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JP2005200630A - Water-absorbing resin material and method for producing the same - Google Patents

Water-absorbing resin material and method for producing the same Download PDF

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JP2005200630A
JP2005200630A JP2004292318A JP2004292318A JP2005200630A JP 2005200630 A JP2005200630 A JP 2005200630A JP 2004292318 A JP2004292318 A JP 2004292318A JP 2004292318 A JP2004292318 A JP 2004292318A JP 2005200630 A JP2005200630 A JP 2005200630A
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water
resin body
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absorbent resin
carboxylic acid
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JP4476768B2 (en
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Hisanori Higashimoto
尚則 東本
Tsutomu Nakagawa
勉 仲川
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Asahi Kasei Chemicals Corp
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Asahi Kasei Chemicals Corp
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Abstract

<P>PROBLEM TO BE SOLVED: To provide a high water-absorbing resin material capable of exhibiting an excellent water-absorbing performance in a pressureless state, capable of exhibiting a high water-absorbing performance in a pressurized state as well, and capable of being most suitably used for a hygienic material, etc., and to provide a method for simply producing the high water-absorbing resin material, without requiring a surface crosslinking treatment process. <P>SOLUTION: This water-absorbing resin material has such a polymer molecular chain that 50 mol% or more of repeating units in the chain are carboxy group-containing units, a carboxy group neutralization rate in a central part of the resin material is not less than 60 mol%, and a carboxy group neutralization rate on an external surface of the resin material is not more than 50 mol%. The method for producing the water-absorbing resin material comprises polymerizing a monomer solution to form a polymer, drying the polymer, and heat-treating the polymer, wherein the monomer solution contains a mixture comprising an alkali metal salt of an unsaturated carboxylic acid and an ammonium salt thereof in an amount of more than 50 mol% based on the mixture, and further contains a condensation-type crosslinking agent. <P>COPYRIGHT: (C)2005,JPO&NCIPI

Description

本発明は、紙おむつ、生理用ナプキン等の衛材材料分野、農林業分野、土木分野等において幅広く利用されている吸水性樹脂体及びその製造方法の関する。特に、高い吸水倍率を必要とする紙おむつ、生理用ナプキン等の衛材材料分野向けの吸水性樹脂体及びその製造方法に関し、更に詳しくは、加圧下及び無加圧下の吸水倍率に優れる吸水性樹脂体及びその製造方法に関する。   The present invention relates to a water-absorbent resin body widely used in the field of sanitary materials such as disposable diapers and sanitary napkins, the field of agriculture and forestry, and the field of civil engineering, and a method for producing the same. In particular, the present invention relates to a water absorbent resin body for the field of sanitary materials such as disposable diapers and sanitary napkins that require a high water absorption capacity, and a method for producing the same, and more specifically, a water absorbent resin excellent in water absorption capacity under pressure and without pressure. The present invention relates to a body and a manufacturing method thereof.

近年、合成高分子の1種として、大量の水を吸収してゲル化する吸水性樹脂が開発され、紙おむつ、生理用ナプキン等の衛材分野、農林業分野、土木分野等に幅広く利用されている。この様な吸水性樹脂として例えば、ポリアクリル酸部分中和物架橋体(例えば特許文献1参照)、澱粉−アクリロニトリルグラフト重合体の加水分解物(例えば特許文献2参照)、澱粉−アクリル酸グラフト重合体の中和物(例えば特許文献3参照)、酢酸ビニル−アクリル酸エステル共重合体の鹸化物(例えば特許文献4参照)、アクリロニトリル共重合体もしくはアクリルアミド共重合体の加水分解物(例えば特許文献5参照)など多くが知られている。   In recent years, a water-absorbing resin that gels by absorbing a large amount of water has been developed as a kind of synthetic polymer, and is widely used in the field of sanitary materials such as disposable diapers and sanitary napkins, agriculture and forestry, and civil engineering. Yes. Examples of such a water-absorbing resin include a crosslinked polyacrylic acid partially neutralized product (see, for example, Patent Document 1), a hydrolyzate of starch-acrylonitrile graft polymer (see, for example, Patent Document 2), and starch-acrylic acid graft weight. Neutralized product of polymer (for example, see Patent Document 3), saponified product of vinyl acetate-acrylic acid ester copolymer (for example, see Patent Document 4), hydrolyzate of acrylonitrile copolymer or acrylamide copolymer (for example, Patent Document) Many are known.

上記の吸水性樹脂が備えるべき特性としては、従来より、体液等の水性液体に接した際の高い吸水倍率や優れた吸収速度、通液性、膨潤ゲルのゲル強度、水性液体を含んだ基材から水を吸い上げる吸引量等が求められている。しかしながら、これらの特性間の関係は必ずしも正の相関関係を示さず、例えば、吸水倍率の高いものほど通液性、ゲル強度、吸収速度等の物性は低下してしまう傾向にあった。   The characteristics that the water-absorbent resin should have include conventionally, a high water absorption ratio when contacting with an aqueous liquid such as body fluid, an excellent absorption rate, liquid permeability, gel strength of swollen gel, and a group containing an aqueous liquid. A suction amount for sucking water from the material is required. However, the relationship between these characteristics does not necessarily show a positive correlation. For example, the higher the water absorption ratio, the lower the physical properties such as liquid permeability, gel strength, and absorption rate.

そこで、このような吸水性樹脂の吸水諸特性をバランス良く改良する方法として吸水性樹脂の表面近傍を架橋する技術が知られており、これまでに様々な方法が提案されている。
例えば、架橋剤として、多価アルコールを用いる方法(例えば特許文献6、7参照)、多価グリシジル化合物、多価アジリジン化合物、多価アミン化合物、多価イソシアネート化合物を用いる方法(例えば特許文献8参照)、グリオキサールを用いる方法(例えば特許文献9参照)、多価金属を用いる方法(例えば特許文献10、11参照)、シランカップリング剤を用いる方法(例えば特許文献12、13、14参照)等が知られている。
また架橋反応時に、架橋剤を吸水性樹脂表面により均一に分布させ、均一な表面架橋を行う試みとして架橋剤の添加時に、不活性無機粉末を存在させる方法(例えば特許文献15、16参照)、二価アルコールを存在させる方法(例えば特許文献17参照)、水とエーテル化合物とを存在させる方法(例えば特許文献18参照)、リン酸を存在させる方法(例えば特許文献19参照)等も知られている。
Thus, as a method for improving the water absorption properties of such a water absorbent resin in a well-balanced manner, a technique for crosslinking the vicinity of the surface of the water absorbent resin is known, and various methods have been proposed so far.
For example, a method using a polyhydric alcohol as a crosslinking agent (see, for example, Patent Documents 6 and 7), a method using a polyvalent glycidyl compound, a polyvalent aziridine compound, a polyvalent amine compound, and a polyvalent isocyanate compound (see, for example, Patent Document 8). ), A method using glyoxal (see, for example, Patent Document 9), a method using a polyvalent metal (see, for example, Patent Documents 10 and 11), a method using a silane coupling agent (see, for example, Patent Documents 12, 13, 14), and the like. Are known.
In addition, a method in which a crosslinking agent is uniformly distributed on the surface of the water-absorbent resin during the crosslinking reaction, and an inert inorganic powder is present when adding the crosslinking agent as an attempt to perform uniform surface crosslinking (see, for example, Patent Documents 15 and 16). Also known are a method in which a dihydric alcohol is present (see, for example, Patent Document 17), a method in which water and an ether compound are present (see, for example, Patent Document 18), and a method in which phosphoric acid is present (see, for example, Patent Document 19). Yes.

また、上記方法の応用例として残留モノマーを低減させる目的で特定組成の中和単量体を上記架橋剤と混合し加熱処理しながら表面架橋する方法(例えば特許文献20、21)も知られている。   In addition, as an application example of the above method, there is also known a method (for example, Patent Documents 20 and 21) in which a neutralized monomer having a specific composition is mixed with the above crosslinking agent for the purpose of reducing residual monomer and surface crosslinking is performed while heat treatment. Yes.

しかし、これらの方法によって吸水性樹脂の諸物性のバランスは改良がなされるものの未だに十分とは言い難く、更なる高品質化が求められている。特に近年の傾向である、吸水性樹脂を多量に使用し薄型化された衛生用品における吸収体に用いられる吸水性樹脂の必要特性を考えた場合、上記の従来方法では、まだまだ十分な物性レベルにまで到達していないのが現状である。   However, although the balance of various physical properties of the water-absorbent resin is improved by these methods, it is still not sufficient, and further higher quality is required. In particular, when considering the necessary characteristics of the water-absorbent resin used in the absorbent article in a sanitary product that has been thinned using a large amount of water-absorbent resin, which is a recent trend, the above-mentioned conventional method still has a sufficient physical property level. It is the current situation that has not yet reached.

また近年、平均寿命の上昇に伴い高齢者向けの紙おむつの需要が増している。高齢者向けの紙おむつにおいては乳幼児向け比べ、紙おむつにかかる荷重が大きいこと、また、一回当たりの排泄量が多いことより、「装着時により重い荷重がかかっても十分な吸収能力を発揮できるような高荷重下での優れた吸水倍率」を有する吸水性樹脂がより強く求められている。
特開昭55−84304号公報 特公昭49−43395号公報 特開昭51−125468号公報 特開昭52−14689号公報 特公昭53−15959号公報 特開昭58−180233号公報 特開昭61−16903号公報 特開昭59−189103号公報 特開昭52−117393号公報 特開昭51−136588号公報 特開昭61−257235号公報 特開昭61−211305号公報 特開昭61−252212号公報 特開昭61−264006号公報 特開昭60−163956号公報 特開昭60−255814号公報 特開平1−292004号公報 特開平2−153903号公報 特表平8−508517号公報 特開平6−122707号公報 特開平6−122708号公報
In recent years, the demand for disposable diapers for the elderly has been increasing with the increase in the average lifespan. Compared to infants, the disposable diaper for elderly people has a larger load on the disposable diaper and the amount of excretion per time is larger. There is a strong demand for a water-absorbing resin having an “excellent water absorption capacity under a high load”.
JP 55-84304 A Japanese Patent Publication No.49-43395 Japanese Patent Laid-Open No. 51-125468 JP-A-52-14689 Japanese Patent Publication No.53-15959 JP 58-180233 A JP-A 61-16903 JP 59-189103 A JP 52-117393 A JP 51-136588 A JP-A-61-257235 JP-A-61-211305 JP-A 61-252212 JP 61-264006 A JP-A-60-163958 JP 60-255814 A JP-A-1-292004 Japanese Patent Laid-Open No. 2-153903 Japanese National Patent Publication No. 8-508517 JP-A-6-122707 JP-A-6-122708

衛生材料用途の吸水性樹脂として備えるべき性能として、様々の性能のなかでも無加圧下、加圧下における高い吸水性能があげられる。しかしこれらの特性は負の相関関係にあり無加圧の吸水性能と加圧下の吸水性能を共に高い水準とすることは従来は困難であった。   The performance to be provided as a water-absorbing resin for hygiene materials includes high water absorption performance under no pressure and under pressure among various performances. However, these characteristics have a negative correlation, and it has been difficult in the past to make both the non-pressurized water absorption performance and the water absorption performance under pressure high.

一方で近年、紙おむつ等の吸収性物品はその使用感、及び機能性の問題から薄型化が進み、吸収層に使用する吸水性樹脂の使用量が増大する傾向にある(例えば特開平2000−463参照)。しかしながら他方では、吸水性樹脂の主な用途である衛生材料用途においては、吸水性組成物の更なる薄型化及びコストダウン等に対応するためにも、吸水性樹脂の使用量の低減を行うことが望まれており、その解決の手段として吸水性樹脂の吸水性能の向上が求められている。   On the other hand, in recent years, absorbent articles such as disposable diapers have been thinned due to problems in use and functionality, and the amount of water-absorbing resin used in the absorbent layer tends to increase (for example, JP-A 2000-463). reference). However, on the other hand, in the hygiene material application, which is the main application of the water-absorbent resin, to reduce the amount of the water-absorbent resin in order to cope with further thinning and cost reduction of the water-absorbent composition. Therefore, improvement of the water absorption performance of the water absorbent resin is demanded as a means for solving the problem.

本発明の目的は、紙おむつ、生理用ナプキン、失禁パッド等の衛生材料に好適に用いることの出来る、従来達成困難であった加圧下及び無加圧下における高い吸水性能を有する吸水性樹脂体または、吸水性樹脂組成物を提供すること及び、本発明の吸水性樹脂体を安価な方法で簡便に製造できる製造方法を提供することにある。   An object of the present invention is a water-absorbent resin body having high water absorption performance under pressure and no pressure, which can be suitably used for sanitary materials such as disposable diapers, sanitary napkins, incontinence pads, etc. An object of the present invention is to provide a water-absorbent resin composition and to provide a production method capable of easily producing the water-absorbent resin body of the present invention by an inexpensive method.

本発明者らは前記課題を解決するため鋭意検討した結果、粒子内の中和率の分布に特定の構造を持つことを特徴とする吸水性樹脂体が優れた吸水性能を示すことを見出した。また、カルボキシル基に対し縮合型架橋剤となる化合物を含有し、少なくとも1種類の不飽和カルボン酸アンモニウム塩が50mol%を越え100mol%以下、不飽和カルボン酸アルカリ金属塩が0mol%以上50mol%未満の単量体成分から吸水性樹脂体を製造することによって、無加圧の吸水性能を犠牲にすることなく加圧下吸水性能の良い吸水性樹脂体を製造することが出来ることを見いだすことにより、本発明を完成させるに至った。   As a result of intensive studies to solve the above problems, the present inventors have found that a water-absorbent resin body characterized by having a specific structure in the distribution of the neutralization rate in the particles exhibits excellent water absorption performance. . Further, it contains a compound that becomes a condensation type crosslinking agent for the carboxyl group, and at least one kind of unsaturated carboxylic acid ammonium salt is more than 50 mol% and not more than 100 mol%, and the unsaturated carboxylic acid alkali metal salt is not less than 0 mol% and less than 50 mol%. By producing a water-absorbent resin body from the monomer component, it is possible to produce a water-absorbent resin body with good water absorption performance under pressure without sacrificing water absorption performance without pressure, The present invention has been completed.

すなわち、本発明は次からなる。
[1]ポリマー分子鎖中における繰り返し単位のうち、50mol%以上がカルボキシル基含有単位からなる吸水性樹脂体であって、樹脂体中心部のカルボキシル基中和率が60mol%以上であり、樹脂体外表面のカルボキシル基中和率が50mol%以下であることを特徴とする吸水性樹脂体。
[2]樹脂体中心部よりも中和率の低い部分が樹脂体外表面から13μm以上の幅で存在する、スキン構造を特徴とする前記[1]に記載の吸水性樹脂体。
[3]下記の(1)及び(2)を満たすことを特徴とする前記[1]あるいは[2]に記載の吸水性樹脂体。
(1)ポリマー分子鎖中におけるカルボキシル基中和塩のうち50mol%以上がアンモニウム塩である。
(2)0.8psiの加圧下における吸水倍率が22倍以上である。
[4]粒度分布が40μm〜1000μmである粉末粒子状の吸水性樹脂であることを特徴とする前記[3]に記載の吸水性樹脂体。
[5]下記の(3)から(5)を満たす単量体溶液を重合、解砕、乾燥、粉砕した後に、あるいは重合、解砕、粉砕、乾燥した後に、加熱処理をすることを特徴とする吸水性樹脂体の製造方法。
(3)少なくとも1種類の不飽和カルボン酸アンモニウム塩(A)、不飽和カルボン酸アルカリ金属塩(B)及びカルボキシル基に対する縮合型架橋剤(C)を含む。
(4)不飽和カルボン酸アンモニウム塩(A)の比率が全不飽和カルボン酸単量体に対して50mol%を越え100mol%以下であり、不飽和カルボン酸アルカリ金属塩(B)の比率が全不飽和カルボン酸単量体に対して0mol%以上50mol%未満である。
(5)カルボキシル基に対する縮合型架橋剤(C)の含有率が全単量体成分の重量に対して0.01重量%以上20重量%以下である。
[6]加熱処理を100〜250℃で行うことを特徴とする前記[5]に記載の吸水性樹脂体の製造方法。
[7]架橋剤としてカルボキシル基に対する縮合型架橋剤(C)に加えて、不飽和単量体重合性の架橋剤(D)を全単量体成分に対し0.005mol%以上1mol%以下含有することを特徴とする、[5]あるいは[6]に記載の吸水性樹脂体の製造方法。
[8]不飽和カルボン酸塩(A)および(B)が(メタ)アクリル酸塩であることを特徴とする前記[5]〜[7]のいずれかに記載の吸水性樹脂体の製造方法。
That is, this invention consists of the following.
[1] Among the repeating units in the polymer molecular chain, 50 mol% or more is a water-absorbent resin body composed of carboxyl group-containing units, and the carboxyl group neutralization rate at the center of the resin body is 60 mol% or more. A water-absorbent resin body having a surface carboxyl group neutralization rate of 50 mol% or less.
[2] The water-absorbent resin body according to the above [1], characterized by a skin structure in which a portion having a lower neutralization rate than the central portion of the resin body exists with a width of 13 μm or more from the outer surface of the resin body.
[3] The water-absorbent resin body according to [1] or [2], wherein the following (1) and (2) are satisfied.
(1) 50 mol% or more of the carboxyl group neutralized salt in the polymer molecular chain is an ammonium salt.
(2) The water absorption magnification under a pressure of 0.8 psi is 22 times or more.
[4] The water-absorbent resin body as described in [3] above, which is a powder particle water-absorbent resin having a particle size distribution of 40 μm to 1000 μm.
[5] It is characterized in that a monomer solution satisfying the following (3) to (5) is polymerized, pulverized, dried, pulverized, or polymerized, pulverized, pulverized, dried, and then heat-treated. A method for producing a water-absorbent resin body.
(3) At least one kind of unsaturated carboxylic acid ammonium salt (A), unsaturated carboxylic acid alkali metal salt (B), and a condensation type crosslinking agent (C) for a carboxyl group.
(4) The ratio of unsaturated carboxylic acid ammonium salt (A) is more than 50 mol% and 100 mol% or less with respect to all unsaturated carboxylic acid monomers, and the ratio of unsaturated carboxylic acid alkali metal salt (B) is all It is 0 mol% or more and less than 50 mol% with respect to the unsaturated carboxylic acid monomer.
(5) The content of the condensation type crosslinking agent (C) with respect to the carboxyl group is 0.01% by weight or more and 20% by weight or less based on the weight of all monomer components.
[6] The method for producing a water absorbent resin body according to [5], wherein the heat treatment is performed at 100 to 250 ° C.
[7] In addition to the condensation type crosslinking agent (C) for the carboxyl group as a crosslinking agent, the unsaturated monomer polymerizable crosslinking agent (D) is contained in an amount of 0.005 mol% to 1 mol% based on the total monomer components. The method for producing a water-absorbent resin body according to [5] or [6], wherein:
[8] The method for producing a water-absorbent resin body according to any one of [5] to [7], wherein the unsaturated carboxylates (A) and (B) are (meth) acrylates. .

本発明の吸水性能は、無加圧の吸水性能を高レベルで保ったままで加圧下でも良好な吸水性能を示し、紙おむつなどの衛生材料用途などに好適である。
また、本発明の製造方法では、従来、無加圧と加圧下の吸水倍率のバランスがよい樹脂を製造するために行われていた表面架橋処理工程を経ることなく、加圧下吸水性能の優れた樹脂を簡便に製造できるため非常に有益である。
The water-absorbing performance of the present invention shows good water-absorbing performance even under pressure while maintaining the non-pressurized water-absorbing performance at a high level, and is suitable for sanitary material applications such as disposable diapers.
Further, in the production method of the present invention, the water absorption performance under pressure is excellent without passing through the surface cross-linking treatment step that has been conventionally performed to produce a resin having a good balance between the non-pressurization and the water absorption capacity under pressure. This is very useful because the resin can be easily produced.

以下、本発明を実施例を用いて更に詳細に説明する。
本発明の吸水性樹脂体は、ポリマー分子鎖中における繰り返し単位の50mol%以上がカルボキシル基含有単位からなる吸水性樹脂体であって、樹脂体中心部のカルボキシル基中和率が60mol%以上であり、樹脂体外表面のカルボキシル基中和率が50mol%以下である吸水性樹脂体である。
Hereinafter, the present invention will be described in more detail with reference to examples.
The water-absorbent resin body of the present invention is a water-absorbent resin body in which 50 mol% or more of the repeating units in the polymer molecular chain are composed of carboxyl group-containing units, and the neutralization rate of the carboxyl group at the center of the resin body is 60 mol% or more. Yes, the water-absorbent resin body has a carboxyl group neutralization rate of 50 mol% or less on the outer surface of the resin body.

ポリマー分子鎖中における繰り返し単位のうちのカルボキシル基含有単位は、50mol%以上であることが必要であり、吸水性能の点から好ましくは80mol%以上、さらに好ましくは90mol%以上である。   Of the repeating units in the polymer molecular chain, the carboxyl group-containing unit needs to be 50 mol% or more, and is preferably 80 mol% or more, more preferably 90 mol% or more from the viewpoint of water absorption performance.

本発明の吸水性樹脂体を構成するカルボキシル基含有単量体としては、アクリル酸、メタアクリル酸、イタコン酸、マレイン酸、クロトン酸、フマル酸、ソルビン酸、けい皮酸、それらの無水物、不飽和カルボン酸単量体の中和塩等が挙げられる。   As the carboxyl group-containing monomer constituting the water-absorbent resin body of the present invention, acrylic acid, methacrylic acid, itaconic acid, maleic acid, crotonic acid, fumaric acid, sorbic acid, cinnamic acid, their anhydrides, And neutralized salts of unsaturated carboxylic acid monomers.

ポリマー分子鎖中のカルボキシル基は部分中和されていることが好ましく、塩基としては、ナトリウム、カリウム、リチウム等のアルカリ金属、アミン類もしくはアンモニアのうちの少なくとも1種類が挙げられる。塩基の種類としては、アンモニアを含む少なくとも1種類以上で部分中和されることが好ましく、アンモニア単独で部分中和されることが最も好ましい。本発明の吸水性樹脂体は、中和率が樹脂体内部で分布構造を持つ。すなわち樹脂体中心部のカルボキシル基中和率が60mol%以上、好ましくは65mol%以上、最も好ましくは70mol%以上であり、樹脂体外表面のカルボキシル基中和率が50mol%以下、好ましくは45mol%以下、最も好ましくは40mol%以下である。樹脂体中心部の中和率が上記の数値であると無加圧における吸水倍率の低下が起こりにくく好ましい。また、樹脂体外表面の中和率が上記の数値であると加圧下の吸水倍率が低下しにくく好ましい。   The carboxyl group in the polymer molecular chain is preferably partially neutralized, and examples of the base include at least one of alkali metals such as sodium, potassium, and lithium, amines, and ammonia. As a kind of base, it is preferable to be partially neutralized with at least one kind including ammonia, and most preferably partially neutralized with ammonia alone. In the water absorbent resin body of the present invention, the neutralization rate has a distributed structure inside the resin body. That is, the carboxyl group neutralization rate at the center of the resin body is 60 mol% or more, preferably 65 mol% or more, most preferably 70 mol% or more, and the carboxyl group neutralization rate on the outer surface of the resin body is 50 mol% or less, preferably 45 mol% or less. Most preferably, it is 40 mol% or less. It is preferable that the neutralization rate of the central part of the resin body is the above-mentioned numerical value because it is difficult for the water absorption capacity to decrease without pressure. Moreover, when the neutralization rate of the outer surface of the resin body is the above numerical value, it is preferable that the water absorption capacity under pressure is difficult to decrease.

本発明の要件である樹脂体内部での中和率の分布構造は、樹脂体外表面と樹脂体中心部の中和率を赤外吸光分析法の一つである顕微ATR法によって測定することにより求めることができる。樹脂体外表面とは当該樹脂体の外部に露出している部分を言い、樹脂体中心部とは当該樹脂体の樹脂体外表面から最も深い部分を言う。樹脂体外表面の中和率の測定は顕微ATR法にて直接樹脂体外表面を測定し、樹脂体中心部の測定は、例えばウルトラミクロトーム(Reichert製 ULTRACUT N)を用いることにより樹脂体を割断して中心部を露出させてから顕微ATR法にて測定する。測定装置は例えばBio−Rad社製 FTS−575などを用いることができる。   The distribution structure of the neutralization rate inside the resin body, which is a requirement of the present invention, is determined by measuring the neutralization rate between the outer surface of the resin body and the center of the resin body by a microscopic ATR method which is one of infrared absorption analysis methods. Can be sought. The resin body outer surface means a portion exposed to the outside of the resin body, and the resin body central portion means the deepest part from the resin body outer surface of the resin body. The neutralization rate of the outer surface of the resin body is measured directly by the microscopic ATR method, and the resin body is measured by cleaving the resin body by using, for example, an ultramicrotome (ULTRACUT N manufactured by Reichert). After exposing the central portion, measurement is performed by the microscopic ATR method. As the measuring apparatus, for example, FTS-575 manufactured by Bio-Rad may be used.

カルボン酸及びカルボキシレートの組成比を規定する指標として、1695cm−1(カルボン酸νC=0 ベースライン1774〜1616cm−1)および1558cm−1(カルボキシレートνCOO ベースライン1616〜1500cm−1)のピーク面積比(1695/1558cm−1)を計算する。別途、全カルボン酸の10mol%,30mol%,50mol%,70mol%,90mol%,100mol%をアンモニアで中和した部分架橋ポリアクリル酸を標準サンプルとして測定し、作成した検量線より組成比を求める。 As an indicator for defining the composition ratio of carboxylic acid and carboxylate, 1,695 cm -1 (carboxylate νC = 0 Baseline 1774~1616cm -1) and 1558cm -1 - peak of (carboxylate νCOO baseline 1616~1500cm -1) The area ratio (1695/1558 cm −1 ) is calculated. Separately, 10 mol%, 30 mol%, 50 mol%, 70 mol%, 90 mol%, and 100 mol% of the total carboxylic acid were measured using partially crosslinked polyacrylic acid neutralized with ammonia as a standard sample, and the composition ratio was determined from the prepared calibration curve. .

本発明における吸水性樹脂体の好ましい1つの態様によれば、樹脂体中心部より中和率の低い部分が樹脂体表層に存在する構造を、樹脂体外表面から13μm以上の幅で持つことを特徴とする。ここで樹脂体中心部より中和率の低い部分が樹脂体表層に存在する構造をスキン構造とする。本発明の樹脂体におけるスキン構造の幅は13μm以上、好ましくは19μm以上である。スキン構造の幅が13μm以上の場合、加圧下の吸水性能が向上するため好ましい。   According to one preferable aspect of the water-absorbent resin body in the present invention, the water-absorbent resin body has a structure in which a portion having a lower neutralization rate than the center portion of the resin body is present on the surface of the resin body with a width of 13 μm or more from the outer surface of the resin body. And Here, a structure in which a portion having a lower neutralization rate than the central portion of the resin body is present on the surface of the resin body is defined as a skin structure. The width of the skin structure in the resin body of the present invention is 13 μm or more, preferably 19 μm or more. When the width of the skin structure is 13 μm or more, the water absorption performance under pressure is improved, which is preferable.

該樹脂体に存在するスキン構造の幅は、IRイメージング測定により測定することが出きる。樹脂体を厚さ2μmの切片にウルトラミクロトーム(Reichert製 ULTRACUT N)を用いて切り出して、IR透過法の要領で測定する。切り出したサンプルの全部位を測定する。樹脂体の切り出しは当該樹脂体において、表面層からの最深部が測定できるように切り出す。IRイメージング測定に用いる装置はPerkin Elmer社製 Spot−Lightなどである。カルボン酸及びカルボキシレートの組成比を規定する指標として、1695cm−1(カルボン酸νC=0 ベースライン1774〜1616cm−1)および1558cm−1(カルボキシレートνCOO ベースライン1616〜1500cm−1)のピーク面積比(1695/1558cm−1)を計算し、Total吸光度イメージをBand Raitoイメージへ変換する。スキン構造の幅は、表面層から表面層のBand Raito値より40%下がった点までとする。 The width of the skin structure existing in the resin body can be measured by IR imaging measurement. The resin body is cut into 2 μm-thick sections using an ultramicrotome (ULTRACUT N manufactured by Reichert), and measured in the manner of the IR transmission method. Measure all parts of the cut sample. The resin body is cut out so that the deepest part from the surface layer can be measured in the resin body. An apparatus used for IR imaging measurement is Spot-Light manufactured by Perkin Elmer. As an indicator for defining the composition ratio of carboxylic acid and carboxylate, 1,695 cm -1 (carboxylate νC = 0 Baseline 1774~1616cm -1) and 1558cm -1 - peak of (carboxylate νCOO baseline 1616~1500cm -1) The area ratio (1695/1558 cm −1 ) is calculated and the total absorbance image is converted to a Band Radio image. The width of the skin structure is from the surface layer to a point 40% lower than the Band Radio value of the surface layer.

本発明の吸水性樹脂体は、加圧下の吸水倍率を高めるために、ポリマー分子鎖中におけるカルボキシル基中和塩のうち50mol%以上がアンモニウム塩であることが好ましい。より好ましくは70mol%以上がアンモニウム塩であり、最も好ましくは100mol%がアンモニウム塩である。   In the water-absorbent resin body of the present invention, 50 mol% or more of the carboxyl group neutralized salt in the polymer molecular chain is preferably an ammonium salt in order to increase the water absorption capacity under pressure. More preferably, 70 mol% or more is an ammonium salt, and most preferably 100 mol% is an ammonium salt.

本発明の吸水性樹脂体の形状は、本発明の趣旨に変更を加える物で無ければ特に限定される物ではなく、吸水性樹脂組成物に広く用いられている球形粒子状粉末、不定形粒子状粉末、短繊維状、長繊維状、シート状などがあげられる。衛生材料分野における使用形態においてパルプとの混合のしやすさなどの取り扱い状の簡便性から、球形粒子状粉末もしくは不定形粒子状粉末は好ましく、その粒度分布は40μm〜1000μmであることが好ましい。さらに好ましくは50μm〜900μmであり、最も好ましくは100〜850μmである。粒径が著しく小さい場合は微紛となり、飛散しやすくなるなど使用の際に問題となる。また、大きい場合は吸水速度の低下、吸収体物品中の吸水性樹脂体の偏りなどが問題となる。   The shape of the water-absorbent resin body of the present invention is not particularly limited as long as it does not change the gist of the present invention. Spherical particulate powders and amorphous particles widely used in water-absorbent resin compositions Powder, short fiber, long fiber, and sheet. From the viewpoint of ease of handling such as ease of mixing with pulp in the usage form in the sanitary material field, spherical particulate powder or irregular particulate powder is preferable, and the particle size distribution is preferably 40 μm to 1000 μm. More preferably, it is 50 micrometers-900 micrometers, Most preferably, it is 100-850 micrometers. When the particle size is remarkably small, it becomes a fine powder, which causes a problem in use such as being easily scattered. On the other hand, when it is large, there are problems such as a decrease in water absorption rate and unevenness of the water absorbent resin body in the absorbent article.

本発明の吸水性樹脂体にさらに消臭剤、抗菌剤、香料、各種の無機粉末、発泡剤、顔料、染料、親水性短繊維、肥料、酸化剤、還元剤、水、塩類等を添加し、これにより、吸水剤に種々の機能を付与させ、吸水性樹脂組成物とすることもできる。   Deodorant, antibacterial agent, fragrance, various inorganic powders, foaming agent, pigment, dye, hydrophilic short fiber, fertilizer, oxidizing agent, reducing agent, water, salt, etc. are further added to the water absorbent resin body of the present invention. Thus, various functions can be imparted to the water-absorbing agent to obtain a water-absorbing resin composition.

本発明の吸水性樹脂体の製造方法は、特に限定されないが、不飽和カルボン酸塩単量体の共重合により得られる樹脂体を、加熱処理する方法が上げられる。加熱処理においては、不飽和カルボン酸単量体の共重合物を中和したもの、もしくは、ニトリル基、アミド基を含有するポリマーを加水分解することによりカルボキシル基を含有する中和された樹脂体を製造して後述の加熱処理をしてもかまわない。カルボン酸塩含有樹脂体を本発明の吸水性樹脂体の構造へ処理するその他の方法としては、均一に中和された樹脂体の表層を酸処理することによりイオン交換させる方法、中和率の異なる2種類のモノマーを用いて層構造になるように重合する方法などがあげられるが、前述の不飽和カルボン酸塩単量体の共重合により得られる樹脂体を加熱処理する方法が好ましい。即ち、少なくとも1種類の不飽和カルボン酸アンモニウム塩(A)、不飽和カルボン酸アルカリ金属塩(B)及びカルボキシル基に対して縮合型となる化合物(C)を含む単量体水溶液を重合、乾燥、粉砕した後に、あるいは重合、粉砕、乾燥した後に、加熱処理する。   Although the manufacturing method of the water absorbing resin body of this invention is not specifically limited, The method of heat-processing the resin body obtained by copolymerization of an unsaturated carboxylate monomer is raised. In the heat treatment, a neutralized resin body containing a carboxyl group by hydrolyzing a polymer containing an unsaturated carboxylic acid monomer or a polymer containing a nitrile group or an amide group May be manufactured and heat treatment described later may be performed. Other methods for treating a carboxylate-containing resin body into the structure of the water-absorbent resin body of the present invention include a method of ion exchange by acid treatment of a surface layer of a uniformly neutralized resin body, Examples of the method include polymerization using a different two kinds of monomers so as to form a layer structure, and a method in which a resin body obtained by copolymerization of the above-described unsaturated carboxylate monomer is heat-treated is preferable. That is, an aqueous monomer solution containing at least one unsaturated carboxylic acid ammonium salt (A), an unsaturated carboxylic acid alkali metal salt (B), and a compound (C) that is condensed with respect to a carboxyl group is polymerized and dried. After the pulverization, or after polymerization, pulverization and drying, heat treatment is performed.

不飽和カルボン酸アンモニウム塩(A)としては、アクリル酸、メタアクリル酸、イタコン酸、マレイン酸、クロトン酸、フマル酸、ソルビン酸、けい皮酸のアンモニウム塩が好ましく、特に、(メタ)アクリル酸のアンモニウム塩が好ましい。   As the unsaturated carboxylic acid ammonium salt (A), acrylic acid, methacrylic acid, itaconic acid, maleic acid, crotonic acid, fumaric acid, sorbic acid, and cinnamic acid ammonium salts are preferred, and in particular, (meth) acrylic acid. The ammonium salt is preferred.

不飽和カルボン酸アルカリ金属塩(B)としては、アクリル酸、メタアクリル酸、イタコン酸、マレイン酸、クロトン酸、フマル酸、ソルビン酸、けい皮酸のアルカリ金属塩が好ましく、特に、(メタ)アクリル酸のアルカリ金属塩が好ましい。不飽和カルボン酸アルカリ金属塩(B)におけるアルカリ金属の種類としてはリチウム、ナトリウム、カリウムなどがある。   The unsaturated carboxylic acid alkali metal salt (B) is preferably an alkali metal salt of acrylic acid, methacrylic acid, itaconic acid, maleic acid, crotonic acid, fumaric acid, sorbic acid, or cinnamic acid. An alkali metal salt of acrylic acid is preferred. Examples of the alkali metal in the unsaturated carboxylic acid alkali metal salt (B) include lithium, sodium and potassium.

不飽和カルボン酸アンモニウム塩(A)と不飽和カルボン酸アルカリ金属塩(B)はその組成において、(A)が50mol%を越え100mol%以下、(B)が0mol%以上50mol%未満になるように調製する。   The composition of the unsaturated carboxylic acid ammonium salt (A) and the unsaturated carboxylic acid alkali metal salt (B) is such that (A) exceeds 50 mol% and 100 mol% or less, and (B) is 0 mol% or more and less than 50 mol%. Prepare to.

本発明の樹脂体には全官能基中の50mol%以上がカルボン酸基となる範囲内であれば、その他の単量体を共重合してもよい。共重合してもよい不飽和単量体としては(メタ)アクリル酸、イタコン酸、マレイン酸、クロトン酸、ソルビン酸、けい皮酸、それらの無水物、ビニルスルフォン酸、アリルスルフォン酸、スチレンスルフォン酸、ビニルトルエンフルフォン酸、2−(メタ)アクリルアミド−2−メチルプロパンスルフォン酸、2−(メタ)アクリロイルエタンスルフォン酸、2−(メタ)アクリロイルプロパンスルフォン酸、2−ヒドロキシルエチルアクリロイルオフォスフェート、2−ヒドロキシルエチルメタクリロイルフォスフェート、フェニル−2−アクリロイロキシエチルフォスフェート、ビニルリン酸などのアニオン性不飽和単量体およびその塩、アクリルアミド、メタアクリルアミド、N−エチル(メタ)アクリルアミド、N−n−プロピル(メタ)アクリルアミド、N−イソプロピル(メタ)アクリルアミド、N,N−ジメチル(メタ)アクリルアミド、2−ヒドロキシエチル(メタ)アクリレート、2−ヒドロキシプロピル(メタ)アクリレート、メトキシポリエチレングリコール(メタ)アクレリート、ポリエチレングリコールモノ(メタ)アクリレート、N−ビニルピロリドン、N−アクリロイルピペジリン、N−アクリロイルピロリジンなどのノニオン性の親水性基含有不飽和単量体が挙げられる。   In the resin body of the present invention, other monomers may be copolymerized as long as 50 mol% or more of all functional groups are within the range where carboxylic acid groups are formed. Unsaturated monomers that may be copolymerized include (meth) acrylic acid, itaconic acid, maleic acid, crotonic acid, sorbic acid, cinnamic acid, their anhydrides, vinyl sulfonic acid, allyl sulfonic acid, styrene sulfone Acid, vinyltoluene sulfonic acid, 2- (meth) acrylamido-2-methylpropanesulfonic acid, 2- (meth) acryloylethanesulfonic acid, 2- (meth) acryloylpropanesulfonic acid, 2-hydroxylethylacryloyl phosphate, Anionic unsaturated monomers and salts thereof such as 2-hydroxylethylmethacryloyl phosphate, phenyl-2-acryloyloxyethyl phosphate, vinyl phosphate, acrylamide, methacrylamide, N-ethyl (meth) acrylamide, Nn -Propyl (Meth) acrylamide, N-isopropyl (meth) acrylamide, N, N-dimethyl (meth) acrylamide, 2-hydroxyethyl (meth) acrylate, 2-hydroxypropyl (meth) acrylate, methoxypolyethylene glycol (meth) acrylate, polyethylene glycol Nonionic hydrophilic group-containing unsaturated monomers such as mono (meth) acrylate, N-vinylpyrrolidone, N-acryloylpiperidine, N-acryloylpyrrolidine and the like can be mentioned.

また、本発明の吸水性樹脂体を得るために、メチル(メタ)アクリレート、エチル(メタ)アクリレート、酢酸ビニルなどの様に重合後の官能基の加水分解によって、吸水性樹脂を形成する親水性単量体を用いて重合してもよい。また、併用できる疎水性単量体としては、スチレン、塩化ビニル、ブタジエン、イソブテン、エチレン、プロピレン、ステアリル(メタ)アクリレート、 ラウリル(メタ)アクリレートなどが挙げられ、これらの中で1種類、もしくは2種類以上を添加することができる。   Further, in order to obtain the water-absorbent resin body of the present invention, hydrophilicity that forms a water-absorbent resin by hydrolysis of functional groups after polymerization, such as methyl (meth) acrylate, ethyl (meth) acrylate, vinyl acetate, etc. You may superpose | polymerize using a monomer. Examples of the hydrophobic monomer that can be used in combination include styrene, vinyl chloride, butadiene, isobutene, ethylene, propylene, stearyl (meth) acrylate, lauryl (meth) acrylate, and the like. More than one type can be added.

吸水性樹脂を架橋する方法としては、例えば、縮合型架橋剤を用いて樹脂中の官能基と反応して架橋される方法、重合性の架橋剤を用いて不飽和単量体と共重合することにより架橋する方法、樹脂に電子線や放射線を照射することで架橋する方法等が上げられ、好ましくは縮合型架橋を用いる方法、最も好ましくは樹脂の官能基と反応する縮合型架橋剤(C)の共存下で、重合性の架橋剤(D)と不飽和単量体を共重合する方法である。   Examples of the method for crosslinking the water-absorbent resin include a method in which a condensation type crosslinking agent is used to react with a functional group in the resin to crosslink, and a polymerizable crosslinking agent is used to copolymerize with an unsaturated monomer. The cross-linking method can be increased by irradiating the resin with an electron beam or radiation. The method preferably uses condensation-type cross-linking, most preferably the condensing type cross-linking agent that reacts with the functional group of the resin (C ) In the coexistence of the polymerizable crosslinking agent (D) and the unsaturated monomer.

カルボキシル基に対する縮合型架橋剤(C)としては、エチレングリコールジグリシジルエーテル、トリメチロールプロパントリグリシジルエーテル、(ポリ)グリセリンポリグリシジルエーテル、ジグリセリンポリグリシジルエーテル、プロピレングリコールジグリシジルエーテル等のグリシジルエーテル化合物;(ポリ)グリセリン、(ポリ)エチレングリコール、プロピレングリコール、1,3−プロパンジオール、ポリオキシエチレングリコール、トリエチレングリコール、テトラエチレングリコール、ジエタノールアミン、トリエタノールアミンなどの多価アルコール類;エチレンジアミン、ジエチレンジアミン、ポリエチレンイミン、ヘキサメチレンジアミンなどの多価アミン類;亜鉛、カルシウム、マグネシウム、アルミニウムなどの多価イオンなどが挙げられ、これらの架橋剤は2種以上用いてもよい。   Glycidyl ether compounds such as ethylene glycol diglycidyl ether, trimethylolpropane triglycidyl ether, (poly) glycerin polyglycidyl ether, diglycerin polyglycidyl ether, propylene glycol diglycidyl ether, etc. Polyhydric alcohols such as (poly) glycerin, (poly) ethylene glycol, propylene glycol, 1,3-propanediol, polyoxyethylene glycol, triethylene glycol, tetraethylene glycol, diethanolamine, triethanolamine; ethylenediamine, di Polyvalent amines such as ethylenediamine, polyethyleneimine, hexamethylenediamine; zinc, calcium, magnesium, aluminum Include such polyvalent ions such as these crosslinking agents may be used two or more.

不飽和単量体重合性の架橋剤(D)とは、重合時に架橋剤となる1分子中に不飽和基を2個以上持つ化合物であり、具体的には、ジエチレングリコールジアクリレート、N,N‘−メチレンビスアクリルアミド、ポリエチレングリコールジアクリレート、ポリプロピレングリコールジアクリレート、トリメチロールプロパンジアリルエーテル、アリルグリシジルエーテル、ペンタエリスリトールトリアリルエーテル、ペンタエリスリトールジアクリレートモノステアレート、ビスフェノールジアクリレート、イソシアヌル酸ジアクリレート、テトラアリルオキシエタン、ジアリルオキシ酢酸塩などが挙げられ、これら架橋剤は2種以上用いてもよい。   The unsaturated monomer polymerizable crosslinking agent (D) is a compound having two or more unsaturated groups in one molecule that becomes a crosslinking agent at the time of polymerization. Specifically, diethylene glycol diacrylate, N, N '-Methylenebisacrylamide, polyethylene glycol diacrylate, polypropylene glycol diacrylate, trimethylolpropane diallyl ether, allyl glycidyl ether, pentaerythritol triallyl ether, pentaerythritol diacrylate monostearate, bisphenol diacrylate, isocyanuric acid diacrylate, tetra Examples include allyloxyethane and diallyloxyacetate, and two or more of these crosslinking agents may be used.

単量体溶液の溶媒は溶解性に優れたものであれば特に限定されない。特に好ましくは水単独であるが、エタノール、メタノール、アセトンなどの親水性溶媒を単独もしくは複数混合して使用しても良い。また、必要に応じて塩化ナトリウムなどの塩類、pHコントロールを目的としたアンモニアなどの塩基性化合物、逆相懸濁重合の際には懸濁剤を添加しても良い。   The solvent of the monomer solution is not particularly limited as long as it has excellent solubility. Particularly preferred is water alone, but hydrophilic solvents such as ethanol, methanol, acetone and the like may be used alone or in combination. If necessary, a salt such as sodium chloride, a basic compound such as ammonia for pH control, or a suspending agent may be added during reverse phase suspension polymerization.

不飽和単量体の重合方法は特に限定されず、(水)溶液重合、逆層懸濁重合、噴霧重合、ベルト重合など一般に広く用いられている方法が適用できる。
重合開始方法も特に限定されず、ラジカル重合開始剤による重合、放射線、電子線などの照射による重合、光増感剤による紫外線重合を行うこともできる。かかるラジカル重合に用いられる開始剤としては、例えば、過硫酸カリウム、過硫酸アンモニウム、過硫酸ナトリウムなどの過硫酸塩;過酸化水素;クメンハイドロパーオキサイド、t−ブチルハイドロパーオキサイド、過酢酸などの有機化酸化物、などの公知の開始剤が挙げられる。酸化性ラジカル重合開始剤を用いる場合はL−アスコルビン酸、ロンガリットなどの還元剤を併用してもよい。重合開始前に予め単量体溶液中の脱酸素操作を行うことは好ましい。具体的な方法として、十分な時間の不活性ガスによるバブリングにより溶存酸素を取り除く方法があげられる。また、反応器内雰囲気も窒素、ヘリウムなどの不活性ガスに置換されていることが好ましい。
The polymerization method of the unsaturated monomer is not particularly limited, and generally used methods such as (water) solution polymerization, reverse layer suspension polymerization, spray polymerization, and belt polymerization can be applied.
The polymerization initiation method is not particularly limited, and polymerization with a radical polymerization initiator, polymerization by irradiation with radiation, electron beam, or ultraviolet polymerization with a photosensitizer can be performed. Examples of the initiator used for such radical polymerization include persulfates such as potassium persulfate, ammonium persulfate and sodium persulfate; hydrogen peroxide; organics such as cumene hydroperoxide, t-butyl hydroperoxide and peracetic acid. Examples thereof include known initiators such as oxide oxides. When an oxidizing radical polymerization initiator is used, a reducing agent such as L-ascorbic acid or Rongalite may be used in combination. It is preferable to perform a deoxygenation operation in the monomer solution in advance before the start of polymerization. As a specific method, there is a method of removing dissolved oxygen by bubbling with an inert gas for a sufficient time. The atmosphere in the reactor is preferably replaced with an inert gas such as nitrogen or helium.

重合反応器内は減圧、常圧、加圧のいずれであっても良い。重合開始温度は通常0〜50℃で行う。重合開始温度で好ましいのは10〜40℃である。重合反応中の反応器内の温度は成り行きに任せてもよく、外部から冷却もしくは加熱により温度制御を行ってもよい。単量体溶液の濃度は10〜70%が好ましく、経済的、反応制御のしやすさなどの観点からは30〜50%が最も好ましい。   The inside of the polymerization reactor may be any of reduced pressure, normal pressure, and increased pressure. The polymerization start temperature is usually 0 to 50 ° C. The polymerization initiation temperature is preferably 10 to 40 ° C. The temperature in the reactor during the polymerization reaction may be determined depending on the situation, and the temperature may be controlled from the outside by cooling or heating. The concentration of the monomer solution is preferably 10 to 70%, and most preferably 30 to 50% from the viewpoint of economy and ease of reaction control.

重合反応後、含水ゲル状の物質が生成する。樹脂を粒子状にするには、この含水ゲル状物質を解砕してから乾燥させ、乾燥後に数百μm程度にまで粉砕し造粒する。もしくは上記含水ゲルを解砕しながら同時に、乾燥後の粒径が最適な大きさになるまで粉砕した後、乾燥させる方法があげられる。粒度分布は40μm〜1000μmに収まることが好ましく、特に好ましくは50μm〜900μm、更に好ましくは100〜850μmである。粉砕方法としては特に制限されるものではなく、従来公知の方法を適宣用いることができる。逆相懸濁重合の場合は乾燥後に適度な大きさに篩い分けする。   After the polymerization reaction, a hydrogel substance is generated. In order to make the resin into particles, this hydrogel material is crushed and dried, and after drying, it is pulverized to about several hundred μm and granulated. Alternatively, a method may be mentioned in which the hydrated gel is pulverized and simultaneously pulverized until the particle size after drying reaches an optimum size and then dried. The particle size distribution is preferably within 40 μm to 1000 μm, particularly preferably 50 μm to 900 μm, and more preferably 100 to 850 μm. The pulverization method is not particularly limited, and a conventionally known method can be appropriately used. In the case of reverse-phase suspension polymerization, it is sieved to an appropriate size after drying.

乾燥方法としては特に限定されるものはなく、通常真空乾燥、熱風乾燥が用いられる。乾燥温度は70℃〜180℃の範囲が好ましく、特に好ましくは90〜140℃である。多段昇温してもよい。乾燥温度は低すぎると乾燥時間に時間がかかりすぎるため経済的でなく、高すぎると吸水性樹脂の分解が起こるため吸水性能の低下を招く。   The drying method is not particularly limited, and usually vacuum drying or hot air drying is used. The drying temperature is preferably in the range of 70 ° C to 180 ° C, particularly preferably 90 to 140 ° C. Multi-stage heating may be performed. If the drying temperature is too low, it takes too much time to dry, which is not economical. If the drying temperature is too high, the water-absorbing resin is decomposed, resulting in a decrease in water absorption performance.

樹脂体の形状は特に限定される物ではないが、いずれの場合も加熱処理する前段階で形状が完成していることが望ましい。
樹脂体の外表層の中和率が内部の中和率よりも低くなるための好ましい方法は、前記記載の製造方法で得られた樹脂体の加熱処理である。加熱処理は、乾燥終了後に連続的に同じ装置内で加熱しても良く、乾燥工程とは独立の工程としても良い。加熱条件は樹脂体の吸水性能を劣化させる条件で無ければ特に限定されるものではなく、中和率の分布構造およびスキン構造の幅によって適時設定される。加熱温度は100〜250℃の範囲であり、好ましくは120〜200℃である。また、樹脂体中の中和率の分布構造および吸水性能の面から加熱温度は乾燥温度よりも10〜150℃高い温度で行われることは好ましく、30〜100℃高い温度で行われることは更に好ましい。加熱時間は10分〜5時間である。樹脂体の内部の中和率が60mol%以上であること、外表層の中和率は50mol%以下の範囲内になるように上記の加熱温度、加熱時間から適宜選択される。
The shape of the resin body is not particularly limited, but in any case, it is desirable that the shape is completed before the heat treatment.
A preferred method for the neutralization rate of the outer surface layer of the resin body to be lower than the internal neutralization rate is a heat treatment of the resin body obtained by the production method described above. The heat treatment may be performed continuously in the same apparatus after completion of drying, or may be a step independent of the drying step. The heating conditions are not particularly limited as long as the water absorption performance of the resin body is not deteriorated, and is appropriately set depending on the distribution structure of the neutralization rate and the width of the skin structure. The heating temperature is in the range of 100 to 250 ° C, preferably 120 to 200 ° C. Further, from the viewpoint of the distribution structure of the neutralization rate in the resin body and the water absorption performance, the heating temperature is preferably 10 to 150 ° C. higher than the drying temperature, and further 30 to 100 ° C. higher. preferable. The heating time is 10 minutes to 5 hours. The neutralization rate inside the resin body is 60 mol% or more, and the neutralization rate of the outer surface layer is appropriately selected from the above heating temperature and heating time so as to be in the range of 50 mol% or less.

以下に本発明の具体的な実施例および比較例を示すが、本発明は下記の実施例に限定されない。
(1)樹脂体外表面と内部の中和率の測定方法
(i)測定装置
測定装置はBio−Rad社製 FTS−575を用いた。
(ii)測定条件
顕微ATR法(結晶板Ge 1回反射)、
Back Ground:Air 常温測定、
アパーチャー:50×50μm、
積算回数:100回
測定によって得られたスペクトルデータから1695cm−1(カルボン酸νC=0 ベースライン1774〜1616cm−1)および1558cm−1(カルボキシレートνCOO ベースライン1616〜1500cm−1)のピーク面積比(1695/1558cm−1)を求める。
Specific examples and comparative examples of the present invention are shown below, but the present invention is not limited to the following examples.
(1) Measuring method of neutralization ratio of resin body outer surface and inner part (i) Measuring device FTS-575 manufactured by Bio-Rad was used as a measuring device.
(Ii) Measurement conditions Microscopic ATR method (crystal plate Ge once reflection),
Back Ground: Air room temperature measurement,
Aperture: 50 × 50 μm,
Peak area of - (baseline 1616~1500Cm -1-carboxylate νCOO) 1695cm from the spectral data obtained by the 100 measurements -1 (carboxylic acid νC = 0 Baseline 1774~1616Cm -1) and 1558cm -1: accumulated number The ratio (1695/1558 cm −1 ) is determined.

(iii)検量線の作成
検量線作成用試料として全カルボン酸の10mol%,30mol%,50mol%,70mol%,90mol%,100mol%をアンモニアで中和した部分架橋ポリアクリル酸を用いた。検量線試料を割断し、中心部分を顕微ATR法にて1試料につき5回実施。−COOH/−COOピーク面積比より検量線(5次多項式近似曲線)を作成した。割断はウルトラミクロトーム(Reichert社製 ULTRACUT N)にて行った。
(Iii) Preparation of calibration curve Partially crosslinked polyacrylic acid obtained by neutralizing 10 mol%, 30 mol%, 50 mol%, 70 mol%, 90 mol%, and 100 mol% of the total carboxylic acid with ammonia was used as a sample for preparing a calibration curve. The calibration curve sample is cleaved, and the central part is performed 5 times per sample by the microscopic ATR method. A calibration curve (5th order polynomial approximation curve) was created from the -COOH / -COO - peak area ratio. The cleaving was performed with an ultramicrotome (ULTRACUT N manufactured by Reichert).

(iv)サンプルの測定
検量線試料と同様に測定を行った。測定試料の粒子径は300〜700μmであった。樹脂体外表面はATR法で直接測定し、樹脂体中心部はウルトラミクロトームにて割断を行ってからATR法にて測定を行った。樹脂体外表面は1試料につき3回、樹脂体中心部は1試料につき5回測定を行い、その平均値を測定結果とした。
(Iv) Sample measurement Measurement was performed in the same manner as the calibration curve sample. The particle diameter of the measurement sample was 300 to 700 μm. The outer surface of the resin body was directly measured by the ATR method, and the central portion of the resin body was cleaved by an ultramicrotome and then measured by the ATR method. The outer surface of the resin body was measured 3 times per sample, and the central part of the resin body was measured 5 times per sample, and the average value was taken as the measurement result.

(2)スキン構造の幅の測定;IRイメージング測定法
(i)前処理
粒径300〜500μmの樹脂体をウルトラミクロトーム(Reichert社製 ULTRACUT N)にて樹脂体の中心部分を測定できるように割断し、厚さ約2μmに切片を作成した。この切片をNaCl結晶板上に平滑に固定し、顕微IRイメージング測定装置にセットした。
(ii)測定装置
IRイメージング測定はPerkin Elmer社製 Spot−Lightを用い、顕微透過法にて行った。
(2) Measurement of the width of the skin structure; IR imaging measurement method (i) Pretreatment Cleaving a resin body having a particle size of 300 to 500 μm so that the central part of the resin body can be measured with an ultramicrotome (ULTRACUT N manufactured by Reichert) Then, a section was prepared to a thickness of about 2 μm. This section was fixed smoothly on a NaCl crystal plate and set in a microscopic IR imaging measurement apparatus.
(Ii) Measuring device IR imaging measurement was performed by a microscopic transmission method using Spot-Light manufactured by Perkin Elmer.

(iii)測定条件
測定スポット径:6.25×6.25μm、
積算回数:4回、
測定雰囲気:Dry Air、
前処理後、30分以内に測定を行った。
(Iii) Measurement conditions Measurement spot diameter: 6.25 × 6.25 μm,
Integration count: 4 times
Measurement atmosphere: Dry Air,
The measurement was performed within 30 minutes after the pretreatment.

(iv)IRスペクトル解析
測定によって得られたスペクトルデータから1695cm−1(カルボン酸νC=0 ベースライン1774〜1616cm−1)および1558cm−1(カルボキシレートνCOO ベースライン1616〜1500cm−1)のピーク面積比(1695/1558cm−1)を計算し、Total吸光度イメージをBand Raitoイメージへ変換し、測定サンプルの外表面が全て内部よりも中和率が低いことを確認した。また、このBand Raitoイメージを断面方向でラインプロファイルをとり、表面層のBand Raito値より40%下がった点までの幅を測定し、スキン構造の幅とした。
Peak of - (baseline 1616~1500Cm -1-carboxylate νCOO) (iv) 1695cm from the spectral data obtained by IR spectrum analysis measurement -1 (carboxylic acid νC = 0 Baseline 1774~1616Cm -1) and 1558Cm -1 The area ratio (1695/1558 cm −1 ) was calculated, and the total absorbance image was converted into a Band Radio image, and it was confirmed that the neutralization rate of the outer surface of all the measurement samples was lower than that of the inner part. In addition, a line profile was taken from the Band Radio image in the cross-sectional direction, and the width up to a point 40% lower than the Band Radio value of the surface layer was measured to obtain the width of the skin structure.

(3)吸水性能測定方法;加圧下吸水法
底面に250メッシュのナイロン網を貼ったアクリル製の円筒形器具(外径35.0mm、内径24.5mm、高さ30mm、重さ D(g))に、吸水性樹脂 E(g)(約0.16g)を均一になるように入れ、重りとして0.0psiでは何ものせないが、0.3psiでは99.3g、0.8psiでは278.3gの分銅(外径24.5mm)をのせる。SUS製シャーレ(内径120mm)に生理食塩水を60cc入れ、円筒形器具を中に1時間置く。所定時間経過後、紙製タオルにて水切りを行い、天秤で器具全体の重量F(g)測定を行う。吸水倍率は次式にて求める。
吸水倍率(g/g)=(F(g)−D(g)−分銅の重さ(g))/E(g)
(3) Water absorption performance measurement method; water absorption method under pressure Cylindrical instrument made of acrylic with a 250 mesh nylon net on the bottom (outer diameter 35.0 mm, inner diameter 24.5 mm, height 30 mm, weight D (g) ), Water-absorbing resin E (g) (about 0.16 g) is uniformly added, and the weight cannot be anything at 0.0 psi, but 99.3 g at 0.3 psi and 278. A 3 g weight (outer diameter 24.5 mm) is placed. 60 cc of physiological saline is placed in a SUS petri dish (inner diameter: 120 mm), and a cylindrical instrument is placed in it for 1 hour. After a predetermined period of time, drain water with a paper towel, and measure the weight F (g) of the entire instrument with a balance. The water absorption ratio is obtained by the following formula.
Water absorption ratio (g / g) = (F (g) −D (g) −weight of weight (g)) / E (g)

(4)吸水性能測定方法;Tea bag法
不織布製のティーバック式袋(7×9cm)に吸水性樹脂A(g)(約0.5g)を均一に入れ、液温25℃の生理食塩水500ccに1時間浸漬する。所定時間後にティーバック式袋を引き上げ、10分間自然に水切りを行った後にティーバック式袋の重量B(g)を測定する。ブランクとして同様の操作を、吸水性樹脂を加えずにティーバック式袋のみで行い、重量C(g)を計測する。吸水倍率を次式より求める。
吸水倍率(g/g)=(B(g)−C(g))/A(g)
(4) Water-absorbing performance measuring method: Tea bag method Water-absorbing resin A (g) (about 0.5 g) is uniformly placed in a non-woven teabag bag (7 × 9 cm), and physiological saline at a liquid temperature of 25 ° C. Immerse in 500 cc for 1 hour. After a predetermined time, the tea bag bag is pulled up and drained naturally for 10 minutes, and then the weight B (g) of the tea bag bag is measured. The same operation as a blank is performed using only a tea bag bag without adding a water-absorbent resin, and the weight C (g) is measured. The water absorption ratio is obtained from the following formula.
Water absorption magnification (g / g) = (B (g) -C (g)) / A (g)

(製造例1)
(アクリル酸の中和によるアクリル酸アンモニウムの調製)
アクリル酸は和光純薬製、試薬特級品を使用した。試薬アクリル酸100gを水91.02gに溶解した。この水溶液を氷浴にて冷却し、液温30℃以下に保ちながら、25重量%のアンモニア水溶液117.94gを攪拌しながら徐々に加え40重量%のアクリル酸アンモニウム水溶液を得た。
(Production Example 1)
(Preparation of ammonium acrylate by neutralization of acrylic acid)
Acrylic acid manufactured by Wako Pure Chemical Industries, Ltd. was used as a reagent special grade. 100 g of reagent acrylic acid was dissolved in 91.02 g of water. This aqueous solution was cooled in an ice bath, and while maintaining the liquid temperature at 30 ° C. or lower, 117.94 g of a 25 wt% aqueous ammonia solution was gradually added with stirring to obtain a 40 wt% aqueous ammonium acrylate solution.

(製造例2)
(アクリルニトリルの加水分解によるアクリル酸アンモニウムの調製)
(1)生体触媒の調製
ニトリラーゼ活性を有するアシネトバクター エスピー AK226(FERM BP−2451)を塩化ナトリウム0.1%、リン酸2水素カリウム0.1%、硫酸マグネシウム7水和物0.05%、硫酸鉄7水和物0.005%、硫酸マンガン5水和物0.005%、硫酸アンモニウム0.1%、硝酸カリウム0.1%(いずれも重量%)を含む水溶液をpH=7に調製した培地で、栄養源としてアセトニトリル0.5重量%を添加し、30℃で好気的に培養した。これを30mMリン酸バッファー(pH=7.0)にて洗浄し菌体懸濁液(乾燥菌体15重量%)を得た。続いてアクリルアミド、N,N’−メチレンビスアクリルアミド、5%N,N,N’,N’−テトラメチルエチレンジアミン水溶液、菌体懸濁液、30mMリン酸緩衝液の混合液に、2.5%過硫酸カリウム水溶液を混合して重量物を得た。最終的な組成は、乾燥菌体濃度3%、30mMリン酸バッファー(pH=7)52%、アクリルアミド18%、メチレンビスアクリルアミド1%、5%N,N,N’,N’−テトラメチルエチレンジアミン水溶液12%、2.5%過硫酸カリウム水溶液14%(何れも重量%)とした。該重合物を約1×3×3mm角の粒子に裁断し固定化菌体を得た。この固定化菌体を30mMリン酸バッファー(pH=7)で洗浄し固定化菌体触媒(以下生体触媒)を調製した。
(Production Example 2)
(Preparation of ammonium acrylate by hydrolysis of acrylonitrile)
(1) Preparation of biocatalyst Acinetobacter sp. AK226 (FERM BP-2451) having nitrilase activity is 0.1% sodium chloride, 0.1% potassium dihydrogen phosphate, 0.05% magnesium sulfate heptahydrate, sulfuric acid In a medium prepared by adjusting an aqueous solution containing iron heptahydrate 0.005%, manganese sulfate pentahydrate 0.005%, ammonium sulfate 0.1%, potassium nitrate 0.1% (both wt%) to pH = 7. Then, 0.5% by weight of acetonitrile was added as a nutrient source and cultured aerobically at 30 ° C. This was washed with a 30 mM phosphate buffer (pH = 7.0) to obtain a cell suspension (dry cell 15% by weight). Subsequently, 2.5% in a mixed solution of acrylamide, N, N′-methylenebisacrylamide, 5% N, N, N ′, N′-tetramethylethylenediamine aqueous solution, cell suspension, and 30 mM phosphate buffer. A potassium persulfate aqueous solution was mixed to obtain a heavy product. The final composition is 3% dry cell concentration, 52% 30 mM phosphate buffer (pH = 7), 18% acrylamide, 1% methylenebisacrylamide, 5% N, N, N ′, N′-tetramethylethylenediamine. An aqueous solution of 12% and a 2.5% potassium persulfate aqueous solution of 14% (both by weight) were used. The polymer was cut into about 1 × 3 × 3 mm square particles to obtain immobilized cells. The immobilized cells were washed with 30 mM phosphate buffer (pH = 7) to prepare an immobilized cell catalyst (hereinafter referred to as biocatalyst).

(2)生体触媒による加水分解
内容積500mlの三角フラスコに蒸留水400gを入れ、これに前述の生体触媒1g(乾燥菌体0.03gに相当)を金網かごに入れたものを液中にセットし、ゴム栓で封をした後、恒温水槽に浸けて内温を20℃に保ち、スターラーで攪拌した。
アクリロニトリルを間欠的に2重量%分フィード(アクリロニトリル濃度は0.5重量%以上で管理)し、アクリル酸アンモニウムの蓄積反応を行ったところ30重量%まで蓄積できた。
得られたアクリル酸アンモニウム水溶液は無色透明であった。また、同一条件で反応液を5L作製し、UF膜(旭化成ペンシル型モジュールSIP−0013)による精製操作を行ったところ、目詰まり等の現象は見られず、全液を処理することができ、高純度30重量%アクリル酸アンモニウム水溶液を得た。この水溶液にメトキシキノン200ppm加え、遮光減圧下にて40重量%まで濃縮し重合に使用した。
(2) Hydrolysis with a biocatalyst 400 g of distilled water is put into an Erlenmeyer flask with an internal volume of 500 ml, and 1 g of the above biocatalyst (corresponding to 0.03 g of dry cells) is put in a wire mesh basket in the liquid. After sealing with a rubber stopper, the inner temperature was kept at 20 ° C. by immersion in a constant temperature water bath, and the mixture was stirred with a stirrer.
Acrylonitrile was intermittently fed in an amount of 2% by weight (acrylonitrile concentration was controlled at 0.5% by weight or more), and an accumulation reaction of ammonium acrylate was carried out, and 30% by weight could be accumulated.
The obtained aqueous solution of ammonium acrylate was colorless and transparent. In addition, when 5 L of the reaction solution was prepared under the same conditions and purified using a UF membrane (Asahi Kasei Pencil type module SIP-0013), no clogging or other phenomena were observed, and the entire solution could be processed. A highly pure 30% by weight ammonium acrylate aqueous solution was obtained. To this aqueous solution, 200 ppm of methoxyquinone was added, and concentrated to 40% by weight under light-shielding reduced pressure, and used for polymerization.

(製造例3)
(アクリル酸の中和によるアクリル酸ナトリウムの調製)
アクリル酸は和光純薬製、試薬特級品を使用した。試薬アクリル酸100gを水81.6gに溶解した。この水溶液を氷浴にて冷却し、液温30℃以下に保ちながら、40.5重量%NaOH水溶液137.1gを攪拌しながら徐々に加え40重量%のアクリル酸ナトリウム水溶液を得た。
(Production Example 3)
(Preparation of sodium acrylate by neutralization of acrylic acid)
Acrylic acid manufactured by Wako Pure Chemical Industries, Ltd. was used as a reagent special grade. 100 g of reagent acrylic acid was dissolved in 81.6 g of water. This aqueous solution was cooled in an ice bath, and while maintaining the liquid temperature at 30 ° C. or lower, 137.1 g of 40.5 wt% NaOH aqueous solution was gradually added with stirring to obtain 40 wt% sodium acrylate aqueous solution.

実施例1
300mlセパラブルフラスコに製造例1の40重量%アクリル酸アンモニウム水溶液を90g、N,N’−メチレンビスアクリルアミドを0.0187g添加する。フラスコは30℃に液温が保たれるようにウォーターバスに浴す。水溶液を窒素ガスでバブリングすることにより脱気し、反応系中を窒素置換した。次に42重量%グリセリン水溶液をシリンジにて0.86g添加、よく攪拌した後にそれぞれ1gの水に溶かした30重量%過酸化水素水溶液0.0917gとロンガリット0.0415gを添加し重合を開始する。内部温度は30℃から開始して反応開始10分で100℃まで上昇する。その後、内部温度が70℃に保たれるように水浴にて3時間加熱する。その後、セパラフラスコよりゲルを取り出し粗解砕を行ってから100℃にて真空乾燥機を用いて乾燥させる。乾燥終了後、ホモジナイザーにて粉砕し、篩い分けにて100〜850μmを回収する。これをイナートオーブンにて窒素雰囲気下で15分間、180℃で加熱する。以上の様にして得られた吸水性樹脂体を吸水性樹脂体(1)とする。
吸水性樹脂体(1)の樹脂体外表面の中和率と樹脂体中心部の中和率を測定した結果と吸水測定の結果を表1に示す。
Example 1
To a 300 ml separable flask, 90 g of 40 wt% ammonium acrylate aqueous solution of Production Example 1 and 0.0187 g of N, N′-methylenebisacrylamide are added. The flask is bathed in a water bath so that the liquid temperature is maintained at 30 ° C. The aqueous solution was deaerated by bubbling with nitrogen gas, and the reaction system was purged with nitrogen. Next, 0.86 g of 42 wt% glycerin aqueous solution was added with a syringe, and after stirring well, 0.0917 g of 30 wt% aqueous hydrogen peroxide solution and 0.0415 g of Rongalite dissolved in 1 g of water were added to initiate polymerization. The internal temperature starts from 30 ° C and rises to 100 ° C in 10 minutes from the start of the reaction. Then, it heats in a water bath for 3 hours so that internal temperature may be maintained at 70 degreeC. Then, after taking out a gel from a Separa flask and carrying out rough crushing, it is made to dry at 100 degreeC using a vacuum dryer. After drying, the mixture is pulverized with a homogenizer, and 100 to 850 μm is collected by sieving. This is heated in an inert oven at 180 ° C. for 15 minutes in a nitrogen atmosphere. The water absorbent resin body obtained as described above is referred to as a water absorbent resin body (1).
Table 1 shows the results of measuring the neutralization rate of the outer surface of the resin body of the water absorbent resin body (1) and the neutralization ratio of the resin body center and the results of water absorption measurement.

実施例2
300mlセパラブルフラスコに製造例1の40重量%アクリル酸アンモニウム水溶液を90g、N,N’−メチレンビスアクリルアミドを0.0187g添加する。フラスコは30℃に液温が保たれるようにウォーターバスに浴す。水溶液を窒素ガスでバブリングすることにより脱気し、反応系中を窒素置換した。次に42重量%グリセリン水溶液をシリンジにて0.86g添加、よく攪拌した後にそれぞれ1gの水に溶かした30重量%過酸化水素水溶液0.0917gとロンガリット0.0415gを添加し重合を開始する。内部温度は30℃から開始して反応開始10分で70℃まで上昇する。その後、内部温度が70℃に保たれるように水浴にて3時間加熱する。その後、セパラフラスコよりゲルを取り出し粗解砕を行ってから100℃にて真空乾燥機を用いて乾燥させる。乾燥終了後、ホモジナイザーにて粉砕し、篩い分けにて100〜850μmを回収する。これをイナートオーブンにて窒素雰囲気下で30分間、170℃で加熱する。このようにして得られた吸水性樹脂体を吸水性樹脂体(2)とする。
吸水性樹脂体(2)の樹脂体外表面の中和率と樹脂体中心部の中和率を測定した結果とIRイメージングにより求めたスキン構造幅の測定結果、及び吸水測定の結果を表1に示す。また、IRイメージングを行ったサンプルの顕微鏡写真を図1に、IRイメージング測定において図1の破線に沿って行った1695/1558cm−1ピーク面積比を数値化したラインプロファイルの結果を図2に示す。
Example 2
To a 300 ml separable flask, 90 g of 40 wt% ammonium acrylate aqueous solution of Production Example 1 and 0.0187 g of N, N′-methylenebisacrylamide are added. The flask is bathed in a water bath so that the liquid temperature is maintained at 30 ° C. The aqueous solution was deaerated by bubbling with nitrogen gas, and the reaction system was purged with nitrogen. Next, 0.86 g of 42 wt% glycerin aqueous solution was added with a syringe, and after stirring well, 0.0917 g of 30 wt% aqueous hydrogen peroxide solution and 0.0415 g of Rongalite dissolved in 1 g of water were added to initiate polymerization. The internal temperature starts from 30 ° C and rises to 70 ° C in 10 minutes from the start of the reaction. Then, it heats in a water bath for 3 hours so that internal temperature may be maintained at 70 degreeC. Then, after taking out a gel from a Separa flask and carrying out rough crushing, it is made to dry at 100 degreeC using a vacuum dryer. After drying, the mixture is pulverized with a homogenizer, and 100 to 850 μm is collected by sieving. This is heated at 170 ° C. in an inert oven for 30 minutes under a nitrogen atmosphere. The water absorbent resin body thus obtained is referred to as a water absorbent resin body (2).
Table 1 shows the results of measuring the neutralization rate of the outer surface of the resin body of the water absorbent resin body (2) and the neutralization ratio of the resin body center, the skin structure width obtained by IR imaging, and the results of water absorption measurement. Show. Moreover, the micrograph of the sample which performed IR imaging is shown in FIG. 1, and the result of the line profile which digitized 1695 / 1558cm -1 peak area ratio performed along the broken line of FIG. 1 in IR imaging measurement is shown in FIG. .

実施例3
300mlフラスコに試薬アクリル酸(和光純薬製、試薬特級品)97.66g、水126.55g、25重量%アンモニア水81.35gを氷冷しながら、液温が30℃を越えないようにゆっくり添加した。さらに活性炭7.8gを加え遮光下1時間攪拌し、活性炭を濾別除去したものを90%中和アクリル酸アンモニウム水溶液とした。
300mlセパラブルフラスコに90%中和アクリル酸アンモニウム水溶液を90g、N,N‘−メチレンビスアクリルアミドを0.0198g添加する。フラスコは30℃に液温が保たれるようにウォーターバスに浴す。水溶液を窒素ガスでバブリングすることにより脱気し、反応系中を窒素置換した。次に42重量%グリセリン水溶液をシリンジにて0.86g添加、よく攪拌した後にそれぞれ1gの水に溶かした30重量%過酸化水素水溶液 0.0953gとロンガリット 0.0419gを添加し重合を開始する。内部温度は30℃から開始して反応開始5分後に102℃まで上昇した。その後、内部温度が70℃に保たれるように水浴にて3時間加熱する。その後、セパラフラスコよりゲルを取り出し粗解砕を行ってから100℃にて4時間、窒素雰囲気のイナートオーブンを用いて乾燥させる。乾燥終了後、ホモジナイザーにて粉砕し、篩い分けにて100〜850μmを回収する。これをイナートオーブンにて窒素雰囲気下で30分間、170℃で加熱する。このようにして得られた吸水性樹脂体を吸水性樹脂体(3)とする。
吸水性樹脂体(3)の樹脂体外表面の中和率と樹脂体中心部の中和率を測定した結果と吸水測定の結果を表1に示す。
Example 3
In a 300 ml flask, 97.66 g of reagent acrylic acid (manufactured by Wako Pure Chemical, special grade reagent), 126.55 g of water, and 81.35 g of 25 wt% aqueous ammonia are slowly cooled so that the liquid temperature does not exceed 30 ° C. Added. Further, 7.8 g of activated carbon was added, stirred for 1 hour under light shielding, and the activated carbon was removed by filtration to obtain a 90% neutralized ammonium acrylate aqueous solution.
To a 300 ml separable flask, 90 g of 90% neutralized ammonium acrylate aqueous solution and 0.0198 g of N, N′-methylenebisacrylamide are added. The flask is bathed in a water bath so that the liquid temperature is maintained at 30 ° C. The aqueous solution was deaerated by bubbling with nitrogen gas, and the reaction system was purged with nitrogen. Next, 0.86 g of 42 wt% glycerin aqueous solution was added with a syringe, and after stirring well, 0.0953 g of 30 wt% aqueous hydrogen peroxide solution dissolved in 1 g of water and 0.0419 g of Rongalite were added to initiate polymerization. The internal temperature started from 30 ° C. and increased to 102 ° C. 5 minutes after the start of the reaction. Then, it heats in a water bath for 3 hours so that internal temperature may be maintained at 70 degreeC. Thereafter, the gel is taken out from the Separa flask and roughly crushed and then dried at 100 ° C. for 4 hours using an inert oven in a nitrogen atmosphere. After drying, the mixture is pulverized with a homogenizer, and 100 to 850 μm is collected by sieving. This is heated at 170 ° C. in an inert oven for 30 minutes under a nitrogen atmosphere. The water absorbent resin body thus obtained is designated as a water absorbent resin body (3).
Table 1 shows the results of measuring the neutralization rate of the outer surface of the resin body of the water absorbent resin body (3) and the neutralization ratio of the central portion of the resin body and the results of water absorption measurement.

実施例4
300mlフラスコに試薬アクリル酸(和光純薬製、試薬特級品)88.64g、水107.05g、25重量%アンモニア水57.43gを氷冷しながら、液温が30℃を越えないようにゆっくり添加した。さらに活性炭7.1gを加え遮光下1時間攪拌し、活性炭を濾別除去したものを70%中和アクリル酸アンモニウム水溶液とした。
300mlセパラブルフラスコに70%中和アクリル酸アンモニウム水溶液を90g、N,N’−メチレンビスアクリルアミドを0.0198g添加する。フラスコは30℃に液温が保たれるようにウォーターバスに浴す。水溶液を窒素ガスでバブリングすることにより脱気し、反応系中を窒素置換した。次に42重量%グリセリン水溶液をシリンジにて0.86g添加、よく攪拌した後にそれぞれ1gの水に溶かした30重量%過酸化水素水溶液 0.0953gとロンガリット 0.0419gを添加し重合を開始する。内部温度は30℃から開始して反応開始5分後に105℃まで上昇した。その後、内部温度が70℃に保たれるように水浴にて3時間加熱する。その後、セパラフラスコよりゲルを取り出し粗解砕を行ってから100℃にて4時間、窒素雰囲気のイナートオーブンを用いて乾燥させる。乾燥終了後、ホモジナイザーにて粉砕し、篩い分けにて100〜850μmを回収する。これをイナートオーブンにて窒素雰囲気下で20分間、170℃で加熱する。このようにして得られた吸水性樹脂体を吸水性樹脂体(4)とする。
吸水性樹脂体(4)の樹脂体外表面の中和率と樹脂体中心部の中和率を測定した結果と吸水測定の結果を表1に示す。
Example 4
In a 300 ml flask, 88.64 g of reagent acrylic acid (manufactured by Wako Pure Chemicals, special grade reagent), 107.05 g of water, and 57.43 g of 25 wt% ammonia water are slowly cooled so that the liquid temperature does not exceed 30 ° C. Added. Further, 7.1 g of activated carbon was added, stirred for 1 hour under light shielding, and the activated carbon was removed by filtration to obtain a 70% neutralized ammonium acrylate aqueous solution.
To a 300 ml separable flask, 90 g of 70% neutralized ammonium acrylate aqueous solution and 0.0198 g of N, N′-methylenebisacrylamide are added. The flask is bathed in a water bath so that the liquid temperature is maintained at 30 ° C. The aqueous solution was deaerated by bubbling with nitrogen gas, and the reaction system was purged with nitrogen. Next, 0.86 g of 42 wt% glycerin aqueous solution was added with a syringe, and after stirring well, 0.0953 g of 30 wt% aqueous hydrogen peroxide solution dissolved in 1 g of water and 0.0419 g of Rongalite were added to initiate polymerization. The internal temperature started from 30 ° C and increased to 105 ° C 5 minutes after the start of the reaction. Then, it heats in a water bath for 3 hours so that internal temperature may be maintained at 70 degreeC. Thereafter, the gel is taken out from the Separa flask and roughly crushed and then dried at 100 ° C. for 4 hours using an inert oven in a nitrogen atmosphere. After drying, the mixture is pulverized with a homogenizer, and 100 to 850 μm is collected by sieving. This is heated in an inert oven at 170 ° C. for 20 minutes in a nitrogen atmosphere. The water absorbent resin body thus obtained is referred to as a water absorbent resin body (4).
Table 1 shows the results of measuring the neutralization rate of the outer surface of the resin body of the water absorbent resin body (4) and the neutralization ratio of the resin body center portion, and the results of water absorption measurement.

実施例5
300mlセパラブルフラスコにアクリル酸19.6g、水15.2g、28重量%のアンモニア水溶液8.7gを添加する。フラスコは30℃に液温が保たれるようにウォーターバスに浴す。水溶液を窒素ガスでバブリングすることにより脱酸素し、反応系中を窒素置換した。次に64重量%グリセリン水溶液を3.1gシリンジにて添加、よく攪拌した後、それぞれ1gの水に溶かした過硫酸アンモニウム 0.0413gとL−アスコルビン酸 0.0005gを添加し重合を開始する。内部温度は30℃から開始して反応開始から5分で75℃まで上昇する。最高到達温度記してから5分後に内部温度が75℃に保たれるように水浴にて3時間加熱する。所定時間経過後、セパラブルフラスコよりゲルを取り出し粗解砕を行ってから100℃にて真空乾燥機を用いて乾燥させる。乾燥終了後、ホモジナイザーにて粉砕し、篩い分けにて100〜850μmを回収する。これをイナートオーブンにて窒素雰囲気下で5時間、150℃で加熱する。以上のようにして得られた吸水性樹脂体を吸水性樹脂体(5)とする。吸水性樹脂体(5)の吸水測定の結果を表2に示す。
Example 5
Add 19.6 g of acrylic acid, 15.2 g of water, and 8.7 g of 28 wt% aqueous ammonia solution to a 300 ml separable flask. The flask is bathed in a water bath so that the liquid temperature is maintained at 30 ° C. The aqueous solution was deoxygenated by bubbling with nitrogen gas, and the reaction system was purged with nitrogen. Next, after adding a 64 wt% glycerin aqueous solution with a 3.1 g syringe and stirring well, 0.0413 g of ammonium persulfate dissolved in 1 g of water and 0.0005 g of L-ascorbic acid are added to initiate polymerization. The internal temperature starts from 30 ° C and increases to 75 ° C in 5 minutes from the start of the reaction. Heat in a water bath for 3 hours so that the internal temperature is maintained at 75 ° C. 5 minutes after recording the maximum temperature. After a predetermined time has elapsed, the gel is taken out from the separable flask and roughly crushed, and then dried at 100 ° C. using a vacuum dryer. After drying, the mixture is pulverized with a homogenizer, and 100 to 850 μm is collected by sieving. This is heated at 150 ° C. in an inert oven for 5 hours under a nitrogen atmosphere. The water absorbent resin body obtained as described above is referred to as a water absorbent resin body (5). Table 2 shows the results of water absorption measurement of the water absorbent resin body (5).

実施例6
300mlセパラブルフラスコに製造例1の40重量%アクリル酸アンモニウム水溶液を90g、エチレングリコールジメタクリレートを0.0250g添加する。フラスコは30℃に液温が保たれるようにウォーターバスに浴す。水溶液を窒素ガスでバブリングすることにより脱酸素し、反応系中を窒素置換した。次に50重量%グリセリン水溶液を2.1gシリンジにて添加、よく攪拌した後、それぞれ1gの水に溶かした30重量%過酸化水素水溶液 0.0917gとロンガリット 0.0415gを添加し重合を開始する。内部温度は30℃から開始して反応開始から10分で100℃まで上昇する。最高到達温度記してから5分後に内部温度が75℃に保たれるように水浴にて3時間加熱する。所定時間経過後、セパラブルフラスコよりゲルを取り出し粗解砕を行ってから100℃にて真空乾燥機を用いて乾燥させる。乾燥終了後、ホモジナイザーにて粉砕し、篩い分けにて100〜850μmを回収する。これをイナートオーブンにて窒素雰囲気下で60分間、150℃で加熱する。以上のようにして得られた吸水性樹脂体を吸水性樹脂体(6)とする。吸水性樹脂体(6)の吸水測定の結果を表2に示す。
Example 6
To a 300 ml separable flask, 90 g of 40% by weight ammonium acrylate aqueous solution of Preparation Example 1 and 0.0250 g of ethylene glycol dimethacrylate are added. The flask is bathed in a water bath so that the liquid temperature is maintained at 30 ° C. The aqueous solution was deoxygenated by bubbling with nitrogen gas, and the reaction system was purged with nitrogen. Next, after adding 50 wt% glycerin aqueous solution with a 2.1 g syringe and stirring well, 0.0917 g of 30 wt% hydrogen peroxide aqueous solution and 0.0415 g of Rongalite each dissolved in 1 g of water are added to initiate polymerization. . The internal temperature starts from 30 ° C and increases to 100 ° C in 10 minutes from the start of the reaction. Heat in a water bath for 3 hours so that the internal temperature is maintained at 75 ° C. 5 minutes after recording the maximum temperature. After a predetermined time has elapsed, the gel is taken out from the separable flask and roughly crushed, and then dried at 100 ° C. using a vacuum dryer. After drying, the mixture is pulverized with a homogenizer, and 100 to 850 μm is collected by sieving. This is heated in an inert oven at 150 ° C. for 60 minutes in a nitrogen atmosphere. The water absorbent resin body obtained as described above is referred to as a water absorbent resin body (6). Table 2 shows the results of water absorption measurement of the water absorbent resin body (6).

実施例7
300mlセパラブルフラスコに製造例1の40重量%アクリル酸アンモニウム水溶液を90g、エチレングリコールジメタクリレートを0.0248g添加する。フラスコは30℃に液温が保たれるようにウォーターバスに浴す。水溶液を窒素ガスでバブリングすることにより脱酸素し、反応系中を窒素置換した。次に50重量%エチレングリコール水溶液を0.72gシリンジにて添加、よく攪拌した後、それぞれ1gの水に溶かした過硫酸アンモニウム 0.0615gとL−アスコルビン酸 0.0007gを添加し重合を開始する。内部温度は30℃から開始して反応開始から10分で70℃まで上昇する。最高到達温度記してから5分後に内部温度が75℃に保たれるように水浴にて3時間加熱する。所定時間経過後、セパラブルフラスコよりゲルを取り出し粗解砕を行ってから100℃にて真空乾燥機を用いて乾燥させる。乾燥終了後、ホモジナイザーにて粉砕し、篩い分けにて100〜850μmを回収する。これをイナートオーブンにて窒素雰囲気下で30分間、170℃で加熱する。以上のようにして得られた吸水性樹脂体を吸水性樹脂体(7)とする。吸水性樹脂体(7)の吸水測定の結果を表2に示す。
Example 7
To a 300 ml separable flask, 90 g of 40 wt% ammonium acrylate aqueous solution of Production Example 1 and 0.0248 g of ethylene glycol dimethacrylate are added. The flask is bathed in a water bath so that the liquid temperature is maintained at 30 ° C. The aqueous solution was deoxygenated by bubbling with nitrogen gas, and the reaction system was purged with nitrogen. Next, after adding a 50 wt% ethylene glycol aqueous solution with a 0.72 g syringe and stirring well, 0.0615 g of ammonium persulfate and 0.0007 g of L-ascorbic acid dissolved in 1 g of water are added to initiate polymerization. The internal temperature starts from 30 ° C and increases to 70 ° C in 10 minutes from the start of the reaction. Heat in a water bath for 3 hours so that the internal temperature is maintained at 75 ° C. 5 minutes after recording the maximum temperature. After a predetermined time has elapsed, the gel is taken out from the separable flask and roughly crushed, and then dried at 100 ° C. using a vacuum dryer. After drying, the mixture is pulverized with a homogenizer, and 100 to 850 μm is collected by sieving. This is heated at 170 ° C. in an inert oven for 30 minutes under a nitrogen atmosphere. The water absorbent resin body thus obtained is referred to as a water absorbent resin body (7). Table 2 shows the results of water absorption measurement of the water absorbent resin body (7).

実施例8
製造例2の生体触媒により得られたアクリル酸アンモニウム40重量%水溶液90gに、架橋剤としてN,N’−メチレンビスアクリルアミド0.0187gを加え溶解した。この溶液を300mlセパラブルフラスコに移し、攪拌しながら30℃で30分間窒素パージを行った。ここにジエチレングリコール0.414gを加え、さらにロンガリット0.0414gを加え、続いて30重量%の過酸化水素水溶液0.092gを加え重合を開始した。開始から5分後から温度が上昇し、最高温度は100℃まで達した。1時間重合を行った後、含水ゲルを5mm角程度に解砕し、窒素雰囲気過のイナートオーブン中で100℃で2時間乾燥した。乾燥ポリマーをホモジナイザーで粉砕後、イナートオーブン中100℃でさらに2時間乾燥した。乾燥後のポリマーを106〜850μmに分級した。その後170℃で30分間加熱を行った。以上のようにして得られた吸水性樹脂体を吸水性樹脂体(8)とする。吸水性樹脂体(8)の吸水測定の結果を表2に示す。
Example 8
0.0187 g of N, N′-methylenebisacrylamide was added as a crosslinking agent to 90 g of a 40 wt% ammonium acrylate aqueous solution obtained by the biocatalyst of Production Example 2 and dissolved. This solution was transferred to a 300 ml separable flask and purged with nitrogen at 30 ° C. for 30 minutes while stirring. 0.414 g of diethylene glycol was added thereto, 0.0414 g of Rongalite was further added, and 0.092 g of a 30 wt% aqueous hydrogen peroxide solution was subsequently added to initiate polymerization. The temperature increased from 5 minutes after the start, and the maximum temperature reached 100 ° C. After polymerization for 1 hour, the hydrogel was crushed to about 5 mm square and dried at 100 ° C. for 2 hours in an inert oven with a nitrogen atmosphere. The dried polymer was pulverized with a homogenizer, and further dried at 100 ° C. in an inert oven for 2 hours. The polymer after drying was classified to 106 to 850 μm. Thereafter, heating was performed at 170 ° C. for 30 minutes. The water absorbent resin body obtained as described above is referred to as a water absorbent resin body (8). Table 2 shows the results of water absorption measurement of the water absorbent resin body (8).

実施例9
製造例2の生体触媒により得られたアクリル酸アンモニウム40重量%水溶液90gに、架橋剤としてN,N’−メチレンビスアクリルアミド0.0187gを加え溶解した。この溶液を300mlセパラブルフラスコに移し、攪拌しながら30℃で30分間窒素パージを行った。ここにトリエチレングリコール0.587gを加え、さらにロンガリット0.0414gを加え、続いて30重量%の過酸化水素水溶液0.092gを加え重合を開始した。開始から3分後から温度が上昇し、最高温度は105℃まで達した。1時間重合を行った後、含水ゲルを5mm角程度に解砕し、窒素雰囲気過のイナートオーブン中で100℃で2時間乾燥した。乾燥ポリマーをホモジナイザーで粉砕後、イナートオーブン中100℃でさらに2時間乾燥した。乾燥後のポリマーを106〜850μmに分級した。その後170℃で30分間加熱を行った。以上のようにして得られた吸水性樹脂体を吸水性樹脂体(9)とする。吸水性樹脂体(9)の吸水測定の結果を表2に示す。
Example 9
0.0187 g of N, N′-methylenebisacrylamide was added as a crosslinking agent to 90 g of a 40 wt% ammonium acrylate aqueous solution obtained by the biocatalyst of Production Example 2 and dissolved. This solution was transferred to a 300 ml separable flask and purged with nitrogen at 30 ° C. for 30 minutes while stirring. To this, 0.587 g of triethylene glycol was added, 0.0414 g of Rongalite was further added, and 0.092 g of a 30 wt% aqueous hydrogen peroxide solution was subsequently added to initiate polymerization. The temperature increased from 3 minutes after the start, and the maximum temperature reached 105 ° C. After polymerization for 1 hour, the hydrogel was crushed to about 5 mm square and dried at 100 ° C. for 2 hours in an inert oven with a nitrogen atmosphere. The dried polymer was pulverized with a homogenizer, and further dried at 100 ° C. in an inert oven for 2 hours. The polymer after drying was classified to 106 to 850 μm. Thereafter, heating was performed at 170 ° C. for 30 minutes. The water absorbent resin body obtained as described above is referred to as a water absorbent resin body (9). Table 2 shows the results of water absorption measurement of the water absorbent resin body (9).

実施例10
製造例2の生体触媒により得られたアクリル酸アンモニウム40重量%水溶液90gに、架橋剤としてN,N’−メチレンビスアクリルアミド0.0187gを加え溶解した。この溶液を300mlセパラブルフラスコに移し、攪拌しながら30℃で30分間窒素パージを行った。ここにエリスリトール0.263gを加え、さらにロンガリット0.0414gを加え、続いて30重量%の過酸化水素水溶液0.092gを加え重合を開始した。開始から1分後から温度が上昇し、最高温度は102℃まで達した。1時間重合を行った後、含水ゲルを5mm角程度に解砕し、窒素雰囲気過のイナートオーブン中で100℃で2時間乾燥した。乾燥ポリマーをホモジナイザーで粉砕後、イナートオーブン中100℃でさらに2時間乾燥した。乾燥後のポリマーを106〜850μmに分級した。その後170℃で30分間加熱を行った。以上のようにして得られた吸水性樹脂体を吸水性樹脂体(10)とする。吸水性樹脂体(10)の吸水測定の結果を表2に示す。
Example 10
0.0187 g of N, N′-methylenebisacrylamide was added as a crosslinking agent to 90 g of a 40 wt% ammonium acrylate aqueous solution obtained by the biocatalyst of Production Example 2 and dissolved. This solution was transferred to a 300 ml separable flask and purged with nitrogen at 30 ° C. for 30 minutes while stirring. 0.263 g of erythritol was added thereto, 0.0414 g of Rongalite was further added, and 0.092 g of a 30% by weight aqueous hydrogen peroxide solution was subsequently added to initiate polymerization. The temperature rose from 1 minute after the start, and the maximum temperature reached 102 ° C. After polymerization for 1 hour, the hydrogel was crushed to about 5 mm square and dried at 100 ° C. for 2 hours in an inert oven with a nitrogen atmosphere. The dried polymer was pulverized with a homogenizer, and further dried at 100 ° C. in an inert oven for 2 hours. The polymer after drying was classified to 106 to 850 μm. Thereafter, heating was performed at 170 ° C. for 30 minutes. The water absorbent resin body obtained as described above is designated as a water absorbent resin body (10). Table 2 shows the results of water absorption measurement of the water absorbent resin body (10).

実施例11
300mlフラスコに試薬アクリル酸(和光純薬製、試薬特級品)118.18g、水168.51g、30重量%のNaOH水溶液を16.03g、25重量%アンモニア水109.38gを氷冷しながら、液温が30℃を越えないようにゆっくり添加した。
300mlセパラブルフラスコに上記単量体水溶液を90g、N,N’−メチレンビスアクリルアミドを0.0378g添加する。フラスコは30℃に液温が保たれるようにウォーターバスに浴す。水溶液を窒素ガスでバブリングすることにより脱気し、反応系中を窒素置換した。次に42重量%グリセリン水溶液をシリンジにて0.86g添加、よく攪拌した後にそれぞれ1gの水に溶かした30重量%過酸化水素水溶液 0.0953gとロンガリット 0.0419gを添加し重合を開始する。内部温度は30℃から開始して反応開始5分後に105℃まで上昇した。その後、内部温度が70℃に保たれるように水浴にて3時間加熱する。その後、セパラフラスコよりゲルを取り出し粗解砕を行ってから100℃にて4時間、窒素雰囲気のイナートオーブンを用いて乾燥させる。乾燥終了後、ホモジナイザーにて粉砕し、篩い分けにて100〜850μmを回収する。これをイナートオーブンにて窒素雰囲気下で30分間、170℃で加熱する。このようにして得られた吸水性樹脂体を吸水性樹脂体(11)とする。
吸水性樹脂体(11)の吸水測定の結果を表2に示す。
Example 11
In a 300 ml flask, 118.18 g of reagent acrylic acid (manufactured by Wako Pure Chemicals, reagent special grade), 168.51 g of water, 16.03 g of 30% by weight NaOH aqueous solution and 109.38 g of 25% by weight ammonia water were cooled with ice. Slow addition was performed so that the liquid temperature did not exceed 30 ° C.
90 g of the monomer aqueous solution and 0.0378 g of N, N′-methylenebisacrylamide are added to a 300 ml separable flask. The flask is bathed in a water bath so that the liquid temperature is maintained at 30 ° C. The aqueous solution was deaerated by bubbling with nitrogen gas, and the reaction system was purged with nitrogen. Next, 0.86 g of 42 wt% glycerin aqueous solution was added with a syringe, and after stirring well, 0.0953 g of 30 wt% aqueous hydrogen peroxide solution dissolved in 1 g of water and 0.0419 g of Rongalite were added to initiate polymerization. The internal temperature started from 30 ° C and increased to 105 ° C 5 minutes after the start of the reaction. Then, it heats in a water bath for 3 hours so that internal temperature may be maintained at 70 degreeC. Thereafter, the gel is taken out from the Separa flask and roughly crushed and then dried at 100 ° C. for 4 hours using an inert oven in a nitrogen atmosphere. After drying, the mixture is pulverized with a homogenizer, and 100 to 850 μm is collected by sieving. This is heated at 170 ° C. in an inert oven for 30 minutes under a nitrogen atmosphere. The water absorbent resin body thus obtained is designated as a water absorbent resin body (11).
Table 2 shows the results of water absorption measurement of the water absorbent resin body (11).

比較例1
300mlセパラブルフラスコに40重量%のアクリル酸アンモニウム水溶液を171.13g、アクリル酸18.53gと水35.34gを加え、38重量%のアクリル酸アンモニウム/アクリル酸=75/25水溶液を得た。活性炭7.8gを加え遮光下1時間攪拌した。活性炭を濾別後、架橋剤としてトリメチロールプロパントリアクリレート0.0968gを加え溶解した。この溶液90gを300mlセパラブルフラスコに移し、攪拌しながら30℃で30分間窒素パージを行った。ここに亜硫酸水素ナトリウム0.018gを加え、続いて過硫酸アンモニウム0.0276gを加えた。1時間重合を行った後、ポリマーを5mm程度に粉砕し、窒素雰囲気のイナートオーブン中で150℃で1時間乾燥した。乾燥ポリマーをホモジナイザーで粉砕後106μm〜850μmに分級した。分級したポリマー100部に、プロピレングリコール2部、水3部、イソプロピルアルコール30部を混合した後、150℃で60分間加熱処理した。以上の様にして得られた樹脂体を比較吸水性樹脂体(1)とする。
比較吸水性樹脂体(1)の樹脂体外表面の中和率と樹脂体中心部の中和率を測定した結果とIRイメージングにより求めたスキン構造幅の測定結果、及び吸水測定の結果を表1に示す。
Comparative Example 1
To a 300 ml separable flask, 171.13 g of 40 wt% ammonium acrylate aqueous solution, 18.53 g of acrylic acid and 35.34 g of water were added to obtain 38 wt% ammonium acrylate / acrylic acid = 75/25 aqueous solution. 7.8 g of activated carbon was added and stirred for 1 hour under light shielding. After the activated carbon was filtered off, 0.0968 g of trimethylolpropane triacrylate was added as a crosslinking agent and dissolved. 90 g of this solution was transferred to a 300 ml separable flask and purged with nitrogen at 30 ° C. for 30 minutes while stirring. To this was added 0.018 g of sodium bisulfite, followed by 0.0276 g of ammonium persulfate. After polymerization for 1 hour, the polymer was pulverized to about 5 mm and dried at 150 ° C. for 1 hour in an inert oven in a nitrogen atmosphere. The dried polymer was pulverized with a homogenizer and classified to 106 μm to 850 μm. After mixing 100 parts of the classified polymer with 2 parts of propylene glycol, 3 parts of water and 30 parts of isopropyl alcohol, the mixture was heat-treated at 150 ° C. for 60 minutes. The resin body obtained as described above is referred to as a comparative water absorbent resin body (1).
Table 1 shows the results of measuring the neutralization rate of the outer surface of the resin body of the comparative water-absorbent resin body (1) and the neutralization ratio of the central portion of the resin body, the measurement results of the skin structure width obtained by IR imaging, and the results of water absorption measurement. Shown in

比較例2
試薬アクリル酸(和光純薬製、試薬特級品)28.32gを水52.96gに溶解した。この水溶液を氷浴にて冷却し、液温30℃以下に保ちながら、25重量%のアンモニア水溶液18.35gを攪拌しながら徐々に加え、40重量%のアクリル酸アンモニウム/アクリル酸=70/30水溶液を得た。このアクリル酸アンモニウム/アクリル酸=70/30水溶液90gを10℃にし、窒素パージを30分行った後、炭酸アンモニウム0.72g、トリアリルアミン0.147gを加えた。開始剤として、過硫酸アンモニウム0.1387gと30重量%過酸化水素水0.0322g、L−アスコルビン酸0.0016gを加えた。1時間重合後解砕し、窒素雰囲気のイナートオーブンにて120℃で2時間乾燥した。乾燥後、ポリマー100部に、エチレングリコールジグリシジルエーテル0.25部、水2部、エタノール2部を混合した後、120℃で60分間加熱処理した。以上の様にして得られた樹脂体を比較吸水性樹脂体(2)とする。
比較吸水性樹脂体(2)の樹脂体外表面の中和率と樹脂体中心部の中和率を測定した結果とIRイメージングにより求めたスキン構造幅の測定結果、及び吸水測定の結果を表1に示す。
Comparative Example 2
Reagent acrylic acid (manufactured by Wako Pure Chemical Industries, special grade reagent) 28.32 g was dissolved in water 52.96 g. This aqueous solution was cooled in an ice bath, and while maintaining the liquid temperature at 30 ° C. or lower, 18.35 g of a 25 wt% aqueous ammonia solution was gradually added with stirring, and 40 wt% ammonium acrylate / acrylic acid = 70/30. An aqueous solution was obtained. After 90 g of this ammonium acrylate / acrylic acid = 70/30 aqueous solution was brought to 10 ° C. and purged with nitrogen for 30 minutes, 0.72 g of ammonium carbonate and 0.147 g of triallylamine were added. As initiators, 0.1387 g of ammonium persulfate, 0.0322 g of 30% by weight hydrogen peroxide, and 0.0016 g of L-ascorbic acid were added. After polymerization for 1 hour, it was crushed and dried in an inert oven in a nitrogen atmosphere at 120 ° C. for 2 hours. After drying, 0.25 part of ethylene glycol diglycidyl ether, 2 parts of water, and 2 parts of ethanol were mixed with 100 parts of the polymer, followed by heat treatment at 120 ° C. for 60 minutes. The resin body obtained as described above is referred to as a comparative water absorbent resin body (2).
Table 1 shows the results of measuring the neutralization rate of the outer surface of the resin body of the comparative water-absorbent resin body (2) and the neutralization ratio of the center of the resin body, the skin structure width obtained by IR imaging, and the results of water absorption measurement. Shown in

比較例3
試薬アクリル酸(和光純薬製、試薬特級品)28.32gを水52.96gに溶解した。この水溶液を氷浴にて冷却し、液温30℃以下に保ちながら、25重量%のアンモニア水溶液18.35gを攪拌しながら徐々に加え、40重量%のアクリル酸アンモニウム/アクリル酸=70/30水溶液を得た。このアクリル酸アンモニウム/アクリル酸=70/30水溶液90gを10℃にし、窒素パージを30分行った後、炭酸アンモニウム0.72g、トリアリルアミン0.147gを加えた。開始剤として、過硫酸アンモニウム0.1387gと30重量%過酸化水素水0.0322g、L−アスコルビン酸0.0016gを加えた。1時間重合後解砕し、窒素雰囲気のイナートオーブンにて150℃で1時間乾燥した。乾燥後、窒素雰囲気のイナートオーブンにて170℃で30分加熱した。以上の様にして得られた樹脂を比較吸水性樹脂体(3)とする。比較吸水性樹脂体(3)の吸水測定の結果を表2に示す。
Comparative Example 3
Reagent acrylic acid (Wako Pure Chemical Industries, reagent special grade) 28.32 g was dissolved in water 52.96 g. This aqueous solution was cooled in an ice bath, and while maintaining the liquid temperature at 30 ° C. or lower, 18.35 g of a 25 wt% aqueous ammonia solution was gradually added with stirring, and 40 wt% ammonium acrylate / acrylic acid = 70/30. An aqueous solution was obtained. After 90 g of this ammonium acrylate / acrylic acid = 70/30 aqueous solution was brought to 10 ° C. and purged with nitrogen for 30 minutes, 0.72 g of ammonium carbonate and 0.147 g of triallylamine were added. As initiators, 0.1387 g of ammonium persulfate, 0.0322 g of 30% by weight hydrogen peroxide, and 0.0016 g of L-ascorbic acid were added. After polymerization for 1 hour, the mixture was crushed and dried in an inert oven in a nitrogen atmosphere at 150 ° C. for 1 hour. After drying, it was heated at 170 ° C. for 30 minutes in an inert oven in a nitrogen atmosphere. The resin obtained as described above is referred to as a comparative water absorbent resin body (3). Table 2 shows the results of water absorption measurement of the comparative water absorbent resin body (3).

比較例4
製造例3で得たアクリル酸ナトリウム水溶液67.75gを水13.35gに溶解した。このアクリル酸ナトリウム水溶液に、アクリル酸8.9gを加え、40重量%のアクリル酸ナトリウム/アクリル酸=70/30水溶液90gを得た。架橋剤としてN,N’−メチレンビスアクリルアミド0.0992gを加え溶解した。この溶液を300mlセパラブルフラスコに移し、攪拌しながら30℃で30分間窒素パージを行った。それぞれ1gの水に溶かしたL−アスコルビン酸 0.0007gと過硫酸アンモニウム 0.046gを添加し重合を開始する。3時間重合を行った後、含水ゲルを5mm角程度に解砕し、窒素雰囲気過のイナートオーブン中で150℃で1時間乾燥した。乾燥ポリマーをホモジナイザーで粉砕後、106〜850μmに分級した。分級したポリマー100部に、プロピレングリコール2部、水3部、イソプロピルアルコール30部を混合した後、170℃で30分間加熱処理した。以上の様にして得られた樹脂を比較吸水性樹脂体(4)とする。比較吸水性樹脂体(4)の吸水測定の結果を表2に示す。
Comparative Example 4
67.75 g of the sodium acrylate aqueous solution obtained in Production Example 3 was dissolved in 13.35 g of water. To this sodium acrylate aqueous solution, 8.9 g of acrylic acid was added to obtain 90 g of 40 wt% sodium acrylate / acrylic acid = 70/30 aqueous solution. As a cross-linking agent, 0.0992 g of N, N′-methylenebisacrylamide was added and dissolved. This solution was transferred to a 300 ml separable flask and purged with nitrogen at 30 ° C. for 30 minutes while stirring. Polymerization is started by adding 0.0007 g of L-ascorbic acid dissolved in 1 g of water and 0.046 g of ammonium persulfate. After polymerization for 3 hours, the hydrogel was crushed to about 5 mm square and dried at 150 ° C. for 1 hour in an inert oven with a nitrogen atmosphere. The dried polymer was pulverized with a homogenizer and then classified to 106 to 850 μm. After mixing 100 parts of the classified polymer with 2 parts of propylene glycol, 3 parts of water and 30 parts of isopropyl alcohol, the mixture was heat-treated at 170 ° C. for 30 minutes. The resin obtained as described above is referred to as a comparative water absorbent resin body (4). Table 2 shows the results of water absorption measurement of the comparative water absorbent resin body (4).

比較例5
製造例1で得たアクリル酸アンモニウム水溶液54.73gに、アクリル酸17.71gと水43.1gを加え、40重量%のアクリル酸アンモニウム/アクリル酸=50/50水溶液90gを得た。活性炭1gを加え遮光下で1時間攪拌した。活性炭を濾別後、この溶液90gに架橋剤としてN,N’−メチレンビスアクリルアミド0.0992gを加え溶解した。この溶液を300mlセパラブルフラスコに移し、攪拌しながら30℃で30分間窒素パージを行った。それぞれ1gの水に溶かしたL−アスコルビン酸 0.0004gと過硫酸アンモニウム 0.046gを添加し重合を開始する。3時間重合を行った後、含水ゲルを5mm角程度に解砕し、窒素雰囲気過のイナートオーブン中で150℃で1時間乾燥した。乾燥ポリマーをホモジナイザーで粉砕後、106〜850μmに分級した。分級したポリマー100部に、プロピレングリコール2部、水3部、イソプロピルアルコール30部を混合した後、170℃で30分間加熱処理した。以上の様にして得られた樹脂を比較吸水性樹脂体(5)とする。比較吸水性樹脂体(5)の吸水測定の結果を表2に示す。
Comparative Example 5
17.54 g of acrylic acid and 43.1 g of water were added to 54.73 g of the aqueous ammonium acrylate solution obtained in Production Example 1 to obtain 90 g of 40 wt% ammonium acrylate / acrylic acid = 50/50 aqueous solution. 1 g of activated carbon was added and stirred for 1 hour in the dark. After filtering off the activated carbon, 0.0992 g of N, N′-methylenebisacrylamide as a cross-linking agent was added to 90 g of this solution and dissolved. This solution was transferred to a 300 ml separable flask and purged with nitrogen at 30 ° C. for 30 minutes while stirring. Polymerization is started by adding 0.0004 g of L-ascorbic acid and 0.046 g of ammonium persulfate dissolved in 1 g of water. After polymerization for 3 hours, the hydrogel was crushed to about 5 mm square and dried at 150 ° C. for 1 hour in an inert oven with a nitrogen atmosphere. The dried polymer was pulverized with a homogenizer and then classified to 106 to 850 μm. After mixing 100 parts of the classified polymer with 2 parts of propylene glycol, 3 parts of water and 30 parts of isopropyl alcohol, the mixture was heat-treated at 170 ° C. for 30 minutes. The resin obtained as described above is referred to as a comparative water absorbent resin body (5). Table 2 shows the results of water absorption measurement of the comparative water absorbent resin body (5).

Figure 2005200630
Figure 2005200630

Figure 2005200630
Figure 2005200630

本発明の吸水性樹脂体およびその製造方法は、衛生材料等で用いられる高い加圧下吸水性能が要求される高吸水性樹脂の用途分野で好適に利用できる。   The water-absorbent resin body and the method for producing the same according to the present invention can be suitably used in the field of application of a highly water-absorbent resin that is required for water absorption performance under high pressure and used for sanitary materials and the like.

IRイメージングを行った試料切片の顕微鏡写真。破線は、測定を行ったラインを示す。A micrograph of a sample section subjected to IR imaging. A broken line shows the line which measured. IRイメージング測定において図1の破線に沿って測定した1695/1558cm−1ピーク面積比を数値化したラインプロファイル。縦軸はピーク面積比、横軸は試料のライン上の測定位置を示す。The line profile which digitized 1695 / 1558cm < -1 > peak area ratio measured along the broken line of FIG. 1 in IR imaging measurement. The vertical axis represents the peak area ratio, and the horizontal axis represents the measurement position on the sample line.

Claims (8)

ポリマー分子鎖中における繰り返し単位のうち、50mol%以上がカルボキシル基含有単位からなる吸水性樹脂体であって、樹脂体中心部のカルボキシル基中和率が60mol%以上であり、樹脂体外表面のカルボキシル基中和率が50mol%以下であることを特徴とする吸水性樹脂体。   Of the repeating units in the polymer molecular chain, 50 mol% or more is a water-absorbent resin body composed of carboxyl group-containing units, the carboxyl group neutralization rate at the center of the resin body is 60 mol% or more, and the carboxyl on the outer surface of the resin body A water-absorbent resin body having a group neutralization rate of 50 mol% or less. 樹脂体中心部よりも中和率の低い部分が樹脂体外表面から13μm以上の幅で存在する、スキン構造を特徴とする請求項1に記載の吸水性樹脂体。   The water-absorbent resin body according to claim 1, wherein a portion having a lower neutralization rate than the central portion of the resin body is present in a width of 13 μm or more from the outer surface of the resin body. 下記の(1)及び(2)を満たすことを特徴とする請求項1あるいは2に記載の吸水性樹脂体。
(1)ポリマー分子鎖中におけるカルボキシル基中和塩のうち50mol%以上がアンモニウム塩である。
(2)0.8psiの加圧下における吸水倍率が22倍以上である。
The water-absorbent resin body according to claim 1 or 2, wherein the following (1) and (2) are satisfied.
(1) 50 mol% or more of the carboxyl group neutralized salt in the polymer molecular chain is an ammonium salt.
(2) The water absorption magnification under a pressure of 0.8 psi is 22 times or more.
粒度分布が40μm〜1000μmである粉末粒子状の吸水性樹脂であることを特徴とする請求項3に記載の吸水性樹脂体。   4. The water absorbent resin body according to claim 3, wherein the water absorbent resin body is a powder particulate water absorbent resin having a particle size distribution of 40 [mu] m to 1000 [mu] m. 下記の(3)から(5)を満たす単量体溶液を重合、解砕、乾燥、粉砕した後に、あるいは重合、解砕、粉砕、乾燥した後に、加熱処理をすることを特徴とする吸水性樹脂体の製造方法。
(3)少なくとも1種類の不飽和カルボン酸アンモニウム塩(A)、不飽和カルボン酸アルカリ金属塩(B)及びカルボキシル基に対する縮合型架橋剤(C)を含む。
(4)不飽和カルボン酸アンモニウム塩(A)の比率が全不飽和カルボン酸単量体に対して50mol%を越え100mol%以下であり、不飽和カルボン酸アルカリ金属塩(B)の比率が全不飽和カルボン酸単量体に対して0mol%以上50mol%未満である。
(5)カルボキシル基に対する縮合型架橋剤(C)の含有率が全単量体成分の重量に対して0.01重量%以上20重量%以下である。
A water-absorbing characteristic, wherein the monomer solution satisfying the following (3) to (5) is polymerized, crushed, dried, pulverized, or polymerized, crushed, pulverized, dried, and then heated. A method for producing a resin body.
(3) At least one kind of unsaturated carboxylic acid ammonium salt (A), unsaturated carboxylic acid alkali metal salt (B), and a condensation type crosslinking agent (C) for a carboxyl group.
(4) The ratio of unsaturated carboxylic acid ammonium salt (A) is more than 50 mol% and 100 mol% or less with respect to all unsaturated carboxylic acid monomers, and the ratio of unsaturated carboxylic acid alkali metal salt (B) is all It is 0 mol% or more and less than 50 mol% with respect to the unsaturated carboxylic acid monomer.
(5) The content of the condensation type crosslinking agent (C) with respect to the carboxyl group is 0.01% by weight or more and 20% by weight or less based on the weight of all monomer components.
加熱処理を100〜250℃で行うことを特徴とする請求項5に記載の吸水性樹脂体の製造方法。   The method for producing a water absorbent resin body according to claim 5, wherein the heat treatment is performed at 100 to 250 ° C. 架橋剤としてカルボキシル基に対する縮合型架橋剤(C)に加えて、不飽和単量体重合性の架橋剤(D)を全単量体成分に対し0.005mol%以上1mol%以下含有することを特徴とする、請求項5あるいは6に記載の吸水性樹脂体の製造方法。   In addition to the condensation type crosslinking agent (C) for the carboxyl group as a crosslinking agent, the unsaturated monomer polymerizable crosslinking agent (D) is contained in an amount of 0.005 mol% to 1 mol% with respect to all monomer components. The method for producing a water-absorbent resin body according to claim 5, wherein the water-absorbent resin body is produced. 不飽和カルボン酸塩(A)および(B)が(メタ)アクリル酸塩であることを特徴とする請求項5〜7のいずれかに記載の吸水性樹脂体の製造方法。   The method for producing a water-absorbent resin body according to any one of claims 5 to 7, wherein the unsaturated carboxylates (A) and (B) are (meth) acrylates.
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