JPH08176081A - Production of n-alkoxymethyl(meth)acrylamide - Google Patents

Production of n-alkoxymethyl(meth)acrylamide

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Publication number
JPH08176081A
JPH08176081A JP33545194A JP33545194A JPH08176081A JP H08176081 A JPH08176081 A JP H08176081A JP 33545194 A JP33545194 A JP 33545194A JP 33545194 A JP33545194 A JP 33545194A JP H08176081 A JPH08176081 A JP H08176081A
Authority
JP
Japan
Prior art keywords
acrylamide
reaction
meth
formula
alkoxymethyl
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
Application number
JP33545194A
Other languages
Japanese (ja)
Other versions
JP3945833B2 (en
Inventor
Hirokazu Yamashita
博万 山下
Toshimori Tano
俊盛 田野
Akira Suzuki
亮 鈴木
Yozo Otsuka
要造 大塚
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Nitto Chemical Industry Co Ltd
Nitto Riken Kogyo Co Ltd
Original Assignee
Nitto Chemical Industry Co Ltd
Nitto Riken Kogyo Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Nitto Chemical Industry Co Ltd, Nitto Riken Kogyo Co Ltd filed Critical Nitto Chemical Industry Co Ltd
Priority to JP33545194A priority Critical patent/JP3945833B2/en
Publication of JPH08176081A publication Critical patent/JPH08176081A/en
Application granted granted Critical
Publication of JP3945833B2 publication Critical patent/JP3945833B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)

Abstract

PURPOSE: To obtain the subject compound with low polymer content, useful for e.g. resin modification, by reaction of N-methylol (meth)acrylamide with an alcohol in the presence of an acid catalyst under aeration to adjust the pH level of the reaction system followed by concentration at reduced pressures. CONSTITUTION: (A) An N-methylol (meth)acrylamide of formula CH2 =C(R1 ) CONHCH2 OH (R1 is H or methyl) or a reaction liquor containing the same is reacted with (B) an alcohol of formula R2 OH (R2 is a 1-3C lower alkyl) in the presence of an acid catalyst under aeration to adjust the pH level of the reaction liquor to >=5 but <8 followed by concentration under reduced pressure under aeration, thus affording (C) the objective N-alkoxymethyl (meth)acrylamide of formula CH2 =C(R1 )CONHCH2 OR2 . Preferably the pH level of the reaction liquor before pH adjustment is 2-5.

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、塗料、インキ、樹脂等
の分野で架橋性モノマーとして利用されているNーアル
コキシメチルアクリルアミドまたはNーアルコキシメチ
ルメタクリルアミド(以下、これらを単にNーアルコキ
シメチル(メタ)アクリルアミドという)の製造方法に
関するものである。
BACKGROUND OF THE INVENTION The present invention relates to N-alkoxymethyl acrylamide or N-alkoxymethyl methacrylamide (hereinafter simply referred to as N-alkoxymethyl) which is used as a crosslinkable monomer in the fields of paints, inks, resins and the like. (Meth) acrylamide).

【0002】[0002]

【従来の技術】Nーアルコキシメチル(メタ)アクリル
アミドは、アクリルアミドまたはメタクリルアミド(以
下、単にこれらを(メタ)アクリルアミドという)をホ
ルムアルデヒドと反応させてメチロール誘導体をつく
り、続いて酸触媒下にアルコールと反応させて製造する
方法が知られている(特公昭38ー23607号公
報)。しかし、(メタ)アクリルアミドおよびその誘導
体は、本来重合性であるため製造工程中の操作によって
はかなりの濃度で重合体を含有するNーアルコシメチル
(メタ)アクリルアミドを与えることがあり、他のモノ
マーや溶剤等と混合した場合、白濁ないし凝集を起こす
ため実用上困難をきたすことがある。例えば、重合体を
含むNーメトキシメチルアクリルアミド1に対しメタク
リル酸メチル3を混合すると白濁を生じ重合物が析出す
るため、このようなNーアルコキシメチル(メタ)アク
リルアミドは樹脂製造用として使用が困難である。一
方、粗Nーアルコキシメチル(メタ)アクリルアミドの
一般的精製法としてはフラッシュ蒸留のような経済的に
極めて不利で、かつその精製過程において更に重合体含
有量を増加させるような方法しか知られていない。
2. Description of the Related Art N-Alkoxymethyl (meth) acrylamide is a methylol derivative prepared by reacting acrylamide or methacrylamide (hereinafter simply referred to as (meth) acrylamide) with formaldehyde, and then reacting with alcohol under an acid catalyst. A method of reacting and producing is known (Japanese Patent Publication No. 38-23607). However, since (meth) acrylamide and its derivatives are inherently polymerizable, N-alkoxymethyl (meth) acrylamide containing a polymer may be provided in a considerable concentration depending on the operation in the manufacturing process, and other monomers or solvents may be used. When mixed with etc., white turbidity or aggregation may occur, which may cause practical difficulties. For example, when N-methoxymethyl acrylamide 1 containing a polymer is mixed with 3 methyl methacrylate, white turbidity occurs and a polymer is deposited. Therefore, such N-alkoxymethyl (meth) acrylamide is difficult to use for resin production. Is. On the other hand, as a general purification method of crude N-alkoxymethyl (meth) acrylamide, only a method such as flash distillation which is economically extremely disadvantageous and which further increases the polymer content in the purification process is known. Absent.

【0003】[0003]

【発明が解決しようとする課題】本発明の目的は、かか
る従来技術の欠点を改善し、精製操作を行うことなく、
樹脂や塗料等の改質成分として用いられた場合に沈澱、
白濁、ないし凝集をおこさない程度に含有重合体濃度の
低いNーアルコキシメチル(メタ)アクリルアミドを経
済的に製造する方法を提供することにある。本発明ら
は、上記の目的を達成すべく鋭意研究した結果、Nーメ
チロールアクリルアミドまたはNーメチロールメタクリ
ルアミド(以下、単にこれらをNーメチロール(メタ)
アクリルアミドという)とアルコールを酸触媒下、空気
を吹き込みながら反応させた後、反応液のPHを5以上
8未満に調整し、空気を吹き込みながら減圧で濃縮する
ことにより含有重合物濃度の低いNーアルコキシメチル
(メタ)アクリルアミドが得られることを見いだし本発
明に到達した。
The object of the present invention is to remedy the drawbacks of the prior art, without the need for purification operations.
Precipitation, when used as a modifying component for resins and paints,
An object of the present invention is to provide a method for economically producing N-alkoxymethyl (meth) acrylamide having a polymer concentration low enough to prevent clouding or aggregation. As a result of earnest studies to achieve the above object, the present inventors have found that N-methylol acrylamide or N-methylol methacrylamide (hereinafter simply referred to as N-methylol (meth)
(Acrylamide) and alcohol are reacted in the presence of an acid catalyst while blowing air, and then the pH of the reaction solution is adjusted to 5 or more and less than 8 and concentrated under reduced pressure while blowing air to reduce N-containing polymer concentration. The inventors have found that alkoxymethyl (meth) acrylamide can be obtained and have reached the present invention.

【0004】[0004]

【問題点を解決するための手段】すなわち、本発明は一
般式(I) CH2 =C(R1 )CONHCH2 OR2 (I) (式中、R1 は水素原子またはメチル基を示し、R2
炭素数1〜3の低級アルキル基を示す)で表されるN−
アルコキシメチル(メタ)アクリルアミドを製造する方
法において、一般式(II) CH2 =C(R1 )CONHCH2 OH (II) (式中、R1 は水素原子またはメチル基を示す)で表さ
れるNーメチロール(メタ)アクリルアミドまたはこれ
らを含有する反応液と一般式(III) R2 OH (III) (式中、R2 は炭素数1〜3の低級アルキル基を示す)
で表されるアルコールを酸触媒の存在下、空気を吹き込
みながら反応させた後、反応液のpHを5以上8未満に
調整し、空気を吹き込みながら減圧で濃縮することを特
徴とするNーアルコキシメチル(メタ)アクリルアミド
の製造方法に関する。
That is, the present invention relates to the general formula (I) CH 2 ═C (R 1 ) CONHCH 2 OR 2 (I) (wherein R 1 represents a hydrogen atom or a methyl group, R 2 represents a lower alkyl group having 1 to 3 carbon atoms)
In the method for producing alkoxymethyl (meth) acrylamide, it is represented by the general formula (II) CH 2 ═C (R 1 ) CONHCH 2 OH (II) (wherein R 1 represents a hydrogen atom or a methyl group). N-methylol (meth) acrylamide or a reaction solution containing them and the general formula (III) R 2 OH (III) (in the formula, R 2 represents a lower alkyl group having 1 to 3 carbon atoms)
N-alkoxy, characterized in that after reacting the alcohol represented by the formula in the presence of an acid catalyst while blowing air, the pH of the reaction liquid is adjusted to 5 or more and less than 8 and concentrated under reduced pressure while blowing air. The present invention relates to a method for producing methyl (meth) acrylamide.

【0005】本発明において使用する一般式(II)で表
されるNーメチロール(メタ)アクリルアミドはそれ自
体でもよく、また(メタ)アクリルアミドとホルムアル
デヒドによるメチロール化反応で生成した反応液でも良
い。後者の場合、反応条件は特に限定するものではな
く、Nーメチロール(メタ)アクリルアミドを含有する
反応生成液が得られる方法であれば良い。好ましい反応
条件の一例は、R.Dowbenko,R.M.Chr
istenson、A.N.Salem,J.Org.
Chem.,28,3458(1963)に記載されて
いる。
The N-methylol (meth) acrylamide represented by the general formula (II) used in the present invention may be itself or may be a reaction solution formed by a methylolation reaction of (meth) acrylamide and formaldehyde. In the latter case, the reaction conditions are not particularly limited, and any method can be used as long as a reaction product solution containing N-methylol (meth) acrylamide can be obtained. An example of preferable reaction conditions is described in R.W. Dowbenko, R .; M. Chr
istenson, A .; N. Salem, J.M. Org.
Chem. , 28, 3458 (1963).

【0006】エーテル化反応においては、Nーメチロー
ル(メタ)アクリルアミドに対してアルコールをモル比
で1以上、好ましくは1.5〜8、より好ましくは2.
2〜6.5の範囲で用いるのがよい。モル比が1未満で
は副生物を生じ易く、8を越えるとアルコールを多量に
使用することになり、経済性の点で好ましくない。エー
テル化反応に用いる一般式(III)で表されるアルコール
としては、メチルアルコール、エチルアルコール、ノル
マルプロピルアルコール、イソプロピルアルコール等の
炭素数1〜3の低級アルキル基を有するアルコールが挙
げられる。
In the etherification reaction, the molar ratio of alcohol to N-methylol (meth) acrylamide is 1 or more, preferably 1.5 to 8, more preferably 2.
It is preferable to use it in the range of 2 to 6.5. If the molar ratio is less than 1, by-products are likely to occur, and if it exceeds 8, a large amount of alcohol is used, which is not preferable in terms of economy. Examples of the alcohol represented by the general formula (III) used in the etherification reaction include alcohols having a lower alkyl group having 1 to 3 carbon atoms such as methyl alcohol, ethyl alcohol, normal propyl alcohol and isopropyl alcohol.

【0007】反応に使用する酸触媒としては、例えば硫
酸、燐酸、塩酸のような無機酸、シュウ酸、マロン酸、
コハク酸、フマル酸、マレイン酸、パラトルエンスルホ
ン酸のような有機酸のいずれでも良い。反応液はPHが
2〜5の範囲内にあるのが好ましい。
Examples of the acid catalyst used in the reaction include inorganic acids such as sulfuric acid, phosphoric acid and hydrochloric acid, oxalic acid, malonic acid,
Any of organic acids such as succinic acid, fumaric acid, maleic acid, and paratoluenesulfonic acid may be used. The reaction solution preferably has a pH in the range of 2-5.

【0008】エーテル化反応は通常還流加熱下に行われ
る。この反応は脱水を伴う平衡反応であるので、溶媒の
留去と共に水分も系外に除かれる場合は、残存するNー
メチロール(メタ)アクリルアミドを所望のNーアルコ
キシメチル(メタ)アクリルアミドへと転化させて、反
応収率を更に向上させることができる。具体的には反応
生成水を含むアルコールを系外に留出させるに際して、
無水アルコールもしくは別途分留して実質的に無水にし
たアルコールを系内に補給することによりその効果をあ
げることができる。
The etherification reaction is usually carried out under reflux heating. Since this reaction is an equilibrium reaction involving dehydration, when water is removed from the system as the solvent is distilled off, the remaining N-methylol (meth) acrylamide is converted to the desired N-alkoxymethyl (meth) acrylamide. Therefore, the reaction yield can be further improved. Specifically, when the alcohol containing the reaction product water is distilled out of the system,
The effect can be enhanced by replenishing the system with anhydrous alcohol or alcohol that has been separately fractionally distilled to be substantially anhydrous.

【0009】反応後、反応液のPHを5以上8未満、好
ましくは5.5〜7の範囲に調整し、濃縮を行う。濃縮
の際の温度は 50〜100℃、好ましくは55〜90℃
の範囲で行うのがよい。
After the reaction, the pH of the reaction solution is adjusted to 5 or more and less than 8, preferably 5.5 to 7, and concentrated. The temperature at the time of concentration is 50 to 100 ° C, preferably 55 to 90 ° C
It is good to do in the range of.

【0010】上記のエーテル化反応および濃縮工程にお
いては、積極的に空気を吹き込みながら行うことが必要
である。これによりエーテル化反応および濃縮工程にお
ける重合体の副生を抑制することができる。空気の吹き
込み量は、エーテル化反応においてはNーメチロール
(メタ)アクリルアミド1モル当り10〜400Nml
/hr、好ましくは15〜200Nml/hrの範囲、
また濃縮工程においては10〜4000Nml/hr、
好ましくは15〜2000Nml/hrの範囲で適宜選
択すればよい。更にハイドロキノンモノメチルエーテ
ル、ハイドロキノン等の従来から知られている重合禁止
剤を併用すると、より安定した結果が得られるが、重合
禁止剤のみの使用ではその効果は不十分である。
In the above etherification reaction and concentration step, it is necessary to positively blow air. As a result, by-products of the polymer in the etherification reaction and the concentration step can be suppressed. The amount of air blown is 10 to 400 Nml per mol of N-methylol (meth) acrylamide in the etherification reaction.
/ Hr, preferably in the range of 15 to 200 Nml / hr,
In the concentration step, 10 to 4000 Nml / hr,
Preferably, it may be appropriately selected within the range of 15 to 2000 Nml / hr. Further, when a conventionally known polymerization inhibitor such as hydroquinone monomethyl ether or hydroquinone is used in combination, more stable results are obtained, but the effect is insufficient when only the polymerization inhibitor is used.

【0011】かくして得られたNーアルコキシメチル
(メタ)アクリルアミドは、メタクリル酸メチルまたは
アセトンを加えても白濁ないし沈澱を生じることなく、
そのまま一般樹脂製造用等として好適に使用可能であ
る。
The N-alkoxymethyl (meth) acrylamide thus obtained does not cloud or precipitate even if methyl methacrylate or acetone is added,
It can be suitably used as it is for production of general resins.

【0012】[0012]

【実施例】以下、実施例および比較例により本発明を具
体的に説明する。なお、製品中の重合体濃度について
は、3倍量のメタクリル酸メチルまたは2倍量のアセト
ンを加えて白濁ないし沈澱を生じる状況を比較して評価
した。これらの条件下で0.1%以上の重合体を含むN
ーアルコキシメチル(メタ)アクリルアミドはその含有
量に応じた沈降物を生じる。
EXAMPLES The present invention will be specifically described below with reference to Examples and Comparative Examples. The concentration of the polymer in the product was evaluated by comparing the situation in which a 3-fold amount of methyl methacrylate or a 2-fold amount of acetone was added to cause clouding or precipitation. N containing 0.1% or more of polymer under these conditions
-Alkoxymethyl (meth) acrylamide produces a sediment depending on its content.

【0013】実施例1 撹拌装置、温度計、および(還流)凝縮器を備えた反応
槽に、86%パラホルムアルデヒド215g(6.16
モル)、アクリルアミド400g(5.63モル)、メ
チルアルコール170g(5.31モル)、ハイドロキ
ノンモノメチルエーテル1.74gおよびトリエチルア
ミン0.24gを加え、60℃で4時間加熱して得たN
ーメチロールアクリルアミドを含む反応液にメチルアル
コール960g(30モル)を追加し、シュウ酸約1g
の添加によりPH3.2に調整した後、60〜70℃、
約100Nml/hrの速度で空気を吹き込みながら還
流加熱した。5時間後反応液を水酸化ナトリウムでPH
6.3に調整し、約80℃、約7Nl/hrの速度で空
気を吹き込みながら減圧で濃縮し、メチルアルコールを
主成分とする留出液930gを回収し、純度98.8%
のNーメトキシメチルアクリルアミド、608gが得ら
れた。その一部をとり、3倍量のメタクリル酸メチルと
混合すると均一な透明溶液が得られ、溶媒添加により白
濁や沈澱の析出は見られなかった。
Example 1 215 g (6.16) of 86% paraformaldehyde was placed in a reaction vessel equipped with a stirrer, a thermometer, and a (reflux) condenser.
Mol), acrylamide 400 g (5.63 mol), methyl alcohol 170 g (5.31 mol), hydroquinone monomethyl ether 1.74 g and triethylamine 0.24 g, and heated at 60 ° C. for 4 hours to obtain N.
-Add 960 g (30 mol) of methyl alcohol to the reaction solution containing methylol acrylamide, and add about 1 g of oxalic acid.
After the pH is adjusted to 3.2 by the addition of 60 to 70 ° C,
The mixture was heated under reflux while blowing air at a rate of about 100 Nml / hr. After 5 hours, the reaction solution was pH adjusted with sodium hydroxide.
Adjusted to 6.3, concentrated under reduced pressure while blowing air at about 80 ° C. and about 7 Nl / hr, to recover 930 g of a distillate containing methyl alcohol as a main component, and a purity of 98.8%.
608 g of N-methoxymethyl acrylamide were obtained. A part of this was taken and mixed with 3 times the amount of methyl methacrylate to obtain a uniform transparent solution, and no cloudiness or precipitation was observed due to the addition of the solvent.

【0014】比較例1 実施例1において、Nーメチロールアクリルアミドを含
む反応液とメチルアルコールのPH3.2での反応およ
びPH6.3での減圧濃縮に際し、空気を吹き込む代わ
りに1.3gのハイドロキノンモノメチルエーテルを重
合禁止剤として追加した以外は実施例1と同様にして反
応を行ったところ、Nーメトキシメチルアクリルアミド
600gが得られた。このものの一部を取り3倍量のメ
タアクリル酸メチルと混合すると白濁し、その沈降物濃
度は0.5%であった。
Comparative Example 1 In Example 1, when the reaction solution containing N-methylolacrylamide and the reaction of methyl alcohol at PH 3.2 and the concentration under reduced pressure at PH 6.3 were performed, 1.3 g of hydroquinone monomethyl was used instead of blowing air. When the reaction was carried out in the same manner as in Example 1 except that ether was added as a polymerization inhibitor, 600 g of N-methoxymethylacrylamide was obtained. When a part of this was taken and mixed with 3 times the amount of methyl methacrylate, it became cloudy and the sediment concentration was 0.5%.

【0015】比較例2 実施例1において、Nーメチロールアクリルアミドを含
む反応液とメチルアルコールのPH3.2での反応およ
びPH6.3での減圧濃縮に際し、空気を吹き込む代わ
りに1.3gのハイドロキノンを重合禁止剤として追加
した以外は実施例1と同様にして反応を行ったところ、
Nーメトキシメチルアクリルアミド606gが得られ
た。、このものの一部を取り3倍量のメタクリル酸メチ
ルと混合すると白濁し、その沈降物濃度は約1%であっ
た。
Comparative Example 2 In Example 1, in the reaction of the reaction liquid containing N-methylolacrylamide and methyl alcohol at PH 3.2 and the concentration under reduced pressure at PH 6.3, 1.3 g of hydroquinone was added instead of blowing air. When the reaction was carried out in the same manner as in Example 1 except that a polymerization inhibitor was added,
606 g of N-methoxymethylacrylamide was obtained. When a part of this was taken and mixed with 3 times the amount of methyl methacrylate, it became cloudy and the sediment concentration was about 1%.

【0016】実施例2 Nーメチロールアクリルアミド(綜研化学社製、純度9
7.6%)1313g(12.7モル)、85.5%変
性エタノール2798g(52モル)およびハイドロキ
ノンモノメチルエーテル3.9gの混合物にシュウ酸約
7gを加えてPH2.6に調整し、85〜87℃、約6
00Nml/hrの速度で空気を吹き込みながら3.5
時間加熱した。留出液は系外に除き、代わりに合計59
6gの変性エタノールを系内に追加した。その後反応液
を水酸化ナトリウムでPH6.3に調整し、約80℃、
約20Nl/hrの速度で空気を吹き込みながら減圧で
濃縮し、純度97.6%のNーエトキシメチルアクリル
アミド、1562gが得られた。その一部をとり、3倍
量のメタクリル酸メチルと混合すると、均一な透明溶液
が得られた。
Example 2 N-methylol acrylamide (manufactured by Soken Chemical Industry Co., Ltd., purity 9)
7.6%) 1313 g (12.7 mol), 85.5% denatured ethanol 2798 g (52 mol) and hydroquinone monomethyl ether 3.9 g were added to the mixture of about 7 g of oxalic acid to adjust the pH to 2.6, 85-85%. 87 ° C, approx. 6
3.5 while blowing air at a speed of 00 Nml / hr
Heated for hours. The distillate was removed outside the system, and instead a total of 59
6 g of denatured ethanol was added to the system. After that, the reaction solution was adjusted to pH 6.3 with sodium hydroxide, about 80 ° C,
The mixture was concentrated under reduced pressure while blowing air at a rate of about 20 Nl / hr to obtain 1562 g of N-ethoxymethylacrylamide having a purity of 97.6%. A part of this was taken and mixed with 3 times the amount of methyl methacrylate to obtain a uniform transparent solution.

【0017】比較例3 実施例2において、Nーメチロールアクリルアミドを含
む反応液とエチルアルコールのPH2.6での反応および
PH6.3 での減圧濃縮に際し、空気を吹き込む代わりに
1.3gのハイドロキノンモノメチルエーテルを重合禁止
剤として追加した以外は実施例2と同様にして反応を行
ったところ、Nーエトキシメチルアクリルアミド153
8gが得られた。このものの一部を取り3倍量のメタク
リル酸メチルと混合すると白濁し、析出物含有濃度は
0.8%であった。
Comparative Example 3 In Example 2, in the reaction of the reaction solution containing N-methylolacrylamide with ethyl alcohol at PH 2.6 and concentration under reduced pressure at PH 6.3, 1.3 g of hydroquinone monomethyl was used instead of blowing air. A reaction was performed in the same manner as in Example 2 except that ether was added as a polymerization inhibitor, and N-ethoxymethylacrylamide 153
8 g was obtained. When a part of this was taken and mixed with 3 times the amount of methyl methacrylate, it became cloudy and the concentration of the precipitate was 0.8%.

【0018】実施例3 撹拌装置、温度計、および(還流)凝縮器を備えた反応
槽に、88%パラホルムアルデヒド 102.3g(3.0 モ
ル)、メタクリルアミド 255.3g(3.00モル)、水120
gおよびハイドロキノンモノメチルエーテル0.9 gを加
え、水酸化ナトリウムでPH12.6に調整したものを60℃
で 1時間加熱してNーメチロールメタクリルアミドを含
む反応液を得た。これにメチルアルコール 480g(15.0
モル)を加え、シュウ酸約 0.9gの添加によりPH3.2
に調整した後、70℃、約50Nml/hrの速度で空気
を吹き込みながら還流加熱した。3 時間後加熱を止め、
反応液を水酸化ナトリウムでpH 5に調整し、 65 ℃、
約5Nl/hrの速度で空気を吹き込みながら濃縮し
て、ほぼ純粋なNーメトキシメチルメタクリルアミド 3
64.7gが得られた。その一部をとり、2倍量のアセトン
と混合すると白濁ないし沈澱を生じず、透明な均一溶液
が得られた。
Example 3 In a reaction vessel equipped with a stirrer, a thermometer, and a (reflux) condenser, 102.3 g (3.0 mol) of 88% paraformaldehyde, 255.3 g (3.00 mol) of methacrylamide and 120% of water were added.
g and hydroquinone monomethyl ether 0.9 g were added and adjusted to pH 12.6 with sodium hydroxide at 60 ° C.
After heating for 1 hour, a reaction solution containing N-methylolmethacrylamide was obtained. Methyl alcohol 480g (15.0
Mol) and then add about 0.9 g of oxalic acid to obtain PH3.2.
Then, the mixture was heated under reflux at 70 ° C. while blowing air at a rate of about 50 Nml / hr. Stop heating after 3 hours,
Adjust the pH of the reaction solution to 5 with sodium hydroxide, and
Concentrate while blowing air at a rate of about 5 Nl / hr to give almost pure N-methoxymethylmethacrylamide 3
64.7 g were obtained. When a part of the solution was taken and mixed with twice the amount of acetone, cloudiness or precipitation did not occur, and a transparent homogeneous solution was obtained.

【0019】実施例4 撹拌装置、温度計、および凝縮器を備えた反応槽に、N
ーメチロールアクリルアミド303g(3.0モル)、
ノルマルプロピルアルコール450g(7.5モル)、
およびハイドロキノンモノメチルエーテル0.9gを仕
込み、シュウ酸を加えてでPH2,9に調整したものを
96〜108℃、約100Nml/hrの速度で空気を
吹き込みながら加熱した。留出液は系外に除き、代わり
に留出量に見合う新規ノルマルプロパノールを合計25
2g系内に追加した。8時間後加熱を止め、反応液を水
酸化ナトリウムでPH6.5に調整し、80〜90℃、
約5Nl/hrの速度で空気を吹き込みながら濃縮し
て、純度97.6%のNーノルマルプロポキシメチルア
クリルアミド414gが得られた。その一部をとり、3
倍量のメタクリル酸メチルと混合すると、均一な透明溶
液が得られ、アセトンとの溶状テストでも白濁ないし沈
澱を生じなかった。
Example 4 A reaction vessel equipped with a stirrer, a thermometer, and a condenser was charged with N 2
-Methylol acrylamide 303g (3.0mol),
450 g (7.5 mol) of normal propyl alcohol,
Then, 0.9 g of hydroquinone monomethyl ether was charged, and the product adjusted to PH2,9 by adding oxalic acid was heated at 96 to 108 ° C at a rate of about 100 Nml / hr while blowing air. The distillate was removed from the system and instead a total of 25 normal propanols corresponding to the amount of distillate were added.
Added to the 2 g system. After heating for 8 hours, the heating was stopped and the reaction solution was adjusted to pH 6.5 with sodium hydroxide.
The mixture was concentrated while blowing air at a rate of about 5 Nl / hr to obtain 414 g of N-normal propoxymethyl acrylamide having a purity of 97.6%. Take a part of it, 3
When mixed with a double amount of methyl methacrylate, a uniform transparent solution was obtained, and no cloudiness or precipitation occurred in the solubility test with acetone.

【0020】実施例5 撹拌装置、温度計、および(還流)凝縮器を備えた反応
槽に、88%パラホルムアルデヒド102g(3.0モ
ル)、アクリルアミド213g(3.0モル)、イソプ
ロピルアルコール180.7g(3.0モル)、ハイド
ロキノンモノメチルエーテル0.9gおよびトリエチル
アミン1.8gを加え、58〜61℃で4時間加熱して
得たNーメチロールアクリルアミドを含む反応液にイソ
プロピルアルコール270.5g(4.5モル)を追加
し、シュウ酸約3.7gの添加によりPH3.32に調
整した後、86〜89℃、約80Nml/hrの速度で
空気を吹き込みながら還流加熱した。16時間後反応液
を水酸化ナトリウムでPH6.3に調整し、約80℃、
約5Nl/hrの速度で空気を吹き込みながら減圧で濃
縮し、純度95.2% のNーイソプロポキシメチルアク
リルアミド、389.8gが得られた。その一部をと
り、3倍量のメタクリル酸メチルと混合すると均一な透
明溶液が得られた。
Example 5 In a reaction vessel equipped with a stirrer, a thermometer, and a (reflux) condenser, 102 g (3.0 mol) of 88% paraformaldehyde, 213 g (3.0 mol) of acrylamide, 180. 7 g (3.0 mol), hydroquinone monomethyl ether 0.9 g and triethylamine 1.8 g were added, and the reaction solution containing N-methylol acrylamide obtained by heating at 58 to 61 ° C. for 4 hours was added with isopropyl alcohol 270.5 g (4 0.5 mol) was added, and the pH was adjusted to 3.32 by adding about 3.7 g of oxalic acid, and then the mixture was heated under reflux at 86 to 89 ° C. while blowing air at a rate of about 80 Nml / hr. After 16 hours, the reaction solution was adjusted to pH 6.3 with sodium hydroxide and heated to about 80 ° C.
The mixture was concentrated under reduced pressure while blowing air at a rate of about 5 Nl / hr to obtain 389.8 g of N-isopropoxymethylacrylamide having a purity of 95.2%. A part thereof was taken and mixed with 3 times the amount of methyl methacrylate to obtain a uniform transparent solution.

【0021】比較例4 実施例5において、Nーメチロールアクリルアミドを含
む反応液とイソプロピルアルコールのPH3.32での
反応およびPH6.3での減圧濃縮に際し、空気を吹き
込む代わりに1.3gのハイドロキノンモノメチルエー
テルを重合禁止剤として追加した以外は実施例5と同様
にしてNーイソプロポキシメチルアクリルアミド382
gが得られた。このものの一部を取り3倍量のメタアク
リル酸メチルと混合すると白濁し、その沈降物体含有濃
度は0.5%であった。
Comparative Example 4 In Example 5, in the reaction of N-methylolacrylamide and the reaction of isopropyl alcohol with PH 3.32 and concentration under reduced pressure with PH 6.3, 1.3 g of hydroquinone monomethyl was used instead of blowing air. N-isopropoxymethylacrylamide 382 was prepared in the same manner as in Example 5 except that ether was added as a polymerization inhibitor.
g was obtained. When a part of this was taken and mixed with 3 times the amount of methyl methacrylate, it became cloudy and the concentration of the sedimented substance was 0.5%.

【0022】[0022]

【発明の効果】本発明の方法によれば、重合体の副生を
有効に抑制でき、樹脂改質等の用途に有用なNーアルコ
キシメチル(メタ)アクリルアミドを効果的に製造する
ことができる。
According to the method of the present invention, the by-product of the polymer can be effectively suppressed, and N-alkoxymethyl (meth) acrylamide useful for resin modification can be effectively produced. .

フロントページの続き (72)発明者 鈴木 亮 福島県いわき市常磐関船町宮下2番地ノ2 日東理研工業株式会社内 (72)発明者 大塚 要造 東京都千代田区丸の内1丁目5番1号 日 東化学工業株式会社内Front Page Continuation (72) Inventor Ryo Suzuki, 2 Miyanoshita No. 2 Miyashita, Joban-Sekisencho, Iwaki, Fukushima Prefecture Nitto RIKEN CORPORATION (72) Inventor Kazo Otsuka 1-5-1, Marunouchi, Chiyoda-ku, Tokyo Nitto Chemical Industry Co., Ltd.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 一般式(I) CH2 =C(R1 )CONHCH2 OR2 (I) (式中、R1 は水素原子またはメチル基を示し、R2
炭素数1〜3の低級アルキル基を示す)で表されるNー
アルコキシメチルアクリルアミドまたはN−アルコキシ
メチルメタクリルアミドを製造する方法において、一般
式(II) CH2 =C(R1 )CONHCH2 OH (II) (式中、R1 は水素原子またはメチル基を示す)で表さ
れるNーメチロールアクリルアミドまたはNーメチロー
ルメタクリルアミド、あるいはこれらのいずれかを含有
する反応液と一般式(III) R2 OH (III) (式中、R2 は炭素数1〜3の低級アルキル基を示す)
で表されるアルコールを酸触媒の存在下に空気を吹き込
みながら反応させた後、反応液のPHを5以上8未満に
調整し、空気を吹き込みながら減圧下で濃縮することを
特徴とするNーアルコキシメチルアクリルアミドまたは
Nーアルコキシメチルメタクリルアミドの製造方法。
1. General formula (I) CH 2 ═C (R 1 ) CONHCH 2 OR 2 (I) (In the formula, R 1 represents a hydrogen atom or a methyl group, and R 2 is a lower group having 1 to 3 carbon atoms. In the method for producing N-alkoxymethylacrylamide or N-alkoxymethylmethacrylamide represented by the formula (II), the formula (II) CH 2 ═C (R 1 ) CONHCH 2 OH (II) (wherein R 1 represents a hydrogen atom or a methyl group), N-methylol acrylamide or N-methylol methacrylamide, or a reaction solution containing any of these and a general formula (III) R 2 OH (III) (formula (Wherein R 2 represents a lower alkyl group having 1 to 3 carbon atoms)
After reacting the alcohol represented by the formula in the presence of an acid catalyst while blowing air, the pH of the reaction solution is adjusted to 5 or more and less than 8 and the mixture is concentrated under reduced pressure while blowing air. A method for producing alkoxymethyl acrylamide or N-alkoxymethyl methacrylamide.
JP33545194A 1994-12-22 1994-12-22 Method for producing N-alkoxymethyl (meth) acrylamide Expired - Lifetime JP3945833B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP33545194A JP3945833B2 (en) 1994-12-22 1994-12-22 Method for producing N-alkoxymethyl (meth) acrylamide

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP33545194A JP3945833B2 (en) 1994-12-22 1994-12-22 Method for producing N-alkoxymethyl (meth) acrylamide

Publications (2)

Publication Number Publication Date
JPH08176081A true JPH08176081A (en) 1996-07-09
JP3945833B2 JP3945833B2 (en) 2007-07-18

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Country Link
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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH08198833A (en) * 1995-01-30 1996-08-06 Dainippon Ink & Chem Inc Production of n-butoxymethyl (meth)acrylamides
JP2006063010A (en) * 2004-08-26 2006-03-09 Mitsui Chemicals Inc Method for preventing polymerization of 2,3-dihydroxypropyl-(meth)acrylamide
JP2007320964A (en) * 1994-09-16 2007-12-13 Mitsubishi Rayon Co Ltd Method for producing n-methylol acrylamide crystal
CN114315625A (en) * 2021-12-28 2022-04-12 徐州博康信息化学品有限公司 Preparation method of acid diffusion inhibitor

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007320964A (en) * 1994-09-16 2007-12-13 Mitsubishi Rayon Co Ltd Method for producing n-methylol acrylamide crystal
JP4678790B2 (en) * 1994-09-16 2011-04-27 三菱レイヨン株式会社 Method for producing N-methylolacrylamide crystals
JPH08198833A (en) * 1995-01-30 1996-08-06 Dainippon Ink & Chem Inc Production of n-butoxymethyl (meth)acrylamides
JP2006063010A (en) * 2004-08-26 2006-03-09 Mitsui Chemicals Inc Method for preventing polymerization of 2,3-dihydroxypropyl-(meth)acrylamide
CN114315625A (en) * 2021-12-28 2022-04-12 徐州博康信息化学品有限公司 Preparation method of acid diffusion inhibitor

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