JPH0420007B2 - - Google Patents

Info

Publication number
JPH0420007B2
JPH0420007B2 JP57035916A JP3591682A JPH0420007B2 JP H0420007 B2 JPH0420007 B2 JP H0420007B2 JP 57035916 A JP57035916 A JP 57035916A JP 3591682 A JP3591682 A JP 3591682A JP H0420007 B2 JPH0420007 B2 JP H0420007B2
Authority
JP
Japan
Prior art keywords
water
meth
liquid
polymerization
acrylamide
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.)
Expired - Lifetime
Application number
JP57035916A
Other languages
Japanese (ja)
Other versions
JPS58154710A (en
Inventor
Hisao Takeda
Yasunori Taniguchi
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.)
HAIMO KK
Original Assignee
HAIMO KK
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 HAIMO KK filed Critical HAIMO KK
Priority to JP3591682A priority Critical patent/JPS58154710A/en
Publication of JPS58154710A publication Critical patent/JPS58154710A/en
Publication of JPH0420007B2 publication Critical patent/JPH0420007B2/ja
Granted legal-status Critical Current

Links

Landscapes

  • Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)

Description

【発明の詳細な説明】 本発明は両性タイプの吸液樹脂に関するもので
ある。従来、水を吸収し保持するものとしてはパ
ルプ製品が多く使われてきた。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、たいへんかさ高いものとなつてしまい、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。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
種々なされてきた。これらの樹脂には澱粉グラフ
ト重合体(特公昭53−46199)ポリアクリル酸塩
の架橋物(特公昭54−30710)等があるが、これ
ら工業化されているもののほとんどはアニオン性
の高吸水性樹脂である。この樹脂の最大の欠点は
蒸留水では高吸水能を示すが、電解質溶液では著
しい吸水能の低下が見られる。高吸水性樹脂の用
途である使い捨ておむつ、生理用ナプキン、土壌
保水剤など純水が対象となることは少なく、ほと
んどが塩を含む液体を対象とするものである。 本発明者らはこの欠点を克服すべく鋭意研究を
した結果、両性タイプの吸液樹脂がアニオン性タ
イプのものより電解質溶液およびアルコールに対
し高い吸液能を有することを知り本発明に到達し
た。 すなわち本発明は下式で表わされるカチオン性
アクリル単量体と(メタ)アクリル酸を10:90〜
90:10のモル比で含有するイオン性単量体1モル
部に対して10モル部以下の(メタ)アクリルアミ
ドを含有する水溶性モノビニル単量体100重量部
に対して0.005〜0.5重量部の水混和性および/ま
たは水溶性ジビニル化合物の共存下に重合を行つ
て製造した膨潤性高分子架橋体からなり、水およ
び/またはアルコールを吸収することを特徴とす
る吸液樹脂である。 但し、R1はHまたはCH3、R2、R3はCH3
C2H5、AはOまたはNH、BはC2H4、C3H6を表
す。 本発明に用いる三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ピル(メタ)アク
リルアミド、ジメチルアミノメチル(メタ)アク
リルアミド等があげられ、カルボキシル基を有す
るビニル単量体としては、(メタ)アクリル酸が
あげられるが本発明において単量体の種類は限定
されのものではなく、これらの単量体の三種類以
上を組合せ用いてもよい。必要に応じて用いられ
る非イオン性水溶性ビニル単量体としてはアクリ
ルアミドが代表的なものであるが特に規定しな
い。三級アミノ基とカルボキシル基を有する単量
体のモル比は吸水しようとする液体のPHなどによ
つて90:10〜10:90の範囲から選択できるが好ま
しくは30:70〜70:30の範囲が吸水能の点から好
ましい。架橋剤として用いる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―メチレンビスアクリルアミドが工業
的に好ましい。ジビニル化合物の量は三級アミノ
基とカルボキシル基を有する単量体あるいは非イ
オン性水溶性単量体の全重量を100重量部とした
時に、0.005〜0.5重量部が好ましく、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。本発明品を重合するにあたつては、通常
水溶液中で行われ、開始剤は一般的に使用されて
いるレドツクス系、アゾ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が、乾燥工程
を考慮するとできるだけ高濃度で行う方が有利で
ある。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つて水分を蒸発させてし
まい、そのまま乾燥行程を経ずに直接粉砕工程へ
持つてゆ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つて、重合を開始させる
温度が異なるために開始剤が機能する温度以上で
重合を開始させれば良く特に限定されるものでは
ない。 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。 実施例 1 ジメチルアミノエチルメタアクリレート44.3
g、アクリル酸12.2gアクリルアミド3.5gを140
gの蒸留水に溶解し、35%塩酸11g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0.09g加えた。開始剤として過硫酸アンモ
ニウム0.024g亜硫酸水素ナトリウム0.024gを添
加し、40℃で重合を開始させた。 実施例 2 ジメチルアミノエチルメタアクリレート39.5g
メタアクリル酸21.6gアクリルアミド8.9gを蒸
留水25gに溶解し、さらにN,N―メチレンビス
アクリルアミド0.07gを加えた。次に開始剤とし
て2,2′―アゾビスイソブチロニトリル0.7gを
溶解したアセトン溶液を10c.c.加えた。この溶液を
85℃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つて水分が蒸発し、含水
率の低い多孔性固体として吸液樹脂を得た。 実施例 3 ジメチルアミノエチルメタアクリレート54.9g
アクリル酸15.1gを蒸留水10gに溶解し、35%塩
酸14gを加えてPHを4にした。N,Nメチレンビ
スアクリルアミド0.21gを加え、さらに開始剤と
して2,2′―アゾビス(2―アミジノプロパン)
塩酸塩0.7gを加えて混合した。この溶液を前述
の箱型容器の中に入れて加熱した。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吸液樹脂を得た。 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
た重合物は乾燥工程を経ずに直接粉砕して粉末状
の吸液樹脂を得た。実施例1〜3の粉末両性吸液
樹脂を市販品(ポリアクリル酸ソーダ架橋物から
成る高吸水性樹脂と比較し吸水試験を行つた。試
験方法は蒸留水1に対し吸液樹脂の粉末1gを
撹拌しながら加え、1時間放置した後、100mesh
のふるいを用いて過し、液量から吸水量を測
定した。また5%食塩水、メタノール1に対し
て粉末5gを加えて同様に試験した。その結果は
吸液倍率(吸液量÷加えた高吸水性樹脂の重量)
によつて表1に示した。 【表】
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an amphoteric type liquid-absorbing resin. Conventionally, pulp products have often been used to absorb and retain water. However, the amount of water absorbed by pulp is about 10 times its own weight, and in order to absorb and retain a large amount of water, a large amount of pulp is required and the product becomes very bulky.
It has the disadvantage that water easily separates when pressure is applied to something that has absorbed water. Therefore, various efforts have been made to develop super absorbent resins that absorb and retain large amounts of water with a small weight. These resins include starch graft polymers (Japanese Patent Publication No. 53-46199) and cross-linked polyacrylates (Japanese Patent Publication No. 54-30710), but most of these industrialized resins are anionic super absorbent resins. It is. The biggest drawback of this resin is that it exhibits high water absorption capacity in distilled water, but a significant drop in water absorption capacity is observed in electrolyte solutions. Super absorbent resins are used in disposable diapers, sanitary napkins, soil water retention agents, and other applications that rarely involve pure water, but mostly liquids containing salt. As a result of intensive research to overcome this drawback, the present inventors found that amphoteric type liquid-absorbing resins have higher liquid-absorbing ability for electrolyte solutions and alcohol than anionic type resins, and arrived at the present invention. . That is, the present invention uses a cationic acrylic monomer represented by the following formula and (meth)acrylic acid in a ratio of 10:90 to
0.005 to 0.5 part by weight per 100 parts by weight of a water-soluble monovinyl monomer containing 10 parts by mole or less of (meth)acrylamide per 1 part by mole of the ionic monomer in a molar ratio of 90:10. It is a liquid-absorbing resin that is made of a swellable polymer crosslinked product produced by polymerization in the coexistence of a water-miscible and/or water-soluble divinyl compound, and is characterized by absorbing water and/or alcohol. However, R 1 is H or CH 3 , R 2 and R 3 are CH 3 ,
C2H5 , A represents O or NH, B represents C2H4 , C3H6 . Examples of vinyl monomers having a tertiary amino group used in the present invention include dimethylaminoethyl (meth)acrylate, diethylaminoethyl (meth)acrylate, dimethylaminopropyl (meth)acrylamide, diethylaminopropyl (meth)acrylamide, and dimethylaminomethyl ( Examples of the vinyl monomer having a carboxyl group include (meth)acrylic acid; however, in the present invention, the type of monomer is not limited; A combination of three or more types may be used. Acrylamide is a typical nonionic water-soluble vinyl monomer that may be used as needed, but is not particularly limited. The molar ratio of the monomer having a tertiary amino group and a carboxyl group can be selected from the range of 90:10 to 10:90 depending on the pH of the liquid to be absorbed, but preferably 30:70 to 70:30. This range is preferable from the viewpoint of water absorption capacity. Examples of the water-miscible or water-soluble divinyl compound used as a crosslinking agent include N,N-methylenebis(meth)acrylamide, tetraethylene glycol di(meth)acrylate, decaethylene glycol di(meth)acrylate, etc. , N,N-methylenebisacrylamide is industrially preferred. The amount of the divinyl compound is preferably 0.005 to 0.5 parts by weight, based on 100 parts by weight of the total weight of the monomer having a tertiary amino group and a carboxyl group or the nonionic water-soluble monomer, and if it is less than this range. The water-containing gel is in a semi-dissolved state, and if it is too large, the degree of crosslinking will increase, and in both cases the water absorption capacity will decrease. The polymerization of the product of the present invention is usually carried out in an aqueous solution, and any commonly used initiator, such as redox type or azo type, may be used. Further, the polymerization concentration is not particularly limited and can be selected within any concentration range, but in consideration of the drying process, it is advantageous to carry out the polymerization at a concentration as high as possible. For example, it is also possible to perform polymerization with a highly concentrated aqueous solution of about 70%, evaporate water by the heat of polymerization generated, and then directly carry it to the pulverization process without going through the drying process. Furthermore, the initiation temperature is not particularly limited, as the temperature at which polymerization is initiated differs depending on the type of initiator, as long as the polymerization is initiated at a temperature higher than the temperature at which the initiator functions. 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 the gist thereof is exceeded. Example 1 Dimethylaminoethyl methacrylate 44.3
g, acrylic acid 12.2g acrylamide 3.5g 140
g of distilled water, and the pH was adjusted to 4 with 11 g of 35% hydrochloric acid. Furthermore, 0.09 g of N,N-methylenebisacrylamide was added. 0.024 g of ammonium persulfate and 0.024 g of sodium bisulfite were added as an initiator, and polymerization was initiated at 40°C. Example 2 Dimethylaminoethyl methacrylate 39.5g
21.6 g of methacrylic acid and 8.9 g of acrylamide were dissolved in 25 g of distilled water, and 0.07 g of N,N-methylenebisacrylamide was added. Next, 10 c.c. of an acetone solution containing 0.7 g of 2,2'-azobisisobutyronitrile as an initiator was added. This solution
They were placed in a box-shaped container (Teflon-treated glass fiber material) heated in a constant-temperature water bath at 85°C. As the temperature of the solution rose, a polymerization reaction started, and water was evaporated by the generated heat of polymerization, yielding a liquid-absorbing resin as a porous solid with a low water content. Example 3 Dimethylaminoethyl methacrylate 54.9g
15.1 g of acrylic acid was dissolved in 10 g of distilled water, and 14 g of 35% hydrochloric acid was added to adjust the pH to 4. Added 0.21 g of N,N methylenebisacrylamide, and further added 2,2'-azobis(2-amidinopropane) as an initiator.
0.7 g of hydrochloride was added and mixed. This solution was placed in the box-shaped container described above and heated. As soon as polymerization started, water evaporated due to the heat of polymerization, yielding a liquid-absorbing resin as a porous solid with a low water content. Example 4 The polymer obtained in Example 1 was dehydrated with acetone, dried, and then ground. Moreover, the polymers obtained in Examples 2 and 3 were directly pulverized without going through a drying process to obtain powdery liquid-absorbing resins. A water absorption test was conducted comparing the powdered ampholytic liquid-absorbent resins of Examples 1 to 3 with a commercially available product (super absorbent resin made of a cross-linked product of sodium polyacrylate). Add with stirring and leave for 1 hour, then 100mesh
The amount of water absorbed was measured from the amount of liquid. Further, 5 g of powder was added to 5% saline solution and 1 part of methanol, and the same test was conducted. The result is the liquid absorption capacity (liquid absorption amount ÷ weight of added super absorbent resin)
The results are shown in Table 1. 【table】

Claims (1)

【特許請求の範囲】 1 下式で表わされるカチオン性アクリル単量体
と(メタ)アクリル酸を10:90〜90:10のモル比
で含有するイオン性単量体1モル部に対して10モ
ル部以下の(メタ)アクリルアミドを含有する水
溶性モノビニル単量体100重量部に対して0.005〜
0.5重量部の水混和性および/または水溶性ジビ
ニル化合物の共存下に重合を行つて製造した膨潤
性高分子架橋体からなり、水および/またはアル
コールを吸収することを特徴とする吸液樹脂。 〔但し、R1はHまたはCH3、R2、R3はCH3
C2H5、AはOまたはNH、BはC2H4、C3H6を表
す。〕 2 請求項1に記載の式で表されるカチオン性ア
クリル単量体と(メタ)アクリル酸の含有モル比
が30:70〜70:30の範囲にあることを特徴とする
請求項1に記載の吸液樹脂。 3 水溶性モノビニル単量体混合物中の(メタ)
アクリルアミドの含有比率が20モル%以下である
ことを特徴とする請求項1に記載の吸液樹脂。
[Claims] 1. 10 to 1 mole part of an ionic monomer containing a cationic acrylic monomer represented by the following formula and (meth)acrylic acid in a molar ratio of 10:90 to 90:10. 0.005 to 100 parts by weight of water-soluble monovinyl monomer containing molar parts or less of (meth)acrylamide
A liquid-absorbing resin comprising a swellable crosslinked polymer produced by polymerization in the coexistence of 0.5 parts by weight of a water-miscible and/or water-soluble divinyl compound, and characterized in that it absorbs water and/or alcohol. [However, R 1 is H or CH 3 , R 2 and R 3 are CH 3 ,
C2H5 , A represents O or NH, B represents C2H4 , C3H6 . 2. Claim 1, wherein the molar ratio of the cationic acrylic monomer represented by the formula according to Claim 1 and (meth)acrylic acid is in the range of 30:70 to 70:30. The liquid-absorbing resin described. 3 (Meta) in water-soluble monovinyl monomer mixture
The liquid-absorbing resin according to claim 1, wherein the content ratio of acrylamide is 20 mol% or less.
JP3591682A 1982-03-09 1982-03-09 Production of amphoteric, highly water-absorptive resin Granted JPS58154710A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3591682A JPS58154710A (en) 1982-03-09 1982-03-09 Production of amphoteric, highly water-absorptive resin

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3591682A JPS58154710A (en) 1982-03-09 1982-03-09 Production of amphoteric, highly water-absorptive resin

Publications (2)

Publication Number Publication Date
JPS58154710A JPS58154710A (en) 1983-09-14
JPH0420007B2 true JPH0420007B2 (en) 1992-03-31

Family

ID=12455350

Family Applications (1)

Application Number Title Priority Date Filing Date
JP3591682A Granted JPS58154710A (en) 1982-03-09 1982-03-09 Production of amphoteric, highly water-absorptive resin

Country Status (1)

Country Link
JP (1) JPS58154710A (en)

Families Citing this family (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB8531838D0 (en) * 1985-12-30 1986-02-05 Wellcome Found Aryl derivatives
FR2649710A1 (en) * 1989-07-12 1991-01-18 Hoechst France AMPHOLYTE HYDROPHILIC POLYMERS, THEIR PREPARATION PROCESS AND THEIR APPLICATION AS ABSORBENT AGENT
US5610208A (en) 1994-02-17 1997-03-11 Nippon Shokubai Co., Ltd. Water-absorbent agent, method for production thereof, and water-absorbent composition
KR0183511B1 (en) * 1994-06-13 1999-04-15 다나카 쇼소 Water absorbent process for producing the same and absorbent article containing the same
USRE38444E1 (en) 1994-06-13 2004-02-24 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

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS52127995A (en) * 1976-04-19 1977-10-27 Johnson & Johnson Hydrophilic random copolymers composition and process for producing same
JPS5813608A (en) * 1981-07-17 1983-01-26 Kao Corp Preparation of crosslinked ampholytic copolymer

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS52127995A (en) * 1976-04-19 1977-10-27 Johnson & Johnson Hydrophilic random copolymers composition and process for producing same
JPS5813608A (en) * 1981-07-17 1983-01-26 Kao Corp Preparation of crosslinked ampholytic copolymer

Also Published As

Publication number Publication date
JPS58154710A (en) 1983-09-14

Similar Documents

Publication Publication Date Title
CA1166792A (en) Alkali metal acrylate polymer excellent in salt solution absorbency and process for producing same
US4612250A (en) Production process for highly water absorbable polymer
EP0242478B1 (en) Water absorbent acrylic copolymers
JP2922216B2 (en) Super absorbent polymer production method
US5250642A (en) Copolymers of ampholytic ion pairs containing vinylic tertiary amine and olefinic comonomers
US5130389A (en) Superabsorbent crosslinked ampholytic ion pair copolymers containing 2-methacryloyloxyethyldimethylammonium
WO1995021876A1 (en) Temperature-sensitive water-absorbing/desorbing polymer composition
JPS5980459A (en) Water-absorbing powdery resin composition
JPH10147606A (en) Production of hydrophilic polymer having rapid rate dissolving or swelling into water
CA2043662C (en) Superabsorbent crosslinked ampholytic ion pair copolymers
JPH0420007B2 (en)
JPH0420006B2 (en)
JP2888866B2 (en) Manufacturing method of water-absorbent resin with excellent heat resistance
JPH0214925B2 (en)
JPH0323567B2 (en)
US4820742A (en) Method for continuous manufacture of solid water absorbing resin
US5508381A (en) Process for preparing highly water absorbent resin
JP3251647B2 (en) Water-absorbing resin and method for producing the same
JPS58154708A (en) Production of highly water-absorptive resin
JPH02242809A (en) Production of saline-resistant and water absorbing resin
JP3141059B2 (en) Temperature-sensitive water-absorbing resin
JPS6256888B2 (en)
JPH0321562B2 (en)
JPH0381310A (en) Dipolar electrolyte hydrophylic polymer, its manufacture and its use as absorbent
JPS60161409A (en) Preparation of resin having high water absorption property