JPS621403B2 - - Google Patents

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Publication number
JPS621403B2
JPS621403B2 JP54099349A JP9934979A JPS621403B2 JP S621403 B2 JPS621403 B2 JP S621403B2 JP 54099349 A JP54099349 A JP 54099349A JP 9934979 A JP9934979 A JP 9934979A JP S621403 B2 JPS621403 B2 JP S621403B2
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Japan
Prior art keywords
polymer
reaction
water
acrylamide
alkali
Prior art date
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Expired
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JP54099349A
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Japanese (ja)
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JPS5624405A (en
Inventor
Katsutoshi Tanaka
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KYORITSU JUKI KOGYO KENKYUSHO KK
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KYORITSU JUKI KOGYO KENKYUSHO KK
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Priority to JP9934979A priority Critical patent/JPS5624405A/en
Publication of JPS5624405A publication Critical patent/JPS5624405A/en
Publication of JPS621403B2 publication Critical patent/JPS621403B2/ja
Granted legal-status Critical Current

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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系重合体水溶液に次亜
ハロゲン酸アルカリおよび苛性アルカリを反応さ
せ、いわゆるホフマン反応を行つた後にポリマー
層を分離し、直接乾燥して経済的に有利にこれを
粉末化する製造方法に関するものである。 アクリルアミド系重合体のホフマン反応につい
ては多くの先行技術が開示されている。Schiller
等〔U.S.P.2729560(1956)〕はアミド基とハロゲ
ンあるいは次亜ハロゲン酸アルカリ、苛性アルカ
リのモル比を1:0.8:1.6〜1:2:4で行つた
後酸で中和しポリマーを析出させ、メタノールや
アセトン等の有機溶媒で脱水後、乾燥し粉末化し
ており、この粉末化した重合体は温水や稀酸には
溶解することが示されている。杉浦等〔工化誌
72,1926(1969)〕はポリアクリルアミド水溶液
にアルカリ性臭素溶液を反応させ、アミド基:臭
素:水酸化ナトリウムのモル比が1:1:6.5の
時、最も良い結果を得ており、アセトンを沈澱剤
として使用している。また千手等〔紙パ技協誌
30,392(1976)、特開昭51−122188号公報〕はホ
フマン反応を低温で行うことの有利さを示してい
る。 またこの他にも吉井等(特公昭46−29441号公
報)鈴木等〔木材学会誌23,204,(1977)〕有吉
等(特開昭53−6602号公報)等多くの技術が開示
され、紙力増強剤、水性向上剤、填料歩留剤等
の抄紙時の内添剤として卓越した性能を示すこと
が知られていながら、実際にポリアクリルアミド
系のホフマン反応物が市場に出ているのは1例か
2例にすぎない。 本発明者はカチオン性の高分子電解質として、
非常に有用なポリアクリルアミド系のホフマン反
応物が何故に商品化されにくいのかを種々検討し
た結果、これには種々の欠陥があることが判明し
た。つまりポリアクリルアミド系のホフマン反応
は水溶液状態で、しかもポリマー濃度が比較的薄
いところで行わなければならないため、商品とし
た場合、輸送費が嵩み、また先行技術で開示され
ているようにカルバモイル基:次亜ハロゲン酸ア
ルカリ:苛性アルカリのモル比が1:1:2でホ
フマン反応を行うと低温反応においてもかなりの
粘度低下が避けられず、高分子量を必要とする場
合には充分の効果が得られない。粘度低下を避け
るためにはカルバモイル基:次亜ハロゲン酸アル
カリ:苛性アルカリの比を1:0.5:1の様に次
亜ハロゲン酸アルカリの仕込み率を減らすことに
より得られるが、この場合にはポリマー水溶液が
アルカリ性のまゝでは残存するカルバモイル基が
加水分解を受け、効果の劣化が著しい。これを酸
で中和し、PH7.5〜8.0で保存してもコロイド滴定
の測定より、カチオン活性基の減少が見られる。
さらにPHを下げると白濁を生じ時間の経過に伴い
ポリマーを分離させ、高分子電解質として使用不
能となつてしまう。 以上述べたようにポリアクリルアミド系のホフ
マン反応物水溶液は粘度の低下、ポリマーの析
出、およびアミノ基の減少という欠点のため商品
化することの極めて困難であることが判明した。
本発明者はポリアクリルアミド系のホフマン反応
物を品質劣化のない、より経済的な方法で供給す
べく鋭意研究の結果、モル比でカルバモイル基と
等モルあるいは等モル以下の次亜ハロゲン酸アル
カリあるいはこれを形成することができる物質と
理論量よりも少なめの苛性アルカリを使用してホ
フマン反応を行い、反応後、一塩基酸である塩酸
等で中和し、ポリマー水溶液のPHを5以下にし、
時間の経過にともないポリマーを沈降させ、上澄
液をデカンテーシヨン等の手法で除去した後のポ
リマー層中の水分をさらに離漿させ、含水率80重
量%(ウエツトベース)以下、(以後含水率はす
べてウエツトベースで表示する)好ましくは70重
量%以下にまで濃縮した後、ドラムドライヤー等
で直接乾燥することにより水分を短時間で蒸発さ
せこれを粉末化したものは冷水にも溶解し、粉末
状態で保存して置けばアミノ基の消失もない安定
した品質のアクリルアミド系重合体ホフマン反応
物が得られることが判明してこの発明に到達した
ものである。 先行技術においても粉末化まで行つている例は
あるが、いづれもメタノールやアセトン等の水吸
収性の有機溶媒を使用しているため、工業化する
場合、イニシヤルコストは勿論のことランニング
コストも高くなり過ぎ、商品としての競争力がな
いため工業化が実施されていないようである。本
願発明の技術によれば有機溶媒の使用は全く必要
なく省エネルギー的製造方法であるため、現在カ
チオン性高分子電解質として一般に商品化されて
いるジメチルアミノエチルメタクリレート系高分
子電解質、およびポリアクリルアミドアミノメチ
ル化物とも価額的にも充分競合可能な製品という
ことができる。 本発明を実施するにあたり、更に詳しく説明す
る必要がある。 本発明に使用できる重合体はアクリルアミド、
メタクリルアミドあるいはこれらの共重合体、さ
らにはこれらと共重合し得る単量体との共重合体
で、アクリルアミド、メタクリルアミドを少くと
も50モル%以上含有する重合体である。これ等と
共重合し得る単量体としては、アクリロニトリ
ル、(メタ)アクリル酸、(メタ)アクリル酸エス
テル類、スチレン、酢酸ビニル、ビニルピリジ
ン、ビニルピロリドン、(メタ)アクリルアミド
N置換体等がある。 ポリアクリルアミドのホフマン反応について次
亜塩素酸ソーダおよび苛性ソーダを使用した場合
を反応式で表わすと とカルバモイル基:次亜ハロゲン酸アルカリ:苛
性アルカリのモル比は1:1:2であり、実際先
行技術においても1:1:2あるいは1:1:2
以上と、次亜ハロゲン酸アルカリはカルバモイル
基と等モルであり、苛性アルカリは次亜ハロゲン
酸アルカリの2倍モルあるいは2倍モル以上使用
するのが一般的である。本発明者はこのホフマン
反応を鋭意研究した結果、次亜ハロゲン酸アルカ
リはカルバモイル基1に対して0.5〜1以下、好
ましくは0.6〜0.8、苛性アルカリは次亜ハロゲン
酸アルカリ1に対して1.4〜2の範囲でホフマン
反応を行つた時にのみ粘度の低下もあまり見られ
ず、酸による中和後、ポリマーの析出も比較的短
時間ですみ、しかも分離したポリマー層は低温で
放置することにより、さらに水を離漿するために
容易に濃縮が可能な重合体が得られることがわか
つた。 反応温度については千手等の提案している低温
にて実施する方法は副反応を避けるためには良い
方法ではあるが、このホフマン反応は反応熱が大
きすぎ、調整しきれず、工業化する場合には現実
的ではない。それよりも反応開始温度を可能な限
り低くしておき、強撹拌下で反応させ、系の温度
が40℃以上に成つても短時間の内に中和して反応
時間を短くすることにより副反応を避ける方法の
方が現実的であり、工業化し易い。高温短時間で
の反応物は低温長時間での反応物と比較してアミ
ノ化率で数%程度低くはなるが性能的には大差の
ない重合体が得られるため、低温反応に必ずしも
拘わる必要はない。 アクリルアミド系重合体のホフマン反応物の酸
中和物が水溶液より析出して来る現象はホフマン
反応中、苛性アルカリによるカルバモイル基の加
水分解の結果生成するカルボキシル基とアミノ基
のポリマーコンプレツクスの形成のためと説明で
きるが、このポリマーの析出にはホフマン反応で
副生される塩による塩析効果も大きく寄与してい
ると考えられる。さらに興味深いことに塩の種類
および塩の濃度により塩溶という現象も見られ
る。例えば析出したポリマーは塩化アンモニウム
や硫酸アンモニウム等の飽和水溶液には完全に溶
解する。 またこの重合体は中和に使用する酸の種類の影
響を受ける。硫酸、シユー酸、リン酸等の二塩基
酸以上の多価の酸を使用して中和した重合体は乾
燥後水に不溶性であり、塩酸、食塩、塩化アンモ
ニウム等の水溶液には可溶である。 さらには塩酸等の一塩基酸で中和した後この重
合体水溶液に硫酸ソーダ等の二価以上のアニオン
基より成る塩を添加しても塩の、ある添加量以上
では不溶性のポリマーとなる。このような事実か
ら本願発明を実施するにあたり、使用するに好し
い酸としては一塩基酸が最もよく、コスト的には
塩酸を使用するのが最もよいが、乾燥後の重合体
が水不溶性にならない範囲で硫酸等の併用も可能
である。 さらに中和時の重合体水溶液のPHは中性および
アルカリ性に於いては乾燥中分子間架橋によりゲ
ル化し、水溶性の重合体は得られない。重合体水
溶液のPHが5以下であれば乾燥中のゲル化は見ら
れず、また保存中の劣化も見られないところの粉
末重合体を得ることができるが、PHを2以下にす
ることは経済的に不利であり、また装置の腐食の
面からも好しくないため、重合体水溶液のPHは5
〜3の間に保つのが得策である。 アクリルアミド系重合体のホフマン反応物水溶
液のPHを酸性にすると0.1重量%濃度(以後濃度
は全て重量%として表示する)の還元粘度が6〜
7以上の分子量の重合体を使用した場合には中和
時に重合体を分離して来るが、これ以下の重合度
のものは中和時は若干白く濁る程度であるが、こ
れを低温で保存しておけば2〜3時間でポリマー
が沈降し上層はほゞ澄明に近い水層となる。この
水層をメタノールに注ぐと白濁し、ごく少量の重
合体が沈降せずに、上層に残留していることがわ
かる。この層分離したポリマー層を取り出すと含
水率80重量%前後であり、これはこのまゝドラム
ドライヤー等で乾燥することは可能であるが、こ
の重合体は低温で放置するだけでもさらに水を離
漿させ、あるいは剪断力を与えることにより、よ
り短時間で水を離漿させ、容易に含水率70%程度
まで濃縮が可能であるため可能な限りこのような
方法で濃縮した方が乾燥作業で除去する水分量が
少くてすみ、より省エネルギー的であつて好まし
い。またこの濃縮は少量の食塩を添加することに
より、より効果的に行うことが可能である。 この含水率70%前後の重合体は低温ではゲル状
で流動性はないが、加温すると流動性が出て来る
ため、造粒して流動層乾燥やバンド乾燥等の方法
では粒子同志が接着し合い乾燥困難である。しか
し加温すると流動性が出て来る特徴を生かし、ド
ラムドライヤーやフイルム状態で乾燥すれば厚さ
3mm以下であれば比較的短時間で乾燥でき、特に
厚さ1mm以下であれば数分間の乾燥時間で良く、
また140〜150℃の乾燥温度を使用しても溶解性の
良好な重合体粉末の製造が可能となつた。 次に本願発明を実施例により具体的に説明する
が本願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〕 0.1%の還元粘度が3.8であるアクリルアミド重
合体水溶液710g(アクリルアミドとして71g)
をビーカーに取り4℃に冷却しておく、別に
NaOClの12%水溶液435g(0.7モル)と48%苛性
ソーダ水溶液83.4g(1モル)を混合冷却して−
5℃にしておく、ビーカーに取つたアクリルアミ
ド重合体水溶液を外部より冷却しながら激しく撹
拌し、次亜塩素酸ソーダと苛性ソーダ混合液を添
加した。撹拌を続けていると1〜2分間の誘導期
間の後、反応熱により急激に温度上昇を示し、外
部からの冷却では間に合はず反応開始後15分では
系の温度は42℃を示し、以後次第に温度は下降
し、30分後には20℃まで低下した。このものに35
%亜硫酸水素ナトリウム3gを添加、撹拌した
後、塩酸を加えて系のPHを4.8とした。この重合
体水溶液は若干白濁はしているが均一であつた。
この重合体水溶液を4℃の冷蔵庫に1夜保存する
ことにより白濁した重合体層と少量のオリゴマー
程度の分子量の重合体を含有する半透明の水層と
に層分離を起した。デカンテーシヨンで水層を除
き、ポリマー層の一部を取出し、含水率を測定し
た所、80.2%であつた。残りの重合体について温
度が上昇しない様に外部から冷却しながら、ゆつ
くり撹拌してやるとさらに水を離漿して、含水率
68.8%の濃度にまで濃縮できた。 この重合体を内温140℃のドラムドライヤーで
で約0.3mmの厚さで乾燥すると3分以内で乾燥で
き、乾燥物を粉砕することにより粉末状態のポリ
アクリルアミドホフマン反応物を得た。この粉末
重合体を水に溶解し、コロイド滴定を行つた結
果、カチオン量は5.23meq/粉末重合体1g
(meqはミリ当量)アニオン量は0.46meq/粉
末重合体1gであつた。 またこの粉末重合体を55℃の恒温槽に入れ21日
間保存の後、水に溶解して測定したコロイド滴定
の結果はカチオン量は5.22meq/粉末重合体1
g、アニオン量は0.44meq/粉末重合体1gで
保存による劣化はほとんど見られなかつた。 〔実施例 2〕 実施例1で使用したものと同一の重合体を使用
してポリアクリルアミドに対する次亜塩素酸ソー
ダおよび苛性ソーダの仕込み率を変化させた一連
の試験を行つた結果を表1に示した。反応方法は
実施例1と同様に行い、中和は塩酸を使用して系
のPHを4±1に調整した。
The present invention is an economically advantageous manufacturing method in which an aqueous acrylamide polymer solution is reacted with an alkali hypohalite and a caustic alkali to perform the so-called Hofmann reaction, and then the polymer layer is separated and directly dried to form a powder. It is related to. Many prior art techniques have been disclosed regarding the Hoffman reaction of acrylamide polymers. Schiller
[USP 2729560 (1956)] set the molar ratio of amide group to halogen or alkali hypohalite or caustic alkali to 1:0.8:1.6 to 1:2:4, and then neutralized with acid to precipitate a polymer. After dehydration with an organic solvent such as methanol or acetone, it is dried and powdered, and it has been shown that this powdered polymer is soluble in hot water and dilute acids. Sugiura et al.
72 , 1926 (1969)] reacted an aqueous polyacrylamide solution with an alkaline bromine solution, and obtained the best results when the molar ratio of amide group:bromine:sodium hydroxide was 1:1:6.5, and precipitated acetone. It is used as an agent. Also, Senju etc. [Paper Paper Technology Association Magazine]
30 , 392 (1976), JP-A-51-122188] shows the advantage of carrying out the Hofmann reaction at low temperatures. In addition, many other technologies have been disclosed, such as Yoshii et al. (Japanese Patent Publication No. 46-29441), Suzuki et al. [Journal of the Japan Society of Wood Science 23 , 204, (1977)], Ariyoshi et al. Although it is known to exhibit excellent performance as an internal additive during paper making such as paper strength enhancers, aqueous properties improvers, filler retention agents, etc., there are actually polyacrylamide-based Hoffmann reactants on the market. are only one or two cases. The present inventor has discovered that as a cationic polymer electrolyte,
As a result of various investigations into why the extremely useful polyacrylamide-based Hofmann reaction product has been difficult to commercialize, it has been found that it has various deficiencies. In other words, the Hofmann reaction of polyacrylamide systems must be carried out in an aqueous solution state and at a relatively low polymer concentration, which increases transportation costs when commercialized, and as disclosed in the prior art, carbamoyl groups: When the Hofmann reaction is carried out at a molar ratio of alkali hypohalite and caustic alkali of 1:1:2, a considerable decrease in viscosity is inevitable even in low-temperature reactions, and a sufficient effect is obtained when a high molecular weight is required. I can't. In order to avoid a decrease in viscosity, the ratio of carbamoyl group: alkali hypohalite: caustic alkali can be obtained by reducing the charging ratio of alkali hypohalite to 1:0.5:1, but in this case, the ratio of alkali hypohalite to caustic alkali is 1:0.5:1. If the aqueous solution remains alkaline, the remaining carbamoyl groups will undergo hydrolysis, resulting in significant deterioration of the effect. Even when this is neutralized with acid and stored at pH 7.5 to 8.0, a decrease in cationic active groups is observed as measured by colloid titration.
If the pH is further lowered, it becomes cloudy and the polymer separates over time, making it unusable as a polymer electrolyte. As mentioned above, it has been found that it is extremely difficult to commercialize polyacrylamide-based Hoffmann reactant aqueous solutions due to the disadvantages of decreased viscosity, polymer precipitation, and decreased amino groups.
As a result of intensive research in order to supply polyacrylamide-based Hoffmann reactants in a more economical manner without quality deterioration, the present inventors found that alkali hypohalite or A Hofmann reaction is carried out using a substance capable of forming this and a smaller amount of caustic alkali than the theoretical amount, and after the reaction, neutralization is carried out with hydrochloric acid, which is a monobasic acid, to bring the pH of the polymer aqueous solution to 5 or less,
As time passes, the polymer is allowed to settle, and the supernatant liquid is removed by a method such as decantation, and the water in the polymer layer is further synergized, resulting in a water content of 80% by weight (wet base) or less (hereinafter referred to as water content). (all expressed on a wet basis) Preferably, after concentrating to 70% by weight or less, drying directly with a drum dryer etc. evaporates the water in a short time and powders it, which dissolves in cold water and becomes a powder. The present invention was achieved based on the finding that a Hofmann reaction product of an acrylamide polymer of stable quality without loss of amino groups can be obtained by storing it in a vacuum. Although there are examples of prior art that have gone as far as powdering, they all use water-absorbing organic solvents such as methanol and acetone, so if they are to be industrialized, not only the initial cost but also the running cost will be high. It seems that industrialization has not been carried out because it has become too much and lacks competitiveness as a product. According to the technology of the present invention, the use of organic solvents is not required at all and the production method is energy-saving, so dimethylaminoethyl methacrylate-based polymer electrolytes and polyacrylamide aminomethyl, which are currently commercialized as cationic polymer electrolytes, are used. It can be said that the product is fully competitive in terms of price with chemical products. In carrying out the present invention, it is necessary to explain it in more detail. Polymers that can be used in the present invention include acrylamide,
It is a copolymer of methacrylamide or a copolymer thereof, or a monomer copolymerizable with these, and contains at least 50 mol% of acrylamide or methacrylamide. Monomers that can be copolymerized with these include acrylonitrile, (meth)acrylic acid, (meth)acrylic acid esters, styrene, vinyl acetate, vinylpyridine, vinylpyrrolidone, (meth)acrylamide N-substituted products, etc. . The Hofmann reaction of polyacrylamide using sodium hypochlorite and caustic soda is expressed as a reaction equation. The molar ratio of carbamoyl group: alkali hypohalite: caustic alkali is 1:1:2, and in fact, in the prior art, it is also 1:1:2 or 1:1:2.
As mentioned above, the alkali hypohalite is equimolar to the carbamoyl group, and the caustic alkali is generally used in an amount twice or more than twice the mole of the alkali hypohalite. As a result of intensive research on this Hofmann reaction, the present inventor found that the alkali hypohalite is 0.5 to 1 or less, preferably 0.6 to 0.8, per 1 carbamoyl group, and the caustic alkali is 1.4 to 1 per 1 carbamoyl group. Only when the Hofmann reaction was carried out in the range of 2, no significant decrease in viscosity was observed, and the precipitation of the polymer after neutralization with acid took a relatively short time.Moreover, by leaving the separated polymer layer at a low temperature, Furthermore, it was found that a polymer that can be easily concentrated to synergate water can be obtained. As for the reaction temperature, the method proposed by Senju et al. of carrying out the reaction at a low temperature is a good method to avoid side reactions, but this Hofmann reaction generates too much reaction heat and cannot be fully controlled, making it difficult to industrialize. is not realistic. Rather, by keeping the reaction initiation temperature as low as possible, allowing the reaction to occur under strong stirring, and even if the system temperature reaches 40°C or higher, it can be neutralized within a short time to shorten the reaction time. Methods that avoid reactions are more realistic and easier to industrialize. It is not necessary to be involved in low-temperature reactions because the reaction product obtained at high temperature for a short time has a lower amination rate by a few percent compared to the reactant at low temperature for a long time, but there is no big difference in performance. There isn't. The phenomenon in which the acid-neutralized product of the Hoffmann reaction product of an acrylamide polymer precipitates from an aqueous solution is due to the formation of a polymer complex of carboxyl groups and amino groups generated as a result of hydrolysis of carbamoyl groups with caustic alkali during the Hoffmann reaction. Although this can be explained as the precipitation of the polymer, the salting out effect due to the salt by-produced in the Hofmann reaction is also considered to be a major contributor to the precipitation of this polymer. More interestingly, the phenomenon of salt dissolution can also be observed depending on the type of salt and the concentration of the salt. For example, the precipitated polymer is completely dissolved in a saturated aqueous solution of ammonium chloride, ammonium sulfate, or the like. The polymer is also affected by the type of acid used for neutralization. Polymers neutralized using dibasic or higher polyhydric acids such as sulfuric acid, oxalic acid, and phosphoric acid are insoluble in water after drying, but are soluble in aqueous solutions such as hydrochloric acid, common salt, and ammonium chloride. be. Furthermore, even if a salt consisting of divalent or higher anion groups, such as sodium sulfate, is added to the aqueous polymer solution after neutralization with a monobasic acid such as hydrochloric acid, the polymer becomes insoluble if the added amount of the salt exceeds a certain amount. Based on these facts, when carrying out the present invention, monobasic acids are the most preferable acids to use, and hydrochloric acid is the best in terms of cost, but the polymer after drying becomes water-insoluble. It is also possible to use sulfuric acid etc. in combination to the extent that it is not necessary. Furthermore, when the pH of the aqueous polymer solution during neutralization is neutral or alkaline, gelation occurs due to intermolecular crosslinking during drying, and a water-soluble polymer cannot be obtained. If the pH of the aqueous polymer solution is 5 or less, it is possible to obtain a powdered polymer that does not undergo gelation during drying or deterioration during storage, but it is not possible to reduce the pH to 2 or less. The pH of the polymer aqueous solution should be set to 5 because it is economically disadvantageous and also undesirable from the standpoint of equipment corrosion.
It is a good idea to keep it between ~3. When the pH of the Hoffmann reaction product aqueous solution of an acrylamide polymer is made acidic, the reduced viscosity at a concentration of 0.1% by weight (hereinafter all concentrations are expressed as weight%) increases from 6 to 6.
If a polymer with a molecular weight of 7 or higher is used, the polymer will separate during neutralization, but if the polymerization degree is lower than this, it will become slightly cloudy during neutralization, but it can be stored at low temperatures. If left for 2 to 3 hours, the polymer will settle and the upper layer will become a nearly clear water layer. When this aqueous layer is poured into methanol, it becomes cloudy, indicating that a very small amount of polymer remains in the upper layer without settling. When this layer-separated polymer layer is taken out, the water content is around 80% by weight, and although it is possible to dry it with a drum dryer, etc., this polymer can further release water by simply leaving it at a low temperature. By applying shearing force or syneresis, water can be synercised in a shorter time and it is possible to easily concentrate the water content to about 70%, so it is better to concentrate using this method as much as possible to make drying work easier. This method is preferable because it requires less water to be removed and is more energy-saving. Further, this concentration can be performed more effectively by adding a small amount of common salt. This polymer with a water content of around 70% is gel-like at low temperatures and has no fluidity, but it becomes fluid when heated, so when it is granulated and subjected to methods such as fluidized bed drying or band drying, the particles adhere to each other. It is difficult to dry them together. However, if you take advantage of the characteristic that it becomes fluid when heated and dry it in a drum dryer or film state, it can be dried in a relatively short time if the thickness is 3 mm or less, and especially if it is 1 mm or less, it will dry in a few minutes. Time is enough,
Furthermore, it has become possible to produce a polymer powder with good solubility even when using a drying temperature of 140 to 150°C. Next, the present invention will be specifically explained with reference to examples, but the present invention is not limited to the following examples unless it exceeds the gist thereof. [Example 1] 710 g of acrylamide polymer aqueous solution with a reduced viscosity of 3.8 at 0.1% (71 g as acrylamide)
Take it in a beaker and cool it to 4℃, separately.
435 g (0.7 mol) of a 12% aqueous solution of NaOCl and 83.4 g (1 mol) of a 48% aqueous solution of caustic soda were mixed and cooled.
The acrylamide polymer aqueous solution taken in a beaker and kept at 5° C. was vigorously stirred while being cooled from the outside, and a mixed solution of sodium hypochlorite and caustic soda was added thereto. As stirring continued, after an induction period of 1 to 2 minutes, the temperature rapidly rose due to the heat of reaction, and external cooling was not enough, and the system temperature reached 42°C 15 minutes after the start of the reaction. After that, the temperature gradually decreased and reached 20°C after 30 minutes. 35 for this thing
After adding 3 g of % sodium bisulfite and stirring, hydrochloric acid was added to adjust the pH of the system to 4.8. This aqueous polymer solution was slightly cloudy but homogeneous.
This aqueous polymer solution was stored in a refrigerator at 4° C. overnight to cause layer separation into a cloudy polymer layer and a translucent aqueous layer containing a small amount of a polymer with a molecular weight similar to that of an oligomer. The water layer was removed by decantation, a portion of the polymer layer was taken out, and the water content was measured and found to be 80.2%. If the remaining polymer is cooled externally to prevent the temperature from rising and is slowly stirred, water will be synergized and the water content will increase.
It was possible to concentrate to a concentration of 68.8%. This polymer was dried to a thickness of about 0.3 mm in a drum dryer at an internal temperature of 140°C, and the dried product was pulverized to obtain a polyacrylamide Hoffmann reaction product in powder form. This powder polymer was dissolved in water and colloid titration was performed, and the amount of cations was 5.23 m e q/1 g of powder polymer.
(m eq is milliequivalent) The amount of anion was 0.46 m eq/1 g of powdered polymer. In addition, after storing this powder polymer in a constant temperature bath at 55℃ for 21 days, it was dissolved in water and measured by colloid titration. The amount of cations was 5.22 m e q/1 powder polymer.
g, the amount of anions was 0.44 m eq/g of powdered polymer, and almost no deterioration was observed during storage. [Example 2] Table 1 shows the results of a series of tests conducted using the same polymer as used in Example 1 and varying the loading ratio of sodium hypochlorite and caustic soda to polyacrylamide. Ta. The reaction method was carried out in the same manner as in Example 1, and the pH of the system was adjusted to 4±1 using hydrochloric acid for neutralization.

〔実施例 3〕[Example 3]

アクリルアミド80g、アクリルニトリル20g、
脱イオン水900gをビーカーに採り窒素を導入し
つつ系の温度を30℃とし過硫酸アンモニウム0.08
g、亜硫酸水素ナトリウム0.08gを添加したとこ
り、重合を開始し、8時間後には重合が完結し
た。この重合体は赤外線吸収スペクトルによれば
2240cm-1にニトリルの吸収があり、アクリルアミ
ド−アクリロニトリル共重合体であることがわか
つた。またこの重合体の粘度はブルツクフイール
ド粘度計で測定したところ、10800センチポイズ
(測定温度25℃)であつた。 この重合体500gをビーカーに取り、0℃に冷
却しておく。別にNaOCl12%水溶液250gと48%
苛性ソーダ水溶液55gを混合冷却して−10℃にし
ておく。ビーカーに取つた重合体水溶液を外部よ
り冷却しつつ激しく撹拌し、次亜塩素酸ソーダと
苛性ソーダ混合液を添加した。撹拌を続けている
と、2〜3分間の誘導期間の後、反応熱により急
激に温度上昇を示し、反応開始20分後には系の温
度は35℃を示し、以後次第に温度は低下し、45分
後には15℃まで下降した。こゝで亜硫酸水素ナト
リウム2gを添加混合した後、塩酸で中和し、系
のPHを4.5とした。この重合体を4℃の冷蔵庫に
入れておくと、2時間後には重合体層と水層とに
相分離した。重合体層を取り出し、その一部で含
水率を測定したところ、79.8%であつた。この含
水率79.8%の重合体200gに食塩20gを添加混合
したところ、さらに水を離漿して重合体の含水率
は65.2%まで濃縮された。この重合体をポリエス
テル系のフイルム(商品名ダイヤホイル)上に約
1mmの厚さに塗り、内温90℃の通風乾燥機で25分
間乾燥することにより、フイルム状態で乾燥品重
合体を得た。この重合体を粉砕することにより粉
末重合体とした。この粉末重合体を水に溶解し、
コロイド滴定した結果、カチオン量は4.72me
q/粉末重合体1g、アニオン量は0.41meq/
粉末重合体1gであつた。
80g of acrylamide, 20g of acrylonitrile,
Pour 900g of deionized water into a beaker, introduce nitrogen and bring the temperature of the system to 30°C, and add 0.08 ammonium persulfate.
When 0.08 g of sodium hydrogen sulfite was added, polymerization started, and the polymerization was completed after 8 hours. According to the infrared absorption spectrum, this polymer
There was a nitrile absorption at 2240 cm -1 , indicating that it was an acrylamide-acrylonitrile copolymer. The viscosity of this polymer was measured using a Bruckfield viscometer and was found to be 10,800 centipoise (measurement temperature: 25°C). Take 500 g of this polymer in a beaker and cool it to 0°C. Separately, 250 g of NaOCl 12% aqueous solution and 48%
Mix and cool 55 g of caustic soda aqueous solution to -10°C. The aqueous polymer solution taken in a beaker was vigorously stirred while being cooled from the outside, and a mixed solution of sodium hypochlorite and caustic soda was added. As stirring continued, after an induction period of 2 to 3 minutes, the temperature rapidly increased due to the heat of reaction, and 20 minutes after the start of the reaction, the temperature of the system reached 35°C, after which the temperature gradually decreased until 45°C. After a few minutes, the temperature dropped to 15°C. After adding and mixing 2 g of sodium bisulfite, the mixture was neutralized with hydrochloric acid to bring the pH of the system to 4.5. When this polymer was placed in a refrigerator at 4°C, it phase-separated into a polymer layer and an aqueous layer after 2 hours. When the polymer layer was taken out and the moisture content of a portion thereof was measured, it was found to be 79.8%. When 20 g of common salt was added and mixed to 200 g of this polymer with a water content of 79.8%, water was further synercised and the water content of the polymer was concentrated to 65.2%. This polymer was applied to a thickness of approximately 1 mm on a polyester film (trade name Diafoil) and dried in a ventilation dryer at an internal temperature of 90°C for 25 minutes to obtain a dried polymer in the form of a film. . This polymer was pulverized to obtain a powdered polymer. Dissolve this powdered polymer in water,
As a result of colloid titration, the amount of cations was 4.72 m e
q/1g of powder polymer, the amount of anions is 0.41m e q/
The amount of powdered polymer was 1 g.

Claims (1)

【特許請求の範囲】[Claims] 1 アクリルアミドおよびメタクリルアミドを少
くとも50モル%以上含有する重合体水溶液にモル
比でカルバモイル基1に対して次亜ハロゲン酸ア
ルカリ、あるいはこれを形成し得る物質0.5以上
1.0以下、および苛性アルカリを次亜ハロゲン酸
アルカリ1に対して1.4以上2以下反応させ、い
わゆるホフマン反応を行つた後、酸を添加し系の
PHを5以下にし、ポリマー層と水層とに分離しポ
リマー層中の含水率を80重量(ウエツトベース)
以下にした後、直接これを乾燥することにより水
分を除去してこれを粉末とすることを特徴とする
アクリルアミド系重合体のホフマン反応物の粉末
化製造法。
1. In an aqueous polymer solution containing at least 50 mol% of acrylamide and methacrylamide, a molar ratio of 1 to 1 carbamoyl group to alkali hypohalite or a substance capable of forming this is 0.5 or more.
1.0 or less, and a caustic alkali is reacted with 1.4 or more and 2 or less of alkali hypohalite to perform the so-called Hofmann reaction, and then an acid is added to the system.
Reduce the pH to 5 or less, separate the polymer layer and water layer, and reduce the water content in the polymer layer to 80% by weight (wet base).
1. A method for producing a powder of a Hofmann reaction product of an acrylamide-based polymer, which is characterized in that the powder is made into a powder by directly drying it to remove moisture.
JP9934979A 1979-08-03 1979-08-03 Method of pulverizing hofmann reaction product of acrylamide polymer Granted JPS5624405A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP9934979A JPS5624405A (en) 1979-08-03 1979-08-03 Method of pulverizing hofmann reaction product of acrylamide polymer

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP9934979A JPS5624405A (en) 1979-08-03 1979-08-03 Method of pulverizing hofmann reaction product of acrylamide polymer

Publications (2)

Publication Number Publication Date
JPS5624405A JPS5624405A (en) 1981-03-09
JPS621403B2 true JPS621403B2 (en) 1987-01-13

Family

ID=14245128

Family Applications (1)

Application Number Title Priority Date Filing Date
JP9934979A Granted JPS5624405A (en) 1979-08-03 1979-08-03 Method of pulverizing hofmann reaction product of acrylamide polymer

Country Status (1)

Country Link
JP (1) JPS5624405A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS62139103U (en) * 1986-02-21 1987-09-02

Families Citing this family (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS57165404A (en) * 1981-04-06 1982-10-12 Oji Kenzai Kogyo Kk Preparation of high polymeric flocculant
JPS58108206A (en) * 1981-12-21 1983-06-28 Konan Kagaku Kogyo Kk Preparation of stable aqueous solution of polyacrylamide modified with cation
JPS6269900A (en) * 1985-09-24 1987-03-31 出光石油化学株式会社 Size agent
JP2860554B2 (en) * 1988-12-28 1999-02-24 三井化学株式会社 Method for producing cationic acrylamide polymer and use thereof
CN1042638C (en) * 1992-07-11 1999-03-24 南开大学 Prepn. and application of series plastics of polyvinyl amine
JP2009150009A (en) * 2007-12-20 2009-07-09 Hymo Corp Internal additive for papermaking and method of using the same
JP5171276B2 (en) * 2008-01-15 2013-03-27 ハイモ株式会社 Inkjet paper coating agent

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS62139103U (en) * 1986-02-21 1987-09-02

Also Published As

Publication number Publication date
JPS5624405A (en) 1981-03-09

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