JPS58154709A - Production of cationic, highly water-absorptive resin - Google Patents
Production of cationic, highly water-absorptive resinInfo
- Publication number
- JPS58154709A JPS58154709A JP3591582A JP3591582A JPS58154709A JP S58154709 A JPS58154709 A JP S58154709A JP 3591582 A JP3591582 A JP 3591582A JP 3591582 A JP3591582 A JP 3591582A JP S58154709 A JPS58154709 A JP S58154709A
- Authority
- JP
- Japan
- Prior art keywords
- water
- acrylamide
- meth
- polymerization
- weight
- 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
Links
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- Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
Abstract
Description
【発明の詳細な説明】
本発明は水溶性単量体をジビニル化合物と共重合させて
、水不溶性で自重の数百倍の水を吸収する高吸水性樹脂
の製法に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for producing a water-insoluble superabsorbent resin that absorbs several hundred times its own weight of water by copolymerizing a water-soluble monomer with a divinyl compound.
従東、水を吸収し保持するものとしては、パルプ製品が
使われて来た。しかしながら、□パルプの吸水量は自重
の10倍程度であり、多量の水を吸収、保持しようとす
るとパルプを多量に必要とし、大変かさ高いものとなっ
てしまい、又、吸水したものに圧力を加えると簡単に水
を分離する欠点を有していた。In Japan, pulp products have been used to absorb and retain water. However, the amount of water absorbed by pulp is about 10 times its own weight, and if you try to absorb and retain a large amount of water, you will need a large amount of pulp, resulting in a very bulky product. It had the disadvantage of easily separating water when added.
そこで、わずかな重量で多量の水を吸収し、保持する高
吸水性樹脂の開発が種々なされて来た。この高吸水性樹
脂は自重の数百倍の水を吸収、保持し、しかも、吸水し
た状態で安定なゲルとなり多少の圧力を加えても水を分
離しない特徴を有している。このような高吸水性樹脂は
使い捨ておむつ、ナプキン、微生物の培地、園芸用保水
剤等、巾広い用途を持っている。すでに開発された高吸
水性樹脂としては、澱粉グラフト重合体(特公昭53−
46199)セルロース変成物(特開昭5O−8037
6)などがあるか、澱粉グラフト暇合体は含水ゲルとし
て長期間使用した場合、澱粉が腐敗するおそれがあり、
また、セルロース変成物では吸水量がセルロースに比較
してそれほど多(はないという欠点を有している。Therefore, various efforts have been made to develop super absorbent resins that absorb and retain large amounts of water with a small weight. This super-absorbent resin absorbs and retains several hundred times its own weight in water, and has the characteristic that it forms a stable gel when it absorbs water, and does not separate water even when a small amount of pressure is applied. Such superabsorbent resins have a wide range of uses, including disposable diapers, napkins, microbial culture media, and water retention agents for gardening. As a super absorbent resin that has already been developed, starch graft polymer
46199) Cellulose modified product (JP-A-5O-8037
6) If starch graft time coalescence is used as a water-containing gel for a long period of time, the starch may rot.
Furthermore, modified cellulose has the disadvantage that it absorbs less water than cellulose.
本発明者らは、この欠点を克服すへく鋭意研究をした結
果、本発明に到達した。The present inventors conducted intensive research to overcome this drawback, and as a result, they arrived at the present invention.
すなわち、本発明は、三級アミノ基もしくは四級アミノ
基を°有するビニル単量体とアクリルアミドをモル比で
25ニア5〜100:0の範囲で共重合するにあたり、
全単量体100重量部に対して0005〜01重量部の
水混和性乃〒水溶性ジヒニル化合物を共存させることを
特徴とするカチオノ性高吸水性樹脂の製法に関するもの
である。That is, in the present invention, when copolymerizing a vinyl monomer having a tertiary amino group or a quaternary amino group and acrylamide at a molar ratio in the range of 25 to 100:0,
The present invention relates to a method for producing a cationic superabsorbent resin, characterized in that 0.005 to 0.01 parts by weight of a water-miscible or water-soluble dihinyl compound is allowed to coexist with 100 parts by weight of the total monomers.
本発明に用いる三級アミノ基もしくは四級アミノ基を有
するビニル単量体としては、ジメチルアミノエチル(メ
タ)アクリレート、ジエチルアミノエチル(メタ)アク
リレート、ジメチルアミノプロピル(メタ)アクリルア
ミド、ジエチルアミノプロビル(メタ)アクリルアミド
、ジメチルアミノメチル(メタ)アクリルアミド、及び
これらを、塩化メチル、ジエチル硫酸、ジメチル硫酸等
で四級化した単量体等があげられるが、本発明において
は、単量体の種類は限定されるものではなく、これらの
二種類以上を剛いてもよい。Examples of vinyl monomers having a tertiary amino group or a quaternary amino group used in the present invention include dimethylaminoethyl (meth)acrylate, diethylaminoethyl (meth)acrylate, dimethylaminopropyl (meth)acrylamide, and diethylaminopropyl (meth)acrylate. ) acrylamide, dimethylaminomethyl (meth)acrylamide, and monomers obtained by quaternizing these with methyl chloride, diethyl sulfate, dimethyl sulfate, etc. However, in the present invention, the types of monomers are limited. However, two or more of these types may be used.
アミノ基を有するビニル単量体とアクリルアミドのモル
比については、アミノ基を有する単量体を25モル%未
満にしてアクリルアミドのモル比を高めると、含水ゲル
の強度は高(なるが、吸水能は低下してしまう。Regarding the molar ratio of the vinyl monomer having an amino group to acrylamide, if the molar ratio of acrylamide is increased by reducing the monomer having an amino group to less than 25 mol%, the strength of the hydrogel increases (although the water absorption capacity decreases). will decrease.
また、水混和性乃至水溶性ジビニル化合物としては、例
えば、N%N−メチレンビス(メタ)アクリルアミド、
ジ(メタ)アクリル酸テトラエチレングリコール、ジ(
メタ)アクリル酸デカエチレングリコール等があげられ
るが、N、N−メチレンヒスアクリルアミドが工業的に
好ましい。ジビニル化合物の熾はアミノ基を有する単量
体とアクリルアミドの重量の和を100重量部とした時
に0.005〜0.1重量部が好まし々、この範囲より
少ないと含水ゲルが半溶解状態となり、又、多いと架橋
度が増加し、いずれも吸水能が低下してしまう。In addition, examples of water-miscible or water-soluble divinyl compounds include N%N-methylenebis(meth)acrylamide,
Tetraethylene glycol di(meth)acrylate, di(meth)acrylate
Examples include decaethylene glycol meth)acrylate, but N,N-methylenehisacrylamide is industrially preferred. The strength of the divinyl compound is preferably 0.005 to 0.1 part by weight when the sum of the weights of the monomer having an amino group and acrylamide is 100 parts by weight, and if it is less than this range, the hydrogel will be in a semi-dissolved state. In addition, if the amount is too large, the degree of crosslinking will increase, and in both cases, the water absorption capacity will decrease.
本発明品を重合するにあたって、通常、水溶液中で行わ
れ、水溶液のPHは3〜7になるように酸によって調整
するのが好ましいが、酸の種類については特に抜定する
ものでElない。The polymerization of the product of the present invention is usually carried out in an aqueous solution, and the pH of the aqueous solution is preferably adjusted to 3 to 7 using an acid, but the type of acid is not particularly selected.
重合開始剤は、一般的に使用されているレドックス系、
アI系など、どのような物を使用してもよい。また、重
合濃度に関しては特に限定せず、任意の濃度範囲で選択
できるか、乾燥工程を考Mすると、できるだけ高濃度で
行う方が有利である。The polymerization initiator is a commonly used redox type,
Any material may be used, such as A-I type. Further, the polymerization concentration is not particularly limited and can be selected within any concentration range, or considering the drying process, it is advantageous to carry out the polymerization at a concentration as high as possible.
例えば、70%程度の高濃度水溶液で重合を行い、発生
する重合熱によって水分を蒸発させてしまい、そのまま
乾燥工程な経すに直接粉砕工程へ持って行く方法も選択
できる。また、開始温度については、開始剤の種類によ
って重合を開始させる温度が異なる為に、開始剤が後締
する一度以トで重合を開始させればよく、特に限定され
るものではない。For example, a method can be selected in which polymerization is carried out using a highly concentrated aqueous solution of about 70%, water is evaporated by the generated heat of polymerization, and the solution is directly taken to a pulverization step after a drying step. Furthermore, the starting temperature is not particularly limited, as the temperature at which polymerization starts varies depending on the type of initiator, and it is sufficient to start the polymerization once the initiator is used.
次に本発明を実施例に基づいてさらに具体的に説明する
が、本発明はその要旨を超えない限り、以下の実施例に
制約されるものではない。Next, the present invention will be described in more detail based on Examples, but the present invention is not limited to the following Examples unless it exceeds the gist thereof.
実施例1
ジメチルアミノエチルメタアクリレート41.3gとア
クリルアミド1g、7gを蒸留水140Sに溶解し、3
5%塩酸27.49でPHを4に調整した。さらにN、
N−メチレンビスアクリルアミドをo、oaf!加えた
。開始剤として2.2′−アノビス(2−アミジノプロ
パン)塩酸塩o、oayを加え、50°Cで重合を開始
させた。Example 1 41.3 g of dimethylaminoethyl methacrylate and 1 g and 7 g of acrylamide were dissolved in distilled water 140S,
The pH was adjusted to 4 with 5% hydrochloric acid at 27.49. Furthermore, N,
N-methylenebisacrylamide o, oaf! added. 2,2'-Anobis(2-amidinopropane) hydrochloride o, oay was added as an initiator, and polymerization was initiated at 50°C.
実施例2
ジメチルアミンエチルメタアクリレート53.8gアク
リルアミド16.211を蒸留水20gに溶解し、95
%硫酸17.5ノヒスイソブチロニトリル0,7gを溶
解したアセトン溶液を1Qcc加えた。この溶液を80
℃の恒温水槽で加温された箱型容器(テフロン加工した
ガラス繊維素材)の中に入れて加熱した。溶液の温度が
上昇すると共に重合反応が開始し、発生する重合熱によ
って水分が蒸発し、含水率の非常に低い多孔性固体とし
て高吸水性樹脂を得た。Example 2 53.8 g of dimethylamine ethyl methacrylate and 16.211 g of acrylamide were dissolved in 20 g of distilled water.
1 Qcc of an acetone solution containing 0.7 g of isobutyronitrile dissolved in 17.5% sulfuric acid was added. 80% of this solution
It was heated by placing it in a box-shaped container (Teflon-treated glass fiber material) heated in a constant temperature water bath at ℃. As the temperature of the solution rose, the polymerization reaction started, and water was evaporated by the generated heat of polymerization, yielding a super absorbent resin as a porous solid with a very low water content.
実施例3
メタアクリロキシエチルトリメチルアンモニウムクロリ
ドの80%水溶液100gに、N、N−メチレ/ビスア
クリルアミド0.06f1を加A、さらに開始剤として
、2.2′−アゾヒス(2−アミジノプロパン)塩酸増
o、 s Iiを加え混合した。この溶液を85°Cの
恒温水槽で加温された前述の箱型容器の中に入れて加熱
した。Example 3 0.06f1 of N,N-methylene/bisacrylamide was added to 100 g of an 80% aqueous solution of methacryloxyethyltrimethylammonium chloride, and 2,2'-azohis(2-amidinopropane) hydrochloric acid was added as an initiator. Add O, S Ii and mix. This solution was placed in the aforementioned box-shaped container heated in a constant temperature water bath at 85°C and heated.
重合が開始すると共に、重合熱により水分が蒸発し、含
水率の低い多孔性固体として高吸水性樹脂を得た。As the polymerization started, water evaporated due to the heat of polymerization, and a super absorbent resin was obtained as a porous solid with a low water content.
実施例4
実施例1で得られた重合物をアセトン脱水し乾燥させた
後粉砕した。また、実施例2.3で得られた重合物は乾
+QT、Pjを経ずに直接粉砕して粉末状の高吸水性樹
脂を得た。Example 4 The polymer obtained in Example 1 was dehydrated with acetone, dried, and then ground. Further, the polymer obtained in Example 2.3 was directly pulverized without passing through drying + QT and Pj to obtain a powdery super absorbent resin.
実施例1〜3の粉末高吸水性樹脂を市販品と比較し、吸
水試験を行った。試験方法は、蒸留水11に高吸水性樹
脂の粉末111を攪拌しながら加え、1時間放画した後
、100meshのふるいを用いてr過し、r液量から
吸水量を測定した。The powdered superabsorbent resins of Examples 1 to 3 were compared with commercially available products, and a water absorption test was conducted. The test method was to add superabsorbent resin powder 111 to distilled water 11 with stirring, leave it for 1 hour, pass through a 100 mesh sieve, and measure the amount of water absorbed from the amount of liquid.
また、1%食塩水、80%メタノール水溶液11に対し
、粉末を5!i加えて同様に吸水量を測定した。Also, 1% saline solution and 80% methanol aqueous solution 11 times, powder 5 times! In addition, water absorption was measured in the same manner.
その結果は、吸水倍率(吸水量÷加えた高吸水性樹脂の
重11)によって表1に示した。The results are shown in Table 1 in terms of water absorption capacity (water absorption amount ÷ weight of added super absorbent resin 11).
表1 吸水性能(吸水倍率)Table 1 Water absorption performance (water absorption capacity)
Claims (1)
体とアクリルアミドを、モル比で25ニア5〜too:
oの範囲で共重合するにあたり、全単量体100重量部
に対して0゜005〜0.1重量部の水混和性乃至水溶
性ジビニル化合物を共存させることを特徴とするカチオ
ノ性高吸水性樹脂の製法If q is a tertiary amino group, a vinyl monomer having a quaternary amino group and acrylamide are combined in a molar ratio of 25 to 5 to too:
0.005 to 0.1 part by weight of a water-miscible or water-soluble divinyl compound is present in the copolymerization in the range of 0.0 to 100 parts by weight of the total monomer. Resin manufacturing method
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP3591582A JPS58154709A (en) | 1982-03-09 | 1982-03-09 | Production of cationic, highly water-absorptive resin |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP3591582A JPS58154709A (en) | 1982-03-09 | 1982-03-09 | Production of cationic, highly water-absorptive resin |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS58154709A true JPS58154709A (en) | 1983-09-14 |
JPH0420006B2 JPH0420006B2 (en) | 1992-03-31 |
Family
ID=12455322
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP3591582A Granted JPS58154709A (en) | 1982-03-09 | 1982-03-09 | Production of cationic, highly water-absorptive resin |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS58154709A (en) |
Cited By (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS63137745A (en) * | 1986-11-28 | 1988-06-09 | Nippon Paint Co Ltd | Preparation of aqueous dispersion of cationic gel fine particles |
JPS63252593A (en) * | 1987-04-08 | 1988-10-19 | Kyoritsu Yuki Co Ltd | Aerobic biological treatment method |
JPS6415130A (en) * | 1987-07-09 | 1989-01-19 | Kyoritsu Yuki Co Ltd | Liquid dispersion of cationic highly water-absorptive resin and its production |
JPH02212505A (en) * | 1988-12-13 | 1990-08-23 | Smith Kline Ltd | Anion exchange polymer |
EP0612241A4 (en) * | 1991-10-21 | 1997-03-05 | Advanced Polymer Systems Inc | Ionic beads useful for controlled release and adsorption. |
US5760080A (en) * | 1994-06-13 | 1998-06-02 | Nippon Shokubai Co., Ltd. | Absorbing agent, process of manufacturing same, and absorbent product containing same |
US6413011B1 (en) | 1997-02-26 | 2002-07-02 | Rohm And Haas Company | Method for producing fast-drying multi-component waterborne coating compositions |
US6475556B1 (en) | 1999-11-25 | 2002-11-05 | Rohm And Haas Company | Method for producing fast drying multi-component waterborne coating compositions |
USRE38444E1 (en) | 1994-06-13 | 2004-02-24 | Nippon Shokubai Co., Ltd. | Absorbing agent, process of manufacturing same, and absorbent product containing same |
EP1570869A1 (en) | 1994-02-17 | 2005-09-07 | Nippon Shokubai Co., Ltd. | Water absorbent agent, method for production thereof, and water absorbent composition |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS50113591A (en) * | 1974-01-17 | 1975-09-05 | ||
JPS541398A (en) * | 1977-06-06 | 1979-01-08 | Konishiroku Photo Ind | Preparation of cationic high moleculare latex |
JPS58157885A (en) * | 1982-02-23 | 1983-09-20 | アライド コロイズ リミテイド | Heat energy accumulating composition and manufacture |
-
1982
- 1982-03-09 JP JP3591582A patent/JPS58154709A/en active Granted
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS50113591A (en) * | 1974-01-17 | 1975-09-05 | ||
JPS541398A (en) * | 1977-06-06 | 1979-01-08 | Konishiroku Photo Ind | Preparation of cationic high moleculare latex |
JPS58157885A (en) * | 1982-02-23 | 1983-09-20 | アライド コロイズ リミテイド | Heat energy accumulating composition and manufacture |
Cited By (13)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS63137745A (en) * | 1986-11-28 | 1988-06-09 | Nippon Paint Co Ltd | Preparation of aqueous dispersion of cationic gel fine particles |
JPS63252593A (en) * | 1987-04-08 | 1988-10-19 | Kyoritsu Yuki Co Ltd | Aerobic biological treatment method |
JPS6415130A (en) * | 1987-07-09 | 1989-01-19 | Kyoritsu Yuki Co Ltd | Liquid dispersion of cationic highly water-absorptive resin and its production |
JPH0553536B2 (en) * | 1987-07-09 | 1993-08-10 | Haimo Kk | |
JPH02212505A (en) * | 1988-12-13 | 1990-08-23 | Smith Kline Ltd | Anion exchange polymer |
EP0612241A4 (en) * | 1991-10-21 | 1997-03-05 | Advanced Polymer Systems Inc | Ionic beads useful for controlled release and adsorption. |
EP1570869A1 (en) | 1994-02-17 | 2005-09-07 | Nippon Shokubai Co., Ltd. | Water absorbent agent, method for production thereof, and water absorbent composition |
US5760080A (en) * | 1994-06-13 | 1998-06-02 | Nippon Shokubai Co., Ltd. | Absorbing agent, process of manufacturing same, and absorbent product containing same |
US6180724B1 (en) | 1994-06-13 | 2001-01-30 | Nippon Shokubai Co., Ltd. | Process for manufacturing an absorbing agent and absorbent material |
USRE38444E1 (en) | 1994-06-13 | 2004-02-24 | Nippon Shokubai Co., Ltd. | Absorbing agent, process of manufacturing same, and absorbent product containing same |
US6054541A (en) * | 1994-06-13 | 2000-04-25 | Nippon Shokubai Co., Ltd. | Process of manufacturing precursor of an absorbing agent |
US6413011B1 (en) | 1997-02-26 | 2002-07-02 | Rohm And Haas Company | Method for producing fast-drying multi-component waterborne coating compositions |
US6475556B1 (en) | 1999-11-25 | 2002-11-05 | Rohm And Haas Company | Method for producing fast drying multi-component waterborne coating compositions |
Also Published As
Publication number | Publication date |
---|---|
JPH0420006B2 (en) | 1992-03-31 |
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