JPH0147598B2 - - Google Patents

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Publication number
JPH0147598B2
JPH0147598B2 JP19923982A JP19923982A JPH0147598B2 JP H0147598 B2 JPH0147598 B2 JP H0147598B2 JP 19923982 A JP19923982 A JP 19923982A JP 19923982 A JP19923982 A JP 19923982A JP H0147598 B2 JPH0147598 B2 JP H0147598B2
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acid
minutes
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JP19923982A
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JPS5994699A (en
Inventor
Hiroyuki Suzuki
Hisao Noguchi
Masao Hamada
Yasutaka Nishi
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Harima Chemical Inc
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Harima Chemical Inc
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Priority to JP19923982A priority Critical patent/JPS5994699A/en
Publication of JPS5994699A publication Critical patent/JPS5994699A/en
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Description

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

本発明はアクリルアミドなどのα,β−不飽和
アミドとアクリロニトリルなどのα,β−不飽和
ニトリルと必要に応じてこれらと共重合可能なノ
ニオン性単量体を含む共重合体を、水酸化ナトリ
ウムなどのアルカリ金属水酸化物、炭酸ナトリウ
ムなどのアルカリ金属炭酸塩またはジメチルアミ
ンなどのアミン系塩基によりアルカリ性下で反応
させることにより、重合体中にアニオン性基およ
びカチオン性基を同時に導入してなる両性重合体
よりなる紙力増強剤に関するものである。 従来よりアクリルアミド−アクリル酸共重合体
又はポリアクリルアミドの部分加水分解反応によ
りカルボキシル基を導入した重合体に代表される
アクリルアミドを主体とするアニオン性重合体
は、製紙業界で硫酸バンドを定着剤として用いる
紙力増強剤などに使用されている。しかしながら
従来のアクリルアミドを主体とするアニオン性紙
力増強剤は、バルブ繊維への定着率は通常60〜80
%といわれており十分な紙力増強効果を発揮して
いるとは言い難い。 本発明者らはパルプ繊維への定着率を高め、優
れた紙力増強効果を発揮する紙力増強剤を得るこ
とを目的として鋭意研究を重ねた結果、本発明に
到つたものである。 すなわち、アクリルアミドなどのα,β−不飽
和アミドと、アクリロニトリルなどのα,β−不
飽和ニトリルとを主体とする共重合体の水溶液
を、水酸化ナトリウムなどのアルカリ金属水酸化
物又はジメチルアミンなどのアミン系塩基を添加
してアルカリ性下反応することにより、重合体中
にアニオン性基およびカチオン性基が同時に導入
された両性重合体が得られることを発見した。ま
たこの両性重合体はパルプ繊維への定着率が90%
以上で従来のアニオン性重合体より高く、紙力増
強効果も著しく優れることを見出し、ここに本発
明を完成するに至つた。 本発明の両性重合体中のアニオン性基は、アミ
ド基がアルカリ性下で加水分解されてカルボキシ
ル基となることにより導入される。又カチオン性
基の導入機構については現在明らかではないが、
アクリルアミドのようなα,β−不飽和アミドの
ホモポリマーではアルカリ性下同様に反応しても
カチオン性基は導入されず、カチオン性基を導入
するためには本発明のようにニトリル基の存在が
不可欠である。このようなことからアミド基の加
水分解反応によりカルボキシル基とともに副生す
るアンモニアがニトリル基と反応することにより
カチオン性を発現するものと考えられる。 本発明の重合体中のα,β−不飽和アミドとし
て、具体的にはアクリルアミド、メタアクリルア
ミド、ジメチルアクリルアミド等が挙げられる。
又α,β−不飽和ニトリルとして、具体的にはア
クリロニトリル、メタアクリロニトリル等が挙げ
られる。またこれらと共重合可能なノニオン性単
量体は、共重合体中に必要に応じて添加できる成
分であつて、具体的にはスチレン、α−メチルス
チレンなどの芳香族炭化水素類、アクリル酸メチ
ル、アクリル酸エチル、アクリル酸ブチル、アク
リル酸2−ヒドロキシエチル、メタアクリル酸メ
チル、メタアクリル酸エチルなどのアクリル酸又
はメタアクリル酸の炭素数1〜8のアルキルエス
テル類、酢酸ビニルプロピオン酸ビニル等のビニ
ルエステル類が使用可能である。 上記のα,β−不飽和アミド成分、α,β−不
飽和ニトリル成分及びノニオン性単量体成分の使
用割合は、α,β−不飽和アミド成分は50〜90モ
ル%であるが好ましくは60〜80モル%が適当であ
る。このα,β−不飽和アミド成分が50モル%以
下では紙力増強効果が十分に発揮されず好ましく
ない。又、α,β−不飽和ニトリル成分は、10〜
50モル%であるが好ましくは20〜40モル%であ
る。このα,β−不飽和ニトリル成分が10モル%
以下では、この後に行うアルカリ性下での反応で
カチオン性基がほとんど導入されず、本発明の特
徴とする両性重合体は得られない。又α,β−不
飽和ニトリル成分が50モル%以上では水に不溶性
となり好ましくない。ノニオン性単量体成分は、
20モル%以下の範囲で必要に応じて添加される成
分である。 上記α,β−不飽和アミド成分、α,β−不飽
和ニトリル成分及びノニオン性単量体成分の共重
合反応は通常の方法で実施でき、特に水溶液重合
が一般的である。 例えば過硫酸アンモニウム、過硫酸カリウム、
過酸化水素等の水溶性過酸化物、あるいはこれら
とジメチルアミン、亜硫酸ナトリウムなどの還元
剤またはアリルアルコール、イソプロピルアルコ
ールなどの連鎖移動剤を組み合せて前記重合性単
量体混合物に対し0.05〜5重量%使用し、水溶媒
で単量体混合物の濃度10〜50重量%濃度、40〜95
℃の温度で1〜5時間窒素ガス雰囲気中で共重合
反応を行う。このようにして前記3つの成分で構
成された共重合体は、15%濃度の水溶液の粘度が
1000〜100000cps(25℃)のものである。 次にこの共重合体の10〜50重量%濃度の水溶液
にアルカリ金属水酸化物、アルカリ金属炭酸塩ま
たはアミン塩基を共重合体に対して1〜15重量%
加え、PH9以上、温度40〜95℃で5〜120分反応
させる。而してアニオン性基1〜20モル%及びカ
チオン性基1〜10モル%が導入された時点で、鉱
酸、有機カルボン酸又は有機スルホン酸等の酸を
加え、PH3〜9として本反応を停止する。ここで
アルカリ金属水酸化物としては具体的に水酸化ナ
トリウム、水酸化カリウム、水酸化リチウム等が
例示できる。また、アルカリ金属炭酸塩としては
炭酸ナトリウム、炭酸カリウム、炭酸リチウム等
が例示できる。又アミン塩基とは具体的に、アン
モニア、メチルアミン、ジメチルアミン、トリメ
チルアミン、ジエチルアミン等の脂肪族アミンが
例示される。ここでアルカリ金属水酸化物、アル
カリ金属炭酸塩およびアミン塩基は、共重合体に
対し1〜15重量%の範囲で加えてPH9以上、好ま
しくはPH10〜13のアルカリ性とする必要がある。
PH9以下ではアミド基の加水分解反応およびカチ
オン性基導入反応の反応速度が極端に遅くなり、
従つて本発明の特徴とする両性重合体は得られな
い。而して、前記共重合体を上記PH以下で、温度
40〜95℃で5〜120分反応させることにより、目
的の両性重合体を得る。ここで反応時間が5分以
下では、得られる重合体水溶液が1週間程度で2
相分離するなど安定性が悪く、好ましくない。ま
た反応時間120分以上ではアミド基の加水分解反
応が進みすぎてカルボキシル基を過剰に生成する
ため、紙力増強効果の上で好ましくない。上記反
応条件下で共重合体中にアニオン性基1〜20モル
%、カチオン性基1〜10モル%が生成した後、鉱
酸、有機カルボン酸または有機スルホン酸等の酸
を加えて水溶液をPH3〜9に下げて本反応を停止
終了させる。ここで鉱酸とは具体的には塩酸、硫
酸、硝酸、リン酸等が例示される。有機カルボン
酸としては具体的には蟻酸、酢酸、プロピオン酸
等が例示できる。又、有機スルホン酸としては、
具体的にメチル硫酸、エチル硫酸、ベンゼンスル
ホン酸等が例示される。 本発明の両性重合体は15%濃度で1000〜
100000cps(25℃)のものであり特に2000〜
50000cps程度が紙力増強剤として使用する上で好
ましい。 本発明の両性重合体を紙力増強剤として内添で
使用する場合、従来のアニオン性紙力増強剤と同
様に硫酸バンドを定着剤としてPH4〜5.5の範囲
で使用することが好ましい。またサイズプレス、
ロールコータなどによる塗布も行うことができ
る。パルプとしては、クラフトパルプ、サルフア
イトパルプ、グランドパルプ、古紙等その種類に
限定はなく、またサイズ剤、填料等通常の製紙用
添加剤を併用、添加することができる。 以下実施例により本発明を説明する。 実施例 1 アクリルアミド42.6g、アクリロニトリル21.2
g(モル比60:40)および水365gを500mlセパラ
ブルフラスコにとり、充分に窒素ガスで重合系内
の酸素を除去した後、過硫酸アンモニウム0.1g
を60℃で添加し、この後80℃まで徐々に昇温して
80℃で2時間窒素ガスを流しながら共重合反応を
行う。その後、15重量%の水酸化ナトリウム水溶
液25gを加え、PH12のアルカリ性下で80℃で15分
間、30分間及び90分間の3種の反応時間で反応さ
せた後、15重量%の硫酸水溶液39gを加えてPHを
下げ、反応を停止させ、各々重合体A,B及びC
を得た。 実施例 2 アクリルアミド49.8g、アクリロニトリル15.9
g〔モル比70:30)、水375gに過硫酸アンモニウ
ム0.1gを加え、実施例1と同様の方法で共重合
反応を行う。この後15重量%の水酸化ナトリウム
水溶液25gを加えてPH12のアルカリ性とし、80℃
で15分、30分および90分の3種の反応時間で反応
を行い、この後15重量%の硫酸水溶液39gを加
え、各々重合体D,E,Fを得た。 実施例 3 アクリルアミド49.8g、アクリロニトリル15.9
g(モル比70:30)、水375gに過硫酸アンモニウ
ム0.1gを加え、実施例1と同様に共重合反応を
行い、この後15重量%ジメチルアミン水溶液30g
加え、PH11のアルカリ性下80℃で30分反応を行
い、次に15重量%塩酸水溶液30gを加えて重合体
Gを得た。 実施例 4 アクリルアミド49.8g、アクリロニトリル15.9
g(モル比70:30)、水375gに過硫酸アンモニウ
ム0.1gを加え、実施例1と同様に共重合反応を
行いこの後15%の水酸化カリウム20gを加えてPH
12のアルカリ性下75℃で30分反応させ、次に15重
量%の塩酸18gを加えて重合体Hを得た。 実施例 5 アクリルアミド42.6g、アクリロニトリル15.9
g、酢酸ビニル8.6g(モル比60:30:10)、水
380gに過硫酸アンモニウム0.1g、亜硫酸ナトリ
ウム0.02gを45℃で加え、この後徐々に昇温しな
がら80℃にする。その後80℃で2時間共重合反応
を続ける。その次に15重量%の水酸化ナトリウム
水溶液16gを加え、PH11のアルカリ性下80℃で30
分間反応させた後、15%の酢酸32gを加えて重合
体Iを得た。 比較例 1 アクリルアミド42.6g、アクリロニトリル15.9
g、アクリル酸ナトリウム9.4g(モル比60:
30:10)、水385gに過硫酸アンモニウム0.1gを
65℃で加え、徐々に昇温して80℃にする。この後
80℃で2時間共重合反応を続ける。そしてその共
重合体をそのまゝ重合体Jとした。 比較例 2 アクリルアミド71g、水405gに過硫酸アンモ
ニウム2g、イソプロピルアルコール1gを65℃
で加える。これにより急激に発熱するので、水浴
で冷却しながら80℃まで昇温するように調整し、
この後80℃で2時間重合反応を続けた。次に15重
量%の水酸化ナトリウム水溶液16gを80℃で加
え、PH11のアルカリ性とし30分反応後15重量%の
塩酸18gを加え、重合体Kを得た。 以上の実施例、比較例で得られた重合体の固形
分、粘度、PH、アニオン量およびカチオン量を表
1に示した。
The present invention uses a copolymer containing an α,β-unsaturated amide such as acrylamide, an α,β-unsaturated nitrile such as acrylonitrile, and optionally a nonionic monomer copolymerizable with these, using sodium hydroxide. An anionic group and a cationic group are simultaneously introduced into the polymer by reacting with an alkali metal hydroxide such as, an alkali metal carbonate such as sodium carbonate, or an amine base such as dimethylamine under alkaline conditions. This invention relates to a paper strength enhancer made of an amphoteric polymer. Conventionally, anionic polymers mainly composed of acrylamide, such as acrylamide-acrylic acid copolymers or polymers into which carboxyl groups have been introduced through a partial hydrolysis reaction of polyacrylamide, have been used in the paper manufacturing industry using sulfuric acid as a fixing agent. It is used as a paper strength enhancer. However, conventional anionic paper strength agents mainly based on acrylamide usually have a fixation rate of 60 to 80% on valve fibers.
%, and it is difficult to say that it has a sufficient effect of increasing paper strength. The present inventors have conducted extensive research with the aim of obtaining a paper strength enhancer that increases the fixation rate to pulp fibers and exhibits an excellent paper strength enhancing effect, and as a result, the present invention was achieved. That is, an aqueous solution of a copolymer mainly composed of an α,β-unsaturated amide such as acrylamide and an α,β-unsaturated nitrile such as acrylonitrile is mixed with an alkali metal hydroxide such as sodium hydroxide or dimethylamine, etc. It has been discovered that an amphoteric polymer in which an anionic group and a cationic group are simultaneously introduced into the polymer can be obtained by adding an amine base and reacting under alkaline conditions. In addition, this amphoteric polymer has a fixation rate of 90% on pulp fibers.
As described above, it has been found that the paper strength enhancing effect is higher than that of conventional anionic polymers and is significantly superior, and the present invention has now been completed. The anionic group in the amphoteric polymer of the present invention is introduced by hydrolyzing the amide group under alkaline conditions to become a carboxyl group. Furthermore, although the mechanism of introduction of the cationic group is currently unclear,
In a homopolymer of α,β-unsaturated amide such as acrylamide, a cationic group is not introduced even if the same reaction is performed under alkaline conditions, and in order to introduce a cationic group, the presence of a nitrile group is required as in the present invention. It is essential. For this reason, it is thought that ammonia, which is produced as a by-product along with carboxyl groups due to the hydrolysis reaction of amide groups, reacts with nitrile groups to develop cationic properties. Specific examples of the α,β-unsaturated amide in the polymer of the present invention include acrylamide, methacrylamide, dimethylacrylamide, and the like.
Specific examples of the α,β-unsaturated nitrile include acrylonitrile and methacrylonitrile. In addition, nonionic monomers that can be copolymerized with these are components that can be added to the copolymer as necessary. Specifically, aromatic hydrocarbons such as styrene and α-methylstyrene, acrylic acid C1-8 alkyl esters of acrylic acid or methacrylic acid such as methyl, ethyl acrylate, butyl acrylate, 2-hydroxyethyl acrylate, methyl methacrylate, and ethyl methacrylate, vinyl acetate vinyl propionate Vinyl esters such as The ratio of the above α,β-unsaturated amide component, α,β-unsaturated nitrile component and nonionic monomer component is such that the α,β-unsaturated amide component is 50 to 90 mol%, but preferably 60-80 mol% is suitable. If the α,β-unsaturated amide component is less than 50 mol %, the paper strength enhancing effect will not be sufficiently exhibited, which is not preferable. In addition, the α,β-unsaturated nitrile component is 10 to
The content is 50 mol%, preferably 20 to 40 mol%. This α,β-unsaturated nitrile component is 10 mol%
In the following, hardly any cationic groups are introduced in the subsequent reaction under alkaline conditions, and the amphoteric polymer, which is a feature of the present invention, cannot be obtained. Moreover, if the α,β-unsaturated nitrile component is more than 50 mol%, it becomes insoluble in water, which is not preferable. The nonionic monomer component is
It is a component that is added as necessary in a range of 20 mol% or less. The copolymerization reaction of the α,β-unsaturated amide component, the α,β-unsaturated nitrile component, and the nonionic monomer component can be carried out by a conventional method, and aqueous solution polymerization is particularly common. For example, ammonium persulfate, potassium persulfate,
A water-soluble peroxide such as hydrogen peroxide, or a combination of these with a reducing agent such as dimethylamine or sodium sulfite, or a chain transfer agent such as allyl alcohol or isopropyl alcohol, is added to the polymerizable monomer mixture in an amount of 0.05 to 5% by weight. % used, concentration of monomer mixture in water solvent 10-50% concentration by weight, 40-95
The copolymerization reaction is carried out in a nitrogen gas atmosphere at a temperature of .degree. C. for 1 to 5 hours. In this way, the copolymer composed of the above three components has a viscosity of 15% aqueous solution.
1000~100000cps (25℃). Next, an alkali metal hydroxide, an alkali metal carbonate, or an amine base is added to an aqueous solution of this copolymer at a concentration of 1 to 15% by weight based on the copolymer.
Add and react for 5 to 120 minutes at a pH of 9 or higher and a temperature of 40 to 95°C. When 1 to 20 mol% of anionic groups and 1 to 10 mol% of cationic groups have been introduced, an acid such as a mineral acid, an organic carboxylic acid, or an organic sulfonic acid is added to adjust the pH to 3 to 9 to carry out the reaction. Stop. Specific examples of the alkali metal hydroxide include sodium hydroxide, potassium hydroxide, lithium hydroxide, and the like. Examples of alkali metal carbonates include sodium carbonate, potassium carbonate, and lithium carbonate. Specific examples of the amine base include ammonia, aliphatic amines such as methylamine, dimethylamine, trimethylamine, and diethylamine. Here, the alkali metal hydroxide, alkali metal carbonate, and amine base must be added in an amount of 1 to 15% by weight based on the copolymer to make the copolymer alkaline with a pH of 9 or more, preferably 10 to 13.
At pH 9 or lower, the reaction rate of amide group hydrolysis reaction and cationic group introduction reaction becomes extremely slow.
Therefore, the amphoteric polymer characteristic of the present invention cannot be obtained. Then, the copolymer was heated at a temperature below the above pH.
The desired amphoteric polymer is obtained by reacting at 40 to 95°C for 5 to 120 minutes. Here, if the reaction time is 5 minutes or less, the obtained polymer aqueous solution will be
It is not preferable because it has poor stability such as phase separation. Further, if the reaction time is 120 minutes or more, the hydrolysis reaction of the amide groups will proceed too much and excessive carboxyl groups will be produced, which is not preferable in terms of the paper strength enhancement effect. After 1 to 20 mol% of anionic groups and 1 to 10 mol% of cationic groups are formed in the copolymer under the above reaction conditions, an acid such as a mineral acid, an organic carboxylic acid, or an organic sulfonic acid is added to form an aqueous solution. The reaction is stopped and completed by lowering the pH to 3-9. Here, specific examples of mineral acids include hydrochloric acid, sulfuric acid, nitric acid, and phosphoric acid. Specific examples of organic carboxylic acids include formic acid, acetic acid, and propionic acid. In addition, as organic sulfonic acids,
Specific examples include methyl sulfate, ethyl sulfate, and benzenesulfonic acid. The amphoteric polymer of the present invention has a concentration of 1000 to 15%.
100000cps (25℃), especially 2000~
Approximately 50,000 cps is preferable for use as a paper strength enhancer. When the amphoteric polymer of the present invention is internally added as a paper strength enhancer, it is preferable to use sulfuric acid as a fixing agent within a pH range of 4 to 5.5, similar to conventional anionic paper strength enhancers. Also size press,
Coating can also be performed using a roll coater or the like. The type of pulp is not limited to kraft pulp, sulfite pulp, ground pulp, waste paper, etc., and ordinary papermaking additives such as sizing agents and fillers can be used or added. The present invention will be explained below with reference to Examples. Example 1 Acrylamide 42.6g, acrylonitrile 21.2g
(mole ratio 60:40) and 365 g of water in a 500 ml separable flask, and after thoroughly removing oxygen in the polymerization system with nitrogen gas, add 0.1 g of ammonium persulfate.
was added at 60°C, and then the temperature was gradually raised to 80°C.
The copolymerization reaction is carried out at 80°C for 2 hours while flowing nitrogen gas. Thereafter, 25 g of a 15% by weight aqueous sodium hydroxide solution was added, and the reaction was carried out at 80°C for 3 reaction times: 15 minutes, 30 minutes, and 90 minutes under alkaline pH 12, and then 39 g of a 15% by weight sulfuric acid aqueous solution was added. In addition, the pH was lowered, the reaction was stopped, and polymers A, B, and C were formed, respectively.
I got it. Example 2 Acrylamide 49.8g, acrylonitrile 15.9g
g [molar ratio 70:30], 0.1 g of ammonium persulfate was added to 375 g of water, and a copolymerization reaction was carried out in the same manner as in Example 1. After that, add 25g of 15% by weight sodium hydroxide aqueous solution to make it alkaline to PH12 and raise the temperature to 80℃.
The reaction was carried out for three reaction times: 15 minutes, 30 minutes, and 90 minutes, and then 39 g of a 15% by weight aqueous sulfuric acid solution was added to obtain polymers D, E, and F, respectively. Example 3 Acrylamide 49.8g, acrylonitrile 15.9g
g (molar ratio 70:30), 0.1 g of ammonium persulfate was added to 375 g of water, a copolymerization reaction was carried out in the same manner as in Example 1, and then 30 g of a 15% by weight dimethylamine aqueous solution was added.
In addition, a reaction was carried out at 80° C. for 30 minutes under alkaline pH 11, and then 30 g of a 15% by weight aqueous hydrochloric acid solution was added to obtain Polymer G. Example 4 Acrylamide 49.8g, acrylonitrile 15.9g
(molar ratio 70:30), 0.1 g of ammonium persulfate was added to 375 g of water, a copolymerization reaction was carried out in the same manner as in Example 1, and then 20 g of 15% potassium hydroxide was added to adjust the pH.
The reaction was carried out for 30 minutes at 75° C. under alkalinity of 12°C, and then 18 g of 15% by weight hydrochloric acid was added to obtain Polymer H. Example 5 Acrylamide 42.6g, acrylonitrile 15.9g
g, vinyl acetate 8.6 g (molar ratio 60:30:10), water
Add 0.1 g of ammonium persulfate and 0.02 g of sodium sulfite to 380 g at 45°C, and then gradually raise the temperature to 80°C. Thereafter, the copolymerization reaction was continued at 80°C for 2 hours. Next, add 16 g of a 15% by weight aqueous sodium hydroxide solution and heat for 30 minutes at 80℃ under alkaline pH 11.
After reacting for a minute, 32 g of 15% acetic acid was added to obtain Polymer I. Comparative example 1 Acrylamide 42.6g, acrylonitrile 15.9g
g, sodium acrylate 9.4 g (molar ratio 60:
30:10), add 0.1 g of ammonium persulfate to 385 g of water.
Add at 65°C and gradually increase the temperature to 80°C. After this
Continue the copolymerization reaction at 80°C for 2 hours. The copolymer was designated as Polymer J. Comparative Example 2 71g of acrylamide, 405g of water, 2g of ammonium persulfate, and 1g of isopropyl alcohol at 65℃
Add with . This causes rapid heat generation, so adjust the temperature to 80℃ while cooling it in a water bath.
Thereafter, the polymerization reaction was continued at 80°C for 2 hours. Next, 16 g of a 15% by weight aqueous sodium hydroxide solution was added at 80° C. to make the mixture alkaline to pH 11, and after reaction for 30 minutes, 18 g of 15% by weight hydrochloric acid was added to obtain Polymer K. Table 1 shows the solid content, viscosity, PH, anion content, and cation content of the polymers obtained in the above Examples and Comparative Examples.

【表】 以上の実施例及び比較例で得られた重合体の内
B,E,G,H,I,J,Kについて、紙力増強
剤としての効果を確認するため、次の実験例に基
づいて行なつた。 実験例 1 L/N(70/30)BKP,GP/LBKP/NBKP
(60/20/20)およびNUKPの3種のパルプを使
用し、各パルプの3%スラリーに、硫酸バンドを
パルプに対して3%加え、さらに各々の重合体を
パルプに対して0.5%加え、5分間撹拌した後タ
ツピースタンダードシートマシンで坪量60g/m2
となるように抄紙した。ついでその紙を4Kg/cm2
で1分間脱水したのち、105℃で3分間乾燥した。
この後シートを20℃、65%PHで24時間調湿した
後、比破裂強度を測定した。 結果を表2に示す。
[Table] Among the polymers B, E, G, H, I, J, and K obtained in the above examples and comparative examples, in order to confirm their effectiveness as paper strength enhancers, the following experimental examples were used. Based on this. Experimental example 1 L/N (70/30) BKP, GP/LBKP/NBKP
Three types of pulp (60/20/20) and NUKP were used, and to a 3% slurry of each pulp, sulfate was added at 3% based on the pulp, and each polymer was added at 0.5% based on the pulp. After stirring for 5 minutes, the basis weight is 60g/ m2 using a Tatsupi standard sheet machine.
The paper was made to look like this. Then weigh the paper at 4Kg/cm 2
After dehydrating for 1 minute, the sample was dried at 105°C for 3 minutes.
Thereafter, the sheet was conditioned at 20° C. and 65% PH for 24 hours, and the specific bursting strength was measured. The results are shown in Table 2.

【表】【table】

【表】 実験例 2 さきほどのGP/LBKP/NBKPにタルクを対
パルプで20%加え、実験例1と同様に硫酸バンド
3%、重合体0.5%及びロジンサイズ剤0.5%を加
え、坪量60g/m2となるように抄紙した。この後
の処理も実験例1と同様に行い、IGT強度(ドラ
イ、ウエツト)および裂断長に換算した引張強度
を測定した。結果を表3に示す。
[Table] Experimental Example 2 Add 20% talc to the pulp to the previous GP/LBKP/NBKP, add 3% sulfuric acid, 0.5% polymer, and 0.5% rosin sizing agent as in Experimental Example 1, and make a 60g basis weight. / m2 . The subsequent treatments were carried out in the same manner as in Experimental Example 1, and the IGT strength (dry, wet) and tensile strength converted to breaking length were measured. The results are shown in Table 3.

【表】 本発明によれば、表1から明らかな如く紙力補
強剤として適した性状を有すると共に、アニオン
性とカチオン性とを併せ持つた両性を有してい
る。而してこれを用いて抄造した紙は、表2及び
表3に示されるように大きな強度を有しており、
紙力補強剤としてすぐれている。
[Table] As is clear from Table 1, the present invention has properties suitable as a paper strength reinforcing agent, and also has amphoteric properties, having both anionic and cationic properties. The paper made using this material has great strength as shown in Tables 2 and 3.
Excellent as a paper strength reinforcing agent.

Claims (1)

【特許請求の範囲】[Claims] 1 α,β−不飽和アミド50〜90モル%、α,β
−不飽和ニトリル10〜50モル%およびこれらと共
重合可能なノニオン性単量体0〜20モル%からな
る共重合体を、水溶液中アルカリ性下で反応させ
てアニオン基1〜20モル%およびカチオン基1〜
10モル%を同時に導入してなることを特徴とする
両性重合体よりなる紙力増強剤。
1 α,β-unsaturated amide 50-90 mol%, α,β
- A copolymer consisting of 10 to 50 mol% of unsaturated nitrile and 0 to 20 mol% of a nonionic monomer copolymerizable with these is reacted in an aqueous solution under alkalinity to form an anionic group of 1 to 20 mol% and a cationic group. Base 1~
A paper strength enhancer comprising an amphoteric polymer, characterized in that 10 mol% of the amphoteric polymer is simultaneously incorporated therein.
JP19923982A 1982-11-12 1982-11-12 Paper strength enhancer comprising Granted JPS5994699A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP19923982A JPS5994699A (en) 1982-11-12 1982-11-12 Paper strength enhancer comprising

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP19923982A JPS5994699A (en) 1982-11-12 1982-11-12 Paper strength enhancer comprising

Publications (2)

Publication Number Publication Date
JPS5994699A JPS5994699A (en) 1984-05-31
JPH0147598B2 true JPH0147598B2 (en) 1989-10-16

Family

ID=16404472

Family Applications (1)

Application Number Title Priority Date Filing Date
JP19923982A Granted JPS5994699A (en) 1982-11-12 1982-11-12 Paper strength enhancer comprising

Country Status (1)

Country Link
JP (1) JPS5994699A (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP3358377B2 (en) * 1995-03-17 2002-12-16 日本ピー・エム・シー株式会社 Surface paper quality improver

Also Published As

Publication number Publication date
JPS5994699A (en) 1984-05-31

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