in the case of the water-absorbing agent, the resin water absorber after removing additive adhered to the surface by washing.
[081] In the water-absorbent resin according to the present invention, the water-holding capacity of the physiological saline solution is preferably 30 g / g or more. The water-holding capacity of physiological saline refers to the mass of physiological saline that can be absorbed by the water-absorbent resin per unit mass, and indicates the degree of the liquid-absorbing capacity of the water-absorbing resin. The water retention capacity of the physiological saline solution is, more preferably 35 g / g or more, and even more preferably 40 g / g or more. The upper limit value of the water-holding capacity of physiological saline solution is preferably 60 g / g or less.
[082] In the water-absorbent resin according to the present invention, the water-absorbing capacity of a physiological saline solution under a load of 4.14 kPa is preferably 16 ml / g or more, more preferably 18 ml / g or more and even more preferably 20 ml / g or more. The upper limit of the water-absorbing capacity of a physiological saline solution under a load of 4.14 kPa is preferably 50 ml / g or less.
[083] The water retention capacity of the physiological saline solution, the water absorption capacity of a physiological saline solution under a load of 4.41 kPa, the water absorption rate of a physiological saline solution, the average diameter of particle and specific BET surface area in the water-absorbent resin described above can be measured in a measurement method described later in the Examples.
[084] In order to give various types of performance to the obtained water-absorbent resin, an additive corresponding to the purpose is mixed, with the result that it is possible to use it as a water-absorbing agent. Examples of such additives include a fine inorganic powder, a surfactant, an oxidizing agent, a reducing agent, a metal chelating agent, a radical chain inhibitor, an antioxidant, an antibacterial agent and a deodorant. For example, 0.05 to 5 parts by weight of a fine inorganic powder are added to 100 parts by weight of water-absorbing resin, and thus it is possible to obtain a water-absorbing agent whose fluidity is increased. Examples of the fine inorganic powder include hydrophilic silica, hydrophobic silica, talc, zeolite powder and aluminum oxide. 3. Absorbent material and absorbent article
[085] The water-absorbent resin according to the present invention forms, for example, the absorbent material used for hygiene materials, such as sanitary articles and disposable diapers, and is preferably used for an absorbent article that includes the absorbent material.
[086] Here, an absorbent material, in which a water-absorbent resin is used comprises, for example, water-absorbent resin and a hydrophilic fiber. The structures of the absorbent material include a dispersion mixture obtained by mixing a water-absorbent resin and a hydrophilic fiber to provide a uniform composition, a sandwich structure in which a water-absorbent resin is sandwiched between the layered hydrophilic fibers, a structure in which a water-absorbent resin and a hydrophilic fiber is wrapped in fabric and the like. It is noted that other components, for example, adhesive binder, such as synthetic adhesive thermal fibers, hot melt adhesives, adhesive emulsions to increase the retention capacity of the form of an absorbent material can be included in the absorbent material.
[087] For the content of a water-absorbent resin in an absorbent material, it is preferably 5 to 95% by mass, more preferably 20 to 90% by mass and even more preferably 30 to 80% by mass. When the content of a water-absorbent resin is less than 5% by mass, the absorption capacity of an absorbent material can be reduced, resulting in leakage and re-wetting of a liquid. On the other hand, when the content of a water-absorbent resin is greater than 95% by mass, the cost of an absorbent material increases, and the feel of the absorbent material becomes harder.
[088] Hydrophilic fibers include cellulose fibers, such as cotton-like pulp obtained from wood, mechanical pulp, chemical pulp, semi-chemical pulp; artificial cellulose fibers, such as rayon and ethyl; comprising synthetic resin fibers such as hydrophilized polyamide, polyester, and polyolefin.
[089] In addition, an absorbent material in which a water-absorbent resin is used can be kept between a liquid-permeable sheet (top sheet) through which a liquid can permeate and a liquid-impermeable sheet (back sheet), through which a liquid cannot permeate to give an absorbent article. The liquid-permeable sheet is arranged on the side to be in contact with the body, while the liquid-impermeable sheet is arranged opposite to the side to be in contact with the body.
[090] Liquid-permeable sheets include non-woven sheets and porous sheets of synthetic air-type resin through, a type of extension, a type of chemical bond, a type of needle punch and the like comprising fibers, such as polyethylene, polypropylene , polyester and the like. In addition, liquid impervious sheets include synthetic resin films comprising a resin, such as polyethylene, polypropylene, polyvinyl chloride and the like. EXAMPLES 4. Example
[091] Hereinafter, the present invention will be described in detail with reference to Examples and Comparative Examples. However, the present invention should in no way be limited to the following Examples and the like.4-1. Evaluation test method [Evaluation test for water-absorbent resin]
[092] Water-absorbent resins obtained from Examples 1 to 7 and Comparative Examples 1 to 4 below have been subjected to several tests described below for evaluation. In the following, each evaluation test method will be described. (1) Capacity for retaining physiological saline water
[093] A cotton bag (Men Broad N ° 60, horizontal 100 mm x vertical 200 mm), in which 2.0 g of a water-absorbent resin was weighed, was placed inside a beaker of 500 ml capacity. 500 g of 0.9% by weight aqueous sodium chloride solution (physiological saline) was poured into the cotton bag, including the water-absorbing resin, at once, so as not to produce a lump, and the upper portion of the cotton bag was tied with a rubber band and was left standing for 30 minutes, with the result that the water-absorbent resin was swollen. The cotton bag after 30 minutes was dehydrated for one minute with a dehydrator (made by Kokusan Centrifuge Co., Ltd., product number: H-122) which was established with a centrifugal force that was 167 L, and the Wa (g) mass of the cotton bag containing the dehydrated swollen gel was measured. The same operation was performed without the addition of water-absorbent resin, the empty mass Wb (g) of the wet cotton bag was measured and the water retention capacity of the physiological saline solution was calculated from the formula below.
[094] Water retention capacity of physiological saline solution (g / g) = [Wa - WB] (g) / water absorbent resin mass (g) (2) Water absorption capacity of a physiological saline solution under a load of 4.14 kPa
[095] A water-absorbing capacity of a physiological saline solution under a 4.14 kPa load of a water-absorbing resin was measured using an X measuring device. A schematic arrangement of the X measuring device is shown in Fig. 1.
[096] The measuring device X shown in Fig. 1 comprises a burette part 1, a conduit 2, a measurement stage 3, a measurement part 4 placed in measurement step 3. In the burette part 1, a plug rubber 14 is attached to the top of a burette 10, and an air inlet tube 11 and a valve 12 are attached to the bottom of burette 10. In addition, a valve 13 is attached to the top of the burette tube air 11. Conduit 2 connects burette part 1 and measurement stage 3. The diameter of conduit 2 is 6 mm. Measurement step 3 has a hole with a diameter of 2 mm in the center, to which conduit 2 is connected. The measuring part 4 is provided with a cylinder 40 and a nylon mesh 41 patched at the bottom of the cylinder 40, as well as a weight 42. The internal diameter of the cylinder 40 is 2.0 cm. The nylon mesh 41 is formed as a 200 mesh (75 pm openings). Furthermore, it is configured in such a way that a predetermined amount of a water-absorbent resin 5 is evenly distributed over the nylon mesh 41. The weight 42 has a diameter of 1.9 cm and a mass of 119.6 g. The weight 42 must be placed on the water absorbent resin of 5 to uniformly apply a load of 4.14 kPa to the water absorbent resin 5.
[097] Using the measuring device X having a structure as described above, firstly, valve 12 and valve 13 on burette part 1 were closed, and then the physiological saline solution adjusted to 25 ° C, was inserted into the burette 10 from the top. Subsequently, the upper part of the burette was covered with rubber plug 14, and then valve 12 and valve 13 on burette part 1 were opened. Then, the height of the measuring stage 3 was adjusted so that the tip of the conduit 2 in the center of the measuring stage 3 is flush with the air inlet of the air inlet tube 11.
[098] Meanwhile, 0.10 g of the water-absorbent resin 5 was evenly distributed over the nylon mesh 41 on the cylinder 40, and then the weight 42 was placed on the water-absorbent resin 5. The measuring part 4 it was arranged so that its center coincides with the conduit entry at the center of measurement stage 3.
[099] The amount of physiological saline solution reduced in the burette 10 (the amount of physiological saline solution absorbed by the water-absorbent resin 5) WC (ml_) was measured continuously from the moment the water-absorbent resin 5 started to absorb Water. At a time of 60 minutes from the beginning of the water absorption, a water-absorbing capacity of a physiological saline solution under a load of 4.14 kPa of the water-absorbing resin was calculated by the following formula.
[0100] Water absorption capacity of a physiological saline solution under a load of 4.14 kPa (ml / g) = CC / 0.10 (g) (3) Water absorption rate of a physiological saline solution
[0101] The water absorption rate of a physiological saline solution was measured inside a room whose temperature was adjusted to 25 ± 1C. 50 ± 0.1 g of physiological saline adjusted to 25 ± 0.2 ° C in a constant temperature water tank was stirred with a magnetic stir bar (8 mm ψ x 30 mm without a ring) at 600 rpm to produce vortex. 2.0 ± 0.002 g of a water-absorbent resin that was obtained was added to the physiological saline solution in one go and the time (in seconds) during which, after adding water-absorbing resin, the vortex was made at disappear and the liquid surface became flat was measured, with the result that time was assumed to be the water absorption rate of a physiological saline solution of the water absorbent resin. (5) Average particle diameter (particle size distribution)
[0102] 50 g of a water-absorbent resin, 0.25 g of amorphous silica (manufactured by Degussa Evonik Japan, Inc., Carplex # 80) was mixed as a lubricant.
[0103] Standard JIS sieves are combined in the following order from the top: an 850 pm opening sieve, a 600 pm opening sieve, a 500 pm opening sieve, a 400 pm opening sieve, a 400 sieve sieve 300 pm openings, a 250 pm openings screen, a 150 pm openings screen and a receiving tray.
[0104] The water-absorbent resin was introduced on top of the combined sieves, and then stirred for 20 minutes, using a low-touch shaker for grading. After classification, the mass of water-absorbent resin that remained in each sieve was calculated as a percentage by mass relative to the total mass to obtain a particle size distribution. When integrating the quantity in each sieve that has the largest particle diameter in this particle size distribution, the relationship between the sieve openings and the integrated value of the percentage of water absorbent resin mass that remained in the sieves was represented graphically in logarithmic probability role. When connecting the graphical representations on the probability paper with a straight line, a particle diameter corresponding to 50% of the mass in the integrated mass percentage is taken as the average particle diameter.
[0105] The proportion of the water-absorbing resin that has a particle diameter of 300 to 400 pm is the proportion of the water-absorbing resin that remains in the 300 pm aperture sieve, and likewise, the proportion of the water-absorbing resin water having a particle diameter of 150 to 850 pm is a value that is obtained by adding all the proportions of the water-absorbing resin left in the sieves of 150 pm, 250 pm, 300 pm, 400 pm, 500 pm and 600 pm. (6) BET specific surface area
[0106] The water-absorbing resin whose particle diameters were adjusted to be passed through a 400 pm opening sieve and to be kept in a 300 pm opening sieve was used for the measurement of the specific surface area. Then, 10 g of the classified sample was dispersed in 100 g of ethanol, washed with an ultrasound cleaning machine (made by SND Co., Ltd., R-103) for 5 minutes and then filtered through a sieve. 300 pm openings. Then, the same washing operation was performed twice, with the result that a measuring sample subjected to washing three times in total was obtained. This sample was dried under thermal vacuum exhaust degassing conditions at 100 ° C for 16 hours. Then, by a method in which a specific surface area measuring device (manufactured by Quantachrome Co. Ltd., Autosorb-1) was used, and the krypton gas was used as an adsorption gas, an adsorption isotherm was measured at a temperature of 77 K and the specific surface area was determined from a BET multipoint graph, with the result that the specific surface area determined was assumed to be the specific BET surface area. 4-2. Examples and Comparative Example [Example 1]
[0107] In Example 1, a separate 2 L cylindrical round-bottom flask with an internal diameter of 110 mm was prepared, which was equipped with a reflux condenser, a drip funnel, a tube for introducing nitrogen gas and stirrer with stirring paddles composed of two sets of 4 blades of inclined blades with a blade diameter of 50 mm. To this flask, 300 g of n-heptane was introduced as a hydrocarbon dispersion medium, 0.74 g of HLB3 sucrose stearic acid ester (manufactured by Mitsubishi-Kagaku Foods Corporation, Ryoto S-370 sugar ester) was added as a surfactant and 0.74 g of maleic anhydride modified ethylene-propylene copolymer (manufactured by Mitsui Chemicals, Inc., high wax 1105A) was added as a polymeric dispersing agent, and heated to 80 ° C comagitation, and a surfactant was dissolved, and then cooled to 50 ° C.
[0108] Meanwhile, 92 g (1.02 mol) of 80% by weight aqueous acrylic acid was introduced into a 500 ml Erlenmeyer flask, and 102.2 g of 30% by weight aqueous sodium hydroxide was added dropwise while cooling from the outside to neutralize 75 mol%. Subsequently, 0.092 g of hydroxyethyl cellulose (made by Sumitomo Seika Chemicals Co., Ltd., HEC AW-15F) as a thickener, 0.092 g (0.339 mmol) of 2,2'-azobis (2-amidinopropane) as a compound azo base, 0.037 g (0.137 mmol) of potassium persulfate as a peroxide, 0.0102 g (0.058 mmol) of diglycidyl ethylene glycol ether as an internal crosslinking agent and 43.8 g of water were added and dissolved to prepare a first step aqueous monomer solution.
[0109] Then the number of stirring revolutions was set to 550 rpm, and the aqueous monomer solution prepared as described above was added to a separate flask, and the atmosphere in the system was completely replaced with nitrogen. Then, the flask was immersed in a 70 ° C water bath to raise the temperature, and the polymerization was carried out for 60 minutes to obtain a first stage polymerized suspension.
[0110] Meanwhile, 128.8 g (1.43 mol) of 80% by weight aqueous acrylic acid was introduced into another 500 ml Erlenmeyer flask, and 143.1 g of 30% by weight aqueous sodium hydroxide was added dropwise while cooling from the outside to neutralize 75 mol%. Subsequently, 0.129 g (0.475 mmol) of 2,2'-azobis (2-amidinopropane) as an azo-based compound, 0.052 g (0.191 mmol) of potassium persulfate as a peroxide, 0.0116 g (0.067 mmol) diglycidyl ether ethylene glycol as an internal crosslinking agent and 15.9 g of water were added and dissolved to prepare a second step aqueous monomer solution.
[0111] After the number of revolutions of rotation of the polymerized suspension was changed to 1000 rpm and then the system was cooled in the separable flask mentioned above at 25 ° C, the entire aqueous second step monomer solution was added to the polymerization in suspension from the first stage, and the atmosphere in the system was completely replaced by nitrogen. Subsequently, the flask was again immersed in a 70 ° C water bath to raise the temperature, and a second stage polymerization was carried out for 30 minutes.
[0112] After the second stage polymerization, the reaction liquid was heated to 125 ° C in an oil bath, and 241 g of water was removed from the system by refluxing n-heptane in azeotropic distillation of n-heptane and water. Then, 4.42 g (0.507 mmol) of 2% by weight aqueous solution of diglycidyl ethylene glycol ether was added as a post-crosslinking agent, and maintained at 80 ° C for 2 hours. Subsequently, the drying step was carried out by evaporating n-heptane, and then a dry resin was obtained. The dried resin was allowed to pass through a sieve with 1000 µm openings to obtain 233.4 g of a water-absorbent resin in the form of second particles, in which the spherical primary particles were agglomerated. The water-absorbent resin obtained in this way was evaluated according to the various test methods as described above.
[0113] It is noted that for the water-absorbing resin obtained, the mass ratio of particles from 150 to 850 pm particles to the entire proportion was 98.2% by mass, and the mass ratio of particles to 300 at 400 pm particles was 39.4% by weight. [Example 2]
[0114] In Example 2, the same operation as in Example 1 was performed, except that 6.62 g (0.761 mmol) of 2% by weight aqueous solution of diglycidyl ethylene glycol ether added as a post-crosslinking agent was changed , with the result that 232.9 g of a water-absorbent resin in the form of secondary particles, in which the spherical primary particles were agglomerated. The water-absorbent resin obtained in this way was evaluated according to the various test methods as described above.
[0115] It is noted that for the obtained water-absorbent resin, the proportion of masses in the 150 to 850 pm particles in relation to the whole proportion was 97.8% by mass, and the mass proportion of particles from 300 to 400 pm particles was 36.5% by weight. [Example 3]
[0116] In Example 3, the same operation as in Example 1 was performed except that, as the internal crosslinking agent added to the monomer from the first step, the diglycidyl ethylene glycol ether was changed to 0.0202 g (0.116 mmol), that the number of stirring revolutions was adjusted to 500 rpm and that the polymerization of the first stage was carried out, with the result that 231.0 g of a water-absorbent resin was obtained in the form of secondary particles in which the spherical primary particles were agglomerated, it was obtained. The water-absorbent resin obtained in this way was evaluated according to the various test methods as described above.
[0117] It is noted that for the water absorbent resin obtained, the mass proportion of particles from 150 to 850 pm particles in relation to the entire proportion was 90.7% by mass, and the mass proportion of particles of 300 at 400 pm particles was 24.2% by weight. [Example 4]
[0118] In Example 4, the same operation as in Example 1 was performed except that, as the internal crosslinking agent added to the monomer of the first step, the diglycidyl ethylene glycol ether was changed to 0.0202 g (0.116 mmol), with the result that 232.1 g of a water-absorbent resin in the form of secondary particles, in which the spherical primary particles were agglomerated, was obtained. The water-absorbent resin obtained in this way was evaluated according to the various test methods as described above.
[0119] Note that for the water-absorbent resin obtained, the mass proportion of particles from 150 to 850 pm particles in relation to the entire proportion was 97.9% by mass, and the mass proportion of particles from 300 to 400 pm particles was 32.6% by mass. [Example 5]
[0120] In Example 5, the same operation as in Example 1 was performed, except that the type of internal cross-linking agent was changed to diglycidyl polyethylene glycol ether (made by Nagase Chemtex Corporation, EXO-861), than polyethylene diglycidyl ether -glycol added to the monomer of the first step was changed to 0.0405 g (0.0369 mmol) and that the polyethylene glycol diglycidyl ether added to the monomer of the second step was changed to 0.0116 g (0.0106 mmol), with the result that 233.8 g of a water-absorbent resin in the form of secondary particles, in which the spherical primary particles were agglomerated, was obtained. The water-absorbent resin obtained in this way was evaluated according to the various test methods as described above.
[0121] Note that for the water-absorbing resin obtained, the mass proportion of particles from 150 to 850 pm particles in relation to the entire proportion was 95.8% by mass, and the mass proportion of particles of 300 to 400 pm particles was 31.3% by weight. [Example 6]
[0122] In Example 6, the same operation as in Example 5 was performed, except that as the internal crosslinking agent added to the monomer of the first step, the polyethylene glycol diglycidyl ether (made by Nagase Chemtex Corporation, EX-861) changed to 0.0810 g (0.0737 mmol), with the result that 232.9 g of a water-absorbent resin in the form of secondary particles, in which the spherical primary particles were agglomerated, was obtained. The water-absorbent resin obtained in this way was evaluated according to the various test methods as described above.
[0123] It is noted that for the water-absorbing resin obtained, the mass proportion of particles from 150 to 850 pm particles in relation to the entire proportion was 95.8% by mass, and the mass proportion of particles of 300 to 400 pm particles were 25.5% by weight. [Example 7]
[0124] In Example 7, the same operation as in Example 5 was performed, except as the internal crosslinking agent added to the monomer of the first step, polyethylene glycol diglycidyl ether (made by Nagase Chemtex Corporation, EX-861) to 0.0639 g (0.0581 mmol), that the number of rotations of the stirring was fixed at 650 rpm and that the polymerization of the first stage was carried out with the result that 231.7 g of a water-absorbent resin in the form of secondary particles, in which the spherical primary particles were agglomerated, was obtained. The water-absorbent resin obtained in this way was evaluated according to the various test methods as described above.
[0125] Note that for the water-absorbing resin obtained, the mass proportion of particles from 150 to 850 pm particles in relation to the entire proportion was 94.5% by mass, and the mass proportion of particles of 300 to 400 pm particles were 29.8% by weight. [Comparative Example 1]
[0126] In Comparative Example 1, reverse phase suspension polymerization was performed using only one peroxide, and thus a water-absorbent resin was produced.
[0127] Specifically, a separate 2 L cylindrical round-bottom flask with an internal diameter of 110 mm was prepared, which was equipped with a reflux condenser, a drip funnel, a tube for introducing nitrogen gas and a stirrer with stirring paddles comprised of two sets of 4 blades of inclined blades with a blade diameter of 50 mm. To this flask, 300 g of n-heptane was introduced as a hydrocarbon dispersion medium, 0.74 g of HLB3 sucrose stearic acid ester (manufactured by Mitsubishi-Kagaku Foods Corporation, Ryoto S-370 sugar ester) was added as a surfactant and 0.74 g of maleic anhydride modified ethylene-propylene copolymer (manufactured by Mitsui Chemicals, Inc., high wax 1105A) was added as a polymeric dispersing agent, and heated to 80 ° C with stirring, and a surfactant was dissolved, and then cooled to 50 ° C.
[0128] Meanwhile, 92 g (1.02 mol) of 80% by weight aqueous acrylic acid was introduced into a 500 ml Erlenmeyer flask, and 102.2 g of 30% by weight aqueous sodium hydroxide was added , drop by drop, while cooling from the outside to perform 75 mol% neutralization. Subsequently, 0.092 g of hydroxylethyl cellulose (manufactured by Sumitomo Seika Chemicals Co., Ltd., HEC AW-15F) as a thickener, 0.074 g (0.274 mmol) of potassium persulfate, 0.0184 g (0.106 mmol) of ether diglycidyl ethylene glycol as an internal crosslinking agent and 43.8 g of ion exchange water were added and dissolved to prepare an aqueous first step monomer solution.
[0129] Next, the number of stirring revolutions was adjusted to 500 rpm, and the aqueous monomer solution prepared as described above was added to a separate flask, and the atmosphere in the system was completely replaced by nitrogen with stirring. Then, the flask was immersed in a 70 ° C water bath to raise the increased temperature, and the polymerization was carried out for 60 minutes to obtain a first stage polymerized suspension.
[0130] Meanwhile, 128.8 g (1.43 mol) of 80% by weight aqueous acrylic acid was introduced into another 500 ml Erlenmeyer flask, and 143.1 g of 30% by weight aqueous sodium hydroxide was added dropwise while cooling from the outside to neutralize 75 mol%. Then 0.104 g (0.382 mmol) of potassium persulfate, 0.0129 g (0.074 mmol) of ethylene glycol glycol ether as an internal cross-linking agent and 15.9 g of ion exchange water were added and dissolved to prepare an aqueous second step monomer solution.
[0131] After the number of revolutions of rotation of the polymerized suspension was changed to 1000 rpm and then the system was cooled in the separable flask mentioned above to 25 ° C, the entire aqueous second step monomer solution was added to the polymerization in suspension from the first stage, and the atmosphere in the system was completely replaced by nitrogen. Subsequently, the flask was again immersed in a 70 ° C water bath to raise the temperature, and a second stage polymerization was carried out for 30 minutes.
[0132] After the second stage polymerization, the reaction liquid was heated to 125 ° C in an oil bath, and 261 g of water was removed from the system by refluxing n-heptane in azeotropic distillation of n-heptane and water. Then, 4.42 g (0.507 mmol) of 2% by weight aqueous solution of diglycidyl ethylene glycol ether was added as a post-crosslinking agent, and maintained at 80 ° C for 2 hours. Subsequently, the drying step was carried out by evaporating n-heptane to obtain a dry resin. The dry resin was allowed to pass through a sieve with 1000 µm openings to obtain 234.5 g of a water-absorbent resin in the form of agglomerated spherical particles. The water-absorbent resin obtained in this way was evaluated according to the various test methods as described above.
[0133] Note that for the water-absorbing resin obtained, the mass proportion of particles from 150 to 850 pm particles in relation to the entire proportion was 98.1% by mass, and the mass proportion of particles of 300 to 400 pm particles was 36.9% by weight. [Comparative Example 2]
[0134] In Comparative Example 2, the same operation as in Comparative Example 1 was performed, except that as the internal crosslinking agent added to the monomer of the first step, the diglycidyl ethylene glycol ether was changed to 0.0156 g (0.090 mmol) , that, as the internal crosslinking agent added to the monomer of the second step, the diglycidyl ethylene glycol ether was changed to 0.0155 g (0.089 mmol) and that 6.62 g (0.761 mmol) of 2% by weight aqueous solution of diglycidyl ethylene glycol ether added as a post-crosslinking agent was changed, with the result that 233.6 g of a water-absorbent resin in the form of secondary particles, in which the spherical primary particles were agglomerated, was obtained. The water-absorbent resin obtained in this way was evaluated according to the various test methods as described above.
[0135] It is noted that for the water-absorbing resin obtained, the mass proportion of particles from 150 to 850 pm particles in relation to the entire proportion was 93.9% in mass, and the mass proportion of particles from 300 to 400 pm particles was 34.7% by weight. [Comparative Example 3]
[0136] In Comparative Example 3, as the internal crosslinking agent added to the monomer from the first step, diglycidyl ethylene glycol ether was changed to 0.0101 g (0.058 mmol), the number of rotations of the agitation was fixed at 500 rpm and the polymerization of the first stage was carried out. Then, the same operation as in Comparative Example 1 was performed, except that as the internal crosslinking agent added to the monomer of the second step, the ethylene glycol diglycidyl ether was changed to 0.0116 g (0.067 mmol), with the result of that 231.8 g of a water-absorbent resin in the form of secondary particles, in which the spherical primary particles were agglomerated, was obtained. The water-absorbent resin obtained in this way was evaluated according to the various test methods as described above.
[0137] It is noted that for the water-absorbing resin obtained, the mass proportion of particles from 150 to 850 pm particles in relation to the entire proportion was 98.0 mass%, and the mass proportion of particles 300 at 400 pm particles was 40.7% by weight. [Comparative Example 4]
[0138] In Comparative Example 4, the same operation as in Example 2 was performed, except that as the internal crosslinking agent added to the monomer of the first step, the diglycidyl ethylene glycol ether was changed to 0.0276 g (0.1584 mmol ), that the number of stirring revolutions was fixed at 500 rpm and that the polymerization of the first stage was carried out, with the result that 232.9 g of a water-absorbent resin in the form of secondary particles, in which the primary particles spherical were clustered, it was obtained. The water-absorbent resin obtained in this way was evaluated according to the various test methods as described above.
[0139] It is noted that for the water-absorbing resin obtained, the mass proportion of particles from 150 to 850 pm particles in relation to the entire proportion was 97.2% in mass, and the mass proportion of particles from 300 to 400 pm particles was 36.4% by weight. 4-3. Evaluation results
[0140] [Results of the evaluation of water-absorbent resin]
[0141] The results of the evaluation of water-absorbent resins obtained in Examples 1 to 7 and Comparative Examples 1 to 4 are shown in Table 1 below. The polymerization conditions are also shown in Table 1. [Table 1]

[0142] As found from table 1, in the method of manufacturing the water-absorbent resin according to Examples 1 to 7, the water-absorbent resin, whose specific BET surface area was controlled was obtained.
[0143] [Results of the evaluation test of absorbent material and absorbent article with water-absorbent resin]
[0144] Then, the absorbent material and absorbent articles were produced using the water absorbent resins obtained in Examples 1, 2, 4 and 6 and Comparative Examples 1, 3 and 4 in the methods described below and were evaluated. (2) Production of absorbent material and absorbent article [Example 8]
[0145] 12 g of the water-absorbent resin obtained in Example 1 and 12 g of crushed pulp (made by Rayonier, Inc. Rayfloc) were used, and were uniformly mixed by papermaking by air, with the result that one core of sheet-shaped absorbent material having a size of 40 cm to 12 cm x was produced. Then, while the top and bottom parts of the absorbent core were being sandwiched between two sheets of tissue paper of equal size to the core of absorbent material and having a base weight of 16 g / m2, a load of 196 kPa was pressed on for 30 seconds, with the result that an absorbent material has been produced. In addition, on the upper surface of the absorbent material, a permeable sheet of porous liquid of the type of polyethylene-polypropylene air passage of the same size as the core of absorbent material and having a base weight of 22 g / m2 was arranged, and a liquid-impermeable sheet of polyethylene having the same size and the same base weight as the liquid-permeable sheet was laid out on the bottom surface, and so the absorbent material was glued, with the result that an absorbent article on which the weight of the base of the water-absorbent type resin was 250 g / m2 and the base weight of the hydrophilic fiber was 250 g / m2 was formed. [Examples 9 to 11 and Comparative Examples 5 to 7]
[0146] In Examples 9 to 11 and Comparative Examples 5 to 7, the same operation as in Example 8 was performed except that, instead of the water-absorbing resin obtained in Example 1, the water-absorbing resins obtained in Examples 2 , 4 and 6 and Comparative Examples 1, 3 and 4 were used, with the result that absorbent articles were obtained. The absorbent articles obtained were assumed, respectively, to be the absorbent articles in Examples 9,10 and 11 and Comparative Examples 5, 6 and 7. (3) Preparation of the test liquid
[0147] As a test liquid, NaCI, CaCI2 and MgSO4 were mixed in the ion exchange water such that NaCI was 0.780% by mass, CaCI2 was 0.022% by mass and MgSO4 was 0.038% by mass, and were dissolved and, in addition, a small amount of Blue No. 1 was mixed. In this way, the test liquid was prepared. (4) Permeation time
[0148] The absorbent article was first placed on a horizontal stage. In the central portion of the absorbent article, a measuring device incorporating a liquid spill cylinder having an inner diameter of 3 cm was placed, and 80 mL of test liquid was poured into the cylinder at a time and a stopwatch was used to measure the time until the test liquid was made to disappear completely, with the result that the time was assumed to be the first permeation time (in seconds).
[0149] Then, the cylinder described above was removed, the absorbent article was stored in its current state and both when 30 minutes had passed and when 60 minutes had elapsed since the beginning of the first round of leakage of the test liquid, the measurement was used in the position as in the first phase, and the same operation was performed, with the result that the second and third permeation times (in seconds) were measured.
[0150] The total time from the first to the third cycles was assumed to be the total permeation time. It is said that as the permeation time is shorter, the absorbent article was more preferable. (5) Remolled quantity
[0151] 120 minutes after the state of the first round of the pouring of the test liquid in the measurement of the permeation time described above, in the vicinity of the position of the absorbent article where the test liquid was poured, the 10 cm square filter paper whose mass (Wd (g), about 50 g) was measured previously, and in it, a weight having a bottom surface of 10 cm x 10 cm and a mass of 5 kg was placed. The load was placed for 5 minutes, and the mass (We (g)) of the filter paper was measured, with the result that the increased mass was assumed to be the amount of wipe (g). It is said that as the amount of resurfacing was decreased, the absorbent article was more preferable. Amount of resurfacing (g) = We - Wd (6) Diffusion length
[0152] Within 5 minutes after measuring the amount of wipe described above, the dimension (cm) of propagation of the absorbent article in the longitudinal direction into which the test liquid is penetrated has been measured. Values after the decimal point have been rounded.
[0153] [Evaluation of the results of the absorbent article]
[0154] Next, in Table 2 below, the results of the evaluation of the absorbent articles obtained in Examples 8 to 11 and Comparative Examples 5 to 7 are shown. [Table 2]

[0155] As shown in Table 2, in comparison with the Comparative Examples, in absorbent articles using water-absorbent resins having specific BET surface area and the appropriate water absorption rate in the Examples, the permeation time performances and the amount of wipes were excellent. EXPLANATION OF REFERENCE NUMBERSX measuring device1 part of burette2 conduit3 measurement stage4 measurement part5 water-absorbing resin

权利要求:
Claims (7)
[0001]
1. A method of making a water-absorbent resin comprising carrying out polymerization in two-phase or more reverse phase suspension polymerization in an ethylenically unsaturated water-soluble monomer in a hydrocarbon dispersion medium in the presence of at least one azo compound, a peroxide and an internal cross-linking agent in each step, characterized in that 0.015 to 0.150 mmol of internal cross-linking agent is used when polymerizing a first step to 1 mol of the water-soluble ethylenically unsaturated monomer, such that an area specific BET surface of secondary particles formed by agglomeration of primary particles is controlled to be less than 0.03 m2 / g, where the secondary particles are classified at 300 to 400 pm.
[0002]
2. Method of manufacturing a water-absorbent resin, according to claim 1, characterized by the fact that an amount used (in moles) of the internal cross-linking agent at the time of polymerization of the second and subsequent steps per 1 mole of water-soluble ethylenically unsaturated monomer of the second and subsequent stages, is 90% or less of an amount used (in moles) of the internal cross-linking agent used at the time of polymerization of the first stage to 1 mole of the water-soluble ethylenically unsaturated monomer used at the time of polymerization of the first stage.
[0003]
3. Water-absorbing resin comprising secondary particles formed by the agglomeration of the primary particles, the resin obtained by carrying out polymerization characterized by the fact that it is obtained by polymerizing an ethylenically unsaturated water-soluble monomer in the presence of an internal cross-linking agent, in whereas a water absorption rate of a physiological saline solution in the water-absorbent resin is 40 to 80 seconds, a particle mass ratio of 150 to 850 pm across the water-absorbent resin is 85% by weight or more, and a particle mass ratio of 300 to 400 pm is 20% by weight or more and a specific BET surface area of particles classified at 300 to 400 pm is less than 0.03 nV / g.
[0004]
4. Water-absorbent resin according to claim 3, characterized in that the average particle diameter of the water-absorbent resin is 200 to 600 pm.
[0005]
5. Water-absorbing agent characterized by the fact that it is obtained by mixing the water-absorbing resin as defined in claim 3 or 4 with a fine inorganic powder.
[0006]
6. Absorbent article characterized by the fact that it is formed using an absorbent material containing the water-absorbent resin as defined in claim 3 or 4.
[0007]
7. Absorbent article characterized by the fact that it is formed by means of an absorbent material that contains the water absorbing agent as defined in claim 5.

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同族专利:

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公开号 | 公开日

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CN105517660A|2016-04-20|

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TW201607961A|2016-03-01|

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CA2951468C|2018-06-05|

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US20170107313A1|2017-04-20|

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BR112017000530A2|2017-11-14|

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EP2993191A1|2016-03-09|

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法律状态:
2020-03-10| B06U| Preliminary requirement: requests with searches performed by other patent offices: procedure suspended [chapter 6.21 patent gazette]|

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2020-09-24| B09A| Decision: intention to grant [chapter 9.1 patent gazette]|

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JP2014143718|2014-07-11|

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JP2014-223725|2014-10-31|

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JP2014223725A|JP5689204B1|2014-07-11|2014-10-31|Water absorbent resin production method, water absorbent resin, water absorbent, absorbent article|

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