JP2004155692A - Method for producing amino group-substituted 1,3,5-triazines - Google Patents

Method for producing amino group-substituted 1,3,5-triazines Download PDF

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JP2004155692A
JP2004155692A JP2002321966A JP2002321966A JP2004155692A JP 2004155692 A JP2004155692 A JP 2004155692A JP 2002321966 A JP2002321966 A JP 2002321966A JP 2002321966 A JP2002321966 A JP 2002321966A JP 2004155692 A JP2004155692 A JP 2004155692A
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amino group
substituted
triazine
amino
producing
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JP4412635B2 (en
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Sumio Manaka
純夫 間仲
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Nippon Soda Co Ltd
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Nippon Soda Co Ltd
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Abstract

<P>PROBLEM TO BE SOLVED: To provide a method for industrially producing a high-purity amino group-substituted 1,3,5-triazine compound in a high yield, with which water is used as a solvent. <P>SOLUTION: In the method for producing the amino group-substituted 1,3,5-triazine by replacing the chlorine atom of a cyanuric chloride with an amino group-containing compound, the method comprises a process for simultaneously adding a deacidifying agent and an amino group-containing compound to a water-containing solution of the cyanuric chloride and carrying out the substitution in the presence of an alkali metal halide. <P>COPYRIGHT: (C)2004,JPO

Description

【0001】
【発明の属する技術分野】
本発明は、反応性染料、蛍光増白剤、またはその中間体として有用なアミノ基置換1,3,5−トリアジン化合物の改良された製造方法に関する。
【0002】
【従来の技術】
塩化シアヌルとアミノ基含有化合物との縮合反応は、例えば、4,4’−ジアミノスチルベン−2,2’−ジスルホン酸またはその塩との反応の場合、通常、水溶媒中、またはアセトン等の有機溶媒−水溶媒中で、必要に応じて少量の非イオン性界面活性剤を共存させて微細に懸濁させた塩化シアヌルと、必要に応じて相間移動触媒存在下にアミノ基含有化合物と反応させ、反応にともなって生成する塩化水素を脱酸剤により中和し、弱酸性から弱アルカリ性で進行させることが有利であることが知られている。
また、脱酸剤としてはアルカリ金属の水酸化物、炭酸塩、酸性炭酸塩、りん酸塩、ホウ酸塩、ぎ酸塩、酢酸塩等、アルカリ土類金属もしくは亜鉛の酸化物、炭酸塩、りん酸塩、ホウ酸塩等、第3級アミン類及び尿素等をあげることができ、これらは塩化水素の生成後、または、場合により生成以前により共存させて用いられる。
置換反応の温度は、塩化シアヌルの第1塩素原子、第2塩素原子、および第3塩素原子について、それぞれ0〜15℃、20〜40℃、および70〜100℃の範囲であることが望ましいことが知られている。(特許文献1〜8を参照)
【0003】
【特許文献1】
特開昭49−32923号公報
【特許文献2】
特開昭47−39217号公報
【特許文献3】
特開昭48−7922号公報
【特許文献4】
特開昭56−2975号公報
【特許文献5】
特公昭45−772号公報
【特許文献6】
特公昭53−6170号公報
【特許文献7】
特開昭47−39210号公報
【特許文献8】
特開昭49−5126号公報
【0004】
【発明が解決しようとする課題】
しかしながら、脱酸剤をアミノ基含有化合物添加後に添加する方法では、スケールアップした場合に、反応系の粘度が増大し撹拌が困難となる結果、脱酸剤を添加した後、トリアジン官能基上の塩素原子等の置換基が部分的に加水分解するという問題があった。
また、脱酸剤を塩化シアヌル類と共存させてアミノ基含有化合物と反応させる方法は、塩化シアヌル類が加水分解しない様に有機溶媒を用いた2相系で反応を行う必要があり、有機溶媒を用いる必要があり、工業的には不利な点があった。
本発明は、水を溶媒として用いることのでき、収率および純度よく工業的にアミノ基置換1,3,5−トリアジン化合物を製造できる方法を提供することを目的とする。
【0005】
本発明者らは、上記課題を解決すべく鋭意検討した結果、アミノ基含有化合物と脱酸剤の塩化シアヌル類への添加方法を工夫することにより、また、粘度の上昇を抑える添加剤を探索することにより、上記課題を解決できることを見出し、本発明を完成するに至った。
【0006】
すなわち、本発明は、
(1)塩化シアヌル類の塩素原子をアミノ基含有化合物で置換し、アミノ基置換1,3,5−トリアジンを製造する方法において、塩化シアヌル類の水含有溶液に脱酸剤とアミノ基含有化合物を同時添加する工程を有することを特徴とするアミノ基置換1,3,5−トリアジンの製造方法に関し、
(2)塩化シアヌル類の水含有溶液に脱酸剤とアミノ基含有化合物を同時添加する工程において、pHを7以下に調整して行うことを特徴とする(1)に記載のアミノ基置換1,3,5−トリアジンの製造方法、
(3)塩素原子を置換するアミノ基の必要当量の40〜90%を予め塩化シアヌル類の水含有溶液に添加する工程を行った後、脱酸剤とアミノ基含有化合物を同時添加する工程を設けることを特徴とする(1)又は(2)に記載のアミノ基置換1,3,5−トリアジンの製造方法、
(4)塩化シアヌル類の水含有溶液が、塩化シアヌル類を界面活性剤存在下水溶媒中に分散させた懸濁溶液であることを特徴とする(1)〜(3)のいずれかに記載のアミノ基置換1,3,5−トリアジンの製造方法に関する。
【0007】
(5)水含有溶媒中、塩化シアヌル類の塩素原子を、アミノ基含有化合物及び脱酸剤と反応させてアミノ基置換1,3,5−トリアジンを製造する方法において、アルカリ金属ハロゲン化物存在下に行うことを特徴とするアミノ基置換1,3,5−トリアジンの製造方法に関し、
(6)脱酸剤が、アルカリ金属水酸化物であることを特徴とする(1)〜(5)のいずれかに記載のアミノ基置換1,3,5−トリアジンの製造方法に関する。
【0008】
【発明の実施の形態】
本発明に用いられる塩化シアヌル類とは、塩化シアヌル、または塩化シアヌルの塩素原子1個もしくは2個が置換された1,3,5−トリアジン化合物を表し、そのような置換基としては、メトキシ基、エトキシ基、n−プロポキシ基、イソプロポキシ基等のアルコキシ基、フェノキシ基、ナフチルオキシ基等のアリールオキシ基、メチルアミノ基、ジメチルアミノ基、エチルアミノ基、ジエチルアミノ基、アニリノ基等のN−置換アミノ基等を例示することができる。特に、脱酸剤により、加水分解を受けやすい置換基の場合に、本発明の方法を好適に用いることができる。
【0009】
本発明に用いられるアミノ基含有化合物とは、塩化シアヌル類の塩素原子と置換し得る1級、または2級のアミノ基を分子内に有する化合物であれば、特に限定されず、アミノ基の数も特に制限されない。具体的には、アニリン、1−アミノベンゼン−2,5−ジスルホン酸もしくはその塩、メタニル酸もしくはその塩、4,4’−ジアミノスチルベン−2,2’−ジスルホン酸またはその塩、スルファミン等を例示することができる。
【0010】
本発明の製造方法は、塩化シアヌル類の水含有溶液に脱酸剤とアミノ基含有化合物を同時添加する工程を有することを特徴とする。このような添加方法を用いることにより、反応系の粘度の上昇を抑えることができ、脱酸剤添加による反応系内のpH調整を容易に行うことができる。
塩化シアヌル類の水含有溶液は、具体的には、溶媒として、水、またはアセトン等の有機溶媒と水との混合系を用いた溶液を例示することができるが、工業的には有機溶媒を用いない系が望ましいことから、溶媒として水のみ用いるのが好ましい。水を溶媒として用いた場合に、より反応を円滑に行うため、界面活性剤を用いて塩化シアヌル類を微細に水中に分散させるのが好ましい。また、そのような界面活性剤として、非イオン系界面活性剤を例示することができる。
また、反応系のpHは、原料および、生成物の加水分解を防止するために、7以下、好ましくは6以下に調整するのが好ましい。
【0011】
用いられる脱酸剤として、具体的には、前述した公知の化合物を用いることができるが、工業的により安価な原料である水酸化ナトリウム、水酸化カリウム等のアルカリ金属水酸化物を、本発明の製造方法では用いることができ、工業的には有利である。
【0012】
同時に添加するとは、同時刻に添加する場合以外にも、相当の間隔をおかずに、両者を添加する操作を含むものとする。添加方法は、特に限定されるものではなく、例えば、滴下する方法、ポンプ等を持ちいて反応液中に導入する方法等を例示することができる。添加は、連続でも、相当の間隔おいて分割して添加する方法であっても構わない。いずれにしても、前述したように、反応系のpHを7以下、好ましくは6以下に制御して添加するのが好ましい。
【0013】
本発明の製造方法は、場合によって、上記した同時添加工程の前に、塩素原子を置換するアミノ基の必要当量の40〜90%を予め塩化シアヌル類の水含有溶液に添加する工程を設けるのが好ましい。特に、塩化シアヌルの第1塩素原子を置換した化合物を用いた場合には、本発明の方法を好適に用いることができる。この場合に、第2塩素原子の反応性が低下するため、予めアミノ基含有化合物のみを添加して反応させた後、脱酸剤およびアミノ基含有化合物を添加することにより、反応系のpHを7以下、好ましくは6以下に抑えることができ、脱酸剤による原料、生成物への影響を少なくすることができる。予め添加する量が、必要当量の40%以下では、脱酸剤の影響を抑えることができず、90%以上では、反応液の粘度が上昇し、同様に脱酸剤の影響を抑えることができない。
【0014】
また、反応温度は、特に、反応性の塩素原子を多く含む場合には、副反応を抑えるためになるべく低温にするのが好まし。しかし、塩素原子の反応性が低下している場合には、反応温度をある程度の高さに保つ必要があり、その場合に、本発明の製造方法を好適に用いることができる。
【0015】
また、本発明の製造方法は、反応系にアルカリ金属ハロゲン化物を共存させて行うことを特徴とする。アルカリ金属ハロゲン化物を共存させることにより、反応液の粘度を減少させることができ、添加する脱酸剤の影響を抑えることができる。用いるアルカリ金属ハロゲン化物として、具体的には、塩化ナトリウム、臭化ナトリウム、塩化カリウム、臭化カリウム等を例示することができる。用いる量は、特に限定されないが、塩化シアヌル類1gに対して、0.05〜0.3gの範囲、より好ましくは、0.1〜0.2gの範囲が好ましい。アルカリ金属ハロゲン化物は、アミノ基含有化合物と反応させる前に塩化シアヌル類と混合しても、またアミノ基含有化合物と混合して、もしくはアミノ基含有化合物と同時に塩化シアヌル類に添加して反応させてもよい。
【0016】
以下、本発明を実施例によりさらに詳細に説明するが、本発明は実施例に限定されるものではない。
【0017】
【実施例】
実施例1
塩化シアヌル(2,4,6−トリクロロ−1,3,5−トリアジン)300kgを0℃の水2600lに0.2kgの非イオン界面活性剤存在下に分散させて、0℃に冷却した。塩化ナトリウム40kgを加え、撹拌下、0℃〜10℃の範囲で、4,4’−ジアミノスチルベン−2,2’−ジスルホン酸ナトリウム塩(DAS)10.5重量%水溶液3089kgと3.9重量%水酸化ナトリウム水溶液を、反応液のpHが2〜3の範囲になる様に同時に滴下した。その後、反応液の温度を25℃に昇温すると共にpH4〜6の範囲になるように3.9重量%水酸化ナトリウム水溶液を滴下して調整し、同温度で1時間撹拌し、熟成を行った。用いた3.9重量%水酸化ナトリウム水溶液は、合計で1670kgであった。反応液の粘度上昇はみられず、十分に撹拌することができた。
反応液の一部を採取し、硫酸でpH2とした後、塩化ナトリウムを添加し、析出した結晶を濾過した後、各種スペクトルを測定し、4,4’−ビス((4,6−ジクロロ−1,3,5−トリアジン−2−イル)アミノ)スチルベン−2,2’−ジスルホン酸が、ほぼ定量的に生成していることを確認した。
【0018】
上記反応液に、水酸化ナトリウム水溶液を滴下してpHを8.5に調整し、液温を60℃まで昇温した。その後、15.5重量%水酸化ナトリウム水溶液380kg、スルファミン211.6kgを、同温度で、pHが5〜6の範囲になる様に、同時滴下し、さらに70℃に昇温して1時間撹拌した。滴下時、反応液粘度の上昇を見られず、撹拌を良好に行うことができた。
その後、ジエタノールアミン(純度80%)357kgを滴下し、次いで15.5重量%水酸化ナトリウム水溶液460gを滴下、100℃に昇温し3時間撹拌した。反応液のpHは7.5〜8.5の範囲であった。
反応液を熱時濾過して不溶物を除去した後、液温80℃で塩化ナトリウム625kgを加え、55℃まで冷却し、析出した結晶と上澄み液をデカンテーションで分離した。その後、さらに80℃まで加熱、50℃までの冷却、上澄みを除去する操作を2回繰り返すことで塩化ナトリウムを除去し、濾別、乾燥し、白色の結晶を780g得た。得られた結晶の各種スペクトルを測定したところ、4,4’−ビス((4−(ビスヒドロキシエチルアミノ)−6−(4−アミノスルホニルアニリノ)−1,3,5−トリアジン−2−イル)アミノ)スチルベン−2,2’−ジスルホン酸ジナトリウム塩であることがわかった。(収率90%)
【0019】
実施例2
2,4,−ジクロロ−6−メトキシ−1,3,5−トリアジン293kgを0℃の水2600lに0.2kgの非イオン界面活性剤存在下に分散させて、0℃に冷却した。塩化ナトリウム40kgを加え、撹拌下、0℃〜10℃の範囲で、DAS10.5重量%水溶液1545kgを滴下し、さらに、DAS10.5重量%1544kgと3.9重量%水酸化ナトリウム水溶液を、反応液のpHが4〜6の範囲、温度が10〜25℃の範囲になる様に同時に滴下した。その後、反応液の温度を60℃に昇温し、pH4〜6の範囲になるように3.9重量%水酸化ナトリウム水溶液を滴下して調整し、同温度で1時間撹拌し、熟成を行った。用いた3.9重量%水酸化ナトリウム水溶液は、合計で1670kgであった。反応液の粘度上昇はみられず、十分に撹拌することができた。
反応液の一部を採取し、硫酸でpH2とした後、塩化ナトリウムを添加し、析出した結晶を濾過した後、各種スペクトルを測定し、4,4’−ビス((4−クロロ−6−メトキシ−1,3,5−トリアジン−2−イル)アミノ)スチルベン−2,2’−ジスルホン酸が、ほぼ定量的に生成していることを確認した。
【0020】
【発明の効果】
以上述べたように、本発明の方法を用いることにより、反応液の粘度の上昇を抑えることができるので、用いる脱酸剤の影響による原料または生成物の加水分解等の副反応を抑えることができる。また、脱酸剤として従来、炭酸塩類はが用いられてきたが、反応中、発泡して反応槽の圧力が上昇するという問題があり、本発明の方法では、工業的により安価なアルカリ金属水酸化物を用いることができる。以上、本発明の方法は、蛍光増白剤また、その中間体として有用な2位アミノ基置換1,3,5−トリアジン類を、工業的に効率よく生産できる方法であり、その産業上の利用価値は高いといえる。
[0001]
TECHNICAL FIELD OF THE INVENTION
The present invention relates to an improved process for producing amino-substituted 1,3,5-triazine compounds useful as reactive dyes, optical brighteners or intermediates thereof.
[0002]
[Prior art]
The condensation reaction between cyanuric chloride and an amino group-containing compound is carried out, for example, in the case of a reaction with 4,4′-diaminostilbene-2,2′-disulfonic acid or a salt thereof, usually in an aqueous solvent or an organic solvent such as acetone. In a solvent-water solvent, a cyanuric chloride finely suspended in the presence of a small amount of a nonionic surfactant as necessary is reacted with an amino group-containing compound in the presence of a phase transfer catalyst as necessary. It is known that it is advantageous to neutralize hydrogen chloride produced by the reaction with a deoxidizing agent and to proceed from weakly acidic to weakly alkaline.
As the deoxidizing agent, hydroxides, carbonates, acid carbonates, phosphates, borates, formates, acetates, etc. of alkali metals, oxides and carbonates of alkaline earth metals or zinc, Examples include tertiary amines such as phosphates and borates, and urea, which are used after hydrogen chloride is produced or in some cases, before hydrogen chloride is produced.
The temperature of the substitution reaction is desirably in the range of 0 to 15 ° C, 20 to 40 ° C, and 70 to 100 ° C for the first chlorine atom, the second chlorine atom, and the third chlorine atom of cyanuric chloride, respectively. It has been known. (See Patent Documents 1 to 8)
[0003]
[Patent Document 1]
JP-A-49-32923 [Patent Document 2]
JP-A-47-39217 [Patent Document 3]
JP-A-48-7922 [Patent Document 4]
JP-A-56-2975 [Patent Document 5]
Japanese Patent Publication No. 45-772 [Patent Document 6]
JP-B-53-6170 [Patent Document 7]
JP-A-47-39210 [Patent Document 8]
JP-A-49-5126
[Problems to be solved by the invention]
However, in the method in which the deoxidizing agent is added after the addition of the amino group-containing compound, when the scale is increased, the viscosity of the reaction system increases and stirring becomes difficult. There is a problem that a substituent such as a chlorine atom is partially hydrolyzed.
In the method of reacting a deoxidizing agent with an amino group-containing compound in the presence of cyanuric chloride, it is necessary to carry out the reaction in a two-phase system using an organic solvent so that the cyanuric chloride is not hydrolyzed. To be used, which is industrially disadvantageous.
An object of the present invention is to provide a method in which water can be used as a solvent and an amino-substituted 1,3,5-triazine compound can be industrially produced with high yield and purity.
[0005]
Means for Solving the Problems The present inventors have conducted intensive studies to solve the above problems, and as a result, searched for an additive that suppresses an increase in viscosity by devising a method of adding an amino group-containing compound and a deoxidizing agent to cyanuric chlorides. As a result, they have found that the above problems can be solved, and have completed the present invention.
[0006]
That is, the present invention
(1) A method for producing an amino-substituted 1,3,5-triazine by substituting a chlorine atom of a cyanuric chloride with an amino group-containing compound, wherein a deoxidizer and an amino group-containing compound are added to a water-containing solution of the cyanuric chloride. A method for producing an amino-substituted 1,3,5-triazine characterized by having a step of simultaneously adding
(2) In the step of simultaneously adding a deoxidizing agent and an amino group-containing compound to a water-containing solution of cyanuric chlorides, the pH is adjusted to 7 or less, and the step is carried out. , 3,5-triazine production method,
(3) a step of adding 40 to 90% of a necessary equivalent of an amino group for substituting a chlorine atom to a water-containing solution of cyanuric chloride in advance, and then simultaneously adding a deoxidizing agent and an amino group-containing compound. The method for producing an amino-substituted 1,3,5-triazine according to (1) or (2), wherein
(4) The method according to any one of (1) to (3), wherein the water-containing solution of cyanuric chlorides is a suspension in which cyanuric chlorides are dispersed in an aqueous solvent in the presence of a surfactant. The present invention relates to a method for producing an amino-substituted 1,3,5-triazine.
[0007]
(5) A method for producing an amino-substituted 1,3,5-triazine by reacting a chlorine atom of cyanuric chloride with an amino group-containing compound and a deoxidizing agent in a water-containing solvent in the presence of an alkali metal halide A method for producing an amino-substituted 1,3,5-triazine characterized by performing
(6) The method for producing an amino-substituted 1,3,5-triazine according to any one of (1) to (5), wherein the deoxidizing agent is an alkali metal hydroxide.
[0008]
BEST MODE FOR CARRYING OUT THE INVENTION
The cyanuric chloride used in the present invention refers to cyanuric chloride or a 1,3,5-triazine compound in which one or two chlorine atoms of cyanuric chloride are substituted, and as such a substituent, a methoxy group An ethoxy group, an n-propoxy group, an alkoxy group such as an isopropoxy group, an aryloxy group such as a phenoxy group and a naphthyloxy group, a methylamino group, a dimethylamino group, an ethylamino group, a diethylamino group, and an N- group such as anilino group. Examples thereof include a substituted amino group. In particular, the method of the present invention can be suitably used for a substituent which is susceptible to hydrolysis by a deoxidizing agent.
[0009]
The amino group-containing compound used in the present invention is not particularly limited as long as it has a primary or secondary amino group capable of substituting for a chlorine atom of cyanuric chloride in the molecule. Is not particularly limited. Specifically, aniline, 1-aminobenzene-2,5-disulfonic acid or a salt thereof, metanilic acid or a salt thereof, 4,4′-diaminostilbene-2,2′-disulfonic acid or a salt thereof, sulfamine, etc. Examples can be given.
[0010]
The production method of the present invention is characterized by including a step of simultaneously adding a deoxidizing agent and an amino group-containing compound to a water-containing solution of cyanuric chlorides. By using such an addition method, an increase in the viscosity of the reaction system can be suppressed, and the pH in the reaction system can be easily adjusted by adding a deoxidizing agent.
As the water-containing solution of cyanuric chlorides, specifically, as a solvent, water or a solution using a mixed system of water and an organic solvent such as acetone can be exemplified. Since it is desirable to use a system that does not use water, it is preferable to use only water as the solvent. In the case where water is used as a solvent, it is preferable to disperse cyanuric chlorides finely in water by using a surfactant in order to perform the reaction more smoothly. Further, as such a surfactant, a nonionic surfactant can be exemplified.
The pH of the reaction system is preferably adjusted to 7 or less, and more preferably to 6 or less in order to prevent hydrolysis of the raw materials and products.
[0011]
As the deoxidizing agent to be used, specifically, the above-mentioned known compounds can be used. However, industrially inexpensive raw materials such as sodium hydroxide and alkali metal hydroxide such as potassium hydroxide are used in the present invention. Is industrially advantageous.
[0012]
Simultaneous addition shall include the operation of adding both without a considerable interval, other than the case of adding at the same time. The method of addition is not particularly limited, and examples thereof include a method of dropping and a method of introducing a reaction solution with a pump or the like. The addition may be continuous or may be a method of dividing and adding at considerable intervals. In any case, as described above, it is preferable to add the reaction system while controlling the pH of the reaction system to 7 or less, preferably 6 or less.
[0013]
The production method of the present invention may optionally include, before the above-mentioned simultaneous addition step, a step of adding 40 to 90% of a necessary equivalent of an amino group for substituting a chlorine atom to a water-containing solution of cyanuric chlorides in advance. Is preferred. In particular, when a compound obtained by substituting the first chlorine atom of cyanuric chloride is used, the method of the present invention can be suitably used. In this case, since the reactivity of the second chlorine atom is reduced, only the amino group-containing compound is added and reacted in advance, and then the deoxidizing agent and the amino group-containing compound are added to adjust the pH of the reaction system. It can be suppressed to 7 or less, preferably 6 or less, and the influence of the deoxidizing agent on the raw materials and products can be reduced. If the amount added in advance is 40% or less of the required equivalent, the effect of the deoxidizing agent cannot be suppressed, and if it is 90% or more, the viscosity of the reaction solution increases, and the effect of the deoxidizing agent can be similarly suppressed. Can not.
[0014]
The reaction temperature is preferably as low as possible to suppress side reactions, especially when a large amount of reactive chlorine atoms is contained. However, when the reactivity of chlorine atoms is low, it is necessary to maintain the reaction temperature at a certain level, and in that case, the production method of the present invention can be suitably used.
[0015]
Further, the production method of the present invention is characterized in that the reaction is carried out in the presence of an alkali metal halide in a reaction system. By coexisting the alkali metal halide, the viscosity of the reaction solution can be reduced, and the influence of the added deoxidizing agent can be suppressed. Specific examples of the alkali metal halide to be used include sodium chloride, sodium bromide, potassium chloride, potassium bromide and the like. The amount used is not particularly limited, but is preferably in the range of 0.05 to 0.3 g, more preferably in the range of 0.1 to 0.2 g, based on 1 g of cyanuric chloride. The alkali metal halide may be mixed with the cyanuric chloride before reacting with the amino group-containing compound, or mixed with the amino group-containing compound, or added to the cyanuric chloride at the same time as the amino group-containing compound and reacted. You may.
[0016]
Hereinafter, the present invention will be described in more detail with reference to examples, but the present invention is not limited to the examples.
[0017]
【Example】
Example 1
300 kg of cyanuric chloride (2,4,6-trichloro-1,3,5-triazine) was dispersed in 2600 l of water at 0 ° C in the presence of 0.2 kg of a nonionic surfactant, and cooled to 0 ° C. 40 kg of sodium chloride is added, and 3089 kg of a 10.5% by weight aqueous solution of sodium 4,4′-diaminostilbene-2,2′-disulfonate (DAS) and 3.9% by weight are added at 0 ° C. to 10 ° C. under stirring. % Sodium hydroxide aqueous solution was simultaneously added dropwise so that the pH of the reaction solution was in the range of 2-3. Thereafter, the temperature of the reaction solution was raised to 25 ° C. and a 3.9% by weight aqueous solution of sodium hydroxide was added dropwise so as to be in the range of pH 4 to 6, and the mixture was stirred at the same temperature for 1 hour to ripen. Was. The 3.9% by weight aqueous sodium hydroxide solution used was 1670 kg in total. There was no increase in the viscosity of the reaction solution, and sufficient stirring was possible.
A part of the reaction solution was collected, adjusted to pH 2 with sulfuric acid, sodium chloride was added, and the precipitated crystals were filtered. Various spectra were measured, and 4,4′-bis ((4,6-dichloro- It was confirmed that 1,3,5-triazin-2-yl) amino) stilbene-2,2′-disulfonic acid was almost quantitatively produced.
[0018]
An aqueous solution of sodium hydroxide was added dropwise to the reaction solution to adjust the pH to 8.5, and the temperature of the solution was raised to 60 ° C. Thereafter, 380 kg of a 15.5% by weight aqueous sodium hydroxide solution and 211.6 kg of sulfamine were simultaneously added dropwise at the same temperature so that the pH was in the range of 5 to 6, and the temperature was further raised to 70 ° C. and stirred for 1 hour. did. At the time of the dropwise addition, no increase in the viscosity of the reaction solution was observed, and the stirring was successfully performed.
Thereafter, 357 kg of diethanolamine (purity: 80%) was added dropwise, then 460 g of a 15.5% by weight aqueous sodium hydroxide solution was added dropwise, and the mixture was heated to 100 ° C. and stirred for 3 hours. The pH of the reaction solution was in the range of 7.5 to 8.5.
After the reaction solution was filtered while hot to remove insolubles, 625 kg of sodium chloride was added at a liquid temperature of 80 ° C., the mixture was cooled to 55 ° C., and the precipitated crystals and the supernatant were separated by decantation. Thereafter, the operation of further heating to 80 ° C, cooling to 50 ° C, and removing the supernatant was repeated twice to remove sodium chloride, separated by filtration, and dried to obtain 780 g of white crystals. When various spectra of the obtained crystals were measured, it was found that 4,4'-bis ((4- (bishydroxyethylamino) -6- (4-aminosulfonylanilino) -1,3,5-triazine-2- Yl) amino) stilbene-2,2'-disulfonate disodium salt. (Yield 90%)
[0019]
Example 2
293 kg of 2,4, -dichloro-6-methoxy-1,3,5-triazine were dispersed in 2600 l of water at 0 ° C in the presence of 0.2 kg of a nonionic surfactant and cooled to 0 ° C. 40 kg of sodium chloride was added, and 1545 kg of 10.5 wt% aqueous solution of DAS was added dropwise at 0 ° C. to 10 ° C. with stirring, and 1544 kg of DAS and 13.9 kg of 3.9 wt% sodium hydroxide solution were further reacted. The solution was simultaneously dropped so that the pH of the solution was in the range of 4 to 6 and the temperature was in the range of 10 to 25 ° C. Thereafter, the temperature of the reaction solution was raised to 60 ° C., and a 3.9% by weight aqueous solution of sodium hydroxide was added dropwise to adjust the pH to a range of 4 to 6, and the mixture was stirred at the same temperature for 1 hour to ripen. Was. The 3.9% by weight aqueous sodium hydroxide solution used was 1670 kg in total. There was no increase in the viscosity of the reaction solution, and sufficient stirring was possible.
A part of the reaction solution was collected, adjusted to pH 2 with sulfuric acid, sodium chloride was added, and the precipitated crystals were filtered. Various spectra were measured, and 4,4′-bis ((4-chloro-6- It was confirmed that methoxy-1,3,5-triazin-2-yl) amino) stilbene-2,2′-disulfonic acid was almost quantitatively produced.
[0020]
【The invention's effect】
As described above, by using the method of the present invention, an increase in the viscosity of the reaction solution can be suppressed, so that side reactions such as hydrolysis of raw materials or products due to the effect of the deoxidizing agent used can be suppressed. it can. Conventionally, carbonates have been used as a deoxidizing agent. However, during the reaction, there is a problem that foaming occurs and the pressure in the reaction tank rises. In the method of the present invention, industrially less expensive alkali metal water is used. An oxide can be used. As described above, the method of the present invention is a method for industrially and efficiently producing a fluorescent whitening agent and a 1,3,5-triazine substituted at the 2-position amino group, which is useful as an intermediate thereof. It can be said that the utility value is high.

Claims (6)

塩化シアヌル類の塩素原子をアミノ基含有化合物で置換し、アミノ基置換1,3,5−トリアジンを製造する方法において、塩化シアヌル類の水含有溶液に脱酸剤とアミノ基含有化合物を同時添加する工程を有することを特徴とするアミノ基置換1,3,5−トリアジンの製造方法。In a method for producing an amino-substituted 1,3,5-triazine by substituting a chlorine atom of cyanuric chloride with an amino group-containing compound, simultaneously adding a deoxidizing agent and an amino group-containing compound to a water-containing solution of cyanuric chloride. A process for producing an amino-substituted 1,3,5-triazine. 塩化シアヌル類の水含有溶液に脱酸剤とアミノ基含有化合物を同時添加する工程において、pHを7以下に調整して行うことを特徴とする請求項1に記載のアミノ基置換1,3,5−トリアジンの製造方法。The amino group-substituted 1,3 according to claim 1, wherein the pH is adjusted to 7 or less in the step of simultaneously adding the deoxidizing agent and the amino group-containing compound to the water-containing solution of cyanuric chlorides. A method for producing 5-triazine. 塩素原子を置換するアミノ基の必要当量の40〜90%を予め塩化シアヌル類の水含有溶液に添加する工程を行った後、脱酸剤とアミノ基含有化合物を同時添加する工程を設けることを特徴とする請求項1又は2に記載のアミノ基置換1,3,5−トリアジンの製造方法。A step of adding 40 to 90% of a necessary equivalent of the amino group for substituting a chlorine atom to a water-containing solution of cyanuric chlorides in advance, and then providing a step of simultaneously adding a deoxidizing agent and an amino group-containing compound. A method for producing an amino-substituted 1,3,5-triazine according to claim 1 or 2. 塩化シアヌル類の水含有溶液が、塩化シアヌル類を界面活性剤存在下水溶媒中に分散させた懸濁溶液であることを特徴とする請求項1〜3のいずれかに記載のアミノ基置換1,3,5−トリアジンの製造方法。The amino group-substituted 1, according to any one of claims 1 to 3, wherein the water-containing solution of cyanuric chlorides is a suspension in which cyanuric chlorides are dispersed in an aqueous solvent in the presence of a surfactant. A method for producing 3,5-triazine. 水含有溶媒中、塩化シアヌル類の塩素原子を、アミノ基含有化合物及び脱酸剤と反応させてアミノ基置換1,3,5−トリアジンを製造する方法において、アルカリ金属ハロゲン化物存在下に行うことを特徴とするアミノ基置換1,3,5−トリアジンの製造方法。In a method of producing an amino-substituted 1,3,5-triazine by reacting a chlorine atom of cyanuric chloride with an amino group-containing compound and a deoxidizing agent in a water-containing solvent, in the presence of an alkali metal halide A method for producing an amino-substituted 1,3,5-triazine characterized by the following. 脱酸剤が、アルカリ金属水酸化物であることを特徴とする請求項1〜5のいずれかに記載のアミノ基置換1,3,5−トリアジンの製造方法。The method for producing an amino-substituted 1,3,5-triazine according to any one of claims 1 to 5, wherein the deoxidizing agent is an alkali metal hydroxide.
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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2012062411A1 (en) * 2010-11-11 2012-05-18 Clariant International Ltd Non metal tanning
CN113549216A (en) * 2021-06-17 2021-10-26 山东迈特新材料科技有限公司 Preparation method of macromolecular triazine charring agent

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2012062411A1 (en) * 2010-11-11 2012-05-18 Clariant International Ltd Non metal tanning
AU2011328554B2 (en) * 2010-11-11 2016-10-06 Stahl International Bv Non metal tanning
CN113549216A (en) * 2021-06-17 2021-10-26 山东迈特新材料科技有限公司 Preparation method of macromolecular triazine charring agent

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