JP3412158B2 - Method for producing 2-acrylamide-2-methylpropanesulfonic acid polymer - Google Patents

Method for producing 2-acrylamide-2-methylpropanesulfonic acid polymer

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Publication number
JP3412158B2
JP3412158B2 JP28884191A JP28884191A JP3412158B2 JP 3412158 B2 JP3412158 B2 JP 3412158B2 JP 28884191 A JP28884191 A JP 28884191A JP 28884191 A JP28884191 A JP 28884191A JP 3412158 B2 JP3412158 B2 JP 3412158B2
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JP
Japan
Prior art keywords
acid
acrylamido
methylpropanesulfonic acid
acrylamide
producing
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.)
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JP28884191A
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Japanese (ja)
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JPH05125037A (en
Inventor
光章 白神
賢治 森
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Dia Nitrix Co Ltd
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Dia Nitrix Co Ltd
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  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、高純度の2−アクリル
アミド−2−メチルプロパンスルホン酸であって、及び
それを効率よく製造する方法、さらにその高純度2−ア
クリルアミド−2−メチルプロパンスルホン酸を用いた
重合体の製造方法に関する。
FIELD OF THE INVENTION The present invention is a highly pure 2-acrylamido-2-methylpropanesulfonic acid, and
A method for producing it efficiently, and its high purity 2-
The present invention relates to a method for producing a polymer using crylamide-2-methylpropanesulfonic acid .

【0002】[0002]

【従来の技術】2−アクリルアミド−2−メチルプロパ
ンスルホン酸は、アクリル繊維等の染色性改良剤として
用いられるほか、重合により有用な単独重合体及び共重
合体を形成する。これらの重合体は、凝集剤、石油回収
用薬剤、分散剤、接着剤、流動性調節剤等として使用さ
れる。かかる2−アクリルアミド−2−メチルプロパン
スルホン酸の一般的な製造方法としては、過剰のアクリ
ロニトリルを反応溶媒を兼ねて用い、その中で発煙硫酸
とイソブチレンを反応させ、その結果得られた2−アク
リルアミド−2−メチルプロパンスルホン酸を反応混合
物より直接析出させる方法がある。得られた粗結晶はア
クリロニトリルで洗浄後乾燥されるが、必要により溶媒
を用い懸濁洗浄または再結晶により精製される。しかし
ながら、再結晶用として、工業的に利用しうる2−アク
リルアミド−2−メチルプロパンスルホン酸に対し溶解
度の高い溶媒は、水、低級アルコール、ジメチルホルム
アミド等に限定されており、従来、これらの溶媒を用い
た場合、以下のような問題点があった。
2. Description of the Related Art 2-Acrylamido-2-methylpropa
In addition to being used as a dyeability improver for acrylic fibers, etc., sulfonic acid forms useful homopolymers and copolymers by polymerization. These polymers are used as a flocculant, a petroleum recovery agent, a dispersant, an adhesive, a fluidity modifier, and the like. Such 2-acrylamido-2-methylpropane
The general production method of sulphonic acid, with an excess of acrylonitrile also as a reaction solvent, is reacted with fuming sulfuric acid and isobutylene therein, the resulting 2- Accession
There is a method of directly precipitating rillamido-2-methylpropanesulfonic acid from the reaction mixture. The obtained crude crystals are washed with acrylonitrile and then dried, and if necessary, purified by suspension washing or recrystallization using a solvent. However, it is a 2-ac which can be industrially used for recrystallization.
Solvents having a high solubility in rylamido-2-methylpropanesulfonic acid are limited to water, lower alcohols, dimethylformamide and the like, and conventionally, when these solvents were used, there were the following problems.

【0003】すなわち、水は2−アクリルアミド−2−
メチルプロパンスルホン酸に対する溶解度が最も高い
が、重合を起こしやすく不適当である。また、ジメチル
ホルムアミドでは2−アクリルアミド−2−メチルプロ
パンスルホン酸の結晶析出が容易でなく、沸点が高いの
で乾燥に時間がかかる。更に、メタノール等の低級アル
コールでは、収率が悪く、また、精製効果も不充分であ
る。一方、含水率3〜80重量%の含水酢酸を溶媒とし
て再結晶する方法も知られている(特開昭54−106
427)。しかしながら、該含水酢酸への2−アクリル
アミド−2−メチルプロパンスルホン酸の溶解度は低
く、効率よく再結晶を行なうためにはなお不充分であ
る。
That is, water is 2-acrylamido-2-
It has the highest solubility in methyl propane sulfonic acid , but is not suitable because it easily causes polymerization. For dimethylformamide, 2-acrylamido-2-methylpro-
Crystallization of pansulfonic acid is not easy and the boiling point is high, so it takes a long time to dry. Furthermore, with lower alcohols such as methanol, the yield is poor and the purification effect is insufficient. On the other hand, a method of recrystallizing using water-containing acetic acid having a water content of 3 to 80% by weight as a solvent is also known (JP-A-54-106).
427). However, the 2-acryl to the hydrous acetic acid
The solubility of amido-2-methylpropanesulfonic acid is low and still insufficient for efficient recrystallization.

【0004】[0004]

【発明が解決しようとする課題】2−アクリルアミド−
2−メチルプロパンスルホン酸は前述のように種々の用
途が考えられるが、特に2−アクリルアミド−2−メチ
ルプロパンスルホン酸を重合体として凝集剤、石油回収
用薬剤等に用いる場合は、より高分子量の製品が要求さ
れる。しかしながら、十分に精製した2−アクリルアミ
ド−2−メチルプロパンスルホン酸を原料としない場合
は、かかる高分子量の重合体を得ることは困難である。
そこで、本発明の目的は、高純度の2−アクリルアミド
−2−メチルプロパンスルホン酸およびそれをより効
率よく製造する方法、並びにその高純度2−アクリルア
ミド−2−メチルプロパンスルホン酸を用いて高分子量
の重合体を製造する方法を提供することにある。
[Problems to be Solved by the Invention] 2-Acrylamide-
2-Methylpropanesulfonic acid can be used for various purposes as described above, but especially 2-acrylamide-2-methyl
When using rupropanesulfonic acid as a polymer for a flocculant, a petroleum recovery agent, etc., a higher molecular weight product is required. However, well-purified 2-acrylic acid
When do-2-methylpropanesulfonic acid is not used as a raw material, it is difficult to obtain such a high molecular weight polymer.
Therefore, an object of the present invention is to obtain high-purity 2-acrylamide.
2-methylpropanesulfonic acid and a method for producing more efficiently it, as well as high-purity 2-Akurirua that
It is an object of the present invention to provide a method for producing a high molecular weight polymer using mido-2-methylpropanesulfonic acid .

【課題を解決するための手段】本発明者等は、従来技術
の問題を解決し、高純度の2−アクリルアミド−2−メ
チルプロパンスルホン酸の結晶を効率よく得る安価な精
製方法として、最も溶解度の高い水を溶媒とした再結晶
精製法について鋭意検討した結果、特定の化合物の結晶
溶媒系への添加による顕著な効果を見い出し、本発明に
到達した。すなわち本発明は、粗2−アクリルアミド−
2−メチルプロパンスルホン酸をフェノール系化合物の
存在下、水を溶媒として再結晶することにより製造され
高純度2−アクリルアミド−2−メチルプロパンスル
ホン酸およびその製造方法、並びにその高純度2−ア
クリルアミド−2−メチルプロパンスルホン酸をアゾ系
重合開始剤の存在下で重合することを特徴とする重合体
の製造方法に関する。以下、本発明を詳細に説明する。
DISCLOSURE OF THE INVENTION The present inventors have solved the problems of the prior art and made it possible to obtain 2-acrylamido-2-methine of high purity.
As an inexpensive purification method for efficiently obtaining crystals of tylpropanesulfonic acid , as a result of diligent studies on a recrystallization purification method using water, which has the highest solubility, as a result, a remarkable effect by the addition of a specific compound to a crystal solvent system was confirmed. Found and arrived at the present invention. That is, the present invention is a crude 2-acrylamide-
Produced by recrystallizing 2-methylpropanesulfonic acid in the presence of a phenolic compound using water as a solvent.
High purity 2-acrylamido-2-methylpropane that
Acid, and a method for producing the same, and high-purity 2-A thereof
The present invention relates to a method for producing a polymer, which comprises polymerizing crylamide-2-methylpropanesulfonic acid in the presence of an azo-based polymerization initiator. Hereinafter, the present invention will be described in detail.

【0005】2−アクリルアミド−2−メチルプロパン
スルホン酸の製造方法は特に限定はないが、通常は、前
述のようにアクリロニトリル、イソブチレンおよび発煙
硫酸を用いて合成し、反応系から析出した沈殿物をアク
リロニトリルで洗浄乾燥した粗2−アクリルアミド−2
−メチルプロパンスルホン酸が用いられる。粗結晶の
−アクリルアミド−2−メチルプロパンスルホン酸は、
アクリルアミド、アクリル酸;メタクリル酸等の不純物
を通常3,000〜30,000ppm程度含有するも
のである。本発明に使用されるフェノール系化合物とし
ては、たとえば下記一般式[I]で示される化合物が用
いられる。該フェノール化合物の多くは一般的な重合禁
止剤として使用されるものである。
2-acrylamido-2-methylpropane
The method for producing the sulfonic acid is not particularly limited, but usually, as described above, it was synthesized using acrylonitrile, isobutylene and fuming sulfuric acid, and the precipitate precipitated from the reaction system was washed with acrylonitrile and dried to obtain crude 2-acrylamide-2.
-Methylpropanesulfonic acid is used. Crude crystal 2
-Acrylamido-2-methylpropanesulfonic acid is
It usually contains impurities such as acrylamide, acrylic acid and methacrylic acid in an amount of about 3,000 to 30,000 ppm. As the phenolic compound used in the present invention, for example, a compound represented by the following general formula [I] is used. Many of the phenol compounds are used as general polymerization inhibitors.

【0006】[0006]

【化1】 [Chemical 1]

【0007】(式中、R1〜R5は、水素原子、水酸基、
アルコキシ基、炭素数1〜5の直鎖もしくは分岐のアル
キル基、アリールアルキル基、または、アルキルもしく
は水酸基で置換されたアリールアルキル基を表す。ま
た、R1〜R5は、ヘテロ原子を含むアルキル基もしくは
アリール基、またはヘテロ原子で結合するアルキル基も
しくはアリール基でもよい。)かかるフェノール系化合
物としては、具体的には、ハイドロキノン、p−メトキ
シフェノール、p−ヒドロキシトルエン、2,5−ジ−
tert−ブチルハイドロキノン、2,5−ジ−ter
t−アルミハイドロキノン、2,2’−メチレンビス
(4−エチル−6−tert−ブチルフェノール)、
2,2’−メチレンビス(4−メチル−6−tert−
ブチルフェノール)、4,4’−ブチリデンビス(6−
tert−ブチル−3−メチルフェノール)、4,4’
−チオビス(6−tert−ブチル−3−メチルフェノ
ール)、1,1’−ビス(4−ヒドロキシフェノール)
シクロヘキサン、2,6−ジ−tert−ブチル−4−
メチルフェノール、モノまたはトリ(α−メチルベンジ
ル)フェノール、dl−α−トコフェロール、ブチルヒ
ドロキシルアニソール等が例示されるが、特にハイドロ
キノン、p−メトキシフェノール等の親水性のフェノー
ル系化合物が好ましい。
(In the formula, R 1 to R 5 are hydrogen atoms, hydroxyl groups,
It represents an alkoxy group, a linear or branched alkyl group having 1 to 5 carbon atoms, an arylalkyl group, or an arylalkyl group substituted with an alkyl group or a hydroxyl group. Further, R 1 to R 5 may be an alkyl group or an aryl group containing a hetero atom, or an alkyl group or an aryl group bound by a hetero atom. ) Specific examples of the phenolic compound include hydroquinone, p-methoxyphenol, p-hydroxytoluene, and 2,5-di-
tert-butyl hydroquinone, 2,5-di-ter
t-aluminum hydroquinone, 2,2'-methylenebis (4-ethyl-6-tert-butylphenol),
2,2'-methylenebis (4-methyl-6-tert-
Butylphenol), 4,4'-butylidene bis (6-
tert-butyl-3-methylphenol), 4,4 '
-Thiobis (6-tert-butyl-3-methylphenol), 1,1'-bis (4-hydroxyphenol)
Cyclohexane, 2,6-di-tert-butyl-4-
Examples thereof include methylphenol, mono- or tri (α-methylbenzyl) phenol, dl-α-tocopherol, butylhydroxylanisole, etc., and hydrophilic phenolic compounds such as hydroquinone and p-methoxyphenol are particularly preferable.

【0008】フェノール系化合物の添加量は、粗2−ア
クリルアミド−2−メチルプロパンスルホン酸に対し
て、通常0.002〜1.0重量%、好ましくは0.0
1〜0.5重量%である。該範囲により少ない場合は
−アクリルアミド−2−メチルプロパンスルホン酸の精
製操作中の重合抑制の効果が充分に期待できない。ま
た、該範囲を越える場合は、精製を行った2−アクリル
アミド−2−メチルプロパンスルホン酸中に残存するフ
ェノール系化合物により、精製2−アクリルアミド−2
−メチルプロパンスルホン酸を更に重合する際に重合阻
害を起こすおそれがあるので好ましくない。本発明に使
用される溶媒の水は、通常蒸留水、脱イオン水が好まし
いが、場合によりアクリロニトリルの飽和水溶液等の
−アクリルアミド−2−メチルプロパンスルホン酸の精
製を阻害しない程度の物質を含む水溶液を用いることも
可能である。すなわち、2−アクリルアミド−2−メチ
ルプロパンスルホン酸精製時にアクリロニトリルを反応
溶媒を兼ねて用い、その中で発煙硫酸とイソブチレンを
反応させて2−アクリルアミド−2−メチルプロパンス
ルホン酸の結晶スラリーを得て、フェノール系化合物と
水を加えて加温溶解後、上層のアクリロニトリル層を分
離し、下層の水溶液より再結晶させる方法も採用するこ
とができる。
The amount of the phenolic compound added is approximately 2-
It is usually 0.002 to 1.0% by weight, preferably 0.0 to 1.0, with respect to crylamide-2-methylpropanesulfonic acid .
It is 1 to 0.5% by weight. 2 if less than the range
-The effect of suppressing polymerization during the purification operation of acrylamido-2-methylpropanesulfonic acid cannot be expected sufficiently. If it exceeds the range, purified 2-acryl
Purified 2-acrylamido-2 by the phenolic compound remaining in amido-2-methylpropanesulfonic acid
-It is not preferable because it may cause polymerization inhibition when further polymerizing methylpropanesulfonic acid . Water of the solvent used in the present invention is usually distilled water, but deionized water is preferred, if appropriate, such as a saturated aqueous solution of acrylonitrile 2
-It is also possible to use an aqueous solution containing a substance that does not inhibit the purification of acrylamido-2-methylpropanesulfonic acid . That is, 2-acrylamido-2-methyi
Acrylonitrile also serves as a reaction solvent during the purification of propane sulfonic acid .
It is also possible to employ a method in which a crystal slurry of rufonic acid is obtained, the phenolic compound and water are added and dissolved by heating, and then the upper acrylonitrile layer is separated and recrystallized from the lower aqueous solution.

【0009】本発明による2−アクリルアミド−2−メ
チルプロパンスルホン酸の再結晶方法は、粗結晶の2−
アクリルアミド−2−メチルプロパンスルホン酸にフェ
ノール系化合物と水を加えて加温溶解し、その後、温度
を下げて再結晶させるものである。2−アクリルアミド
−2−メチルプロパンスルホン酸の溶解温度は、通常3
0〜90℃であるが、結晶効率、及びモノマーの安定
性、安全性等を考慮すると40〜60℃で溶解するのが
好ましい。また、結晶化温度は結晶収率を上げるため、
5〜20℃の低温が好ましい。再結晶の効率を更に上げ
るには、40〜60℃で粗2−アクリルアミド−2−メ
チルプロパンスルホン酸を溶解した後、系内を減圧にし
て水を蒸発、濃縮させ、水の気化熱を利用して冷却しな
がら結晶化し、次に5〜10℃の低温に保持して結晶化
を完結する方法が有利である。かくして得られた2−ア
クリルアミド−2−メチルプロパンスルホン酸の結晶
は、素早く濾過または遠心分離した後、乾燥される。こ
の結果、不純物が通常1000ppm以下好ましくは5
00ppm以下の高純度2−アクリルアミド−2−メチ
ルプロパンスルホン酸の結晶が得られる。
2-acrylamido-2-me according to the present invention
Recrystallization method of chill propanesulfonic acid, crude crystals of 2-
This is a method in which a phenolic compound and water are added to acrylamido-2-methylpropanesulfonic acid and dissolved by heating, and then the temperature is lowered to recrystallize. 2-acrylamide
The melting temperature of 2-methylpropanesulfonic acid is usually 3
The temperature is 0 to 90 ° C., but it is preferable to dissolve at 40 to 60 ° C. in consideration of crystallization efficiency, monomer stability, safety and the like. In addition, since the crystallization temperature increases the crystal yield,
A low temperature of 5-20 ° C is preferred. To further increase the efficiency of recrystallization, crude 2-acrylamido-2- meth at 40-60 ° C is used.
After dissolving chillpropanesulfonic acid , the pressure in the system is reduced to evaporate and concentrate water, and the crystallization is performed while cooling by utilizing the heat of vaporization of water, and then kept at a low temperature of 5 to 10 ° C for crystallization. The method of completing the above is advantageous. 2-A thus obtained
Crystals of crylamido-2-methylpropanesulfonic acid are dried by rapid filtration or centrifugation. As a result, impurities are usually 1000 ppm or less, preferably 5
High-purity 2-acrylamido-2- methy of 00 ppm or less
Crystals of rupropanesulfonic acid are obtained.

【0010】本発明の高純度2−アクリルアミド−2−
メチルプロパンスルホン酸は、単独重合またはアクリル
酸またはメタクリル酸およびそれらの誘導体、アクリル
アミド、メタクリルアミドおよびそれらの誘導体等と共
重合することができる。特に高分子量の重合体を得るた
めには、使用するラジカル重合開始剤はアゾ系の重合開
始剤が好ましい。例えば2,2’−アゾビス−(2−ア
ミジノプロパン)・2塩酸塩、アゾビス−(N,N−ジ
メチレンイソブチルアミジン)・2塩酸塩、4,4’−
アゾビス−(4−シアノ吉草酸)−2−ナトリウム等が
挙げられる。ラジカル重合開始剤の使用量は、単独重合
の場合は2−アクリルアミド−2−メチルプロパンスル
ホン酸、また共重合の場合は2−アクリルアミド−2−
メチルプロパンスルホン酸と他の共重合可能なモノマー
の混合物の重量に対して通常0.005〜5重量%、好
ましくは0.05〜0.5重量%である。重合温度は、
通常10〜150℃の範囲で目的の重合物の分子量に応
じて選択される。水溶液状で重合する場合、好ましい温
度は40〜80℃である。
High purity 2-acrylamido-2- of the present invention
Methyl propane sulfonic acid can be homopolymerized or copolymerized with acrylic acid or methacrylic acid and their derivatives, acrylamide, methacrylamide and their derivatives and the like. Particularly, in order to obtain a polymer having a high molecular weight, the radical polymerization initiator used is preferably an azo type polymerization initiator. For example, 2,2'-azobis- (2-amidinopropane) dihydrochloride, azobis- (N, N-dimethyleneisobutylamidine) dihydrochloride, 4,4'-
Azobis- (4-cyanovaleric acid) -2-sodium and the like can be mentioned. The amount of radical polymerization initiator used is 2-acrylamido-2-methylpropane sulfone in the case of homopolymerization.
Folic acid , or 2-acrylamide-2- in the case of copolymerization
The amount is usually 0.005 to 5% by weight, preferably 0.05 to 0.5% by weight, based on the weight of the mixture of methylpropanesulfonic acid and another copolymerizable monomer. The polymerization temperature is
It is usually selected in the range of 10 to 150 ° C. according to the molecular weight of the desired polymer. When polymerizing in the form of an aqueous solution, the preferred temperature is 40 to 80 ° C.

【0011】重合方法は、特に制限されないが、水溶液
重合を例示するならば撹拌下重合する方法、静置容器中
で断熱状態で重合する方法、シート状で除熱しつつ重合
する方法、油中水型エマルジョンまたは分散状態で重合
する方法が例示される。撹拌下重合する方法としては、
2−アクリルアミド−2−メチルプロパンスルホン酸
ナトリウム塩水溶液に窒素ガスを通じて酸素を除いたの
ち、ラジカル重合開始剤を添加し、窒素ガス気流下、所
定温度に保持する方法が例示される。
The polymerization method is not particularly limited, but if an aqueous solution polymerization is exemplified, a method of polymerization with stirring, a method of polymerization in an adiabatic state in a stationary container, a method of polymerization while removing heat in a sheet form, water-in-oil A method of polymerizing in a type emulsion or dispersion state is exemplified. As a method of polymerizing with stirring,
An example is a method in which oxygen is removed from an aqueous solution of a sodium salt of 2-acrylamido-2-methylpropanesulfonic acid through nitrogen gas, then a radical polymerization initiator is added, and the mixture is maintained at a predetermined temperature under a nitrogen gas stream.

【0012】[0012]

【実施例】以下、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超えない限り、以下の実
施例に限定されるものではない。 (粗2−アクリルアミド−2−メチルプロパンスルホン
の製造例) 撹拌器、温度計、ガス吹込管を備えた反応器にアクリロ
ニトリル100モル部、発煙硫酸22モル部を仕込み−
40℃に保持した。そこへ20モル部のイソブチレンを
20分かけて吹きこんだ。この間反応器内の温度を−4
5〜−35℃に保持した。吹込み終了後、反応液の温度
を55℃まで昇温し、更に60分間保持して反応を完結
させた。イソブチレンの吹き込み終了と同時に2−アク
リルアミド−2−メチルプロパンスルホン酸の結晶が析
出し始め、スラリー状となった。この結晶を濾過し、ア
クリロニトリルで洗浄後30℃の減圧乾燥器で8時間乾
燥し、2−アクリルアミド−2−メチルプロパンスルホ
ン酸粗結晶を得た。
EXAMPLES The present invention will be described in more detail below with reference to examples, but the present invention is not limited to the following examples unless it exceeds the gist thereof. (Crude 2-acrylamido-2-methylpropane sulfone
Example of production of acid ) 100 mol parts of acrylonitrile and 22 mol parts of fuming sulfuric acid were charged in a reactor equipped with a stirrer, a thermometer, and a gas blowing tube.
Hold at 40 ° C. 20 mol parts of isobutylene was blown thereinto over 20 minutes. During this time, the temperature in the reactor was set to -4
Hold at 5--35 ° C. After the completion of blowing, the temperature of the reaction solution was raised to 55 ° C. and kept for 60 minutes to complete the reaction. At the same time as the blowing of isobutylene ends, 2-act
Crystals of lylamido-2-methylpropanesulfonic acid began to precipitate, and a slurry was formed. The crystals were filtered, washed with acrylonitrile and dried in a vacuum dryer at 30 ° C. for 8 hours to give 2-acrylamido-2-methylpropanesulfone.
Crude acid crystals were obtained.

【0013】この2−アクリルアミド−2−メチルプロ
パンスルホン酸粗結晶を、高速液体クロマトグラフィー
(以下HPLCと略す)で分析したところ、2−アクリ
ルアミド−2−メチルプロパンスルホン酸以外の不純物
(アクリルアミド、アクリル酸、メタクリル酸等)は、
8,300ppm含まれていた。 実施例1 撹拌器と冷却管、温度計を備えた300mlの四ッ口フ
ラスコに、前記製造例で得られた2−アクリルアミド−
2−メチルプロパンスルホン酸粗結晶150g、p−メ
トキシフェノール0.05g及び脱塩水100gを入
れ、40℃の温浴に浸して撹拌した。均一に溶解した
後、冷却管を取り外し、キャピラリーを取り付けた。抜
き出し側に冷却管、トラップを取り付け、5mmHgで
減圧脱水しながら約50gの水を留去した時点で浴を外
し、内部の沸騰が納まった後で常圧に戻した。次に、5
℃の恒温槽に浸して結晶化を完結させた。次に、結晶を
含む液をとりだし、グラスフィルターで減圧濾過し、5
℃の冷水50mlで2回洗浄した後、更に35℃で8時
間減圧乾燥を行い、103gの精製2−アクリルアミド
−2−メチルプロパンスルホン酸結晶を得た。
This 2-acrylamido-2-methylpro
Bread sulfonic acid crude crystal was analyzed by high performance liquid chromatography (hereinafter abbreviated as HPLC), 2-acrylate
Impurities other than luamido-2-methylpropanesulfonic acid (acrylamide, acrylic acid, methacrylic acid, etc.)
It contained 8,300 ppm. Example 1 In a 300 ml four-necked flask equipped with a stirrer, a cooling tube, and a thermometer, the 2-acrylamide- obtained in the above Production Example was placed.
150 g of 2-methylpropanesulfonic acid crude crystals, 0.05 g of p-methoxyphenol and 100 g of demineralized water were added, and the mixture was immersed in a warm bath at 40 ° C. and stirred. After uniformly dissolving, the cooling tube was removed and the capillary was attached. A cooling pipe and a trap were attached to the extraction side, and when about 50 g of water was distilled off while dehydrating under reduced pressure at 5 mmHg, the bath was removed, and after the boiling in the interior was stopped, the pressure was returned to normal pressure. Then 5
Crystallization was completed by immersing in a constant temperature bath at ℃. Next, the liquid containing the crystals was taken out and filtered under reduced pressure with a glass filter to obtain 5
After washing twice with 50 ml of cold water at ℃, it was further dried under reduced pressure at 35 ℃ for 8 hours, and 103 g of purified 2-acrylamide.
2-Methylpropanesulfonic acid crystals were obtained.

【0014】該結晶中の不純物量をHPLCで求めた結
果を表−1に示す。得られた精製2−アクリルアミド−
2−メチルプロパンスルホン酸結晶を、水溶液中で水酸
化ナトリウムで中和して30重量%の2−アクリルアミ
ド−2−メチルプロパンスルホン酸のナトリウム塩(以
2−アクリルアミド−2−メチルプロパンスルホン酸
−Naと略す)水溶液を調製した。この溶液9.06g
を50mlの封管に取り、更に、15.94gの30重
量%アクリルアミド水溶液および2.75gの脱塩水を
入れ、均一に溶解した。次に、重合開始剤として0.2
重量%のNN’−アゾビス−(2−アミジノプロパン)
・2塩酸塩水溶液2.25gを入れ、全量を30gとし
た。封管内を窒素ガスで充分に置換し、密封した後、5
0℃の恒温水槽中で4時間重合させたところ、25重量
%のアクリルアミド/2−アクリルアミド−2−メチル
プロパンスルホン酸−Naの共重合体を得た。このとき
の重合率を臭素法により測定した。また、該重合体を
0.1g/dlの濃度に溶解し、25℃でオストワルド
粘度計を用いて還元粘度(ηsp/c)を求めた。結果
を表−1に示す。
Table 1 shows the results of HPLC analysis of the amount of impurities in the crystals. Obtained purified 2-acrylamide-
The 2-methylpropanesulfonic acid crystals were neutralized with sodium hydroxide in an aqueous solution to give 30% by weight of 2-acrylic amine.
An aqueous solution of sodium salt of do-2-methylpropanesulfonic acid (hereinafter abbreviated as 2-acrylamido-2-methylpropanesulfonic acid- Na) was prepared. 9.06 g of this solution
Was taken in a 50 ml sealed tube, and 15.94 g of a 30 wt% acrylamide aqueous solution and 2.75 g of demineralized water were further added and uniformly dissolved. Next, 0.2 as a polymerization initiator
Wt% NN'-azobis- (2-amidinopropane)
-Adding 2.25 g of dihydrochloride aqueous solution, the total amount was 30 g. After thoroughly replacing the inside of the sealed tube with nitrogen gas and sealing it, 5
When polymerized in a constant temperature water bath of 0 ° C. for 4 hours, 25% by weight of acrylamide / 2-acrylamido-2-methyl
A propanesulfonic acid- Na copolymer was obtained. The polymerization rate at this time was measured by the bromine method. Further, the polymer was dissolved in a concentration of 0.1 g / dl, and the reduced viscosity (ηsp / c) was determined at 25 ° C. using an Ostwald viscometer. The results are shown in Table-1.

【0015】実施例2、3 フェノール系化合物として、p−メトキシフェノールの
代わりに表−1に示す化合物を0.05g用いた以外は
実施例1と同様に2−アクリルアミド−2−メチルプロ
パンスルホン酸の再結晶及び重合を行った。結果を表−
1に示す。 比較例1、2 フェノール系化合物の代わりに、重合禁止剤として一般
的に用いられる表−1に示す化合物を0.05g用いた
以外は実施例1と同様に2−アクリルアミド−2−メチ
ルプロパンスルホン酸の再結晶及び重合を行った。結果
を表−1に示す。 比較例3 再結晶精製を行うことなく、2−アクリルアミド−2−
メチルプロパンスルホン酸の粗結晶をそのまま使用して
実施例1と同様に重合した結果を表−1に示す。比較例4 実施例1において重合開始剤としてアゾ化合物の代わり
に過硫酸アンモニウムを用いた以外は同様に重合したと
ころ、重合率が99.6%、得られた重合体の還元粘度
は13.5であった。
Examples 2 and 3 2-acrylamido-2-methylpropanesulfonic acid was used in the same manner as in Example 1 except that 0.05 g of the compound shown in Table 1 was used instead of p-methoxyphenol as the phenol compound. Was recrystallized and polymerized. Table of results
Shown in 1. Comparative Examples 1 and 2 2-acrylamido-2-methylpropane sulfone was used in the same manner as in Example 1 except that 0.05 g of the compound shown in Table 1 which was generally used as a polymerization inhibitor was used in place of the phenol compound. The acid was recrystallized and polymerized. The results are shown in Table-1. Comparative Example 3 2-acrylamide-2-without purification by recrystallization
The results of polymerization in the same manner as in Example 1 using crude crystals of methylpropanesulfonic acid as they are are shown in Table 1. Comparative Example 4 Polymerization was conducted in the same manner as in Example 1 except that ammonium persulfate was used instead of the azo compound as a polymerization initiator. The polymerization rate was 99.6%, and the obtained polymer had a reduced viscosity of 13.5. there were.

【0016】[0016]

【表1】 [Table 1]

【0017】実施例4 撹拌器、冷却管及び、温度計を備えた300mlの四ッ
口フラスコに、2−アクリルアミド−2−メチルプロパ
ンスルホン酸粗結晶150g、p−メトキシフェノール
0.05gおよび脱塩水100gを入れ、40℃の温浴
に浸して撹拌した。2−アクリルアミド−2−メチルプ
ロパンスルホン酸の粗結晶が溶解した後、撹拌しながら
浴を10℃まで冷却し、更に撹拌を止めて5℃にすると
2−アクリルアミド−2−メチルプロパンスルホン酸
結晶が析出した。5℃で8時間保持した後、グラスフィ
ルターで減圧濾過した。次に、5℃の冷水50mlで2
回洗浄した後、更に、得られた結晶を35℃で8時間減
圧乾燥を行った。得られた結晶は50.6gであり、H
PLCで分析した不純物量は106ppmであった。ま
た、該結晶を用いて実施例1と同様に重合を行なったと
ころ、重合率は100%、重合体の還元粘度は26.7
であった。
Example 4 A 300 ml four-necked flask equipped with a stirrer, a condenser and a thermometer was charged with 2-acrylamido-2-methylpropanone.
The crude crystals of sulfonic acid ( 150 g), p-methoxyphenol (0.05 g) and demineralized water (100 g) were added, and the mixture was immersed in a warm bath at 40 ° C and stirred. 2-acrylamido-2-methyl
After the crude crystals of lopansulfonic acid were dissolved, cool the bath to 10 ° C with stirring and stop stirring at 5 ° C.
Crystals of 2-acrylamido-2-methylpropanesulfonic acid were precipitated. After holding at 5 ° C. for 8 hours, it was filtered under reduced pressure with a glass filter. Next, 2 with 50 ml of cold water at 5 ° C
After washing twice, the obtained crystals were further dried under reduced pressure at 35 ° C. for 8 hours. The obtained crystal weighs 50.6 g, and H
The amount of impurities analyzed by PLC was 106 ppm. Polymerization was carried out in the same manner as in Example 1 using the crystals, and the polymerization rate was 100% and the reduced viscosity of the polymer was 26.7.
Met.

【0018】比較例5 実施例4と同じフラスコに100gの10重量%含水酢
酸を入れ、40℃の温浴に浸し、そこに2−アクリルア
ミド−2−メチルプロパンスルホン酸粗結晶を少しづつ
加えて撹拌したが、溶解しにくかったので更に温浴の温
度を60℃とし、12gの2−アクリルアミド−2−メ
チルプロパンスルホン酸粗結晶を溶解させた。次に、実
施例4と同様に再結晶の操作を行ったが、得られた結晶
は6.6gにすぎず、結晶収率は極めて低く、また不純
物量も226ppmであった。
Comparative Example 5 100 g of 10% by weight hydrous acetic acid was placed in the same flask as in Example 4, immersed in a warm bath at 40 ° C., and 2-acrylamido-2-methylpropanesulfonic acid crude crystals were added little by little and stirred. However, since it was difficult to dissolve, the temperature of the warm bath was further set to 60 ° C., and 12 g of 2-acrylamido-2-methylpropanesulfonic acid crude crystal was dissolved. Next, a recrystallization operation was performed in the same manner as in Example 4, but the obtained crystals were only 6.6 g, the crystal yield was extremely low, and the amount of impurities was 226 ppm.

【0019】[0019]

【発明の効果】本発明の高純度2−アクリルアミド−2
−メチルプロパンスルホン酸の製造方法によれば、工業
的に安価な方法で、効率よく高純度の2−アクリルアミ
ド−2−メチルプロパンスルホン酸の結晶を得ることが
できるのみならず、該結晶を用いれば極めて高分子量の
(共)重合体を得ることができ、水溶性または親水性高
分子等の用途分野、例えば高分子凝集剤や石油回収用薬
剤に寄与するところが大である。
EFFECT OF THE INVENTION High-purity 2-acrylamide-2 of the present invention
- According to the manufacturing method of methylpropanesulfonic acid, at industrially inexpensive method efficiently high-purity 2-acrylamide
Not only crystals of do-2-methylpropanesulfonic acid can be obtained, but also extremely high molecular weight (co) polymers can be obtained by using the crystals, and the application fields of water-soluble or hydrophilic polymers, etc. For example, it largely contributes to a polymer flocculant and a petroleum recovery agent.

───────────────────────────────────────────────────── フロントページの続き (56)参考文献 特開 昭54−106427(JP,A) 特開 昭54−163524(JP,A) 特開 昭50−82010(JP,A) 特公 昭44−31328(JP,B1) (58)調査した分野(Int.Cl.7,DB名) C08F 20/00 C07C 303/00 C07C 309/00 CA(STN) REGISTRY(STN)─────────────────────────────────────────────────── ─── Continuation of the front page (56) Reference JP-A-54-106427 (JP, A) JP-A-54-163524 (JP, A) JP-A-50-82010 (JP, A) JP-B-44- 31328 (JP, B1) (58) Fields surveyed (Int.Cl. 7 , DB name) C08F 20/00 C07C 303/00 C07C 309/00 CA (STN) REGISTRY (STN)

Claims (3)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 粗2−アクリルアミド−2−メチルプロ
パンスルホン酸を、フェノール系化合物の存在下、水を
溶媒として再結晶してなる高純度2−アクリルアミド−
2−メチルプロパンスルホン酸を、アゾ系重合開始剤の
存在下で重合することを特徴とする2−アクリルアミド
−2−メチルプロパンスルホン酸重合体の製造方法。
1. Crude 2-acrylamido-2-methylpro
Pansulphonic acid, water in the presence of phenolic compounds
High-purity 2-acrylamide obtained by recrystallization as a solvent
2-methylpropanesulfonic acid is used as an azo polymerization initiator.
2-acrylamide characterized by polymerizing in the presence
A method for producing a 2-methylpropanesulfonic acid polymer.
【請求項2】 高純度2−アクリルアミド−2−メチル
プロパンスルホン酸の不純物が500ppm以下である
請求項1の2−アクリルアミド−2−メチルプロパンス
ルホン酸重合体の製造方法。
2. High-purity 2-acrylamido-2-methyl
Impurity of propanesulfonic acid is less than 500ppm
2-Acrylamido-2-methylpropanes according to claim 1.
Method for producing rufonic acid polymer.
【請求項3】 高純度2−アクリルアミド−2−メチル
プロパンスルホン酸を、アゾ系重合開始剤の存在下で水
溶液重合する請求項1又は2の2−アクリルアミド−2
−メチルプロパンスルホン酸重合体の製造方法。
3. High-purity 2-acrylamido-2-methyl
Propanesulfonic acid is treated with water in the presence of an azo polymerization initiator.
Solution polymerization, 2-acrylamido-2 according to claim 1 or 2.
-A method for producing a methylpropanesulfonic acid polymer.
JP28884191A 1991-11-05 1991-11-05 Method for producing 2-acrylamide-2-methylpropanesulfonic acid polymer Expired - Lifetime JP3412158B2 (en)

Priority Applications (1)

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JP28884191A JP3412158B2 (en) 1991-11-05 1991-11-05 Method for producing 2-acrylamide-2-methylpropanesulfonic acid polymer

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JP3412158B2 true JP3412158B2 (en) 2003-06-03

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