JPH08127577A - Production of 4-methylenetetrahydropyran - Google Patents

Production of 4-methylenetetrahydropyran

Info

Publication number
JPH08127577A
JPH08127577A JP28759594A JP28759594A JPH08127577A JP H08127577 A JPH08127577 A JP H08127577A JP 28759594 A JP28759594 A JP 28759594A JP 28759594 A JP28759594 A JP 28759594A JP H08127577 A JPH08127577 A JP H08127577A
Authority
JP
Japan
Prior art keywords
sulfate
methylenetetrahydropyran
methyltetrahydropyran
hydroxy
formula
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.)
Pending
Application number
JP28759594A
Other languages
Japanese (ja)
Inventor
Hideji Iwasaki
秀治 岩崎
Takashi Onishi
孝志 大西
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.)
Kuraray Co Ltd
Original Assignee
Kuraray 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 Kuraray Co Ltd filed Critical Kuraray Co Ltd
Priority to JP28759594A priority Critical patent/JPH08127577A/en
Publication of JPH08127577A publication Critical patent/JPH08127577A/en
Pending legal-status Critical Current

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  • Pyrane Compounds (AREA)

Abstract

PURPOSE: To obtain the subject compound useful as a raw material for medicines and agrochemicals by intermittently or continuously feeding hydroxy- methyltetrahydropyran into a reactor containing a sulfate suspended in a sulfate- insoluble solvent and carrying out the dehydrating reaction. CONSTITUTION: (A) 4-Hydroxy-4-methyltetrahydropyran of formula I is intermittently or continuously fed into a reactor containing (B) a sulfate (e.g. copper sulfate or sodium sulfate) suspended in a sulfate-insoluble solvent (e.g. toluene or hexane) and the dehydrating reaction is carried out while distilling away the resultant product in the reactor. Thereby, 4-methylenetetrahydropyran of formula II is obtained. The compound of formula I is obtained by hydrating 4-methyl-5,6-dihydro-2H-pyran which is an isomer of formula III in the presence of a mineral acid such as sulfuric acid. Furthermore, the amount of the sulfate is preferably 0.001-100 pts.wt., especially preferably 0.01-10 pts.wt. based on 100 pts.wt. component (A).

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、医薬品や農薬の原料と
して有用な4−メチレンテトラヒドロピランを、工業的
規模でかつ経済的に製造するのに有利な方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an advantageous method for producing 4-methylenetetrahydropyran useful as a raw material for pharmaceuticals and agricultural chemicals on an industrial scale and economically.

【0002】[0002]

【従来の技術】4−メチレンテトラヒドロピランは医薬
品や農薬品の原料として有効に利用されている化合物で
あり、それは例えばイソプレンを合成する際にイソブテ
ンおよびホルムアルデヒドからの副生物として生成する
(Chem.Abstr.77,134876,197
1)か、あるいは、4,4−ジメチル−1,3−ジオキ
サ−シクロヘキサンの熱分解の際に式(3)で示される
異性体の4−メチル−5,6−ジヒドロ−2Hピランと
混合した状態で生成する(Pet.Chem.USSR
(Engl.,Transl,)7(1967)92)
ことがすでに知られている。
BACKGROUND OF THE INVENTION 4-Methylenetetrahydropyran is a compound which is effectively used as a raw material for pharmaceuticals and agricultural chemicals, and it is produced as a by-product from isobutene and formaldehyde in the synthesis of isoprene (Chem. Abstr. .77, 134876, 197
1) or alternatively it was mixed with the isomeric 4-methyl-5,6-dihydro-2Hpyran of formula (3) during the thermal decomposition of 4,4-dimethyl-1,3-dioxa-cyclohexane. Generate in state (Pet.Chem.USSR
(Engl., Transl,) 7 (1967) 92).
Is already known.

【0003】[0003]

【化3】 Embedded image

【0004】そして、ピラン類の一般的製造方法として
次のような方法が検討されている。 (1)式(4)で示されるようなジオール類の閉環反応
を利用する方法、例えば、それをスルホン酸エステルに
した後に塩基によって閉環させる方法。(特開平3−7
7879号公報)
The following methods have been studied as a general method for producing pyrans. (1) A method utilizing a ring-closing reaction of diols represented by the formula (4), for example, a method of converting it into a sulfonate and then ring-closing with a base. (JP-A-3-7
(Japanese Patent No. 7879)

【0005】[0005]

【化4】 [Chemical 4]

【0006】(2)式(1)で示されるアルコールを、
中性アルミナ、塩基を含浸させたアルミナ、シリカ等の
固体触媒によって脱水する方法。 (3)式(1)で示されるアルコールを、硫酸塩触媒に
よって脱水する方法。(特願平5−291324号)
(2) The alcohol represented by the formula (1) is
A method of dehydrating with a solid catalyst such as neutral alumina, alumina impregnated with a base, or silica. (3) A method of dehydrating the alcohol represented by the formula (1) with a sulfate catalyst. (Japanese Patent Application No. 5-291324)

【0007】[0007]

【化5】 Embedded image

【0008】しかるに前記(1)の方法は、当量以上の
スルホニルハライドを必要とし、また閉環反応後はスル
ホン酸塩が析出するため、工業的規模での製法としては
実用的でない。また前記(2)の方法は、生成したピラ
ン類の分解によって、イソプレンとホルムアルデヒドが
生成するという欠点を有する。さらに前記(3)の方法
は、ピラン類への選択率は高いものの、目的の4−メチ
レンテトラヒドロピランへの選択率は低く、35%程度
に過ぎない。
However, the above method (1) requires an equivalent amount or more of sulfonyl halide, and the sulfonate is precipitated after the ring-closing reaction, so that it is not practical as an industrial scale production method. Further, the method (2) has a drawback that isoprene and formaldehyde are produced by decomposition of the produced pyrans. Further, the method (3) has a high selectivity to pyrans, but has a low selectivity to the target 4-methylenetetrahydropyran, which is only about 35%.

【0009】[0009]

【発明が解決しようとする課題】本発明の目的は、前記
の諸問題を解消するとともに、工業的規模で効率良く4
−メチレンテトラヒドロピランを製造せんとするもので
ある。
SUMMARY OF THE INVENTION The object of the present invention is to solve the above-mentioned various problems, and to improve efficiency on an industrial scale.
-To produce methylenetetrahydropyran.

【0010】[0010]

【課題を解決するための手段】上記目的は、本発明によ
れば、式(1)
According to the present invention, the above object is achieved by the formula (1).

【0011】[0011]

【化6】 [Chemical 6]

【0012】で示される4−ヒドロキシ−4−メチルテ
トラヒドロピランを、硫酸塩存在下に脱水反応させるこ
とにより、式(2)
By dehydrating 4-hydroxy-4-methyltetrahydropyran represented by the formula (2) in the presence of a sulfate,

【0013】[0013]

【化7】 [Chemical 7]

【0014】で示される4−メチレンテトラヒドロピラ
ンの製造方法であって、硫酸塩を硫酸塩不溶性溶媒に懸
濁させている反応器中に4−ヒドロキシ−4−メチルテ
トラヒドロピランを断続的または連続的に供給すると共
に、該反応器中の生成物を留出させながら脱水反応を行
うことを特徴とする4−メチレンテトラヒドロピランの
製造方法により達成することができる。
A method for producing 4-methylenetetrahydropyran represented by the following formula, wherein 4-hydroxy-4-methyltetrahydropyran is intermittently or continuously added to a reactor in which sulfate is suspended in a sulfate-insoluble solvent. It can be achieved by a method for producing 4-methylenetetrahydropyran, characterized in that the dehydration reaction is carried out while the product in the reactor is being distilled off while being fed to the reactor.

【0015】本発明の4−メチレンテトラヒドロピラン
の製造方法において、製造原料である式(1)
In the method for producing 4-methylenetetrahydropyran of the present invention, the raw material of formula (1)

【0016】[0016]

【化8】 Embedded image

【0017】の4−ヒドロキシ−4−メチルテトラヒド
ロピランは、式(3)
4-hydroxy-4-methyltetrahydropyran of formula has the formula (3)

【0018】[0018]

【化9】 [Chemical 9]

【0019】で示される異性体の4−メチル−5,6−
ジヒドロ−2Hピランを硫酸、燐酸のような鉱酸、また
は酸性イオン交換樹脂、ゼオライト、活性白土等の固体
酸の存在下に水和させることによって容易に得られる。
The isomer of 4-methyl-5,6-
It is easily obtained by hydrating dihydro-2Hpyran in the presence of a mineral acid such as sulfuric acid or phosphoric acid, or a solid acid such as an acidic ion exchange resin, zeolite or activated clay.

【0020】4−ヒドロキシ−4−メチルテトラヒドロ
ピランは酸性条件下で異性体の4−メチル−5,6−ジ
ヒドロ−2Hピランを水和させた後、系内を中和し、さ
らに有機溶媒で抽出し、抽出溶媒を除去し、続いて単蒸
発させることによって次段階の反応に十分な純度に容易
に精製できる。
4-Hydroxy-4-methyltetrahydropyran is obtained by hydrating the isomeric 4-methyl-5,6-dihydro-2Hpyran under acidic conditions, neutralizing the system, and then using an organic solvent. It can be easily purified to sufficient purity for the next step reaction by extraction, removal of the extraction solvent, followed by simple evaporation.

【0021】本発明において使用する硫酸塩は、例え
ば、硫酸銅、硫酸ナトリウム、硫酸ニッケル、硫酸マグ
ネシウム、硫酸カリウム、硫酸ジルコニウム、さらに硫
酸水素ナトリウム、硫酸水素カリウム等の硫酸水素塩等
である。
The sulfate used in the present invention is, for example, copper sulfate, sodium sulfate, nickel sulfate, magnesium sulfate, potassium sulfate, zirconium sulfate, and hydrogen sulfate such as sodium hydrogen sulfate and potassium hydrogen sulfate.

【0022】これらの硫酸塩については、水和物であっ
てもあるいは無水物であってもよく、市販品を粉末とし
て用いても、あるいは結晶として用いてもよく、さらに
は市販品を溶融、凝固させて適当な大きさに粉砕したも
のを用いてもよい。
These sulfates may be hydrates or anhydrides, commercially available products may be used as powders or crystals, and further commercially available products may be melted, You may use what was solidified and grind | pulverized to suitable size.

【0023】本発明において4−ヒドロキシ−4−メチ
ルテトラヒドロピランは、硫酸塩不溶性溶媒に懸濁させ
ている反応器中に断続的または連続的に供給される。そ
の際使用される硫酸塩不溶性溶媒としては、酸性条件下
安定なものであればいかなるものであっても構わない。
すなわち、芳香族炭化水素例えばトルエン、キシレン、
メシチレン、そのハロゲン化物であるジクロロベンゼ
ン、飽和炭化水素例えばヘキサン、デカン、ドデカン、
パラフィン、エーテル類としてジフェニルエーテル、ジ
オクチルエーテルなどが使用される。しかしながら本発
明の製造方法においては、反応を行う温度が高温であ
り、また反応系が反応留出型であるので、反応中の操作
として常圧下で使用できるものが好ましく、尚且つ留出
中に含まれない程度の目的物との沸点差の或る方が、反
応後の蒸留回収等により好ましいことは言うまでもな
い。
In the present invention, 4-hydroxy-4-methyltetrahydropyran is intermittently or continuously fed into a reactor suspended in a sulfate-insoluble solvent. Any sulfate-insoluble solvent used at that time may be used as long as it is stable under acidic conditions.
That is, aromatic hydrocarbons such as toluene, xylene,
Mesitylene, its halide dichlorobenzene, saturated hydrocarbons such as hexane, decane, dodecane,
Paraffin and ethers such as diphenyl ether and dioctyl ether are used. However, in the production method of the present invention, since the reaction temperature is high and the reaction system is a reaction distillation type, it is preferable that it can be used under normal pressure as an operation during the reaction, and still during distillation. It is needless to say that the one having a boiling point difference from the target substance which is not contained is preferable for distillation recovery after the reaction.

【0024】4−ヒドロキシ−4−メチルテトラヒドロ
ピランの脱水反応の反応温度は、用いる触媒によって異
なり、例えば硫酸銅を用いるときは170℃程度である
のがよく、硫酸水素ナトリウムでは150℃程度である
のがよい。
The reaction temperature for the dehydration reaction of 4-hydroxy-4-methyltetrahydropyran depends on the catalyst used, and is preferably about 170 ° C. when using copper sulfate and about 150 ° C. for sodium hydrogensulfate. Is good.

【0025】反応は加圧下〜減圧下で行うことが出来
る。生成物を反応系からより早く留出させるためには減
圧下での反応が適当であるが、反応をより容易に行うた
めには大気圧下でもよく、これによっても十分な反応結
果が得られる。
The reaction can be carried out under pressure or under reduced pressure. The reaction under reduced pressure is suitable for distilling the product out of the reaction system faster, but it may be under atmospheric pressure for easier reaction, which also provides sufficient reaction results. .

【0026】反応触媒である硫酸塩の量は初期に仕込ま
れる4−ヒドロキシ−4−メチルテトラヒドロピラン1
00重量部に対して0.001〜100重量部程度であ
り、より高い選択性を得るためには、0.01〜10重
量部が適当である。
The amount of the sulfate as the reaction catalyst is the amount of 4-hydroxy-4-methyltetrahydropyran 1 initially charged.
It is about 0.001 to 100 parts by weight with respect to 00 parts by weight, and 0.01 to 10 parts by weight is suitable for obtaining higher selectivity.

【0027】4−ヒドロキシ−4−メチルテトラヒドロ
ピランの脱水反応は、前記したように液層反応蒸留形式
によって行う。
The dehydration reaction of 4-hydroxy-4-methyltetrahydropyran is carried out by the liquid layer reactive distillation system as described above.

【0028】具体的には、反応器中に、4−ヒドロキシ
−4−メチルテトラヒドロピランと溶媒及び触媒を初期
仕込し、所定の温度まで昇温する。この昇温に伴って脱
水反応が進行し、生成物である4−メチレンテトラヒド
ロピランと異性体の4−メチル−5,6−ジヒドロ−2
Hピランと水が留出し始める。
Specifically, 4-hydroxy-4-methyltetrahydropyran, a solvent and a catalyst are initially charged in a reactor and the temperature is raised to a predetermined temperature. The dehydration reaction proceeds with this temperature increase, and 4-methylenetetrahydropyran as a product and 4-methyl-5,6-dihydro-2 as an isomer.
H-piran and water begin to distill.

【0029】このときに4−ヒドロキシ−4−メチルテ
トラヒドロピランを反応系中にフィードし、系内の触媒
濃度が変化しないようにし、これによって安定的な選択
性を得ることが出来る。
At this time, 4-hydroxy-4-methyltetrahydropyran is fed into the reaction system so that the catalyst concentration in the system does not change, whereby stable selectivity can be obtained.

【0030】反応開始に於ける初期仕込の溶媒と4−ヒ
ドロキシ−4−メチルテトラヒドロピランの混合比は溶
媒100重量部に対して4−ヒドロキシ−4−メチルテ
トラヒドロピランは2000重量部以下が適当であり、
10〜1000重量部が好ましい。
At the start of the reaction, the mixing ratio of the initially charged solvent and 4-hydroxy-4-methyltetrahydropyran is preferably 2000 parts by weight or less of 4-hydroxy-4-methyltetrahydropyran with respect to 100 parts by weight of the solvent. Yes,
10 to 1000 parts by weight is preferable.

【0031】液層反応蒸留によって得られる反応生成物
は、4−メチレンテトラヒドロピランと該化合物の異性
体の4−メチル−5,6−ジヒドロ−2Hピランの混合
物からなる有機層と水層とである。
The reaction products obtained by the liquid layer reactive distillation are an organic layer and a water layer which are composed of a mixture of 4-methylenetetrahydropyran and 4-methyl-5,6-dihydro-2Hpyran which is an isomer of the compound. is there.

【0032】有機層に於ける4−メチレンテトラヒドロ
ピランと異性体の4−メチル−5,6−ジヒドロ−2H
ピランとの分離は常圧下での蒸留によって容易に分離す
ることが出来る。すなわち反応生成物として得られる有
機層を乾燥後蒸留することによって、目的とする4−メ
チレンテトラヒドロピランが得られる。
4-Methylenetetrahydropyran and the isomeric 4-methyl-5,6-dihydro-2H in the organic layer
Separation from pyran can be easily achieved by distillation under normal pressure. That is, the desired 4-methylenetetrahydropyran is obtained by distilling the organic layer obtained as a reaction product and then distilling it.

【0033】反応によって副生する異性体の4−メチル
−5,6−ジヒドロ−2Hピランは再び水和工程に戻す
ことによって4−ヒドロキシ−4−メチルテトラヒドロ
ピランとし、本発明の4−メチレンテトラヒドロピラン
の製造方法に於ける仕込原料として使用できる。
The isomer 4-methyl-5,6-dihydro-2Hpyran, which is a by-product of the reaction, is returned to the hydration step to give 4-hydroxy-4-methyltetrahydropyran, which is the 4-methylenetetrahydro of the present invention. It can be used as a raw material in the production method of pyran.

【0034】[0034]

【実施例】以下、本発明の4−メチレンテトラヒドロピ
ランの具体的な製造方法を実施例に基づいて説明する。
EXAMPLES A specific method for producing 4-methylenetetrahydropyran of the present invention will be described below based on examples.

【0035】参考例(4−ヒドロキシ−4−メチルテト
ラヒドロピランの製造) 4−メチル−5,6−ジヒドロ−2Hピラン100gと
35%硫酸水150gとを反応器内で50℃に加温し、
70時間撹拌した。
Reference Example (Production of 4-hydroxy-4-methyltetrahydropyran) 100 g of 4-methyl-5,6-dihydro-2Hpyran and 150 g of 35% sulfuric acid water were heated to 50 ° C. in a reactor,
Stir for 70 hours.

【0036】次いで、反応系内を中和し、酢酸エチルで
抽出し、酢酸エチルをカットした後に蒸発処理すること
によって、4−ヒドロキシ−4−メチルテトラヒドロピ
ラン106g(収率90%)を得た。
Next, the reaction system was neutralized, extracted with ethyl acetate, ethyl acetate was cut off, and then evaporated to obtain 106 g of 4-hydroxy-4-methyltetrahydropyran (yield 90%). .

【0037】実施例1 100mlの3口フラスコに40gのパラフィンと40
gの4−ヒドロキシ−4−メチルテトラヒドロピランと
0.2gの硫酸ナトリウムを投入し160℃まで昇温し
た。反応開始後の生成物の留出に伴って、4−ヒドロキ
シ−4−メチルテトラヒドロピランをフィードした。2
時間の反応を行うことによって97.1gの留出物を得
た。また、該留出物中の有機層は81.1gであった。
この有機層に於ける4−メチレンテトラヒドロピランと
異性体の4−メチル−5,6−ジヒドロ−2Hピランと
の混合物の濃度は99.7重量%であり、4−メチレン
テトラヒドロピランと4−メチル−5,6−ジヒドロ−
2Hピランとの重量比は41:59である。前記の有機
層(81.1g)を蒸留することによって、30.7g
の4−メチレンテトラヒドロピラン(純度99%以上)
を得た。
Example 1 40 g of paraffin and 40 g in a 100 ml three-necked flask.
g of 4-hydroxy-4-methyltetrahydropyran and 0.2 g of sodium sulfate were added and the temperature was raised to 160 ° C. 4-Hydroxy-4-methyltetrahydropyran was fed along with the distillation of the product after the start of the reaction. Two
By carrying out the reaction for an hour, 97.1 g of distillate was obtained. The organic layer in the distillate was 81.1 g.
The concentration of the mixture of 4-methylenetetrahydropyran and the isomeric 4-methyl-5,6-dihydro-2Hpyran in this organic layer was 99.7% by weight, and 4-methylenetetrahydropyran and 4-methyl -5,6-dihydro-
The weight ratio with 2H pyran is 41:59. By distilling the above organic layer (81.1 g), 30.7 g
4-methylenetetrahydropyran (purity 99% or more)
I got

【0038】実施例2 100mlの3口フラスコに40gのパラフィンと20
gの4−ヒドロキシ−4−メチルテトラヒドロピランと
0.1gの硫酸水素ナトリウムを投入し160℃まで昇
温した。反応開始後の生成物の留出に伴って、4−ヒド
ロキシ−4−メチルテトラヒドロピランをフィードし
た。2時間の反応を行うことによって111.1gの留
出物を得た。また、該留出物中の有機層は92.8gで
あった。この有機層に於ける4−メチレンテトラヒドロ
ピランと異性体の4−メチル−5,6−ジヒドロ−2H
ピランとの混合物の濃度は99.7重量%であり、4−
メチレンテトラヒドロピランと4−メチル−5,6−ジ
ヒドロ−2Hピランとの重量比は46:54である。前
記の有機層(92.8g)を蒸留することによって、4
0.6gの4−メチレンテトラヒドロピラン(純度99
%以上)を得た。
Example 2 40 g of paraffin and 20 g in a 100 ml three-necked flask.
g of 4-hydroxy-4-methyltetrahydropyran and 0.1 g of sodium hydrogensulfate were added and the temperature was raised to 160 ° C. 4-Hydroxy-4-methyltetrahydropyran was fed along with the distillation of the product after the start of the reaction. By carrying out the reaction for 2 hours, 111.1 g of distillate was obtained. The organic layer in the distillate was 92.8 g. 4-Methylenetetrahydropyran and the isomeric 4-methyl-5,6-dihydro-2H in this organic layer
The concentration of the mixture with pyran is 99.7% by weight,
The weight ratio of methylenetetrahydropyran to 4-methyl-5,6-dihydro-2Hpyran is 46:54. By distilling the above organic layer (92.8 g), 4
0.6 g of 4-methylenetetrahydropyran (purity 99
% Or more).

【0039】実施例3 100mlの3口フラスコに40gのメシチレンと40
gの4−ヒドロキシ−4−メチルテトラヒドロピランと
0.1gの硫酸ナトリウムを投入し165℃まで昇温し
た。反応開始後の生成物の留出に伴って、4−ヒドロキ
シ−4−メチルテトラヒドロピランをフィードした。2
時間の反応を行うことによって122.8gの留出物を
得た。また、該留出物中の有機層は102.1gであっ
た。この有機層に於ける4−メチレンテトラヒドロピラ
ンと異性体の4−メチル−5,6−ジヒドロ−2Hピラ
ンとの混合物の濃度は99.8重量%であり、4−メチ
レンテトラヒドロピランと4−メチル−5,6−ジヒド
ロ−2Hピランとの重量比は55:45である。前記の
有機層(102.1g)を蒸留することによって、5
4.3gの4−メチレンテトラヒドロピラン(純度99
%以上)を得た。
Example 3 40 g mesitylene and 40 g in a 100 ml three-necked flask.
g of 4-hydroxy-4-methyltetrahydropyran and 0.1 g of sodium sulfate were added and the temperature was raised to 165 ° C. 4-Hydroxy-4-methyltetrahydropyran was fed along with the distillation of the product after the start of the reaction. Two
122.8 g of distillate was obtained by carrying out the reaction for a period of time. The organic layer in the distillate was 102.1 g. The concentration of the mixture of 4-methylenetetrahydropyran and the isomeric 4-methyl-5,6-dihydro-2Hpyran in this organic layer was 99.8% by weight, and 4-methylenetetrahydropyran and 4-methyl The weight ratio with -5,6-dihydro-2Hpyran is 55:45. By distilling the above organic layer (102.1 g), 5
4.3 g of 4-methylenetetrahydropyran (purity 99
% Or more).

【0040】[0040]

【発明の効果】本発明によれば、医薬品及び農薬品の原
料として有用な4−メチレンテトラヒドロピランを、工
業的に効率よく得ることができる。
INDUSTRIAL APPLICABILITY According to the present invention, 4-methylenetetrahydropyran useful as a raw material for pharmaceuticals and agricultural chemicals can be industrially obtained efficiently.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 式(1) 【化1】 で示される4−ヒドロキシ−4−メチルテトラヒドロピ
ランを、硫酸塩存在下に脱水反応させることにより、式
(2) 【化2】 で示される4−メチレンテトラヒドロピランの製造方法
であって、硫酸塩を硫酸塩不溶性溶媒に懸濁させている
反応器中に4−ヒドロキシ−4−メチルテトラヒドロピ
ランを断続的または連続的に供給すると共に、該反応器
中の生成物を留出させながら脱水反応を行うことを特徴
とする4−メチレンテトラヒドロピランの製造方法。
1. Formula (1): 4-hydroxy-4-methyltetrahydropyran represented by the formula is dehydrated in the presence of a sulfate to give a compound of formula (2): A method for producing 4-methylenetetrahydropyran represented by the following formula, wherein 4-hydroxy-4-methyltetrahydropyran is intermittently or continuously fed into a reactor in which a sulfate is suspended in a sulfate-insoluble solvent. At the same time, a dehydration reaction is performed while distilling the product in the reactor, and a method for producing 4-methylenetetrahydropyran.
JP28759594A 1994-10-27 1994-10-27 Production of 4-methylenetetrahydropyran Pending JPH08127577A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP28759594A JPH08127577A (en) 1994-10-27 1994-10-27 Production of 4-methylenetetrahydropyran

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP28759594A JPH08127577A (en) 1994-10-27 1994-10-27 Production of 4-methylenetetrahydropyran

Publications (1)

Publication Number Publication Date
JPH08127577A true JPH08127577A (en) 1996-05-21

Family

ID=17719330

Family Applications (1)

Application Number Title Priority Date Filing Date
JP28759594A Pending JPH08127577A (en) 1994-10-27 1994-10-27 Production of 4-methylenetetrahydropyran

Country Status (1)

Country Link
JP (1) JPH08127577A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100379300B1 (en) * 2000-11-06 2003-04-10 주식회사 중외제약 Sequential catalytic asymmetric allyl transfer reactions for the enantioselective synthesis of new pyran derivatives
EP1493737A1 (en) * 2003-07-04 2005-01-05 Kao Corporation Process for producing a pyran compound
EP1516879A1 (en) * 2003-09-17 2005-03-23 Kao Corporation Process for producing pyran
JP2005112844A (en) * 2003-09-17 2005-04-28 Kao Corp Method for production of pyran

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100379300B1 (en) * 2000-11-06 2003-04-10 주식회사 중외제약 Sequential catalytic asymmetric allyl transfer reactions for the enantioselective synthesis of new pyran derivatives
EP1493737A1 (en) * 2003-07-04 2005-01-05 Kao Corporation Process for producing a pyran compound
EP1516879A1 (en) * 2003-09-17 2005-03-23 Kao Corporation Process for producing pyran
JP2005112844A (en) * 2003-09-17 2005-04-28 Kao Corp Method for production of pyran
US7064221B2 (en) 2003-09-17 2006-06-20 Kao Corporation Process for producing pyran
JP4545478B2 (en) * 2003-09-17 2010-09-15 花王株式会社 Piran production method

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