JPS61118406A - Production of water-soluble polyvinylamine - Google Patents
Production of water-soluble polyvinylamineInfo
- Publication number
- JPS61118406A JPS61118406A JP24029884A JP24029884A JPS61118406A JP S61118406 A JPS61118406 A JP S61118406A JP 24029884 A JP24029884 A JP 24029884A JP 24029884 A JP24029884 A JP 24029884A JP S61118406 A JPS61118406 A JP S61118406A
- Authority
- JP
- Japan
- Prior art keywords
- polymer
- water
- hydrolysis
- vinylformamide
- ammonia
- 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
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明は有機汚泥の脱水用凝集剤および製紙工業におけ
る炉水性向上剤あるいは填料歩留向 ・止剤としてすぐ
れた性能を有する水溶性ポリビニルアミンの製造方法に
関する。[Detailed Description of the Invention] [Industrial Application Field] The present invention provides a water-soluble polyvinylamine having excellent performance as a flocculant for dewatering organic sludge, a furnace aqueous property improver in the paper industry, or a filler retention agent. Relating to a manufacturing method.
N−ビニルホルムアミドをラジカル重合させて得られる
重合体を加水分解することにより水溶性ポリビニルアミ
ンが得られることは特開昭5r−23roy号公報によ
シ知られている。It is known from JP-A-5R-23ROY that water-soluble polyvinylamine can be obtained by hydrolyzing a polymer obtained by radical polymerization of N-vinylformamide.
N−ビニルホルムアミドの重合によシ得られるN−ビニ
ルホルムアミド重合体をメタノール等の親水性溶媒を用
いて精製したのち塩基性加水分解を水溶性の良好なポリ
ビニルアミンが取得できるが、精製を行なわすに加水分
解すれば、反応の進行に伴ない架橋反応が生起し、水不
溶性の重合体が生成するとともに重合体が褐色に着色す
る。Polyvinylamine with good water solubility can be obtained by basic hydrolysis after the N-vinylformamide polymer obtained by polymerization of N-vinylformamide is purified using a hydrophilic solvent such as methanol. When hydrolyzed, a crosslinking reaction occurs as the reaction progresses, producing a water-insoluble polymer and coloring the polymer brown.
この理由は必ずしも明らかではないが、M−ビニルホル
ムアミド重合体中に含有される不純物が塩基性条件下に
分解してアセトアルデヒドが生成し、これが重合体の加
水分解により生じたポリビニルアミンと架橋反応をおこ
すためと推定される。The reason for this is not necessarily clear, but impurities contained in the M-vinylformamide polymer decompose under basic conditions to produce acetaldehyde, which undergoes a crosslinking reaction with polyvinylamine produced by hydrolysis of the polymer. It is presumed that the purpose was to cause trouble.
N−ビニルホルムアミド重合体を前述のように精製する
には多量の沈澱溶媒と洗浄溶媒を必要とするので工業的
には望ましい方法ではなく、精製を行なわずに高分子量
の水溶性ポリビニルアミンを取得する方法が待望されて
いた。Purifying the N-vinylformamide polymer as described above requires a large amount of precipitation solvent and washing solvent, so it is not an industrially desirable method, and high molecular weight water-soluble polyvinylamine can be obtained without purification. A method to do this has been long awaited.
すなわち、本発明の目的は、N−ビニルホルムアミドを
重合させて得られるN−ビニルホルムアミド重合体をn
*することなく塩基性加水分解して水溶性ポリビニルア
ミンを製造する方法を提供するにあり、かかる目的は、
N−と二Nホルムアミド重合体にアンモニア、第1級ア
ミンまたは@コ級アミンを添加したのち塩基性加水分解
することにより達成される。That is, the object of the present invention is to produce an N-vinylformamide polymer obtained by polymerizing N-vinylformamide.
*The purpose is to provide a method for producing water-soluble polyvinylamine by basic hydrolysis without
This is achieved by adding ammonia, primary amines or co-class amines to N- and diN formamide polymers, followed by basic hydrolysis.
以下に本発明の詳細な説明する。The present invention will be explained in detail below.
本発明において、N−ビニルホルムアミド重合体として
は、N−ビニルホルムアミドのホモポリマーのみならず
、他のとニルモノマーとの共重合体も使用することがで
きる。このようなどニルモノマーとしては水溶性のとニ
ルモノマーが好ましく、(メタ)アクリルアミド、N−
アルキル(メタ)アクリルアミド、N、N−ジアルキル
(メタ)アクリルアミド、N、N−ジアルキルアミノア
ルキル(メタ)アクリルアミド、(メタ)アクリルアミ
ドアルキルトリメチルアンモニウム塩、(メタ)アクリ
ルアミドアルカ/スルホン酸塩、(メタ)アクリロニト
リル、(メタ)アクリル酸塩、ジアルキルアミノアルキ
ル(メタ)アクリレート、N−ビニルピロリド7、N−
アルキル−N−ビニルホルムアミド、N−アルキル−N
−ビニルアセトアミド、ジアリルジアルキルアンモニウ
ム塩、ビニルピリジ/、ビニルイミダゾール、ビニルベ
ンジルトリプルキルアンモニウム塩、ビニルスルホン酸
塩などが挙げられる。In the present invention, as the N-vinylformamide polymer, not only a homopolymer of N-vinylformamide but also a copolymer with other vinyl monomers can be used. As such nyl monomers, water-soluble nyl monomers are preferred, such as (meth)acrylamide, N-
Alkyl (meth)acrylamide, N,N-dialkyl (meth)acrylamide, N,N-dialkylaminoalkyl (meth)acrylamide, (meth)acrylamidoalkyltrimethylammonium salt, (meth)acrylamide alkyl/sulfonate, (meth) Acrylonitrile, (meth)acrylate, dialkylaminoalkyl (meth)acrylate, N-vinylpyrrolide 7, N-
Alkyl-N-vinylformamide, N-alkyl-N
-vinylacetamide, diallyldialkylammonium salt, vinylpyridi/, vinylimidazole, vinylbenzyl triplekylammonium salt, vinylsulfonate and the like.
N−ビニルホルムアミドの重合ま九は共重合は、ラジカ
ル重合開始剤、特にコ、2′−7ゾビスーコーアミジノ
ブロノくンまたはアゾビス−N、N’−ジメチレンイソ
ブテルアミジ/の塩酸塩、硫Wl塙もしくは酢酸塩、あ
るいは弘、弘′−アゾビスーφ−クアノ吉草酸のアルカ
リ金属塩またはアンモニウム塩などの水溶性アゾ化合物
をモノマーに対して/ 00〜/ 0000 ppm
、好ましくはj 00〜j 000 ppm使用し、3
0〜IOθ℃、好ましくはぞ0〜20℃で行なわれる。The polymerization or copolymerization of N-vinylformamide can be carried out using a radical polymerization initiator, especially co-, 2'-7zobis-coamidinobronobrono or azobis-N,N'-dimethyleneisobuteramide/. Water-soluble azo compounds such as hydrochloride, sulfuric acid or acetate, or alkali metal salts or ammonium salts of Hiro', Hiro'-azobis-φ-quanovaleric acid, based on the monomer, / 00 to / 0000 ppm
, preferably using j 00 to j 000 ppm, 3
It is carried out at a temperature of 0 to IOθ°C, preferably 0 to 20°C.
重合の形式は特に限定されることなく、七ツマ−を溶解
する溶媒中で重合を行ない重合体の溶液ま九は沈澱を得
る方法、約−〇重量−以下のモノマー水溶液を用いて重
合を行ない重合体水溶液を得る方法、約20−?jii
景−の高濃度の七ツマー水溶液を用いて重合を行ない重
合体の含水固型物を得る方法、高濃度のモノマー水溶液
を有機溶媒中に2濁させて重合を行ない重合体の分散物
を得る方法あるいは塊状重合法など適宜選択することが
できる。The type of polymerization is not particularly limited, and polymerization may be carried out in a solvent that dissolves the polymer to obtain a polymer solution or precipitate, or polymerization may be carried out using an aqueous monomer solution having a weight of about -00 weight or less. How to obtain an aqueous polymer solution, about 20-? jiii
A method of polymerizing using a highly concentrated aqueous solution of a monomer to obtain a water-containing solid polymer; a method of obtaining a polymer dispersion by suspending a highly concentrated aqueous monomer solution in an organic solvent and polymerizing it; The method or bulk polymerization method can be selected as appropriate.
本発明はかくして得られるN−ビニルホルムアミド重合
体を塩基性加水分解する際に適用され、特に高分子量の
重合体を加水分解する際に有効であるので、その効果は
還元粘度(l規定食塙水中、0./f/dAの重合体濃
度で測定した粘度)が3以上である重合体の加水分解に
適用する場合に顕著である。The present invention is applied to the basic hydrolysis of the N-vinylformamide polymer thus obtained, and is particularly effective in hydrolyzing high molecular weight polymers. This is remarkable when applied to the hydrolysis of polymers whose viscosity (measured in water at a polymer concentration of 0./f/dA) is 3 or more.
N−ビニルホルムアミド重合体にアンモニア、第7級ア
ミンまたは第2級アミンを添加したのち塩基性加水分解
を行なうことにより、加水分解反応中の架橋反応が回避
され、重合体の着色も防止し得る。第1Rまたは第2級
アミンとしては低級アミンを使用することが好ましく、
メチルアミン、エチルアミン、n−ブチルアミン、エタ
ノールアミン、エチレンジアミン、ジエチレントリアミ
ン、ジメチルアミン、ジエチルアミン、ジェタノールア
ミン、N−メチルエタノールアミン、モルホリンなどが
例示される。これらのアンモニア及びアミンは通常、水
溶液状あるいは適当な溶媒に溶解してN−ビニルホルム
アミド重合体に添加されるが、アンモニア及び低沸点の
アミンは重合体の水溶液あるいは分散液中にガス状で添
加することもできる。1ンモニア、第1級アミンまたは
第1級アミンの添加量はN−ビニルホルムアミド重合体
のアミド基に対して0.00 /〜l当量、好ましくは
0,0/〜0.2当量の範囲内で選択される。添加時期
は重合体の塩基性加水分解が実質的に開始される以前で
あればよいが、添加後1o−to℃で10−200分間
保持したのち、加水分解触媒として強塩基性物質を加え
ることが好ましい。By adding ammonia, a 7th-class amine, or a secondary amine to an N-vinylformamide polymer and then performing basic hydrolysis, crosslinking reaction during the hydrolysis reaction can be avoided and coloring of the polymer can also be prevented. . It is preferable to use a lower amine as the 1R or secondary amine,
Examples include methylamine, ethylamine, n-butylamine, ethanolamine, ethylenediamine, diethylenetriamine, dimethylamine, diethylamine, jetanolamine, N-methylethanolamine, and morpholine. These ammonia and amines are usually added to the N-vinylformamide polymer in the form of an aqueous solution or dissolved in a suitable solvent, but ammonia and amines with a low boiling point are added in the form of a gas to the aqueous solution or dispersion of the polymer. You can also. The amount of ammonia, primary amine, or primary amine added is within the range of 0.00/~l equivalent, preferably 0.0/~0.2 equivalent, based on the amide group of the N-vinylformamide polymer. is selected. The addition time may be before the basic hydrolysis of the polymer substantially starts, but after addition, the strong basic substance should be added as a hydrolysis catalyst after being held at 1o-to℃ for 10-200 minutes. is preferred.
強塩基性物質としてはアルカリ金属の水酸化物、アルカ
リ土類金属の水酸化物、第≠級アンモニウムヒドロキシ
ドなどが挙げられるが、特に水酸化ナトリウムおよび水
酸化カリウムが好ましい。これらの強塩基性物質は通常
、!重量%程度ないし飽和濃度の範囲の水溶液としてN
−ビニルホルムアミド重合体711[、N−ビニルホル
ムアミド重合体含水固型物あるいはN −ビニルホルム
アミド重合体を分散させた分散媒に添加され、コQ〜i
oo℃、好ましくは50〜100℃で加水分解反応が実
施される。強塩基性物質の使用量は、通常、目的とする
加水分解率を得るために加水分解すべきアミド基に対し
て/〜3倍当景であり、to%以下の加水分解率を得る
場合には/ −/、に倍当童が適当である。本発明にお
いては、強塩基性物質の使用量を主とする条件を適宜調
整することによシ、任意の加水分解率の水溶性ポリビニ
ルアミンを得ることができる。また、所望により、塩基
性加水分解終了後、酸により中和して水溶性ポリビニル
アミン塩を得ることもできる。Examples of the strong basic substance include alkali metal hydroxides, alkaline earth metal hydroxides, and primary ammonium hydroxide, with sodium hydroxide and potassium hydroxide being particularly preferred. These strongly basic substances are usually! N as an aqueous solution in the range of weight % to saturation concentration.
- Vinylformamide polymer 711 [, N-vinylformamide polymer hydrated solid or N-vinylformamide polymer is added to the dispersion medium in which it is dispersed, and
The hydrolysis reaction is carried out at oo<0>C, preferably from 50 to 100[deg.]C. The amount of strong basic substance used is usually 3 times the amide group to be hydrolyzed in order to obtain the desired hydrolysis rate, and when obtaining a hydrolysis rate of to% or less,は/ −/, にだいだう is appropriate. In the present invention, water-soluble polyvinylamine having an arbitrary hydrolysis rate can be obtained by appropriately adjusting the conditions, mainly the amount of the strong basic substance used. Further, if desired, after the basic hydrolysis is completed, it can be neutralized with an acid to obtain a water-soluble polyvinylamine salt.
次に本発明を実施例により更に具体的に説明するが、本
発明はその要旨を逸脱しない限り以下の実施例に限定さ
れるものではない。Next, the present invention will be explained in more detail with reference to examples, but the present invention is not limited to the following examples unless it departs from the gist thereof.
比較例/〜コ 実施例/〜6
攪拌機、冷却管、温度計及び窒素導入管を備えた/lの
弘ツロセパラプルフラスコKN −(α−メトキシエチ
ル)ホルムアミドの熱分解により合成したN−ビニルホ
ルムアミド!Jjt、脱塩水tys、りVおよび10M
負−のλ、λ′−アゾビスー2−アミジノプロパン・コ
塩酸塩水溶液/、!1を導入し、窒素ガス気流下攪拌し
つつro’r、にて7時間重合した。生成物中に含有ス
るN−ビニルホルムアミド及びBl−(α−メトキシエ
チル)ホルムアミドは重合体の水溶液の重量に対し、そ
れぞれ、0.3 %および、0.1俤であった。重合体
をl規定食塩水中にo、i t/dtの濃度の溶液とな
し、オストワルドの粘度計を用いて25℃で測定した還
元粘度はηBT)10−4jlであった。得られた重合
体水溶液に脱塩水A&19を加えて撹拌し均一に希釈し
たのち重合体水溶液λ乙srを攪拌機、冷却管、及び温
度計を備えたよOwtlの3ソロフラスコに入れた。次
いで第1表に示す種類と量の添加物を加えコO℃にて3
0分攪拌後λoz量−の水酸化ナトリウム水溶液Jj
fを加え直ちに昇温し7r℃で7時間、加水分解を行っ
た。冷却後濃塙酸を用いて生成物のpHを7.OK調節
した。Comparative Examples/~Co Examples/~6 N-vinyl synthesized by thermal decomposition of KN-(α-methoxyethyl)formamide Formamide! Jjt, demineralized water tys, riV and 10M
Negative λ, λ'-azobis-2-amidinopropane cohydrochloride aqueous solution/,! 1 was introduced, and polymerization was carried out for 7 hours on a RO'R while stirring under a nitrogen gas stream. The amounts of N-vinylformamide and Bl-(α-methoxyethyl)formamide contained in the product were 0.3% and 0.1%, respectively, based on the weight of the aqueous polymer solution. The polymer was dissolved in normal saline at a concentration of o, it/dt, and the reduced viscosity measured at 25° C. using an Ostwald viscometer was ηBT) 10−4 jl. Desalinated water A & 19 was added to the obtained aqueous polymer solution, stirred and diluted uniformly, and then the aqueous polymer solution λotsr was placed in a 3-Solo flask equipped with a stirrer, a cooling tube, and a thermometer. Next, add the types and amounts of additives shown in Table 1 and heat at 0°C.
After stirring for 0 minutes, λoz amount of sodium hydroxide aqueous solution Jj
Immediately after adding f, the temperature was raised and hydrolysis was carried out at 7r°C for 7 hours. After cooling, the pH of the product was adjusted to 7. Adjusted to OK.
結果を第7表に示す。The results are shown in Table 7.
加水分解率はl/≠00規定のポリビニル硫酸カリウム
水溶液により生成物の水溶液をpHJの条件下トルイジ
ンブルーを指示薬として用いたコロイド滴定値より算出
した。The hydrolysis rate was calculated from the colloid titration value of an aqueous solution of the product using a polyvinyl potassium sulfate aqueous solution of normal l/≠00 under pHJ conditions using toluidine blue as an indicator.
*/) 水に不溶で塩酸により中和できない。*/) Insoluble in water and cannot be neutralized with hydrochloric acid.
*λ) アンモニア水を水酸化ナトリウム添加後に添加
した。*λ) Aqueous ammonia was added after adding sodium hydroxide.
*3) 加水分解反応時 増粘した。*3) Thickened during hydrolysis reaction.
本発明によれば、N−ビニルホルムアミドを重合して得
られるN−ビニルホルムアミド重合体を精製することな
く環基性加水分解して高分子量の水溶性ポリビニルアミ
ンを取得することが可卵であり、反応器の材質上問題の
ある強酸性条件下の加水分解を行なわずに高品質の水溶
性ポリビニルアミンが製造し得る。According to the present invention, it is possible to obtain a high molecular weight water-soluble polyvinylamine by cyclic hydrolysis without purifying an N-vinylformamide polymer obtained by polymerizing N-vinylformamide. High-quality water-soluble polyvinylamine can be produced without hydrolysis under strongly acidic conditions, which is problematic due to the material of the reactor.
出 願 人 三菱化成工業株式会社 代 理 人 弁理士 長谷用 −ほか/名Sender: Mitsubishi Chemical Industries, Ltd. Representative Patent Attorney Hase - Others/Names
Claims (1)
1級アミンまたは第2級アミンを添加したのち塩基性加
水分解することを特徴とする水溶性ポリビニルアミンの
製造方法。(1) A method for producing water-soluble polyvinylamine, which comprises adding ammonia, a primary amine or a secondary amine to an N-vinylformamide polymer, and then subjecting it to basic hydrolysis.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP24029884A JPS61118406A (en) | 1984-11-14 | 1984-11-14 | Production of water-soluble polyvinylamine |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP24029884A JPS61118406A (en) | 1984-11-14 | 1984-11-14 | Production of water-soluble polyvinylamine |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS61118406A true JPS61118406A (en) | 1986-06-05 |
JPH0535163B2 JPH0535163B2 (en) | 1993-05-25 |
Family
ID=17057385
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP24029884A Granted JPS61118406A (en) | 1984-11-14 | 1984-11-14 | Production of water-soluble polyvinylamine |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS61118406A (en) |
Cited By (14)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS636198A (en) * | 1986-06-20 | 1988-01-12 | 三菱化学株式会社 | Cationic paper strength enhancer |
DE3909004A1 (en) * | 1989-03-18 | 1990-09-27 | Basf Ag | USE OF NON-HYDROLYSED N-VINYLFORMAMIDE UNITS CONTAINING COPOLYMERS IN PAPER PRODUCTION |
WO1990011253A1 (en) * | 1989-03-18 | 1990-10-04 | Basf Aktiengesellschaft | Use of non-hydrolysed copolymers containing n-vinyl formamide units as flocculation and dehydrating agents |
US5119532A (en) * | 1990-03-30 | 1992-06-09 | Kabushiki Kaisha Toka-Rida-Denki-Seisakusho | Buckle apparatus |
US5324792A (en) * | 1993-03-25 | 1994-06-28 | Air Products And Chemicals, Inc. | Process for making amidine-containing polymers |
US5391710A (en) * | 1993-03-25 | 1995-02-21 | Air Products And Chemicals, Inc. | Production of amine functional polymers having improved purity |
US5436299A (en) * | 1994-12-20 | 1995-07-25 | Air Products And Chemicals, Inc. | Decarbonylation of N-vinylformamide copolymers |
US5491199A (en) * | 1995-02-22 | 1996-02-13 | Air Products And Chemicals, Inc. | One step production of low salt vinylamine polymers |
US5681912A (en) * | 1993-11-12 | 1997-10-28 | Betzdearborn Inc. | Water-soluble cationic copolymers and their use as flocculants and drainage retention aids |
JPH11315116A (en) * | 1998-03-09 | 1999-11-16 | Natl Starch & Chem Investment Holding Corp | Production of polymer from n-vinyl formamide monomer |
WO2003102036A1 (en) * | 2002-05-31 | 2003-12-11 | Mitsubishi Chemical Corporation | Amine-functional copolymer and process for producing the same |
WO2010023799A1 (en) | 2008-09-01 | 2010-03-04 | ダイヤニトリックス株式会社 | Method for producing n-vinyl carboxylic acid amide polymer |
WO2010030372A2 (en) | 2008-09-12 | 2010-03-18 | Sekisui Specialty Chemicals America Llc | Improved nvf copolymer process |
WO2015068806A1 (en) | 2013-11-08 | 2015-05-14 | 三菱レイヨン株式会社 | Method for producing vinylamine (co)polymer |
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US6811839B2 (en) | 2000-11-09 | 2004-11-02 | Canon Kabushiki Kaisha | Recording medium and image forming process using the same |
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Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5823809A (en) * | 1981-07-18 | 1983-02-12 | バスフ・アクチエンゲゼルシヤフト | Linear basic polymer, manufacture and use |
-
1984
- 1984-11-14 JP JP24029884A patent/JPS61118406A/en active Granted
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5823809A (en) * | 1981-07-18 | 1983-02-12 | バスフ・アクチエンゲゼルシヤフト | Linear basic polymer, manufacture and use |
Cited By (20)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS636198A (en) * | 1986-06-20 | 1988-01-12 | 三菱化学株式会社 | Cationic paper strength enhancer |
DE3909004A1 (en) * | 1989-03-18 | 1990-09-27 | Basf Ag | USE OF NON-HYDROLYSED N-VINYLFORMAMIDE UNITS CONTAINING COPOLYMERS IN PAPER PRODUCTION |
WO1990011253A1 (en) * | 1989-03-18 | 1990-10-04 | Basf Aktiengesellschaft | Use of non-hydrolysed copolymers containing n-vinyl formamide units as flocculation and dehydrating agents |
US5225088A (en) * | 1989-03-18 | 1993-07-06 | Basf Aktiengesellschaft | Use of nonhydrolyzed copolymers containing n-vinylformamide units as flocculants and drainage aids |
US5119532A (en) * | 1990-03-30 | 1992-06-09 | Kabushiki Kaisha Toka-Rida-Denki-Seisakusho | Buckle apparatus |
US5324792A (en) * | 1993-03-25 | 1994-06-28 | Air Products And Chemicals, Inc. | Process for making amidine-containing polymers |
US5367035A (en) * | 1993-03-25 | 1994-11-22 | Air Products And Chemicals, Inc. | Poly(vinylammonium formate) and process for making the same |
US5391710A (en) * | 1993-03-25 | 1995-02-21 | Air Products And Chemicals, Inc. | Production of amine functional polymers having improved purity |
US5393842A (en) * | 1993-03-25 | 1995-02-28 | Air Products And Chemicals, Inc. | Poly(vinylammonium formate) |
US5401808A (en) * | 1993-03-25 | 1995-03-28 | Air Products And Chemicals, Inc. | Poly(vinylammonium formate) and process for making amidine-containing polymers |
US5681912A (en) * | 1993-11-12 | 1997-10-28 | Betzdearborn Inc. | Water-soluble cationic copolymers and their use as flocculants and drainage retention aids |
US5436299A (en) * | 1994-12-20 | 1995-07-25 | Air Products And Chemicals, Inc. | Decarbonylation of N-vinylformamide copolymers |
DE19606440A1 (en) * | 1995-02-22 | 1996-08-29 | Air Prod & Chem | One-step process for the production of low-salt vinylamine polymers |
US5491199A (en) * | 1995-02-22 | 1996-02-13 | Air Products And Chemicals, Inc. | One step production of low salt vinylamine polymers |
DE19606440C2 (en) * | 1995-02-22 | 2002-10-17 | Univ Pittsburgh Pittsburgh | One-step process for the production of low-salt vinylamine polymers |
JPH11315116A (en) * | 1998-03-09 | 1999-11-16 | Natl Starch & Chem Investment Holding Corp | Production of polymer from n-vinyl formamide monomer |
WO2003102036A1 (en) * | 2002-05-31 | 2003-12-11 | Mitsubishi Chemical Corporation | Amine-functional copolymer and process for producing the same |
WO2010023799A1 (en) | 2008-09-01 | 2010-03-04 | ダイヤニトリックス株式会社 | Method for producing n-vinyl carboxylic acid amide polymer |
WO2010030372A2 (en) | 2008-09-12 | 2010-03-18 | Sekisui Specialty Chemicals America Llc | Improved nvf copolymer process |
WO2015068806A1 (en) | 2013-11-08 | 2015-05-14 | 三菱レイヨン株式会社 | Method for producing vinylamine (co)polymer |
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JPH0535163B2 (en) | 1993-05-25 |
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