JP3460714B2 - Method for inhibiting thermal decomposition of cycloalkanone oxime - Google Patents

Method for inhibiting thermal decomposition of cycloalkanone oxime

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Publication number
JP3460714B2
JP3460714B2 JP2002011225A JP2002011225A JP3460714B2 JP 3460714 B2 JP3460714 B2 JP 3460714B2 JP 2002011225 A JP2002011225 A JP 2002011225A JP 2002011225 A JP2002011225 A JP 2002011225A JP 3460714 B2 JP3460714 B2 JP 3460714B2
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JP
Japan
Prior art keywords
oxime
thermal decomposition
cycloalkanone oxime
cycloalkanone
amount
Prior art date
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JP2002011225A
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Japanese (ja)
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JP2002234866A (en
Inventor
浩司 梶栗
勝 北村
保彦 東尾
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Sumitomo Chemical Co Ltd
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Sumitomo Chemical Co Ltd
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Description

【発明の詳細な説明】 【0001】 【産業上の利用分野】本発明は、シクロアルカノンオキ
シムの熱分解を抑制する方法に関する。 【0002】 【従来の技術及び発明が解決しようとする課題】シクロ
アルカノンオキシムを高温で使用する場合、例えば気化
して使用する際にシクロアルカノンオキシムの熱分解が
起こる。このため該シクロアルカノンオキシムがロスす
るという問題点や、さらにはこの熱分解生成物が続いて
実施される化学操作にとって有害となることもあり、熱
分解の抑制が課題となっていた。 【0003】シクロアルカノンオキシムの熱分解を抑制
する方法としては、例えばシクロヘキサノンオキシムの
気化帯域にアルカリ金属またはアルカリ土類金属の金属
自体あるいはその酸化物、水酸化物、アルコラートより
選ばれた一種以上を存在させる方法が提案されている
(特公昭47−41909号公報)。 【0004】しかしながら、該方法はシクロアルカノン
オキシムの熱分解を充分に抑制することができず満足し
得る方法ではなかった。 【0005】 【課題を解決するための手段】このような状況に鑑み、
本発明者らは、シクロアルカノンオキシムの熱安定性に
ついて種々検討した結果、特定の化合物を存在させるこ
とによってシクロアルカノンオキシムの熱分解を容易
に、しかも効率的に抑制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、下記一般式(1) NR123 (1) (式中、R1、R2 および3は、それぞれ水素原子また
低級アルキル基を表わす。)で示される化合物を、シ
クロアルカノンオキシムに対して0.1〜200モル%
存在させることを特徴とするシクロアルカノンオキシム
の熱分解抑制方法を提供するものである。 【0007】以下、本発明を詳細に説明する。本発明に
おけるシクロアルカノンオキシムは、特に限定されるも
のではないが、例えばシクロペンタノンオキシム、シク
ロヘキサノンオキシム、シクロヘプタノンオキシム、シ
クロオクタノンオキシム、シクロノナノンオキシム、シ
クロデカノンオキシム等の通常、炭素数5〜10のシク
ロアルカノンオキシムが挙げられる。 【0008】熱分解を抑制する化合物としては、下記
般式(1) NR123 (1) (式中、R1、R2 および3は、それぞれ水素原子また
低級アルキル基を表わす。)で示される化合物が用い
られる。 【0009】該具体化合物としては、例えばモノメチル
アミン、ジメチルアミン、トリメチルアミン、モノエチ
ルアミン、ジエチルアミン、トリエチルアミン、モノプ
ロピルアミン、ジプロピルアミン、トリプロピルアミ
ン、モノブチルアミン、ジブチルアミン、トリブチルア
ミン等の全炭素数1〜12の低級アルキルアミン類、ア
ンモニアが挙げられる。これらは単独で用いてもよい
し、混合して用いてもよい。 【0010】上記化合物の使用量は、シクロアルカノン
オキシムに対して、0.1〜200モル%である。 【0011】上記化合物を使用する態様は、特に限定さ
れるものではなく、例えばシクロアルカノンオキシムと
予め混合してもよいし、あるいは別々の系から導入して
もよい。また、これらの際にシクロアルカノンオキシム
をアルコール、ベンゼン、トルエン等の有機溶媒に溶解
して用いてもよい。 【0012】本発明は、シクロアルカノンオキシムを気
化して用いる場合に、とりわけ効果的に熱分解を抑制で
きる。シクロアルカノンオキシムの種類によっても異な
るが、気化帯域の温度は、例えば常圧の場合は通常16
0℃以上であり、また減圧の場合は常圧時より低い温度
でも可能である。 【0013】 【発明の効果】以上、記述したように本発明によれば、
上記特定の化合物を存在させることによってシクロアル
カノンオキシムの熱分解を容易に、しかも効率的に抑制
することができる。また、この特定の化合物は、回収す
ることによって再利用することができる。 【0014】 【実施例】次に本発明を実施例により具体的に説明する
が、本発明はこれら実施例に限定されるものではない。 【0015】実施例1 350℃に設定した電気炉に内径10mm、長さ40cmの
石英管を挿入し、該石英管にシクロヘキサノンオキシム
43.5重量%を含有するメタノール溶液を6.9g/
hrの割合で供給した。この際、キャリアガスとして5容
量%アンモニアを含有した窒素ガスを4.2l/hrの割
合で供給し、シクロヘキサノンオキシムを気化させた。
この時のアンモニア量は、シクロヘキサノンオキシムに
対して約35モル%であった。この操作を256時間継
続した後、シクロヘキサノンオキシム溶液の供給を停止
した。窒素ガス雰囲気下で冷却した後、石英管壁に付着
した炭素質物質の重量を測定したところ、26.6mgで
あった。 【0016】比較例1 実施例1における5容量%アンモニアを含有した窒素ガ
スの代わりに、キャリアガスとして窒素ガス4.2l/
hrを用いた以外は、実施例1と同様にしてシクロヘキサ
ノンオキシムを気化させた。窒素ガス雰囲気下で冷却し
た後、実施例1と同様に炭素質物質の重量を測定したと
ころ、225.5mgであった。 【0017】実施例2 内容積50mlのステンレス製密封容器にシクロヘキサノ
ンオキシム1g及び5.6重量%アンモニア水1滴
(0.03g)を加え窒素置換した後、180℃に設定
したオーブン中にて1時間加熱した。このときのアンモ
ニア量は、シクロヘキサノンオキシムに対して1モル%
であった。冷却した後、残存物をガスクロマトグラフに
よって測定したところ、シクロヘキサノンオキシム量は
仕込みに対して93重量%であった。 【0018】比較例2 実施例2におけるアンモニア水の代わりに、16.7重
量%水酸化カリウム水溶液1滴(0.03g)を加えた
以外は、実施例2と同様に行なった。このときの水酸化
カリウム量は、シクロヘキサノンオキシムに対して1モ
ル%であった。冷却した後、残存物をガスクロマトグラ
フによって測定したところ、シクロヘキサノンオキシム
量は仕込みに対して85重量%であった。 【0019】比較例3 実施例2においてアンモニア水を加えなかったこと以外
は、実施例2と同様に行なった。冷却した後、残存物を
ガスクロマトグラフによって測定したところ、シクロヘ
キサノンオキシム量は仕込みに対して82重量%であっ
た。 【0020】実施例3 実施例2におけるアンモニア水の代わりに、29.8重
量%のトリエチルアミン水溶液1滴(0.03g)を加
えた以外は、実施例2と同様に行なった。このときのト
リエチルアミン量は、シクロヘキサノンオキシムに対し
て1モル%であった。冷却した後、残存物をガスクロマ
トグラフによって測定したところ、シクロヘキサノンオ
キシム量は仕込みに対して92重量%であった。
Description: BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for suppressing the thermal decomposition of cycloalkanone oxime. [0002] When a cycloalkanone oxime is used at a high temperature, for example, when the cycloalkanone oxime is used after being vaporized, thermal decomposition of the cycloalkanone oxime occurs. For this reason, there is a problem that the cycloalkanone oxime is lost, and furthermore, the thermal decomposition product may be harmful to a chemical operation to be performed subsequently. [0003] As a method for suppressing the thermal decomposition of cycloalkanone oxime, for example, in the vaporization zone of cyclohexanone oxime, at least one metal selected from the group consisting of an alkali metal or an alkaline earth metal itself, and oxides, hydroxides, and alcoholates thereof. Has been proposed (Japanese Patent Publication No. 47-41909). However, this method cannot sufficiently suppress the thermal decomposition of cycloalkanone oxime, and is not a satisfactory method. [0005] In view of such a situation,
The present inventors have conducted various studies on the thermal stability of cycloalkanone oxime and found that thermal decomposition of cycloalkanone oxime can be easily and efficiently suppressed by the presence of a specific compound. Was completed. Namely, the present invention is represented by the following general formula (1) NR 1 R 2 R 3 (1) ( wherein, R 1, R 2 and R 3 are also each a hydrogen atom
It represents a lower alkyl group. The compound represented by), shea
0.1 to 200 mol% based on the chloralkanone oxime
An object of the present invention is to provide a method for suppressing thermal decomposition of cycloalkanone oxime, which is characterized in that it is present. Hereinafter, the present invention will be described in detail. The cycloalkanone oxime in the present invention is not particularly limited, for example, cyclopentanone oxime, cyclohexanone oxime, cycloheptanone oxime, cyclooctanone oxime, cyclononanone oxime, cyclodecanone oxime, etc. C5-10 cycloalkanone oxime is mentioned. [0008] As the compound which suppresses pyrolysis one <br/> general formula (1) NR 1 R 2 R 3 (1) ( wherein below, R 1, R 2 and R 3 are also each a hydrogen atom
It represents a lower alkyl group. ) Are used . The specific compounds include, for example, monomethylamine, dimethylamine, trimethylamine, monoethylamine, diethylamine, triethylamine, monopropylamine, dipropylamine, tripropylamine, monobutylamine, dibutylamine, tributylamine and the like. 1 to 12 lower alkylamines and ammonia. These may be used alone or as a mixture. The above compound is used in an amount of 0. 1 to cycloalkanone oxime. 1 to 200 mol%. The mode of using the above compound is not particularly limited. For example, it may be mixed with cycloalkanone oxime in advance or introduced from a separate system. In these cases, the cycloalkanone oxime may be used by dissolving it in an organic solvent such as alcohol, benzene or toluene. According to the present invention, when cycloalkanone oxime is used after being vaporized, thermal decomposition can be particularly effectively suppressed. Depending on the type of cycloalkanone oxime, the temperature of the vaporization zone is typically 16 at normal pressure.
It is 0 ° C. or higher, and in the case of reduced pressure, a lower temperature than at normal pressure is also possible. As described above, according to the present invention,
The thermal decomposition of cycloalkanone oxime can be easily and efficiently suppressed by the presence of the above specific compound. Also, this specific compound can be reused by being recovered. Next, the present invention will be described in detail with reference to examples, but the present invention is not limited to these examples. EXAMPLE 1 A quartz tube having an inner diameter of 10 mm and a length of 40 cm was inserted into an electric furnace set at 350 ° C., and 6.9 g / methanol solution containing 43.5% by weight of cyclohexanone oxime was inserted into the quartz tube.
Supplied at the rate of hr. At this time, as a carrier gas, a nitrogen gas containing 5% by volume of ammonia was supplied at a rate of 4.2 l / hr to vaporize cyclohexanone oxime.
At this time, the amount of ammonia was about 35 mol% based on cyclohexanone oxime. After continuing this operation for 256 hours, the supply of the cyclohexanone oxime solution was stopped. After cooling in a nitrogen gas atmosphere, the weight of the carbonaceous material attached to the quartz tube wall was measured and found to be 26.6 mg. Comparative Example 1 In place of the nitrogen gas containing 5% by volume of ammonia in Example 1, 4.2 l / nitrogen gas was used as a carrier gas.
Cyclohexanone oxime was vaporized in the same manner as in Example 1 except that hr was used. After cooling in a nitrogen gas atmosphere, the weight of the carbonaceous substance was measured in the same manner as in Example 1 and found to be 225.5 mg. Example 2 1 g of cyclohexanone oxime and 1 drop (0.03 g) of 5.6% by weight ammonia water were added to a stainless steel sealed container having an inner volume of 50 ml and the atmosphere was replaced with nitrogen, and the mixture was placed in an oven set at 180 ° C. Heated for hours. At this time, the amount of ammonia was 1 mol% with respect to cyclohexanone oxime.
Met. After cooling, the residue was measured by gas chromatography to find that the amount of cyclohexanone oxime was 93% by weight based on the charged amount. Comparative Example 2 The procedure of Example 2 was repeated, except that 1 drop (0.03 g) of a 16.7% by weight aqueous solution of potassium hydroxide was added instead of the aqueous ammonia. At this time, the amount of potassium hydroxide was 1 mol% based on cyclohexanone oxime. After cooling, the residue was measured by gas chromatography to find that the amount of cyclohexanone oxime was 85% by weight based on the charged amount. Comparative Example 3 The procedure of Example 2 was repeated, except that no aqueous ammonia was added. After cooling, the residue was measured by gas chromatography to find that the amount of cyclohexanone oxime was 82% by weight based on the charged amount. Example 3 The procedure of Example 2 was repeated, except that one drop (0.03 g) of a 29.8% by weight aqueous solution of triethylamine was added instead of the aqueous ammonia. At this time, the amount of triethylamine was 1 mol% based on cyclohexanone oxime. After cooling, the residue was measured by gas chromatography to find that the amount of cyclohexanone oxime was 92% by weight based on the charged amount.

───────────────────────────────────────────────────── フロントページの続き (56)参考文献 特開 平2−193957(JP,A) (58)調査した分野(Int.Cl.7,DB名) C07C 249/14 C07C 251/44 ──────────────────────────────────────────────────続 き Continuation of the front page (56) References JP-A-2-193957 (JP, A) (58) Fields investigated (Int. Cl. 7 , DB name) C07C 249/14 C07C 251/44

Claims (1)

(57)【特許請求の範囲】 【請求項1】下記一般式(1) NR123 (1) (式中、R1、R2およびR3は、それぞれ水素原子また
は低級アルキル基を表わす。)で示される化合物を、シ
クロアルカノンオキシムに対して0.1〜200モル%
存在させることを特徴とするシクロアルカノンオキシム
の熱分解抑制方法(ただし、シクロアルカノンオキシム
を硫酸アンモニウム水溶液で洗浄している間は除く)
(57) [Claims] [Claim 1] NR 1 R 2 R 3 (1) wherein R 1 , R 2 and R 3 are each a hydrogen atom or a lower alkyl group In the amount of 0.1 to 200 mol% based on cycloalkanone oxime.
A method for suppressing the thermal decomposition of cycloalkanone oxime, wherein cycloalkanone oxime is present.
Except during washing with an aqueous solution of ammonium sulfate) .
JP2002011225A 2002-01-21 2002-01-21 Method for inhibiting thermal decomposition of cycloalkanone oxime Expired - Fee Related JP3460714B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
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Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
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Related Parent Applications (1)

Application Number Title Priority Date Filing Date
JP00284092A Division JP3309413B2 (en) 1992-01-10 1992-01-10 Method for inhibiting thermal decomposition of cycloalkanone oxime

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JP3460714B2 true JP3460714B2 (en) 2003-10-27

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN114478309A (en) * 2022-02-24 2022-05-13 江苏扬农化工集团有限公司 Preparation method of cyclohexanone oxime steam and preparation method of caprolactam
CN114478310A (en) * 2022-02-24 2022-05-13 江苏扬农化工集团有限公司 Gasification method of cyclohexanone oxime and preparation method of caprolactam

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