JPH04227705A - Production of salt-resistant water absorbing resin - Google Patents

Production of salt-resistant water absorbing resin

Info

Publication number
JPH04227705A
JPH04227705A JP9521591A JP9521591A JPH04227705A JP H04227705 A JPH04227705 A JP H04227705A JP 9521591 A JP9521591 A JP 9521591A JP 9521591 A JP9521591 A JP 9521591A JP H04227705 A JPH04227705 A JP H04227705A
Authority
JP
Japan
Prior art keywords
salt
water
absorbing resin
resistant water
producing
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
JP9521591A
Other languages
Japanese (ja)
Other versions
JP2901368B2 (en
Inventor
Yoshio Irie
好夫 入江
Katsuhiro Kajikawa
勝弘 梶川
Masa Takahashi
雅 高橋
Teruaki Fujiwara
藤原 晃明
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Nippon Shokubai Co Ltd
Original Assignee
Nippon Shokubai Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Nippon Shokubai Co Ltd filed Critical Nippon Shokubai Co Ltd
Priority to JP9521591A priority Critical patent/JP2901368B2/en
Publication of JPH04227705A publication Critical patent/JPH04227705A/en
Application granted granted Critical
Publication of JP2901368B2 publication Critical patent/JP2901368B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Abstract

PURPOSE:To inexpensively produce a water absorbing resin having high gel strength, small change of absorption magnification with salt concentration of aqueous solution to be absorbed and excellent salt resistance. CONSTITUTION:The objectives can be attained by production of a salt-resistant water absorbing resin wherein an aqueous solution of at least one monomer component (A) selected from a group consisting of an unsaturated carboxylic acid and a salt thereof is subjected to aqueous solution polymerization in the presence of 1-30 pts.wt. water absorbing resin (B) based on 100 pts.wt. of the monomer component.

Description

【発明の詳細な説明】[Detailed description of the invention]

【0001】0001

【産業上の利用分野】本発明は、耐塩性吸水性樹脂の製
造方法に関するものである。詳しく述べると、ゲル強度
が高くかつ耐塩性が改良された吸水性樹脂の製造方法に
関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for producing a salt-resistant water-absorbing resin. More specifically, the present invention relates to a method for producing a water-absorbing resin that has high gel strength and improved salt resistance.

【0002】0002

【従来の技術】吸水性樹脂は従来から、おむつ、生理用
品、土壌保水剤、シール剤をはじめとする各種吸水材料
に利用されている。
BACKGROUND OF THE INVENTION Water-absorbing resins have been used in various water-absorbing materials such as diapers, sanitary products, soil water retention agents, and sealants.

【0003】このような吸水性樹脂としてはカルボキシ
ル基等の電解質構造を有するものと、ノニオン性の親水
性セグメントを有するものに大別され、前者としては例
えばアクリル酸(塩)重合体の架橋体(特開昭55−8
4,304号公報等)、澱粉−アクリロニトリルグラフ
ト共重合体の加水分解物(特公昭49−43,395号
公報)、澱粉−アクリル酸のグラフト共重合体の中和物
(特公昭53−46,199号公報)、アクリル酸エス
テル−酢酸ビニル共重合体のケン化物(特公昭53−1
3,495号公報)が、後者としては架橋ポリビニルア
ルコール変性物(特開昭54−20093号公報)、ポ
リエチレンオキサイド部分架橋物(特開昭61−130
,324号公報)等が知られている。
[0003] Such water-absorbing resins are roughly divided into those having electrolyte structures such as carboxyl groups and those having nonionic hydrophilic segments.The former include, for example, crosslinked acrylic acid (salt) polymers. (Unexamined Japanese Patent Publication No. 55-8
4,304, etc.), hydrolysates of starch-acrylonitrile graft copolymers (Japanese Patent Publication No. 49-43,395), neutralized products of starch-acrylic acid graft copolymers (Japanese Patent Publication No. 53-46, etc.) , No. 199), saponified product of acrylic acid ester-vinyl acetate copolymer (Japanese Patent Publication No. 53-1
3,495), but the latter include cross-linked polyvinyl alcohol modified products (JP-A-54-20093) and polyethylene oxide partially cross-linked products (JP-A-61-130).
, No. 324), etc. are known.

【0004】吸水性樹脂は、その特質から種々の水溶液
を吸収させる目的で幅広く産業分野に使用されているが
、吸収させる液の種類によっては吸収倍率が非常に異な
り、例えば、おむつに使用した場合には、尿中の塩濃度
の変化により吸収倍率が変化して品質のフレにつながっ
たり、塩濃度により膨潤体積が変化するため、農園芸分
野や止水剤の分野での用途が制限される場合があった。
[0004] Water-absorbent resins are widely used in industrial fields for the purpose of absorbing various aqueous solutions due to their characteristics, but the absorption capacity varies greatly depending on the type of liquid to be absorbed. For example, when used in diapers, The absorption capacity changes due to changes in the salt concentration in urine, leading to quality fluctuations, and the swelling volume changes depending on the salt concentration, which limits its use in the fields of agriculture, horticulture, and water-stopping agents. There was a case.

【0005】例えば、前者のカルボキシ基等の電解質構
造を有する吸水性樹脂は一般にゲル強度が高く、かつ純
水(脱イオン水)等では非常に高い吸収倍率を示すもの
の、食塩等の電解質を有する溶液に対しては吸収倍率が
著しく低下し、いわゆる耐塩性が低いという問題点があ
る。
For example, the former water-absorbing resin having an electrolyte structure such as a carboxyl group generally has a high gel strength and exhibits a very high absorption capacity in pure water (deionized water), etc. When used as a solution, there is a problem that the absorption capacity is significantly lowered and so-called salt tolerance is low.

【0006】後者のノニオン性親水性セグメントを有す
る吸水性樹脂は電解質溶液に対する吸収倍率の低下は小
さく、耐塩性という面では優れているが、ゲル強度が弱
く、吸水速度もおそく、吸収倍率の絶対値も低いもので
ある。
The latter water-absorbent resin having a nonionic hydrophilic segment has a small decrease in absorption capacity for electrolyte solutions and is excellent in terms of salt resistance, but its gel strength is weak, its water absorption rate is slow, and its absolute absorption capacity is low. The value is also low.

【0007】また、耐塩性の優れた樹脂として、強電改
質であるスルホン酸基を導入した吸水性樹脂(特開昭6
1−36,309号公報、特開昭56−161,412
号公報)も知られているが、多価イオンを含んだ液に対
しては優れた耐塩性を発揮するが、一価イオンを含んだ
液に対してはアクリル酸塩架橋体等と同様に耐塩性に劣
ったものである。しかも、原料にスルホン酸基を有する
モノマーを使うため高価である。
[0007] In addition, as a resin with excellent salt resistance, a water-absorbing resin (Japanese Patent Laid-Open No. 6-117) into which a sulfonic acid group, which is a strong electric modification, has been introduced is also used.
Publication No. 1-36,309, JP-A-56-161,412
Although it is known that it exhibits excellent salt resistance against liquids containing multivalent ions, it exhibits excellent salt resistance against liquids containing monovalent ions, similar to acrylate crosslinked products. It has poor salt tolerance. Moreover, since a monomer having a sulfonic acid group is used as a raw material, it is expensive.

【0008】[0008]

【発明が解決しようとする課題】したがって本発明の目
的は、耐塩性吸水性樹脂の製造方法を提供することにあ
る。
SUMMARY OF THE INVENTION Therefore, an object of the present invention is to provide a method for producing a salt-resistant water-absorbing resin.

【0009】本発明の他の目的は、ゲル強度が大きく、
かつ吸収させる水溶液の塩濃度による吸収倍率の変化が
小さい耐塩性に優れた吸水性樹脂を安価に製造する方法
を提供することにある。
Another object of the present invention is to provide a gel with high gel strength;
Another object of the present invention is to provide a method for inexpensively producing a water-absorbing resin with excellent salt resistance and a small change in absorption capacity depending on the salt concentration of an aqueous solution to be absorbed.

【0010】0010

【課題を解決するための手段】上記諸目的は、不飽和カ
ルボン酸およびその塩よりなる群から選ばれた少なくと
も1種の単量体成分(A)の水溶液を、該単量体成分(
A)100重量部当たり吸水性樹脂(B)1〜30重量
部の割合で存在させて水溶液重合することよりなる耐塩
性吸水性樹脂の製造方法により達成される。
[Means for Solving the Problems] The above objects are achieved by preparing an aqueous solution of at least one monomer component (A) selected from the group consisting of unsaturated carboxylic acids and salts thereof.
A) This is achieved by a method for producing a salt-resistant water-absorbing resin, which comprises polymerizing the water-absorbing resin (B) in an aqueous solution in an amount of 1 to 30 parts by weight per 100 parts by weight.

【0011】[0011]

【作用】本発明の製造方法による得られる耐塩性吸水性
樹脂は、耐塩性、ゲル強度が、ともに著しく優れている
。また本発明においては得られた耐塩性吸水性樹脂中に
含まれる特定粒度範囲の樹脂をさらに吸水性樹脂(B)
として繰り返し用いることもでき、例えば細かい粒度範
囲の樹脂を吸水性樹脂(B)として用いた場合には得ら
れた製品は、例えば149μm以下の微粉の混在量が著
しく低減され、吸収諸特性、経済性にも優れたものとな
るばかりでなく、これを用いて紙おむつ、生理綿等の各
種吸収物品に加工する際に微粉が飛散する心配もなく、
労働衛生の面での問題も解消するという利点をも有する
ものである。したがって、本発明により得られる耐塩性
吸水性樹脂は、その特性を生かし、おむつ、生理用品、
農園芸用、シール剤、推進工法用滑剤、地盤掘削におけ
る逸泥防止、泥水の固定剤、カーペット下敷、農業用被
覆剤等に有効に使用できる。
[Function] The salt-resistant water-absorbing resin obtained by the production method of the present invention is extremely excellent in both salt resistance and gel strength. In addition, in the present invention, a resin having a specific particle size range contained in the obtained salt-resistant water-absorbing resin is further added to the water-absorbing resin (B).
For example, when a resin with a fine particle size range is used as the water-absorbing resin (B), the resulting product has a significantly reduced amount of fine powder of, for example, 149 μm or less, and has improved absorption properties and economy. Not only does it have excellent properties, but there is no fear of fine powder scattering when it is processed into various absorbent products such as disposable diapers and sanitary cotton.
It also has the advantage of eliminating problems in terms of occupational health. Therefore, the salt-resistant water-absorbent resin obtained by the present invention can be used in diapers, sanitary products, etc. by taking advantage of its properties.
It can be effectively used for agricultural and horticultural purposes, as a sealant, as a lubricant for propulsion methods, to prevent slippage of mud in ground excavation, as a fixing agent for muddy water, as a carpet underlay, as a coating for agriculture, etc.

【0012】本発明に用いられる不飽和カルボン酸とし
ては、例えば(メタ)アクリル酸、クロトン酸、イタコ
ン酸、マレイン酸、フマル酸、シトラコン酸等が、また
不飽和カルボン酸の塩としては、これらのアルカリ金属
塩、アンモニウム塩のおよび置換アンモニウム塩等を挙
げることができ、これらの中から1種または2種以上を
用いることができる。
Examples of the unsaturated carboxylic acids used in the present invention include (meth)acrylic acid, crotonic acid, itaconic acid, maleic acid, fumaric acid, citraconic acid, etc., and salts of unsaturated carboxylic acids include these. Alkali metal salts, ammonium salts, substituted ammonium salts, and the like can be mentioned, and one or more of these can be used.

【0013】ただし、耐塩性が優れた吸水性樹脂を得る
ために、不飽和カルボン酸および/またはその塩として
アクリル酸および/またはアクリル酸塩を必須成分とし
て用いるのが好ましい。特にアクリル酸10〜70モル
%、好ましくは20〜40モル%およびアクリル酸塩9
0〜30モル%、好ましくは80〜60モル%よりなる
ものが好ましい。
However, in order to obtain a water-absorbing resin with excellent salt resistance, it is preferable to use acrylic acid and/or acrylate as an essential component as the unsaturated carboxylic acid and/or its salt. In particular acrylic acid 10-70 mol%, preferably 20-40 mol% and acrylate salt 9
Preferably, the content is 0 to 30 mol%, preferably 80 to 60 mol%.

【0014】単量体成分(A)には、上記不飽和カルボ
ン酸および/またはその塩以外に、他の不飽和単量体が
含まれていてもよい。
The monomer component (A) may contain other unsaturated monomers in addition to the unsaturated carboxylic acid and/or its salt.

【0015】他の不飽和単量体としては、例えば2−ア
クリルアミド−2−メチルプロパンスルホン酸、ビニル
スルホン酸、(メタ)アリルスルホン酸、スチレンスル
ホン酸、スルホエチル(メタ)アクリレート、スルホプ
ロピル(メタ)アクリレート、ビニルトルエンスルホン
酸等の不飽和スルホン酸およびそれらの塩;N,N−ジ
メチルアミノエチル(メタ)アクリレート、N,N−ジ
エチルアミノエチル(メタ)アクリレート等の不飽和ア
ミン化合物およびそれらの塩;ヒドロキシエチル(メタ
)アクリレート、メトキシエチル(メタ)アクリレート
、ヒドロキシプロピル(メタ)アクリレート、ポリエチ
レングリコールモノ(メタ)アクリレート、ポリプロピ
レングリコールモノ(メタ)アクリレート、メトキシポ
リエチレングリコールモノ(メタ)アクリレート、メト
キシポリプロピレングリコールモノ(メタ)アクリレー
ト、(メタ)アクリル酸メチル、(メタ)アクリル酸エ
チル等の(メタ)アクリル酸エステル;(メタ)アクリ
ルアミド、N−ヘキシル(メタ)アクリルアミド、N−
メチロール(メタ)アクリルアミド、N,Nジメチル(
メタ)アクリルアミド等の不飽和アミド;スチレン、α
−メチルスチレン、o−メチルスチレン、p−メチルス
チレン等のスチレンまたはその誘導体;(メタ)アクリ
ロニトリル、酢酸ビニル等を挙げることができ、これら
の1種、または2種以上を単量体成分(A)中の50重
量%未満、好ましくは40重量%未満の範囲で用いるこ
とができる。
Examples of other unsaturated monomers include 2-acrylamido-2-methylpropanesulfonic acid, vinylsulfonic acid, (meth)allylsulfonic acid, styrenesulfonic acid, sulfoethyl (meth)acrylate, and sulfopropyl (meth)acrylate. ) Unsaturated sulfonic acids and their salts such as acrylate and vinyltoluenesulfonic acid; Unsaturated amine compounds and their salts such as N,N-dimethylaminoethyl (meth)acrylate and N,N-diethylaminoethyl (meth)acrylate ;Hydroxyethyl (meth)acrylate, methoxyethyl (meth)acrylate, hydroxypropyl (meth)acrylate, polyethylene glycol mono(meth)acrylate, polypropylene glycol mono(meth)acrylate, methoxypolyethylene glycol mono(meth)acrylate, methoxypolypropylene glycol (Meth)acrylic acid esters such as mono(meth)acrylate, methyl (meth)acrylate, and ethyl (meth)acrylate; (meth)acrylamide, N-hexyl (meth)acrylamide, N-
Methylol (meth)acrylamide, N,N dimethyl (
Unsaturated amides such as meth)acrylamide; styrene, α
- Styrene or its derivatives such as methylstyrene, o-methylstyrene, p-methylstyrene; (meth)acrylonitrile, vinyl acetate, etc., and one or more of these may be used as the monomer component (A ), preferably less than 40% by weight.

【0016】本発明に用いられる吸水性樹脂(B)は吸
水して含水ゲル状物となり得る水不溶性樹脂であれば特
に制限されず、例えばカルボキシメチルセルロース架橋
物、架橋ポリビニルアルコール変性物、架橋イソブチレ
ン−無水マレイン酸共重合体、アクリル酸エステル−酢
酸ビニル共重合架橋体のケン化物、ポリエチレンオキシ
ド部分架橋物、澱粉−アクリロニトリルグラフト共重合
架橋体の加水分解物、澱粉−アクリル酸のグラフト共重
合架橋体の中和物、部分中和(メタ)アクリル酸重合体
の架橋体等が挙げられる。
The water-absorbing resin (B) used in the present invention is not particularly limited as long as it is a water-insoluble resin that can absorb water and become a water-containing gel, such as crosslinked carboxymethylcellulose, modified crosslinked polyvinyl alcohol, and crosslinked isobutylene. Maleic anhydride copolymer, saponified crosslinked acrylic acid ester-vinyl acetate copolymer, partially crosslinked polyethylene oxide, hydrolyzate of starch-acrylonitrile graft copolymer, crosslinked starch-acrylic acid graft copolymer neutralized products, crosslinked products of partially neutralized (meth)acrylic acid polymers, and the like.

【0017】好ましくは、部分中和(メタ)アクリル酸
重合体の架橋体で、例えば特開昭56−93,716号
公報、特開昭56−131,608号公報、特開昭56
−147,806号公報、特開昭58−71907号公
報、特開昭58−117,222号公報、特公昭54−
30,710号公報、特公昭54−37,994号公報
、特公昭53−46,200号公報、米国特許第4,0
41,228号公報で開示されていた吸水能が100〜
1000倍の吸水性樹脂等は、いずれも本発明の吸水性
樹脂(B)として好ましく利用できる。中でも、単量体
成分を均一に吸収して膨潤し、IPN構造やグラフト化
を効率よく起こして優れた耐塩性吸水性樹脂を得るため
に、吸水性樹脂(B)としては、含水率が0.1〜10
重量%の粉末状のものが好ましい。また、単量体成分(
A)の吸水を速やかに起こさせるためにも、吸水性樹脂
(B)は、その90〜100重量%が1〜149μm、
特に1〜74μmの粒子径を有するが好ましい。
Preferably, a crosslinked product of partially neutralized (meth)acrylic acid polymer is used, for example, JP-A-56-93,716, JP-A-56-131,608, JP-A-56
-147,806, JP 58-71907, JP 58-117,222, JP 54-
30,710, Japanese Patent Publication No. 54-37,994, Japanese Patent Publication No. 53-46,200, U.S. Patent No. 4,0
The water absorption capacity disclosed in Publication No. 41,228 is 100~
Any 1000 times more water-absorbent resin can be preferably used as the water-absorbent resin (B) of the present invention. Among them, in order to obtain an excellent salt-resistant water-absorbent resin by uniformly absorbing monomer components and swelling, and efficiently creating an IPN structure and grafting, the water-absorbent resin (B) has a water content of 0. .1-10
% by weight in powder form is preferred. In addition, the monomer component (
In order to cause the water absorption of A) to occur promptly, 90 to 100% by weight of the water absorbent resin (B) has a diameter of 1 to 149 μm,
In particular, it is preferable to have a particle size of 1 to 74 μm.

【0018】吸水性樹脂(B)を構成するもとの単量体
成分(A)は、同じであっても異なっていてもよいが、
最終的に得られる吸水性樹脂の物性や後述するように、
本発明の操作を繰り返す場合を考えると、同一組成であ
ることが好ましい。また、吸水性樹脂(B)を得るため
の重合方法も、水溶液重合であっても、その他の重合方
法であってもよいが、同じく本発明の操作を繰り返す場
合を考えると、水溶液重合であることが好ましい。また
、前記不飽和カルボン酸の重合体を、そのカルボキシル
基が0.3〜0.9当量、好ましくは、0.6〜0.8
当量中和されてなるものであってもよい。このような吸
水性樹脂(B)としては、通常の製法により得られる吸
水性樹脂、または必要により特定粒度範囲を選んだ吸水
性樹脂を用いてもよく、市販の吸水性樹脂製品を当事者
に周知の粉砕機によりさらに粉砕して得てもよく、また
、本発明の製造方法の水溶液重合を行った後、乾燥、分
級して得られる耐塩性吸水性樹脂中に含まれる吸水性樹
脂(B)と同様の粒度範囲の樹脂(C)を除去し、再度
吸水性樹脂(B)として繰り返し用いてもよい。また、
吸水性樹脂(B)は、粒子の表面部分の架橋密度が高め
られるような処理を施されたものでもよい。
The original monomer components (A) constituting the water absorbent resin (B) may be the same or different;
The physical properties of the water-absorbing resin finally obtained and as described later,
Considering the case where the operation of the present invention is repeated, it is preferable that the composition be the same. Further, the polymerization method for obtaining the water-absorbent resin (B) may be aqueous solution polymerization or other polymerization method, but considering the case where the operation of the present invention is repeated, aqueous solution polymerization is preferred. It is preferable. Further, the unsaturated carboxylic acid polymer has a carboxyl group of 0.3 to 0.9 equivalent, preferably 0.6 to 0.8 equivalent.
It may be equivalently neutralized. As such a water-absorbing resin (B), a water-absorbing resin obtained by a normal manufacturing method, or a water-absorbing resin with a specific particle size range selected as necessary may be used. Alternatively, the water-absorbing resin (B) contained in the salt-resistant water-absorbing resin obtained by drying and classifying the aqueous solution polymerization of the production method of the present invention. The resin (C) having the same particle size range may be removed and used repeatedly as the water absorbent resin (B). Also,
The water absorbent resin (B) may be treated to increase the crosslinking density of the surface portion of the particles.

【0019】吸水性樹脂(B)の使用量は、耐塩性が特
に優れた吸水性樹脂を効率よく得るために、単量体成分
(A)100重量部に対して1〜30重量部、好ましく
は5〜20重量部である。この量が30重量部を越すと
、単量体成分(A)の中に吸水性樹脂(B)が均一に分
散膨潤し得ず、樹脂が析出した状態になり、所望とする
吸収倍率の高い耐塩性吸水性樹脂が得られない。また、
1重量部未満では、本発明の意思するところの耐塩性が
発現しない。また、吸水性樹脂(B)の単量体成分(A
)への添加は、単量体成分(A)の重合が開始するまで
に行うのが一般的であるが、重合開始後、未だ系が流動
性を保持している状態であれば、この時期に吸水性樹脂
(B)を添加することもできる。
The amount of water-absorbing resin (B) to be used is preferably 1 to 30 parts by weight per 100 parts by weight of monomer component (A) in order to efficiently obtain a water-absorbing resin with particularly excellent salt resistance. is 5 to 20 parts by weight. If this amount exceeds 30 parts by weight, the water-absorbing resin (B) cannot be uniformly dispersed and swollen in the monomer component (A), and the resin precipitates, resulting in a desired high absorption capacity. A salt-resistant water-absorbing resin cannot be obtained. Also,
If it is less than 1 part by weight, the salt tolerance intended by the present invention will not be achieved. In addition, the monomer component (A) of the water absorbent resin (B)
) is generally added before the start of polymerization of monomer component (A), but if the system still maintains fluidity after the start of polymerization, it may be added at this time. A water-absorbing resin (B) can also be added thereto.

【0020】本発明の製造方法によれば、架橋剤を用い
ずに単量体成分(A)を吸水性樹脂(B)の存在下で水
溶液重合するだけでも、該単量体成分(A)が該吸収性
樹脂(B)にグラフトまたはIPN構造をとりながら重
合するために、耐塩性吸水性樹脂を得ることができると
推測されるが、更に、ゲル強度がよりすぐれた吸水性樹
脂を得るために、重合時単量体成分(A)に架橋剤を配
分しておくのが好ましい。
According to the production method of the present invention, even if the monomer component (A) is polymerized in an aqueous solution in the presence of the water-absorbing resin (B) without using a crosslinking agent, the monomer component (A) It is presumed that a salt-resistant water-absorbing resin can be obtained because it is polymerized while taking a graft or IPN structure on the absorbent resin (B), but in addition, a water-absorbing resin with better gel strength can be obtained. Therefore, it is preferable to allocate a crosslinking agent to the monomer component (A) during polymerization.

【0021】本発明に用いることができる架橋剤として
は、例えばエチレングリコールジ(メタ)アクリレート
、ジエチレングリコールジ(メタ)アクリレート、トリ
エチレングリコールジ(メタ)アクリレート、プロピレ
ングリコールジ(メタ)アクリレート、ポリエチレング
リコールジ(メタ)アクリレート、トリメチロールプロ
パントリ(メタ)アクリレート、ペンタエリスリトール
トリ(メタ)アクリレート、ペンタエリスリトールジ(
メタ)アクリレート、N,N´−メチレンビス(メタ)
アクリルアミド、イソシアヌル酸トリアリル、トリメチ
ロールプロパンジ(メタ)アリルエーテル等の1分子中
にエチレン性不飽和基を2個以上有する化合物;エチレ
ングリコール、ジエチレングリコール、トリエチレング
リコール、ポリエチレングリコール、グリセリン、ポリ
グリセリン、プロピレングリコール、ジエタノールアミ
ン、トリジエタノールアミン、ポリプロピレングリコー
ル、ポリビニルアルコール、ペンタエリスリトール、ソ
ルビット、ソルビタン、グルコース、マンニット、マン
ニタン、ショ糖、ブドウ糖などの多価アルコール;エチ
レングリコールジグリシジルエーテル、ポリエチレング
リコールジグリシジルエーテル、グリセリントリグリシ
ジルエーテル等のポリグリシジルエーテル;エピクロル
ヒドリン、α−メチルクロルヒドリン等のハロエポキシ
化合物;グルタールアルデヒド、グリオキザール等のポ
リアルデヒド;エチレンジアミン等のポリアミン類;水
酸化カルシウム、塩化カルシウム、炭酸カルシウム、酸
化カルシウム、塩化硼砂マグネシウム、酸化マグネシウ
ム、塩化アルミニウム、塩化亜鉛および塩化ニッケル等
の周期律表2A族、3B族、8族の金属の水酸化物、ハ
ロゲン化物、炭酸塩、酸化物、硼砂等の硼酸塩、アルミ
ニウムイソプロピラート等の多価金属化合物等が挙げら
れ、これらの1種または2種以上を、反応性を考慮した
上で適宜選んで用いることができるが、1分子中にエチ
レン性不飽和基を2個以上有する化合物を架橋剤として
用いるのが最も好ましい。
Examples of crosslinking agents that can be used in the present invention include ethylene glycol di(meth)acrylate, diethylene glycol di(meth)acrylate, triethylene glycol di(meth)acrylate, propylene glycol di(meth)acrylate, and polyethylene glycol. Di(meth)acrylate, trimethylolpropane tri(meth)acrylate, pentaerythritol tri(meth)acrylate, pentaerythritol di(
meth)acrylate, N,N'-methylenebis(meth)
Compounds having two or more ethylenically unsaturated groups in one molecule such as acrylamide, triallyl isocyanurate, trimethylolpropane di(meth)allyl ether; ethylene glycol, diethylene glycol, triethylene glycol, polyethylene glycol, glycerin, polyglycerin, Polyhydric alcohols such as propylene glycol, diethanolamine, tridiethanolamine, polypropylene glycol, polyvinyl alcohol, pentaerythritol, sorbitol, sorbitan, glucose, mannitol, mannitan, sucrose, glucose; ethylene glycol diglycidyl ether, polyethylene glycol diglycidyl ether, Polyglycidyl ethers such as glycerin triglycidyl ether; haloepoxy compounds such as epichlorohydrin and α-methylchlorohydrin; polyaldehydes such as glutaraldehyde and glyoxal; polyamines such as ethylenediamine; calcium hydroxide, calcium chloride, calcium carbonate, and oxidized Hydroxides, halides, carbonates, oxides of metals in Groups 2A, 3B, and 8 of the Periodic Table such as calcium, magnesium chloride, magnesium oxide, aluminum chloride, zinc chloride, and nickel chloride, boric acid such as borax, etc. salts, polyvalent metal compounds such as aluminum isopropylate, etc., and one or more of these can be selected and used as appropriate after considering the reactivity. Most preferably, a compound having two or more groups is used as a crosslinking agent.

【0022】これらの架橋剤は必要かつ充分な効果を発
現させるために単量体成分(A)に対して0.001〜
0.1モル%、特に好ましくは0.01〜0.05モル
%の量で用いるのがより好ましい。0.1モル%を越え
ると吸収倍率自体の低下を招く場合があるので注意を要
する。
[0022] These crosslinking agents are used in a proportion of 0.001 to 0.001 to the monomer component (A) in order to exhibit the necessary and sufficient effect.
More preferably, it is used in an amount of 0.1 mol%, particularly preferably 0.01 to 0.05 mol%. If it exceeds 0.1 mol %, the absorption capacity itself may decrease, so care must be taken.

【0023】本発明においてはその重合方法として水溶
性重合を用いることが必須である。他の重合法、例えば
逆相懸濁重合、噴霧重合、沈殿重合等では、単量体成分
(A)中に吸水性樹脂(B)が安定に分散して均一に存
在し得ず、本発明の意思する耐塩性の効果は得られない
In the present invention, it is essential to use water-soluble polymerization as the polymerization method. In other polymerization methods, such as reverse-phase suspension polymerization, spray polymerization, and precipitation polymerization, the water-absorbing resin (B) cannot be stably dispersed and uniformly present in the monomer component (A). The desired salt tolerance effect cannot be obtained.

【0024】また、水溶液重合は単量体成分(A)中に
吸水性樹脂(B)を均一に分散し、グラフト反応等を効
率よく行わせるために、撹拌混合下に行うことが好まし
い。そのためには回転撹拌軸を有する反応容器内で該回
転撹拌軸の剪断力により、重合に伴い生成するゲル状物
を、細分化しながら重合を行うことが更に好ましく、例
えば特開昭57−34,101号公報、US−A−4,
625,001およびEP0343,919に開示され
ているように複数の回転撹拌軸を有する反応容器として
ニーダーを用いるのが最も好ましい。
[0024] Furthermore, the aqueous solution polymerization is preferably carried out under stirring and mixing in order to uniformly disperse the water-absorbing resin (B) in the monomer component (A) and to carry out the grafting reaction efficiently. For this purpose, it is more preferable to carry out the polymerization in a reaction vessel having a rotating stirring shaft while fragmenting the gel-like material produced during polymerization by the shearing force of the rotating stirring shaft. No. 101, US-A-4,
Most preferably, a kneader is used as the reaction vessel with multiple rotating stirring shafts, as disclosed in EP 0 343,919.

【0025】重合の開始方法としては、例えばラジカル
重合開始触媒を用いる方法、活性エネルギー線を照射す
る方法等が挙げられる。ラジカル重合開始触媒としては
、例えば過酸化水素、ベンゾイルパーオキサイド等の過
酸化物;2−2´−アゾビス−2−アミジノプロパン二
塩酸塩、アゾビスイソブチロニトリル等のアゾ化合物;
過硫酸アンモニウム、過硫酸カリウム、過硫酸ナトリウ
ム等の過硫酸塩等のラジカル発生剤や、これらラジカル
発生剤と亜硫酸水素ナトリウム、L−アスコルビン酸、
第一鉄塩等の還元剤との組み合わせによるレドックス系
開始剤などが用いられる。その使用量は、単量体成分(
A)に対して0.01〜1.0重量%、好ましくは0.
05〜0.5重量%である。水溶液重合するに際して、
重合用溶媒としては水だけを用いるのが好ましいが、必
要によりメタノール、エタノール、イソプロパノール、
アセトン、ジメチルホルムアミド、ジメチルスルホキシ
ド等の親水性有機溶剤を水に添加して用いてもよい。
Examples of methods for initiating polymerization include a method using a radical polymerization initiation catalyst and a method of irradiating active energy rays. Examples of radical polymerization initiation catalysts include peroxides such as hydrogen peroxide and benzoyl peroxide; azo compounds such as 2-2'-azobis-2-amidinopropane dihydrochloride and azobisisobutyronitrile;
Radical generators such as persulfates such as ammonium persulfate, potassium persulfate, and sodium persulfate, and combinations of these radical generators with sodium bisulfite, L-ascorbic acid,
A redox initiator in combination with a reducing agent such as a ferrous salt is used. The amount used is based on the monomer component (
0.01 to 1.0% by weight, preferably 0.01 to 1.0% by weight based on A).
05 to 0.5% by weight. During aqueous solution polymerization,
It is preferable to use only water as the polymerization solvent, but methanol, ethanol, isopropanol,
A hydrophilic organic solvent such as acetone, dimethylformamide, dimethyl sulfoxide, etc. may be added to water.

【0026】水溶液重合時の単量体成分(A)の濃度は
特に制限されずに広い範囲とすることができるが、重合
反応の制御の容易さや、収率を考慮すれば、単量体成分
(A):水の比率を1:9〜7:3(重量比)、特に3
:7〜5:5の範囲とするのが好ましい。
The concentration of the monomer component (A) during aqueous solution polymerization is not particularly limited and can be set within a wide range, but in consideration of ease of controlling the polymerization reaction and yield, (A):Water ratio of 1:9 to 7:3 (weight ratio), especially 3
It is preferable to set it as the range of :7-5:5.

【0027】本発明において耐塩性とは、吸収させる水
溶液中の塩濃度における、吸収倍率の変化の程度が少な
いことを意味し、耐塩性=生理食塩水の吸収倍率/純水
(脱イオン水)の吸収倍率と定義される。
[0027] In the present invention, salt tolerance means that the degree of change in absorption capacity is small depending on the salt concentration in the aqueous solution to be absorbed, and salt tolerance = absorption capacity of physiological saline/pure water (deionized water). It is defined as the absorption capacity of

【0028】吸水性樹脂の耐塩性が向上すると、例えば
紙おむつや生理用品中の吸収剤に用いた場合には、尿中
の塩濃度の影響をうけにくく、安定した吸収倍率を有し
液体の吸収性に優れたものとなり、また、海水等のシー
ル剤に用い場合には、シール効果が塩濃度によって影響
され難くなる利点がある。
If the salt resistance of the water-absorbing resin is improved, for example, when used as an absorbent in disposable diapers or sanitary products, it will be less affected by the salt concentration in urine, and will have a stable absorption capacity and absorb liquid. Furthermore, when used as a sealant for seawater, etc., there is an advantage that the sealing effect is less affected by salt concentration.

【0029】[0029]

【実施例】以下、実施例により本発明を詳細に説明する
が、本発明の範囲はこれらの実施例によって何ら制限さ
れるものではない。
EXAMPLES The present invention will be explained in detail below with reference to Examples, but the scope of the present invention is not limited in any way by these Examples.

【0030】耐塩性吸水性樹脂の吸収倍率、ゲル強度は
、次に示す方法により測定した。
The absorption capacity and gel strength of the salt-resistant water-absorbing resin were measured by the following methods.

【0031】(1)純水(脱イオン水)の吸収倍率;耐
塩性吸水性樹脂約0.05gを不織布製のティーバッグ
式袋(40mm×150mm)に均一に入れ、大過剰の
純水(脱イオン水)に30分間浸漬し、引き上げてペー
パー上で水切りを行い、吸液後の重量を測定した。空の
ティーバッグ式袋自体を同様の手順で吸液した時の重量
をブランクとして、次式にしたがって純水(脱イオン水
)の吸収倍率を算出した。純水(脱イオン水)の吸収倍
率(g/g)=( 吸液後の重量g−ブランクg)/(
耐塩性樹脂の重量g) (2)生理食塩水の吸収倍率;耐塩性吸水性樹脂約0.
2gを不織布製のティーバッグ式袋(40mm×150
mm)に均一に入れ、大過剰の生理食塩水(0.9重量
%NaCl)に30分間浸漬し膨潤させ、引き上げてペ
ーパー上で水切りをし、吸液後の重量を測定した。空の
ティーバッグ式袋自体を同様の手順で吸液した時の重量
をブランクとして、次式にしたがって純水の吸収倍率を
算出した。
(1) Absorption capacity of pure water (deionized water): Approximately 0.05 g of salt-resistant water-absorbing resin is uniformly placed in a non-woven tea bag type bag (40 mm x 150 mm), and a large excess of pure water ( The sample was immersed in deionized water for 30 minutes, pulled out and drained on paper, and the weight after absorbing the liquid was measured. The absorption capacity of pure water (deionized water) was calculated according to the following formula using the weight of an empty tea bag itself as a blank after absorbing the liquid in the same manner. Absorption capacity of pure water (deionized water) (g/g) = (weight after absorption g - blank g) / (
Weight of salt-resistant resin (g) (2) Absorption capacity of physiological saline; salt-resistant water-absorbent resin approximately 0.
2g in a non-woven tea bag type bag (40mm x 150mm)
mm), immersed in a large excess of physiological saline (0.9% by weight NaCl) for 30 minutes to swell, pulled out, drained on paper, and measured the weight after absorbing the liquid. The absorption capacity of pure water was calculated according to the following formula using the weight of an empty tea bag itself as a blank after absorbing the liquid in the same manner.

【0032】生理食塩水の吸収倍率(g/g)=(吸液
後の重量g−ブランクg)/(耐塩性樹脂の重量g)な
お、耐塩性は、耐塩性=生理食塩水の吸収倍率/純水(
脱イオン水)の吸収倍率で表す。
Absorption capacity of physiological saline (g/g) = (weight after absorption g - blank g) / (weight of salt-resistant resin g) Note that salt tolerance = absorption capacity of physiological saline /Pure water(
It is expressed as the absorption capacity of deionized water).

【0033】(3)ゲル強度;膨潤ヒドロゲルを、半径
2.5cmの円盤を具備する応力レオメーターにより、
試料の厚み0.1cm、振動周波数1.0Hzの条件下
に測定した。膨潤ヒドロゲルの剪断弾性率をもってゲル
強度とした。なお、膨潤ヒドロゲルは、耐塩性吸水性樹
脂を人工尿(尿素  1.9重量%、NaCl  0.
8重量%、CaCl2  0.1重量%、MgSO4 
 0.1重量%)に1時間浸漬し膨潤させた後、過剰の
人工尿を濾紙で除去することによって得た。
(3) Gel strength: The swollen hydrogel was measured using a stress rheometer equipped with a disk with a radius of 2.5 cm.
The measurement was performed under the conditions that the sample thickness was 0.1 cm and the vibration frequency was 1.0 Hz. The shear modulus of the swollen hydrogel was defined as gel strength. The swollen hydrogel was prepared by mixing a salt-resistant water-absorbing resin with artificial urine (1.9% by weight of urea, 0.0% by weight of NaCl).
8% by weight, CaCl2 0.1% by weight, MgSO4
0.1% by weight) for 1 hour to swell, and then excess artificial urine was removed with a filter paper.

【0034】実施例1羽根の回転径が120mmのシグ
マ型羽根を2本有した内容積10リットルのジャケット
付きステンレス製双腕型ニーダーに、アクリル酸ナトリ
ウム75モル%およびアクリル酸25モル%からなる単
量体成分(A)の水溶液4400g(単量体成分の濃度
37重量%)と、架橋剤としてのトリメチルメチロール
プロパンアクリレート2.72g(0.05モル%対単
量体成分(A))とを入れ、窒素ガスを吹き込んで反応
系内を窒素置換した。次いで2本のシグマ型羽根を、回
転させながら、吸水性樹脂(日本触媒化学工業株式会社
製、アクアリックCA)をハンマーミルで粉砕し、10
0メッシュの金網を通過させて得られた粒子径1〜14
9μmの吸水性樹脂(B)162g(10重量%対単量
体成分(A))を入れ、ジャケットに30℃の温水を通
すことによって反応径内を加熱しながら、開始剤として
過硫酸ナトリウム1.20gと亜硫酸水素ナトリウム1
.10gとを添加した。重合反応開始後更に60分間重
合反応を続行して得られたゲル重合体は、約3mmの径
の細粒に細分化されていた。得られたゲル重合体を金網
上で150℃の温度条件下に2時間熱風乾燥した。この
乾燥物をハンマーミルを用いて粉砕し、耐塩性吸水性樹
脂を得た。得られた耐塩性吸水性樹脂の性能を表1に示
す。
Example 1 A jacketed stainless steel double-arm kneader having an internal volume of 10 liters and having two sigma-type blades with a rotating diameter of 120 mm was charged with a mixture of 75 mol% sodium acrylate and 25 mol% acrylic acid. 4400 g of an aqueous solution of monomer component (A) (concentration of monomer component 37% by weight), 2.72 g of trimethylmethylolpropane acrylate as a crosslinking agent (0.05 mol% to monomer component (A)) was added and nitrogen gas was blown into the reaction system to replace the inside of the reaction system with nitrogen. Next, while rotating the two sigma-type blades, a water-absorbing resin (Nippon Shokubai Kagaku Kogyo Co., Ltd., Aqualic CA) was crushed with a hammer mill, and
Particle size 1 to 14 obtained by passing through a wire mesh of 0 mesh
162 g of a 9 μm water-absorbing resin (B) (10% by weight vs. monomer component (A)) was added, and while heating the inside of the reaction diameter by passing 30°C hot water through the jacket, 11 g of sodium persulfate was added as an initiator. .20g and 1 sodium bisulfite
.. 10g was added. The gel polymer obtained by continuing the polymerization reaction for another 60 minutes after the start of the polymerization reaction was subdivided into fine particles with a diameter of about 3 mm. The obtained gel polymer was dried with hot air on a wire mesh at a temperature of 150° C. for 2 hours. This dried product was pulverized using a hammer mill to obtain a salt-resistant water-absorbing resin. Table 1 shows the performance of the obtained salt-resistant water-absorbing resin.

【0035】実施例2実施例1において吸水性樹脂(B
)の量を407g(25重量%対単量体成分(A))と
する以外は、実施例1と同様な操作を繰り返して、耐塩
性吸水性樹脂を得た。この耐塩性吸水性樹脂の性能を表
1に示す。
Example 2 In Example 1, water absorbent resin (B
) was changed to 407 g (25% by weight vs. monomer component (A)), but the same operation as in Example 1 was repeated to obtain a salt-resistant water-absorbing resin. Table 1 shows the performance of this salt-resistant water absorbent resin.

【0036】実施例3実施例2において架橋剤を用いな
かった以外は、実施例2と同様な操作を繰り返して、耐
塩性吸水性樹脂を得た。この耐塩性吸水性樹脂の性能を
表1に示す。
Example 3 A salt-resistant water-absorbing resin was obtained by repeating the same operations as in Example 2, except that no crosslinking agent was used in Example 2. Table 1 shows the performance of this salt-resistant water absorbent resin.

【0037】実施例4実施例1で用いたのと同様の双腕
型ニーダーに、アクリル酸ナトリウム282gおよびア
クリル酸108gおよびスルホエチルアクリレートのナ
トリウム塩606gからなる単量体成分(A)の水溶液
2490g(単量体成分の濃度40重量%)と、架橋剤
としてのトリメチルメチロールプロパントリアクリレー
ト0.888g(0.04モル%対単量体成分(A))
とを入れ、窒素ガスを吹き込んで反応系内を窒素置換し
た。次いで2本のシグマ型羽根を、それぞれ回転させな
がら、実施例1で用いた吸水性樹脂(B)97g(10
重量%対単量体成分(A))を入れ、ジャケットに30
℃の温水を通すことによって反応系内を加熱しながら、
重合開始剤として過硫酸ナトリウム0.9gとL−アス
コルビン酸0.038gとを添加した。重合反応開始後
更に90分間重合反応を続行して得られたゲル重合体は
、約3mmの径の細粒に細分化されていた。得られたゲ
ル重合体を金網上で150℃の温度条件下に2時間熱風
乾燥した。この乾燥物をハンマーミルを用いて粉砕し、
耐塩性吸水性樹脂を得た。得られた耐塩性吸水性樹脂の
性能を表1に示す。
Example 4 In a double-arm kneader similar to that used in Example 1, 2490 g of an aqueous solution of monomer component (A) consisting of 282 g of sodium acrylate, 108 g of acrylic acid, and 606 g of sodium salt of sulfoethyl acrylate was added. (concentration of monomer component 40% by weight) and 0.888 g of trimethylmethylolpropane triacrylate as a crosslinking agent (0.04 mol% vs. monomer component (A))
and nitrogen gas was blown into the reaction system to replace the inside of the reaction system with nitrogen. Next, while rotating the two sigma-type blades, 97 g (10
% by weight vs. monomer component (A)) and put 30% by weight into the jacket.
While heating the reaction system by passing hot water at ℃,
0.9 g of sodium persulfate and 0.038 g of L-ascorbic acid were added as polymerization initiators. The gel polymer obtained by continuing the polymerization reaction for an additional 90 minutes after the start of the polymerization reaction was subdivided into fine particles with a diameter of about 3 mm. The obtained gel polymer was dried with hot air on a wire mesh at a temperature of 150° C. for 2 hours. This dried product is crushed using a hammer mill,
A salt-resistant water absorbent resin was obtained. Table 1 shows the performance of the obtained salt-resistant water-absorbing resin.

【0038】実施例5実施例4において架橋剤を用いな
かった以外は、実施例4と同様な操作を繰り返して、耐
塩性吸水性樹脂を得た。この耐塩性吸水性樹脂の性能を
表1に示す。実施例6実施例4において吸水性樹脂(B
)の量を49.8g(5重量%対単量体成分(A))と
する以外は、実施例4と同様な操作を繰り返して、耐塩
性吸水性樹脂を得た。この耐塩性吸水性樹脂の性能を表
1に示す。
Example 5 A salt-resistant water-absorbing resin was obtained by repeating the same procedure as in Example 4, except that no crosslinking agent was used. Table 1 shows the performance of this salt-resistant water absorbent resin. Example 6 In Example 4, water absorbent resin (B
) was changed to 49.8 g (5% by weight vs. monomer component (A)), but the same operation as in Example 4 was repeated to obtain a salt-resistant water-absorbent resin. Table 1 shows the performance of this salt-resistant water absorbent resin.

【0039】実施例7実施例1において吸水性樹脂(B
)の量を20メッシュの金網を通過した粒子径1〜84
0μmの粉末とする以外は、実施例1と同様な操作を繰
り返して、耐塩性吸水性樹脂を得た。この耐塩性吸水性
樹脂の性能を表1に示す。
Example 7 In Example 1, water absorbent resin (B
) with a particle diameter of 1 to 84 that passed through a 20 mesh wire mesh.
A salt-resistant water-absorbing resin was obtained by repeating the same operation as in Example 1 except that the powder had a particle size of 0 μm. Table 1 shows the performance of this salt-resistant water absorbent resin.

【0040】比較例1実施例1において吸水性樹脂(B
)の量を3256g(50重量%対単量体成分(A))
とする以外は、実施例1と同様な操作を繰り返して、比
較用樹脂を得た。この比較用樹脂の性能を表1に示す。
Comparative Example 1 In Example 1, water absorbent resin (B
) amount to 3256g (50% by weight vs. monomer component (A))
A comparative resin was obtained by repeating the same operation as in Example 1 except for the following. The performance of this comparative resin is shown in Table 1.

【0041】比較例2実施例1において吸水性樹脂(B
)を用いなかった以外は、実施例1と同様な操作を繰り
返して、比較用樹脂を得た。この比較用樹脂の性能を表
1に示す。
Comparative Example 2 In Example 1, water absorbent resin (B
) was not used, but the same operation as in Example 1 was repeated to obtain a comparative resin. The performance of this comparative resin is shown in Table 1.

【0042】比較例3実施例1において架橋剤量を27
.2g(0.5モル%対単量体成分(A))とし、かつ
吸水性樹脂(B)を用いなかった以外は、実施例1と同
様な操作を繰り返して、比較用樹脂を得た。この比較用
樹脂の性能を表1に示す。
Comparative Example 3 In Example 1, the amount of crosslinking agent was changed to 27
.. A comparative resin was obtained by repeating the same operation as in Example 1, except that the amount was 2 g (0.5 mol % vs. monomer component (A)) and the water-absorbing resin (B) was not used. The performance of this comparative resin is shown in Table 1.

【0043】比較例4減圧乾燥法にて充分に脱水を行っ
た平均分子量10万のポリエチレンオキシド樹脂20部
およびトリエチレンジアミン0.05部をアセトニトリ
ル280部中に加え、窒素雰囲気中30〜40℃にて完
全に溶解せしめた後、1,4−フェニレンジイソシアナ
ート0.2部を加え70℃にて5時間反応を行い、水に
不溶性の均一な樹脂溶液を得た。この反応生成物をガラ
スシャーレ中に流延し40℃にて真空乾燥を行い、粉砕
することにより比較用樹脂を得た。この比較用樹脂の性
能を表1に示す。
Comparative Example 4 20 parts of a polyethylene oxide resin having an average molecular weight of 100,000 and 0.05 part of triethylenediamine, which had been thoroughly dehydrated using a vacuum drying method, were added to 280 parts of acetonitrile, and the mixture was heated to 30 to 40°C in a nitrogen atmosphere. After completely dissolving the mixture, 0.2 part of 1,4-phenylene diisocyanate was added and the reaction was carried out at 70°C for 5 hours to obtain a uniform water-insoluble resin solution. This reaction product was cast into a glass Petri dish, vacuum dried at 40°C, and pulverized to obtain a comparative resin. The performance of this comparative resin is shown in Table 1.

【0044】比較例5実施例3において吸水性樹脂(B
)を用いなかった以外は、実施例3と同様な操作を繰り
返して、比較用樹脂を得た。この比較用樹脂の性能を表
1に示す。
Comparative Example 5 In Example 3, water absorbent resin (B
) was not used, but the same operation as in Example 3 was repeated to obtain a comparative resin. The performance of this comparative resin is shown in Table 1.

【0045】比較例6攪拌機、還流冷却器、温度計、窒
素ガス導入管および滴下ロートを付した2リットルの四
つ口セパラブルフラスコにシクロヘキサン1.0リット
ルを取り、分散剤としてソルビタンモノステアレート3
.0gを加えて溶解させ、窒素ガスを吹き込んで溶存酸
素を追い出した。
Comparative Example 6 1.0 liter of cyclohexane was placed in a 2 liter four-necked separable flask equipped with a stirrer, reflux condenser, thermometer, nitrogen gas inlet tube and dropping funnel, and sorbitan monostearate was added as a dispersant. 3
.. 0 g was added and dissolved, and nitrogen gas was blown in to drive out the dissolved oxygen.

【0046】別にフラスコ中にアクリル酸ナトリウム8
4.6g、アクリル酸21.6gおよび架橋剤としてN
,N´−メチレンビスアクリルアミド0.0925g(
0.05モル%対単量体成分(A))をイオン交換水1
97gに溶解し、更に実施例1で用いた吸水性樹脂(B
)10.6g(10重量%対単量体成分(A))を加え
て単量体水溶液を調整した。
Separately, in a flask, add 88% of sodium acrylate.
4.6 g, 21.6 g of acrylic acid and N as a crosslinking agent.
, N'-methylenebisacrylamide 0.0925g (
0.05 mol% of monomer component (A)) in ion-exchanged water 1
97g of the water-absorbing resin (B) used in Example 1.
) 10.6 g (10% by weight vs. monomer component (A)) was added to prepare an aqueous monomer solution.

【0047】この単量体水溶液に過硫酸カリウム0.1
5gを加えて溶解させた後、窒素ガスを吹き込んで水溶
液内に溶存する酸素を追い出した。
Add 0.1 potassium persulfate to this monomer aqueous solution.
After adding and dissolving 5 g, nitrogen gas was blown into the aqueous solution to drive out oxygen dissolved in the aqueous solution.

【0048】次いで、このフラスコ内の単量体水溶液を
上記セパラブルフラスコに加えて、撹拌することにより
分散させた。その後、浴温を65℃に昇温して重合反応
を開始させた後、2時間この温度を保持して重合を完了
した。重合終了後シクロヘキサンとの共沸脱水により含
水ゲル中の水を留去した後、濾過し、比較用樹脂を得た
。この比較用樹脂の性能を表1に示す。
Next, the aqueous monomer solution in this flask was added to the separable flask and dispersed by stirring. Thereafter, the bath temperature was raised to 65° C. to initiate the polymerization reaction, and this temperature was maintained for 2 hours to complete the polymerization. After the polymerization was completed, the water in the hydrous gel was distilled off by azeotropic dehydration with cyclohexane, and then filtered to obtain a comparative resin. The performance of this comparative resin is shown in Table 1.

【0049】[0049]

【表1】[Table 1]

【0050】[0050]

【発明の効果】本発明の不飽和カルボン酸およびその塩
よりなる群から選ばれた少なくとも1種の単量体成分(
A)の水溶液を、該単量体成分(A)100重量部当た
り吸水性樹脂(B)1〜30重量部の割合で存在させて
水溶液重合することよりなる耐塩性吸水性樹脂の製造方
法により得られた耐塩性が向上した耐塩性吸水性樹脂を
、例えば紙おむつや生理用品中の吸収剤に用いた場合に
は、尿中の塩濃度の影響をうけにくく、安定した吸収倍
率を有し液体の吸収性に優れたものとなり、また、海水
等のシール剤に用い場合には、シール効果が塩濃度によ
って影響され難くなる利点がある。
Effect of the invention: At least one monomer component selected from the group consisting of unsaturated carboxylic acids and salts thereof of the present invention (
By a method for producing a salt-resistant water-absorbing resin, which comprises polymerizing an aqueous solution of A) in a ratio of 1 to 30 parts by weight of the water-absorbing resin (B) per 100 parts by weight of the monomer component (A). When the obtained salt-resistant water-absorbing resin with improved salt resistance is used as an absorbent in disposable diapers or sanitary products, for example, it is less affected by the salt concentration in urine, has a stable absorption capacity, and can be used as a liquid absorbent. It has excellent absorbency, and when used as a sealant for seawater, etc., it has the advantage that the sealing effect is less affected by salt concentration.

Claims (18)

【特許請求の範囲】[Claims] 【請求項1】  不飽和カルボン酸およびその塩よりな
る群から選ばれた少なくとも1種の単量体成分(A)の
水溶液を、該単量体成分(A)100重量部当たり吸水
性樹脂(B)1〜30重量部の割合で存在させて水溶液
重合することよりなる耐塩性吸水性樹脂の製造方法。
Claim 1: An aqueous solution of at least one monomer component (A) selected from the group consisting of unsaturated carboxylic acids and salts thereof is added to a water-absorbing resin (per 100 parts by weight of the monomer component (A)). B) A method for producing a salt-resistant water-absorbing resin, which comprises polymerizing in an aqueous solution in the presence of 1 to 30 parts by weight.
【請求項2】  水溶液重合が撹拌混合下に行われる請
求項1に記載の耐塩性吸水性樹脂の製造方法。
2. The method for producing a salt-resistant water-absorbing resin according to claim 1, wherein the aqueous solution polymerization is carried out under stirring and mixing.
【請求項3】  水溶液重合が複数の回転撹拌軸を有す
る反応容器内で撹拌混合下に行われる請求項2に記載の
耐塩性吸水性樹脂の製造方法。
3. The method for producing a salt-resistant water-absorbing resin according to claim 2, wherein the aqueous solution polymerization is carried out under stirring and mixing in a reaction vessel having a plurality of rotating stirring shafts.
【請求項4】  複数の回転撹拌軸を有する反応容器が
ニーダーである請求項3に記載の耐塩性吸水性樹脂の製
造方法。
4. The method for producing a salt-resistant water-absorbing resin according to claim 3, wherein the reaction vessel having a plurality of rotating stirring shafts is a kneader.
【請求項5】  単量体成分(A)に対して架橋剤を0
.001〜0.1モル%の量で用いる請求項1に記載の
耐塩性吸水性樹脂の製造方法。
[Claim 5] 0 crosslinking agent is added to the monomer component (A).
.. The method for producing a salt-resistant water-absorbing resin according to claim 1, wherein the salt-resistant water-absorbing resin is used in an amount of 0.001 to 0.1 mol%.
【請求項6】  該単量体成分(A)100重量部当た
り該吸水性樹脂(B)5〜20重量部の量の存在下に水
溶液重合が行われる請求項1に記載の耐塩性吸水性樹脂
の製造方法。
6. The salt-resistant water absorbent according to claim 1, wherein the aqueous solution polymerization is carried out in the presence of 5 to 20 parts by weight of the water absorbent resin (B) per 100 parts by weight of the monomer component (A). Method of manufacturing resin.
【請求項7】  該吸水性樹脂(B)の含水率が0.1
〜10重量%である請求項1に記載の耐塩性吸水性樹脂
の製造方法。
[Claim 7] The water content of the water absorbent resin (B) is 0.1.
The method for producing a salt-resistant water-absorbing resin according to claim 1, wherein the amount is 10% by weight.
【請求項8】  該吸水性樹脂(B)の90〜100重
量%が1〜149μmの粒径を有するものである請求項
1に記載の耐塩性吸水性樹脂の製造方法。
8. The method for producing a salt-resistant water-absorbing resin according to claim 1, wherein 90 to 100% by weight of the water-absorbing resin (B) has a particle size of 1 to 149 μm.
【請求項9】  該吸水性樹脂(B)が水溶液重合によ
り得られるものである請求項1に記載の耐塩性吸水性樹
脂の製造方法。
9. The method for producing a salt-resistant water-absorbing resin according to claim 1, wherein the water-absorbing resin (B) is obtained by aqueous solution polymerization.
【請求項10】  該吸水性樹脂(B)が単量体成分(
A)を重合することにより得られるものである請求項1
に記載の耐塩性吸水性樹脂の製造方法。
10. The water-absorbing resin (B) comprises a monomer component (
Claim 1, which is obtained by polymerizing A)
A method for producing a salt-resistant water-absorbing resin as described in .
【請求項11】  該単量体成分(A)が(メタ)アク
リル酸、クロトン酸、イタコン酸、マレイン酸、フマル
酸、シトラコン酸およびそれらの塩よりなる群から選ば
れた少なくとも1種のものである請求項1に記載の耐塩
性吸水性樹脂の製造方法。
11. The monomer component (A) is at least one member selected from the group consisting of (meth)acrylic acid, crotonic acid, itaconic acid, maleic acid, fumaric acid, citraconic acid, and salts thereof. The method for producing a salt-resistant water-absorbing resin according to claim 1.
【請求項12】  該単量体成分(A)が(メタ)アク
リル酸およびそれらの塩よりなる群から選ばれた少なく
とも1種のものである請求項1に記載の耐塩性吸水性樹
脂の製造方法。
12. Production of the salt-resistant water-absorbing resin according to claim 1, wherein the monomer component (A) is at least one member selected from the group consisting of (meth)acrylic acid and salts thereof. Method.
【請求項13】  該単量体成分(A)が(メタ)アク
リル酸10〜70モル%およびアクリル酸塩90〜30
モル%よりなるものである請求項12に記載の耐塩性吸
水性樹脂の製造方法。
13. The monomer component (A) comprises 10 to 70 mol % of (meth)acrylic acid and 90 to 30 mol % of an acrylic acid salt.
13. The method for producing a salt-resistant water-absorbing resin according to claim 12, wherein the salt-resistant water-absorbing resin is composed of mol%.
【請求項14】  該単量体成分(A)に対して架橋剤
を0.001〜0.1モル%の量で用いる請求項13に
記載の耐塩性吸水性樹脂の製造方法。
14. The method for producing a salt-resistant water-absorbing resin according to claim 13, wherein the crosslinking agent is used in an amount of 0.001 to 0.1 mol % based on the monomer component (A).
【請求項15】  該吸水性樹脂(B)が部分中和アク
リル酸塩重合体の架橋体である請求項1に記載の耐塩性
吸水性樹脂の製造方法。
15. The method for producing a salt-resistant water-absorbing resin according to claim 1, wherein the water-absorbing resin (B) is a crosslinked product of a partially neutralized acrylate polymer.
【請求項16】  該吸水性樹脂(B)が請求項13に
記載の単量体成分(A)を水溶液重合して得られるもの
である請求項1に記載の耐塩性吸水性樹脂の製造方法。
16. The method for producing a salt-resistant water-absorbing resin according to claim 1, wherein the water-absorbing resin (B) is obtained by aqueous solution polymerization of the monomer component (A) according to claim 13. .
【請求項17】  該吸水性樹脂(B)が架橋剤を0.
001〜0.1モル%含有しアクリル酸中のカルボキシ
ル基を0.3〜0.9当量中和してなる単量体の重合体
の架橋体である請求項15に記載の耐塩性吸水性樹脂の
製造方法。
17. The water-absorbing resin (B) contains a crosslinking agent of 0.0%.
16. The salt-resistant water absorbent according to claim 15, which is a crosslinked product of a monomer polymer containing 0.001 to 0.1 mol% and neutralized with 0.3 to 0.9 equivalents of carboxyl groups in acrylic acid. Method of manufacturing resin.
【請求項18】  水溶液重合により得られた含水吸水
性樹脂を乾燥し、ついで分級により該吸水性樹脂(B)
の粒度範囲に相当する吸水性樹脂(C)を除去する請求
項1に記載の耐塩性吸水性樹脂の製造方法。
18. The water-containing water absorbent resin obtained by aqueous solution polymerization is dried, and then classified to produce the water absorbent resin (B).
2. The method for producing a salt-resistant water-absorbing resin according to claim 1, wherein the water-absorbing resin (C) having a particle size range of .
JP9521591A 1990-04-27 1991-04-25 Method for producing salt-resistant water-absorbent resin Expired - Lifetime JP2901368B2 (en)

Priority Applications (1)

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Application Number Priority Date Filing Date Title
JP2-110089 1990-04-27
JP11008990 1990-04-27
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US9775927B2 (en) 2009-09-29 2017-10-03 Nippon Shokubai Co., Ltd. Particulate water absorbent and process for production thereof
US8952116B2 (en) 2009-09-29 2015-02-10 Nippon Shokubai Co., Ltd. Particulate water absorbent and process for production thereof
KR20160128350A (en) 2014-03-03 2016-11-07 가부시키가이샤 닛폰 쇼쿠바이 Method for producing polyacrylic acid (salt)-based water-absorbable resin
US9896529B2 (en) 2014-03-03 2018-02-20 Nippon Shokubai Co., Ltd. Method for producing polyacrylic acid (salt)-based water-absorbable resin
JP2019533502A (en) * 2016-10-06 2019-11-21 メディケム テクノロジー スポレチノスト エス ルチェニム オメゼニム Cervical dilator using osmosis and hydrogel and method for producing the same
WO2021044690A1 (en) 2019-09-06 2021-03-11 ユニ・チャーム株式会社 Method for producing recycled superabsorbent polymer, method for producing superabsorbent polymer using recycled superabsorbent polymer, and recycled superabsorbent polymer

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