JPH04364173A - Production of isocyanuric acid - Google Patents

Production of isocyanuric acid

Info

Publication number
JPH04364173A
JPH04364173A JP30699990A JP30699990A JPH04364173A JP H04364173 A JPH04364173 A JP H04364173A JP 30699990 A JP30699990 A JP 30699990A JP 30699990 A JP30699990 A JP 30699990A JP H04364173 A JPH04364173 A JP H04364173A
Authority
JP
Japan
Prior art keywords
urea
alkali metallic
alkali metal
solvent
isocyanuric acid
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
JP30699990A
Other languages
Japanese (ja)
Other versions
JP2915132B2 (en
Inventor
Shinichi Kawahara
信一 河原
Takahiro Tejima
隆裕 手嶋
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.)
Tokuyama Corp
Original Assignee
Tokuyama Corp
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 Tokuyama Corp filed Critical Tokuyama Corp
Priority to JP30699990A priority Critical patent/JP2915132B2/en
Publication of JPH04364173A publication Critical patent/JPH04364173A/en
Application granted granted Critical
Publication of JP2915132B2 publication Critical patent/JP2915132B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Abstract

PURPOSE:To obtain the subject compound useful as an industrial intermediate raw material for germicides, resin modifying agents, crosslinking assistants, etc., in high yield by heating urea in the presence of an alkali metallic compound. CONSTITUTION:Urea is reacted in the presence of an alkali metallic hydride (e.g. lithium hydride), an alkali metallic amide (e.g. sodium amide) or an alkali metallic isocyanurate (e.g. monopotassium isocyanurate) in an organic solvent (e.g. tetraethylene glycol dimethyl ether) at 100-300 deg.C to afford the subject compound. The alkali metallic compound is used at (1/1) to (1/1000) molar ratio to the urea. Thereby, the reaction temperature can be reduced from that in conventional methods by >=50 deg.C and the energy cost can be reduced to prolong the longevity of the solvent.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は尿素を原料としてイソシアヌル酸(以下、CA
と略記する。)を製造する方法に関する。
DETAILED DESCRIPTION OF THE INVENTION [Industrial Application Field] The present invention provides isocyanuric acid (hereinafter referred to as CA) using urea as a raw material.
It is abbreviated as ).

〔従来の技術及び発明が解決しようとする課題〕CAは
工業的に有用な中間原料である。例えば、CAを塩素化
した塩化イソシアヌルは、粒状で簡便かつ活性が高いプ
ール殺菌剤として広く用いられており、又、アリル化し
たアリルイソシアヌレートは樹脂改質剤や架橋助剤とし
て好適に用いられている。
[Prior art and problems to be solved by the invention] CA is an industrially useful intermediate raw material. For example, isocyanuric chloride, which is obtained by chlorinating CA, is widely used as a granular, simple, and highly active pool disinfectant, and allyl isocyanurate, which is obtained by allylating it, is suitably used as a resin modifier and crosslinking agent. ing.

このような工業的に有用なCAは、一般に有機溶媒中で
尿素を加熱することにより製造される。
Such industrially useful CA is generally produced by heating urea in an organic solvent.

その反応を示せば下記式(1)のとおりである。The reaction is shown in the following formula (1).

しかし、アンモニアガス発生雰囲気下、高温で長時間溶
媒を加熱すると溶媒が一部劣化する。そこで溶媒の寿命
を長くするには反応温度を低下させることが好ましいが
、(1)式で示される反応を短時間で完全に進行させる
には200℃以上の温度が必要であるとされている。し
かし、温度を上げすぎると生成したCAがアンモニアと
反応し、却ってCAの収率が低下する。
However, when the solvent is heated at high temperature for a long time in an atmosphere where ammonia gas is generated, the solvent partially deteriorates. Therefore, in order to extend the life of the solvent, it is preferable to lower the reaction temperature, but it is said that a temperature of 200°C or higher is required to allow the reaction represented by equation (1) to proceed completely in a short time. . However, if the temperature is raised too much, the generated CA will react with ammonia, and the yield of CA will actually decrease.

〔課題を解決するための手段〕[Means to solve the problem]

そこで本発明者らは、上記の方法において反応温度を従
来より低下させる方法について鋭意研究した。その結果
、特定の化合物を共存させることにより反応温度を従来
より低くしても、CAが短時間でほぼ定量的に得られ、
かつCAとアンモニアとの反応もほとんど生じないこと
を見出し、本発明を完成した。
Therefore, the present inventors have conducted intensive research into a method for lowering the reaction temperature in the above method compared to the conventional method. As a result, even if the reaction temperature is lower than before by coexisting a specific compound, CA can be obtained almost quantitatively in a short time,
Furthermore, they found that almost no reaction occurs between CA and ammonia, and completed the present invention.

即ち、本発明は、尿素を有機溶媒中でアルカリ金属水素
化物、アルカリ金属アミド化物又はイソシアヌル酸のア
ルカリ金属塩(以下、これらを単にアルカリ金属化合物
ともいう。)の存在下に加熱することを特徴とするイソ
シアヌル酸の製造法である。
That is, the present invention is characterized in that urea is heated in an organic solvent in the presence of an alkali metal hydride, an alkali metal amide, or an alkali metal salt of isocyanuric acid (hereinafter also simply referred to as an alkali metal compound). This is a method for producing isocyanuric acid.

本発明において用いられる有機溶媒は、イソシアヌル酸
の製造反応温度、一般には100℃以上で液体であり、
アルカリ金属化合物の1種類もしくは2種類以上を溶解
させ、かつ、それ自身が反応しないものであれば公知の
ものが何ら制限されずに使用し得る。有機溶媒として好
適な化合物としては例えば、エチレングリコールジメチ
ルエーテル、ジエチレングリコールジメチルエーテル、
トリエチレングリコールジメチルエーテル、テトラエチ
レングリコールジメチルエーテルなどのポリエチレング
リコールジメチルエーテル類;2−メチルピロリドン、
2,4−ジメチルピロリドン、2,2,4−トリメチル
ピロリドン、2−シクロヘキシルピロリドン、2−シク
ロヘキシル−4−メチルピロリドン、2−シクロヘキシ
ル−4,4−ジメチルピロリドンなとのピロリドン誘導
体類;ジメチルスルホキシド、N,N−ジメチルホルム
アミドなどがある。
The organic solvent used in the present invention is liquid at the isocyanuric acid production reaction temperature, generally 100°C or higher,
Any known alkali metal compound can be used without any restriction as long as it dissolves one or more alkali metal compounds and does not react itself. Examples of compounds suitable as organic solvents include ethylene glycol dimethyl ether, diethylene glycol dimethyl ether,
Polyethylene glycol dimethyl ethers such as triethylene glycol dimethyl ether and tetraethylene glycol dimethyl ether; 2-methylpyrrolidone,
pyrrolidone derivatives such as 2,4-dimethylpyrrolidone, 2,2,4-trimethylpyrrolidone, 2-cyclohexylpyrrolidone, 2-cyclohexyl-4-methylpyrrolidone, 2-cyclohexyl-4,4-dimethylpyrrolidone; dimethylsulfoxide; Examples include N,N-dimethylformamide.

上記の有機溶媒の使用量は、特に制限されないが、得ら
れるCAの収率を勘案すると、尿素の濃度が1〜90重
量%の範囲となるように選ぶことが好ましい。
The amount of the organic solvent to be used is not particularly limited, but considering the yield of CA obtained, it is preferably selected so that the concentration of urea is in the range of 1 to 90% by weight.

次に、アルカリ金属水素化物は、水素化リチウム、水素
化ナトリウム、水素化カリウムが挙げられ、アルカリ金
属アミド化物は、リチウムアミド、ナトリウムアミド、
カリウムアミドが挙げられ、イソシアヌル酸のアルカリ
金属塩は、イソシアヌル酸のモノリチウム塩、ジリチウ
ム塩、トリリチウム塩、モノナトリウム塩、ジナトリウ
ム塩、トリナトリウム塩、モノカリウム塩、ジカリウム
塩、トリカリウム塩等が挙げられる。これらの中でもC
Aの収率を高くするためには、ナトリウム化合物を用い
ることが好ましい。
Next, examples of alkali metal hydrides include lithium hydride, sodium hydride, and potassium hydride, and examples of alkali metal amidides include lithium amide, sodium amide,
Alkali metal salts of isocyanuric acid include monolithium salt, dilithium salt, trilithium salt, monosodium salt, disodium salt, trisodium salt, monopotassium salt, dipotassium salt, tripotassium salt of isocyanuric acid. etc. Among these, C
In order to increase the yield of A, it is preferable to use a sodium compound.

これらのアルカリ金属化合物の使用量は、CAを高収率
で得るためには尿素に対してモル比で1/1〜1/10
00の範囲であることが好ましく、更には1/10〜1
/40であることがより好ましい。有機溶媒、尿素、及
びアルカリ金属化合物の導入順序は特に限定されない。
The amount of these alkali metal compounds to be used is 1/1 to 1/10 in molar ratio to urea in order to obtain CA in high yield.
The range is preferably 00, more preferably 1/10 to 1
/40 is more preferable. The order of introduction of the organic solvent, urea, and alkali metal compound is not particularly limited.

反応温度は、前記(1)式の反応を進行させて、且つ生
成するCAの分解を防止するためには好ましくは100
℃〜3000℃の範囲で、更に好ましくは150℃〜2
00℃である。反応時間は好ましくは10分間以上で、
更に好ましくは1時間以上である。
The reaction temperature is preferably 100 ℃ in order to advance the reaction of the above formula (1) and prevent the decomposition of the generated CA.
℃~3000℃, more preferably 150℃~2
It is 00℃. The reaction time is preferably 10 minutes or more,
More preferably, the time is 1 hour or more.

(効果) 本発明の方法によれば、従来法より反応温度を50℃以
上下げることができる。これにより、エネルギーコスト
を低減させることができ、また、溶媒の寿命を延ばすこ
とができる。
(Effects) According to the method of the present invention, the reaction temperature can be lowered by 50° C. or more compared to the conventional method. This can reduce energy costs and extend the life of the solvent.

(実施例) 実施例1 容量300mlの三っ口フラスコに溶媒としてテトラエ
チレングリコールジメチルエーテルを100g入れ、1
50℃に加熱し、攪拌しながら、尿素10g及び尿素に
対し1/40モル量の水素化ナトリウムを添加した。5
時間150℃で攪拌を続けた。
(Example) Example 1 Put 100g of tetraethylene glycol dimethyl ether as a solvent into a 300ml three-neck flask, and add 100g of tetraethylene glycol dimethyl ether as a solvent.
While heating to 50° C. and stirring, 10 g of urea and 1/40 molar amount of sodium hydride based on urea were added. 5
Stirring was continued at 150°C for an hour.

その後、室温まで冷却し生じた沈殿物を濾取した。Thereafter, the mixture was cooled to room temperature and the resulting precipitate was collected by filtration.

また、濾液から溶媒を留去すると固体が得られた。Further, a solid was obtained when the solvent was distilled off from the filtrate.

この沈殿物と濾液から得られた固体はそれぞれ6.10
g及び1.00gであった。元素分析、赤外線吸収スペ
クトル及び質量分析からどちらもCAと同定した。また
収率は両者あわせて99%であった。
The solids obtained from this precipitate and filtrate were each 6.10
g and 1.00 g. Both were identified as CA from elemental analysis, infrared absorption spectrum, and mass spectrometry. The total yield was 99%.

比較例1 水素化ナトリウムを加えないこと以外実施例1と同様に
反応を行った結果、沈殿物と濾液から得られた固体はそ
れぞれ3.50g及び4.55gであった。実施例1と
同様にしてこれらの分析を行った結果、尿素、ビウレッ
ト、トリウレットの混合物で、まったくCAは含まれて
いなかった。
Comparative Example 1 The reaction was carried out in the same manner as in Example 1 except that sodium hydride was not added. As a result, the solids obtained from the precipitate and the filtrate were 3.50 g and 4.55 g, respectively. These analyzes were carried out in the same manner as in Example 1, and the result was that it was a mixture of urea, biuret, and triuret, and contained no CA at all.

比較例2 水素化ナトリウムを用いず、温度を200℃にして反応
を行なったこと以外は実施例1と同様にして反応を行な
った。その結果、尿素の添加率は96%であり、CAの
選択率は99%であった。
Comparative Example 2 A reaction was carried out in the same manner as in Example 1, except that sodium hydride was not used and the reaction was carried out at a temperature of 200°C. As a result, the urea addition rate was 96% and the CA selectivity was 99%.

実施例2 溶媒に2−シクロヘキシルピロリドンを用いること以外
は実施例1と同様に反応を行なった。尿素の転化率は9
7%でCAの選択率は99%であった。
Example 2 The reaction was carried out in the same manner as in Example 1 except that 2-cyclohexylpyrrolidone was used as the solvent. The conversion rate of urea is 9
7% and the selectivity of CA was 99%.

実施例3 表1で示したアルカリ金属化合物を用いること以外は実
施例1と同様に反応を行なった。結果は表1の通りであ
った。
Example 3 The reaction was carried out in the same manner as in Example 1 except that the alkali metal compounds shown in Table 1 were used. The results are shown in Table 1.

Claims (1)

【特許請求の範囲】[Claims] 尿素を有機溶媒中でアルカリ金属水素化物、アルカリ金
属アミド化物又はイソシアヌル酸のアルカリ金属塩の存
在下に加熱することを特徴とするイソシアヌル酸の製造
法。
A method for producing isocyanuric acid, which comprises heating urea in an organic solvent in the presence of an alkali metal hydride, an alkali metal amide, or an alkali metal salt of isocyanuric acid.
JP30699990A 1990-11-15 1990-11-15 Method for producing isocyanuric acid Expired - Fee Related JP2915132B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP30699990A JP2915132B2 (en) 1990-11-15 1990-11-15 Method for producing isocyanuric acid

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP30699990A JP2915132B2 (en) 1990-11-15 1990-11-15 Method for producing isocyanuric acid

Publications (2)

Publication Number Publication Date
JPH04364173A true JPH04364173A (en) 1992-12-16
JP2915132B2 JP2915132B2 (en) 1999-07-05

Family

ID=17963798

Family Applications (1)

Application Number Title Priority Date Filing Date
JP30699990A Expired - Fee Related JP2915132B2 (en) 1990-11-15 1990-11-15 Method for producing isocyanuric acid

Country Status (1)

Country Link
JP (1) JP2915132B2 (en)

Also Published As

Publication number Publication date
JP2915132B2 (en) 1999-07-05

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