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JPS6042778B2 - Method for producing alkoxyalkylidene compounds - Google Patents
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JPS6042778B2 - Method for producing alkoxyalkylidene compounds - Google Patents

Method for producing alkoxyalkylidene compounds

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Publication number
JPS6042778B2
JPS6042778B2 JP52065197A JP6519777A JPS6042778B2 JP S6042778 B2 JPS6042778 B2 JP S6042778B2 JP 52065197 A JP52065197 A JP 52065197A JP 6519777 A JP6519777 A JP 6519777A JP S6042778 B2 JPS6042778 B2 JP S6042778B2
Authority
JP
Japan
Prior art keywords
reaction
alkoxyalkylidene
formula
producing
solvent
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.)
Expired
Application number
JP52065197A
Other languages
Japanese (ja)
Other versions
JPS53149912A (en
Inventor
信幸 山本
登 長谷川
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.)
Mitsubishi Chemical Corp
Original Assignee
Nippon Synthetic Chemical Industry 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 Nippon Synthetic Chemical Industry Co Ltd filed Critical Nippon Synthetic Chemical Industry Co Ltd
Priority to JP52065197A priority Critical patent/JPS6042778B2/en
Publication of JPS53149912A publication Critical patent/JPS53149912A/en
Publication of JPS6042778B2 publication Critical patent/JPS6042778B2/en
Expired 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)

Description

【発明の詳細な説明】 オルト酸エステルと活性メチレン化合物とを反応せしめ
て相当するアルコキシアルキリデン化合物を製造する方
法は、従来から数多くの文献に記載されている。
DETAILED DESCRIPTION OF THE INVENTION Methods for producing the corresponding alkoxyalkylidene compounds by reacting orthoacid esters with active methylene compounds have been described in numerous literatures.

例えば上記化合物の一種であるアルコキシメチレンマロ
ン、酸エステルの製造に関しては特開昭51−4123
号公報に記載されている。該方法はオルト蟻酸エステル
とマロン酸エステルとを(1)カルボン酸又はカルボン
酸無水物と(2)塩化亜鉛、塩化鉄等のルイス酸との混
合触媒の存在下に反応せめるものであり純度の高い製品
が得られる点で有利であるが、本発明者等が検討したと
ころ該方法には次のような問題点があることが明かとな
つた。1 使用触媒である塩化物は激しい腐蝕性を有す
るため、通常耐蝕性材質の最も代表的なものであるステ
ンレスチールでさえも反応時において腐蝕されて反応液
中にその一部が溶出して反応に好ましくない影響を与え
ると共に、反応装置自体の強度にも悪影響をおよぼすの
で、かかる装置の腐蝕の心配もない方法で上記化合物を
製造する必要があること。2 更に該方法では反応終了
後に末反応オルト蟻酸エステルを回収して、反応のろ過
操作を行い、触媒を戸別した後、製品の蒸留分取を行う
必要がある。
For example, regarding the production of alkoxymethylene malone, which is one of the above compounds, and acid ester, JP-A No. 51-4123
It is stated in the No. This method involves reacting an orthoformic acid ester and a malonic acid ester in the presence of a mixed catalyst of (1) a carboxylic acid or carboxylic acid anhydride and (2) a Lewis acid such as zinc chloride or iron chloride. Although this method is advantageous in that a high-quality product can be obtained, the inventors' studies revealed that the method has the following problems. 1 The catalyst used, chloride, is highly corrosive; therefore, even stainless steel, which is the most typical corrosion-resistant material, is corroded during the reaction, and some of it is eluted into the reaction solution, causing the reaction. It is necessary to produce the above-mentioned compound by a method that does not cause any fear of corrosion of the reactor, since it has an unfavorable effect on the reactor and the strength of the reactor itself. 2. Furthermore, in this method, it is necessary to recover the end-reacted orthoformate ester after the completion of the reaction, perform a filtration operation for the reaction, and after distributing the catalyst from person to person, perform fractional distillation of the product.

かかる触媒の濾別を行わないと生成製品が分解して収率
が低下するのである。かかる操作は、工業的製造法とし
てみた場合、熱時枦過、減圧蒸留の一旦停止等、繁雑さ
及び所要時間の増加につながり、必らずしも有利な製造
条件ではない。、しかるに本発明者はかかる問題を解決
するために鋭意研究を重ねた結果、溶媒の存在下又は不
存在下に式R_。
If the catalyst is not filtered out, the product will decompose and the yield will decrease. When viewed as an industrial production method, such operations are not necessarily advantageous production conditions, as they require increased complexity and time, such as thermal filtration and temporary suspension of vacuum distillation. However, as a result of extensive research to solve this problem, the present inventors have found that the formula R_ in the presence or absence of a solvent.

C(OR_、)O〔ここでアルキル基、R_。は水素、
アルキル基、アリル基、アルアルキル基を示す。〕で表
わされるオルト酸エステルと式H2C<:゜ 〔ここで
R3、R4は−COOR,を示す。〕で表わされる活性
メチレン化合物とを反応させて一般式R2♀6〈;゛
〔R1、R2、R3、R4は前記と同様で表わされるア
ルコキシアルキリデン化合物を製造する方法において、
触媒として(1)炭素数が1〜5の低級カルボン酸無水
物と(2)カルボン酸の亜鉛塩又は無機オキシ酸の亜鉛
塩を使用する場合には、装置の腐蝕を完全に防止し得る
と共に装置の材質の溶出によつて反応が阻害されること
なく円滑に反応を進行せしめ得ること、及び、反応液よ
り触媒を淵別する事なく、反応液の蒸留を行うことが出
来容易に目的化合物が得られること、更に、かかる反応
時に炭化水素溶媒を使用することにより、アルコキシア
ルキリデン化合物の収率が向上するという新規な事実を
見出し本発明を完成するに至つた。本発明において使用
する触媒として(1)に属するものとしては無水酢酸、
無水プロピオン酸、無水コハクが挙げられる。
C(OR_,)O [here, alkyl group, R_. is hydrogen,
Indicates an alkyl group, an allyl group, and an aralkyl group. ] and the formula H2C<:゜ [Here, R3 and R4 represent -COOR. ] by reacting with an active methylene compound represented by the general formula R2♀6〈;゛
[In the method for producing an alkoxyalkylidene compound in which R1, R2, R3, and R4 are represented as above,
When (1) a lower carboxylic acid anhydride having 1 to 5 carbon atoms and (2) a zinc salt of a carboxylic acid or a zinc salt of an inorganic oxyacid are used as catalysts, corrosion of the equipment can be completely prevented and The reaction can proceed smoothly without being inhibited by elution of the material of the device, and the reaction solution can be distilled without separating the catalyst from the reaction solution, making it easy to obtain the target compound. The present inventors have completed the present invention by discovering the novel fact that the yield of an alkoxyalkylidene compound can be improved by using a hydrocarbon solvent during such a reaction. Catalysts used in the present invention that belong to (1) include acetic anhydride,
Examples include propionic anhydride and succinic anhydride.

更に(2)に属するものとしては酢酸亜鉛、硫酸亜鉛、
リン酸亜鉛等が挙げられる。かかる触媒の中でも無水酢
酸一酢酸亜鉛、無水酢酸一硫酸亜鉛の組合せが特に有効
である。かかる触媒の使用量はオルト酸エステルに対し
て(1)成分が0.05〜0.5モル(2)成分が0.
00001〜0.001モル程度が好ましい。又、本発
明て使用する炭化水素溶媒としてはn−オクタン、ベン
ゼン、トルエン、o−キシレン等が挙げられるが、トル
エン、o−キシレンが特に有効である。
Furthermore, those belonging to (2) include zinc acetate, zinc sulfate,
Examples include zinc phosphate. Among such catalysts, a combination of acetic anhydride, zinc monoacetate, and acetic anhydride, zinc monosulfate, is particularly effective. The amount of the catalyst to be used is 0.05 to 0.5 mol of component (1) to 0.5 mol of component (2) based on the orthoacid ester.
The amount is preferably about 00001 to 0.001 mol. Further, examples of the hydrocarbon solvent used in the present invention include n-octane, benzene, toluene, o-xylene, etc., and toluene and o-xylene are particularly effective.

かかる溶媒の用量はオルト酸エステル1モルに対して8
0〜1000m1が好ましい。本発明に使用するオルト
酸エステルとしてはオルト蟻酸メチル、オルト酢酸エチ
ル、オルト蟻酸エチル、オルトプロピオン酸エステル等
が挙げられ、更に活性メチレン化合物の代表的な例とし
てはマロン酸ジエチルが挙げられる。本発明の方法はオ
ルト蟻酸エチルとマロン酸ジエチルとからエトキシメチ
レンマロン酸ジエチルを製造する場合に特に有用である
The dosage of such solvent is 8 per mole of orthoate ester.
0 to 1000 m1 is preferable. Examples of orthoacid esters used in the present invention include methyl orthoformate, ethyl orthoacetate, ethyl orthoformate, orthopropionate, and a typical example of the active methylene compound includes diethyl malonate. The process of the present invention is particularly useful in producing ethoxymethylene diethyl malonate from ethyl orthoformate and diethyl malonate.

本発明の方法を実施するに当つては、オルト酸エステル
と活性メチレン化合物と更に望ましくは炭化水素溶媒を
混合し攪拌下に加熱する。
In carrying out the method of the present invention, the orthoacid ester, the active methylene compound, and preferably a hydrocarbon solvent are mixed and heated under stirring.

原料の仕込み割合はオルト酸エステルニ活性メチレン化
合物=11〜3:1(モル比)好ましくは1.1:1〜
2.0:1程度が適当である。
The charging ratio of raw materials is orthoate ester diactive methylene compound = 11 to 3:1 (mole ratio), preferably 1.1:1 to
A ratio of about 2.0:1 is appropriate.

反応温度は100〜160℃、反応時間は1〜U時間が
望ましい。上記反応において副生するアルコールを系外
に留去させ、かつ溶媒を使用する時は使用溶媒は常に反
応系内に存在するようにすると収率が向上する。そのた
めには普通は反応温度および生成アルコールの沸点より
高い沸点を有する炭化水素溶媒を選べば良いが、必ずし
もそれに限るものではなく、反応温度付近あるいは反応
温度以下の沸点を有する炭化水素であつても使用可能で
ある。かかる沸点の比効的低い溶媒を用いる場合、反応
槽に精留装置をとりつけ、生成アルコールのみを留出さ
せ、溶媒は還流させながら反応を行えば良い。又反応温
度より非常に低い沸点を有する溶媒を使用する場合、目
的とする反応温度までの昇温操作が困難となる恐れがあ
れば、溶媒の使用量を減らしたり、分割仕込みすること
によつて解決し得る。又、生成アルコールが使用溶媒と
共沸組成物を作り溶媒が生成アルコール共に留出してし
まう場合にも反応の途中で適宜溶媒を追加仕込みすれば
よい。反応は常圧、加圧、減圧のいずれの場合にも実施
可能である。反応終了時は反応液を減圧蒸留して目的物
を得る。
The reaction temperature is preferably 100 to 160°C, and the reaction time is preferably 1 to U hours. The yield can be improved by distilling the alcohol by-produced in the above reaction out of the system and by ensuring that the solvent is always present in the reaction system when a solvent is used. For this purpose, it is usually sufficient to select a hydrocarbon solvent that has a boiling point higher than the reaction temperature and the boiling point of the alcohol produced, but this is not necessarily the case. Available for use. When using such a solvent with a relatively low boiling point, a rectification device may be attached to the reaction tank to distill out only the produced alcohol, and the reaction may be carried out while the solvent is refluxed. In addition, when using a solvent with a boiling point much lower than the reaction temperature, if there is a risk that it will be difficult to raise the temperature to the desired reaction temperature, reduce the amount of solvent used or charge it in parts. It can be solved. Further, even if the produced alcohol forms an azeotropic composition with the solvent used and the solvent is distilled off together with the produced alcohol, the solvent may be added as appropriate during the reaction. The reaction can be carried out under normal pressure, increased pressure, or reduced pressure. At the end of the reaction, the reaction solution is distilled under reduced pressure to obtain the desired product.

本発明で得られるアルコキシアルキリデン化合物は医薬
あるいはその他の有機合成品の中間体として有用なもの
である。
The alkoxyalkylidene compounds obtained in the present invention are useful as intermediates for pharmaceuticals or other organic synthetic products.

次に実例を挙げて本発明の方法を更に詳しく説明する実
例1 攪拌器、滴下器及び精留管(2.0cmφ×30C77
りを備えた50077!Lのフラスコ中にオルト蟻酸エ
チル1.3モル、マロン酸ジエチル1.0モル、無水酢
酸0.10モル、酢酸亜鉛0.0001モル(1%エタ
ノール溶液として2.19y)o−キシレン100m1
を仕込んだ145〜155℃で5時間反応を行ない更に
155℃で0.時間反応を続行した。
Next, the method of the present invention will be explained in more detail by giving examples.Example 1 Stirrer, dropper, and rectifying tube (2.0 cmφ x 30C77
50077 with features! In a L flask, 1.3 mol of ethyl orthoformate, 1.0 mol of diethyl malonate, 0.10 mol of acetic anhydride, 0.0001 mol of zinc acetate (2.19y as a 1% ethanol solution) 100 ml of o-xylene
The reaction was carried out at 145 to 155°C for 5 hours, and the reaction was further heated to 155°C for 0. The reaction was continued for an hour.

得られた反応終了液を減圧蒸留し、130〜135℃/
5wnHg留分を捕集した。消費したオルト蟻酸エチル
に対するエトキシメチレンマロン酸ジエチルの収率は7
6%、マロン酸ジエチルに対する収率は85%であつた
。又、反応液の腐蝕性を試験するために以下の実験を行
つた。前記反応粗液200m1にアセトンで脱脂乾燥し
た研磨軟鋼板(3−×50朗×1.h)を浸漬し165
℃、7日間経過後の腐蝕量を浸漬前後の重量減にて測定
し、その腐蝕率をYldlhrで求めた。
The obtained reaction-completed liquid was distilled under reduced pressure and heated to 130-135℃/
A 5wnHg fraction was collected. The yield of diethyl ethoxymethylene malonate based on the consumed ethyl orthoformate is 7
The yield was 85% based on diethyl malonate. In addition, the following experiment was conducted to test the corrosivity of the reaction solution. A polished mild steel plate (3 × 50 mm × 1. h) that had been degreased and dried with acetone was immersed in 200 ml of the crude reaction solution for 165 ml.
After 7 days at ℃, the amount of corrosion was measured by weight loss before and after immersion, and the corrosion rate was determined by Yldlhr.

その結果を本発明の場合は腐蝕率0であり、テストピー
ス表面に変化はなかつた。一方対照例1として酢酸亜鉛
に代えて塩化亜鉛を使用した以外は実例1と同一の実験
を行つた。
The results showed that the corrosion rate was 0 in the case of the present invention, and there was no change in the surface of the test piece. On the other hand, as Control Example 1, the same experiment as Example 1 was conducted except that zinc chloride was used instead of zinc acetate.

(但し反応液の蒸留前に末反応のオルト蟻酸エチルを追
出、塩化亜鉛を沖別した。)オルト蟻酸エチルに対する
エトキシメチレンマロン酸ジエチルの収率は76%であ
り、マロン酸ジエチルに対する収率は81%であつた。
(However, before distilling the reaction solution, the terminally reacted ethyl orthoformate was expelled and the zinc chloride was removed.) The yield of ethoxymethylene diethyl malonate relative to ethyl orthoformate was 76%, and the yield relative to diethyl malonate was 76%. was 81%.

又、腐蝕率は0.01yId1hrであり、テストピー
ス表面は黒変し、腐蝕の進行が推察された。尚対照例1
で塩化亜鉛の炉別を行わないと収率は70%に低下した
。実施2実例1における酢酸亜鉛に代えて硫酸亜鉛は使
用した以外は同例と同じ実験を行つた。
Further, the corrosion rate was 0.01yId1hr, and the surface of the test piece turned black, suggesting that corrosion had progressed. Control example 1
If zinc chloride was not separated in the furnace, the yield decreased to 70%. Example 2 The same experiment as in Example 1 was carried out except that zinc sulfate was used instead of zinc acetate.

オルト蟻酸エチルに対するエトキシメチレンマロン酸ジ
エチルの収率は75%、腐蝕率はOであつた。実例3実
例1においてo−キシレンの使用を省略した以外は同例
と同じ実験を行つた。
The yield of diethyl ethoxymethylene malonate based on ethyl orthoformate was 75%, and the corrosion rate was O. Example 3 The same experiment as in Example 1 was carried out except that the use of o-xylene was omitted.

オルト蟻酸エチルに対するエトキシメチレンマロン酸ジ
エチルの収率は70%、腐蝕は0であつた。対照例2と
して上記例で酢酸亜鉛に代えて塩化亜鉛を使用したとこ
ろエトキシメチレンマロン酸ジエチルの収率は70%、
腐蝕率は0.01y1d1hrであつた。(但し反応後
の蒸留前に塩化亜鉛を沖別した。)塩化亜鉛が共存する
状態で反応液を蒸留したところ目的物の収率は65%に
低下した。
The yield of diethyl ethoxymethylenemalonate based on ethyl orthoformate was 70%, and corrosion was 0. As Control Example 2, when zinc chloride was used in place of zinc acetate in the above example, the yield of diethyl ethoxymethylene malonate was 70%.
The corrosion rate was 0.01y1d1hr. (However, zinc chloride was removed before distillation after the reaction.) When the reaction solution was distilled in the presence of zinc chloride, the yield of the target product decreased to 65%.

実例4 実例1と同装置(但し蒸留管は2.2cfnφ×108
C!RL)にオルト蟻酸エチル1.5モル、マロン酸ジ
エチル1.0モル、無水酢酸0.1モル、酢酸亜鉛0.
0001モル、ベンゼン110m1を仕込んだ。
Example 4 Same device as Example 1 (however, the distillation tube is 2.2cfnφ×108
C! RL), 1.5 mol of ethyl orthoformate, 1.0 mol of diethyl malonate, 0.1 mol of acetic anhydride, and 0.0 mol of zinc acetate.
0001 mol and 110 ml of benzene were charged.

120〜140℃で1時間、更に140℃で7時間、1
40〜160℃で2時間反応を行つた。
1 hour at 120-140℃, further 7 hours at 140℃, 1
The reaction was carried out at 40-160°C for 2 hours.

(反応の途中、ベンゼン770m1を滴下仕込みした。
)エトキシメチレンマロン酸ジエチルの収率は70%で
あつた。腐蝕率は0であつた。実例5 実例1におけるo−キシレンに代えてトルエンを使用し
た以外は同例と同じ方法を行つた。
(During the reaction, 770 ml of benzene was added dropwise.
) The yield of diethyl ethoxymethylenemalonate was 70%. The corrosion rate was 0. Example 5 The same method as Example 1 was carried out except that toluene was used in place of o-xylene in Example 1.

Claims (1)

【特許請求の範囲】 1 溶媒の存在下又は不存在下で、式R_2C(OR_
1)_3[ここでR_1はアルキル基、R_2は水素、
アルキル基、アリル基を示す。 ]で表わされるオルト酢酸エステル式▲数式、化学式、
表等があります▼[ここでR_3、R_4は−COOR
_1を示す。]で表わされる活性メチレン化合物と反応
させて一般式▲数式、化学式、表等があります▼[R_
1、R_2、R_3、R_4は前記と同様]で表わされ
るアルコキシアルキリデン化合物を製造する方法におい
て、触媒として(1)炭素数が1〜5の低級カルボン酸
無水物と(2)カルボン酸の亜鉛塩又は無機オキシ酸の
亜鉛塩を使用することを特徴とするアルコキシアルキリ
デン化合物の製造法。
[Claims] 1. In the presence or absence of a solvent, the formula R_2C(OR_
1)_3 [where R_1 is an alkyl group, R_2 is hydrogen,
Indicates an alkyl group or an allyl group. ] Orthoacetate formula ▲ mathematical formula, chemical formula,
There are tables etc. ▼ [Here, R_3 and R_4 are -COOR
Indicates _1. ] By reacting with an active methylene compound represented by the general formula ▲ There are mathematical formulas, chemical formulas, tables, etc. ▼ [R_
1, R_2, R_3, R_4 are the same as above] In the method for producing an alkoxyalkylidene compound represented by (1) a lower carboxylic acid anhydride having 1 to 5 carbon atoms and (2) a zinc salt of a carboxylic acid as a catalyst. Or, a method for producing an alkoxyalkylidene compound, which comprises using a zinc salt of an inorganic oxyacid.
JP52065197A 1977-06-01 1977-06-01 Method for producing alkoxyalkylidene compounds Expired JPS6042778B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP52065197A JPS6042778B2 (en) 1977-06-01 1977-06-01 Method for producing alkoxyalkylidene compounds

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP52065197A JPS6042778B2 (en) 1977-06-01 1977-06-01 Method for producing alkoxyalkylidene compounds

Publications (2)

Publication Number Publication Date
JPS53149912A JPS53149912A (en) 1978-12-27
JPS6042778B2 true JPS6042778B2 (en) 1985-09-25

Family

ID=13279942

Family Applications (1)

Application Number Title Priority Date Filing Date
JP52065197A Expired JPS6042778B2 (en) 1977-06-01 1977-06-01 Method for producing alkoxyalkylidene compounds

Country Status (1)

Country Link
JP (1) JPS6042778B2 (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2589466B1 (en) * 1985-11-04 1988-10-14 Rhone Poulenc Spec Chim PROCESS FOR THE PREPARATION OF COMPOUNDS CARRYING ALKOXYALKYLIDENE PATTERNS
US5214186A (en) * 1991-12-03 1993-05-25 Eastman Kodak Company Process for the preparation of arylidine dyes using an active methylene compound
US7161024B2 (en) * 2003-07-10 2007-01-09 Schering Corporation Process for the preparation and purification of 2-(alkoxyalkylidene)-3-ketoalkanoic acid esters from 3-ketoalkanoic acid esters

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