WO2004069780A1 - Process for production of adipic acids having side chains - Google Patents
Process for production of adipic acids having side chains Download PDFInfo
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- WO2004069780A1 WO2004069780A1 PCT/JP2004/001403 JP2004001403W WO2004069780A1 WO 2004069780 A1 WO2004069780 A1 WO 2004069780A1 JP 2004001403 W JP2004001403 W JP 2004001403W WO 2004069780 A1 WO2004069780 A1 WO 2004069780A1
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- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C51/00—Preparation of carboxylic acids or their salts, halides or anhydrides
- C07C51/16—Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation
- C07C51/31—Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation of cyclic compounds with ring-splitting
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- the present invention relates to a method for producing a branched adipic acid which is useful for applications such as a polyamide modifier, a polyester modifier, a cosmetic base, and a raw material of polyester or polyamide.
- the method for producing 2,5-getyl adipic acid is as follows: 1,3-butadiene and sodium metal are reacted in dimethyl ether at -70 ° C, and magnesium bromide; There is known a method for producing the desired 2,5-getyl adipic acid by reacting (see US Pat. No. 3,375,272).
- a peroxide such as ditert-butylperoxide is used as a catalyst, and propionic acid and acetylene are reacted at 120 ° C in n-nonane.
- a method for producing the desired 2,5-dimethyladipic acid is known (see US Pat. No. 3,549,977).
- An object of the present invention is to provide an industrially suitable method for producing a branched adipic acid.
- the present invention provides the following (1) to (3).
- R 7 represents formyl or hydroxymethyl, and is a single bond or a double bond.
- a general formula (II) characterized by including a step of reacting in the presence of a hydroxide of an alkaline earth metal.
- examples of the alkyl include linear or branched alkyl having 1 to 1 ° carbon atoms, and specific examples thereof include methyl, ethyl, propyl, isopropyl, and butyl. And isobutyl, sec-butyl, tert-butyl, pentyl, hexyl, heptyl, octyl, nonyl, decyl and the like, and among them, methyl or ethyl is preferable.
- Compound (I) which is a raw material of the production method of the present invention, can be obtained by cyclizing an acrolein derivative by a known method (US Pat. Accordingly, the obtained dihydropyran derivative is converted to hydrogen It can be obtained by reduction.
- hydroxides of alkaline metal or alkaline earth metals include hydroxide hydroxide, sodium hydroxide, magnesium hydroxide, calcium hydroxide, and the like. These may be used alone or in combination of two or more.
- the amount of hydroxide of alkali metal or earth metal used is preferably 1.5 mol or more, more preferably 1.5 to 5.5 mol, per 1 mol of compound (I). It is preferably 0 mol, and more preferably 1.8 to 3.0 mol. ''
- the reaction temperature is preferably from 200 to 320 ° C, more preferably from 200 to 250 ° C, and further preferably from 220 to 250 ° C. More preferably, the temperature is 250 ° C.
- the reaction is carried out at normal pressure or under pressure, preferably at most 2.0 MPa, more preferably at most 1.0 MPa.
- the reaction time is not particularly limited, but is preferably 5 hours or more, and more preferably 5 to 20 hours.
- reaction solvent In the reaction, a reaction solvent may be used, and the reaction solvent is not particularly limited as long as it does not affect the reaction.
- the reaction solvent include ether solvents such as dibenzyl ether, hydrocarbon solvents such as liquid paraffin, and the like, and these may be used as a mixture.
- the amount of the reaction solvent is not particularly limited, but is preferably 50 to 200% by weight, more preferably 70 to 150% by weight, based on the compound (I). '
- the reaction may be performed by adding a metal oxide such as zinc oxide or copper oxide as a catalyst.
- a metal oxide such as zinc oxide or copper oxide
- the amount of the catalyst to be used is preferably 0.1 to 5% by weight based on the compound (I). '
- the compound (II) can be obtained in the form of a salt of an alkali metal or an alkaline earth metal.
- the compound (II) can be obtained by adding an aqueous solution of sulfuric acid, hydrochloric acid or the like thereto.
- the obtained compound (II) may be subjected to a purification operation such as extraction, crystallization, or distillation from the reaction solution or the like in order to improve the purity.
- the production method of the present invention is an industrially suitable production method that is simple, inexpensive, and excellent in safety.
- Compound (II) is useful for applications such as polyamide modifiers, polyester modifiers, cosmetic bases, and raw materials for polyesters or polyamides.
- the reaction solution containing 2,5-getyl sodium adipic acid salt was cooled to 100 ° C or less, dissolved in 400 g of distilled water, and further precipitated by adding dropwise 420 g of 30% sulfuric acid.
- 5-Jetyl adipine yeast was collected by filtration.
- the obtained crude 2,5-diethyladipate was dissolved in 300 ml of methyl isobutyl ketone, washed with water, and concentrated under reduced pressure at 60 ° C to obtain 183 g of a residue containing 2,5-diethyladipate. Obtained.
- the residue was crystallized from n-hexane to obtain 170 g (yield: 85%) of white crystals of 2,5-getyladipic acid.
- the physical property values of the obtained 2,5-getyladipic acid are shown below.
- the starting materials were 2,5-diethyltetrahydropyran-1-methanol 172.0 g (1. Omo 1), potassium hydroxide (manufactured by Kanto Chemical Co., Ltd.) 99.0 g (3.0 mo 1) and liquid paraffin 60
- S manufactured by Chuo Kasei Co., Ltd.
- S was changed to 200 g, to give 158 g (yield 79%) of white crystals of 2,5-getyladipic acid.
- Example 3 Synthesis of 2,5-diethyladipate
- the raw materials were 2,5-tetraethyl-1,4-dihydro-2H-pyran-1-2-carboaldehyde '168.0 g (1.0 Omo 1), hydroxide hydroxide (Kanto Chemical Co., Ltd.) 99.0 g ( 3. Omo 1) and liquid paraffin 60 S (manufactured by Chuo Kasei Co., Ltd.) were changed to 200 g, and the same operation as in Example 1 was carried out to obtain 131 g of 2,5-getylazivic acid as white crystals (yield 65 %).
- an industrially suitable method for producing a branched adipic acid which is useful for applications such as a polyamide modifier, a polyester modifier, a cosmetic base, a polyester or a polyamide raw material, and the like.
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Abstract
Description
明 細 書 Specification
分岐アジピン酸の製造方法 Method for producing branched adipic acid
技術分野 Technical field
本発明は、 ポリアミド改質剤、 ポリエステル改質剤、化粧品基剤、 ポリエステル またはポリアミ ドの原料等の用途に有用である分岐アジピン酸の製造方法に関す る。 The present invention relates to a method for producing a branched adipic acid which is useful for applications such as a polyamide modifier, a polyester modifier, a cosmetic base, and a raw material of polyester or polyamide.
背景技術 Background art
従来、 分岐アジピン酸の製造方法として以下の①、 ②の方法が知られている。 Conventionally, the following methods (1) and (2) have been known as methods for producing branched adipic acid.
① 2 , 5—ジェチルアジピン酸の製造方法としては、 1 , 3—ブタジエンと金属ナ トリウムをジメチルエーテル中、 - 7 0 °Cで反応させた後、臭化マグネシウム;^よ び二酸化炭素を順次反応させ、 目的とする 2 , 5—ジェチルアジピン酸を製造する 方法が知られている (米国特許第 3 3 7 5 2 7 2号明細書参照) 。 (1) The method for producing 2,5-getyl adipic acid is as follows: 1,3-butadiene and sodium metal are reacted in dimethyl ether at -70 ° C, and magnesium bromide; There is known a method for producing the desired 2,5-getyl adipic acid by reacting (see US Pat. No. 3,375,272).
② 2 , 5—ジメチルアジビン酸の製造方法としては、 ジ tert—プチルパ一ォキサイ ド等の過酸化物を触媒として用い、 n—ノナン中、 プロピオン酸とアセチレンとを 1 2 0 °Cで反応させ、 目的とする 2, 5—ジメチルアジピン酸を製造する方法が知 られている (米国特許第 3 5 4 9 6 9 7号明細書参照) 。 (2) As a method for producing 2,5-dimethylazivic acid, a peroxide such as ditert-butylperoxide is used as a catalyst, and propionic acid and acetylene are reacted at 120 ° C in n-nonane. A method for producing the desired 2,5-dimethyladipic acid is known (see US Pat. No. 3,549,977).
しかしながら、① 2 , 5—ジェチルアジピン酸の製造方法の場合には、 金属ナト リウムを使用しており、 この化合物は、 自然発火性があり、水と反応して爆発する 等の性質を有しているため安全性上の問題がある。 However, in the case of the method for producing ①2,5-getyl adipic acid, sodium metal is used, and this compound has properties such as spontaneous combustion and explosion upon reaction with water. There are safety issues.
また、 ② 2, 5—ジメチルアジビン酸を製造する方法の場合には、 加熱、 衝撃等 により爆発する性質をもつ過酸ィ匕物および空気または酸素との混合により非常に 広い爆発限界を有するアセチレンを使用するため安全性上の問題がある。 (2) In the case of the method for producing 2,5-dimethylazivic acid, it has a very wide explosion limit due to mixing with air or oxygen and a peroxidic sulphate which has the property of exploding by heating, impact, etc. There are safety issues due to the use of acetylene.
以上のように、 これ ¾ 2.つの方法は、 工業的な製造方法としては、 実用上、 満足 される方法ではない。 As described above, these two methods are not practically satisfactory as industrial manufacturing methods.
発明の開示 Disclosure of the invention
本発明の目的は、分岐アジピン酸の工業的に適した製造方法を提供することにあ る。 An object of the present invention is to provide an industrially suitable method for producing a branched adipic acid.
本発明は、 以下の (1 )〜(3 ) を提供する。 The present invention provides the following (1) to (3).
( 1 ) 一般式 ( I ) (1) General formula (I)
(式中、 R R2、 R3、 R4、 R5および R6は、 同 または異なって水素原子ま たはアルキルを表し、 R7は、 ホルミルまたはヒドロキシメチルを表し、 は、 単結合または二重結合を表す。 ただし、 II1、 R2、 R3、 R4、 ; R5および R6 のうち少なくとも 1つは、 アルキルである)で表される化合物を、 アルカリ金属ま たはアル力リ土類金属の水酸化物の存在下、反応させる工程を含むことを特徴とす る一般式 (I I) (Wherein, RR 2 , R 3 , R 4 , R 5 and R 6 are the same or different and represent a hydrogen atom or alkyl, R 7 represents formyl or hydroxymethyl, and is a single bond or a double bond. Represents a heavy bond, provided that at least one of II 1 , R 2 , R 3 , R 4 ; R 5 and R 6 is alkyl) A general formula (II) characterized by including a step of reacting in the presence of a hydroxide of an alkaline earth metal.
R1 R2 R4 R6 R 1 R 2 R 4 R 6
HOOC— C—— C C C— COOH HOOC— C—— C C C— COOH
H R3 R5 H (Π) HR 3 R 5 H (Π)
(式中、 R R2、 R3、 R4、 : 5および R6 は、 それそれ前記と同義である) で 表される分岐アジピン酸の製造方法。 (Wherein, RR 2 , R 3 , R 4 , 5 and R 6 are each as defined above).
(2) R1および R6がアルキルであり、 R2、 R3、 R4および R5が水素原子であ る上記 (1)記載の分岐アジピン酸め製造方法。 (2) The method for producing a branched adipic acid according to the above (1), wherein R 1 and R 6 are alkyl and R 2 , R 3 , R 4 and R 5 are hydrogen atoms.
( 3 )アル力リ金属またはアル力リ土類金属の水酸化物が水酸化ナトリウムまたは 水酸化力リウムである上記( 1 )または( 2 )に記載の分岐アジピン酸の製造方法。 以下、 一般式 (I)で表される化合物を化合物 (I) と、 一般式 (I I)で表さ れる分岐アジピン酸を化合物 (I I) と表現することもある。 (3) The method for producing branched adipic acid according to the above (1) or (2), wherein the hydroxide of alkali metal or alkaline earth metal is sodium hydroxide or lithium hydroxide. Hereinafter, the compound represented by the general formula (I) may be referred to as a compound (I), and the branched adipic acid represented by the general formula (II) may be referred to as a compound (II).
一般式中の各基の定義において、アルキルとしては、例えば、炭素数 1〜 1◦の、 直鎖または分岐状のアルキルがあげられ、 その具体例としては、 メチル、 ェチル、 プロピル、 イソプロピル、 ブチル、 ィソブチル、 s e c—ブチル、 t e r t—ブチ ル、 ペンチル、 へキシル、 ヘプチル、 ォクチル、 ノニル、 デシル等があげられ、 中 でも、 メチルまたはェチルが好ましい。 In the definition of each group in the general formula, examples of the alkyl include linear or branched alkyl having 1 to 1 ° carbon atoms, and specific examples thereof include methyl, ethyl, propyl, isopropyl, and butyl. And isobutyl, sec-butyl, tert-butyl, pentyl, hexyl, heptyl, octyl, nonyl, decyl and the like, and among them, methyl or ethyl is preferable.
本発明の製造方法の原料である化合物 (I) は、 公知の方法 (米国特許第 2910520号等) またはこれら'に準じた方法により、例えば、 ァクロレイン誘 導体を環化するか、 または、 必要に応じて、得られたジヒドロピラン誘導体を水素 還元することにより得ることができる。 Compound (I), which is a raw material of the production method of the present invention, can be obtained by cyclizing an acrolein derivative by a known method (US Pat. Accordingly, the obtained dihydropyran derivative is converted to hydrogen It can be obtained by reduction.
アル力リ金属またはアル力リ土類金属の水酸化物としては、水酸化力リゥム、水 酸化ナトリウム、水酸化マグネシウム、水酸ィ匕カルシウム等があげられる。 これら は、 単独で、 または 2種類以上、 併用して使用してもよい。 Examples of hydroxides of alkaline metal or alkaline earth metals include hydroxide hydroxide, sodium hydroxide, magnesium hydroxide, calcium hydroxide, and the like. These may be used alone or in combination of two or more.
アル力リ金属またはアル力リ土類金属の水酸化物の使用量は、化合物( I ) 1モ ルに対して、 1 . 5モル以上であるのが好ましく、 さらには 1 . 5 ~ 5 . 0モルで あるのが好ましく、 さらにほ、 1 . 8〜3 . 0モルであるのがより好ましい。 ' 本発明の製造方法において、反応温度は、 2 0 0〜3 2 0 °Cであるのが好ましく、 さらには 2 0 0〜2 5 0 °Cであるのが好ましく、さらには 2 2 0〜2 5 0 °Cである のがより好ましい。 The amount of hydroxide of alkali metal or earth metal used is preferably 1.5 mol or more, more preferably 1.5 to 5.5 mol, per 1 mol of compound (I). It is preferably 0 mol, and more preferably 1.8 to 3.0 mol. '' In the production method of the present invention, the reaction temperature is preferably from 200 to 320 ° C, more preferably from 200 to 250 ° C, and further preferably from 220 to 250 ° C. More preferably, the temperature is 250 ° C.
反応は、 常圧または加圧条件下、 好ましくは 2 . O MP a以下、 より好ましくは 1 . O MP a以下で行われる。 The reaction is carried out at normal pressure or under pressure, preferably at most 2.0 MPa, more preferably at most 1.0 MPa.
反応時間は特に限定されないが、 5時間以上であることが好ましく、 5〜2 0時 間であるのがより好ましい。 The reaction time is not particularly limited, but is preferably 5 hours or more, and more preferably 5 to 20 hours.
反応において、反応溶媒を使用してもよく、該反応溶媒は、反応に影響をおよぼ さないものであれば、 特に限定されない。'該反応溶媒としては、例えば、 ジベンジ ルエーテル等のエーテル系溶媒、流動パラフィン等の炭化水素系溶媒等があげられ、 これらを混合して用いてもよい。反応溶媒の使用量は、 特に限定されないが、化合 物(I ) に対して、 好ましくは 5 0〜2 0 0重量%、 より好ましくは 7 0〜1 5 0 重量%である。 ' In the reaction, a reaction solvent may be used, and the reaction solvent is not particularly limited as long as it does not affect the reaction. Examples of the reaction solvent include ether solvents such as dibenzyl ether, hydrocarbon solvents such as liquid paraffin, and the like, and these may be used as a mixture. The amount of the reaction solvent is not particularly limited, but is preferably 50 to 200% by weight, more preferably 70 to 150% by weight, based on the compound (I). '
また、反応時間の短縮や収率の向上を目的として、酸化亜鉛や酸化銅等の金属酸 化物等を触媒として添加して反応を行ってもよい。該触媒の使用量は、化合物( I ) に対して、 0 . 1〜 5重量%であるのが好ましい。 ' Further, for the purpose of shortening the reaction time and improving the yield, the reaction may be performed by adding a metal oxide such as zinc oxide or copper oxide as a catalyst. The amount of the catalyst to be used is preferably 0.1 to 5% by weight based on the compound (I). '
反応後、化合物(I I ) は、 アルカリ金属またはアルカリ土類金属の塩の形態で 得られるが、 これに、硫酸、塩酸等の水溶液等を加えることにより、化合物(I I ) を得ることができる。 After the reaction, the compound (II) can be obtained in the form of a salt of an alkali metal or an alkaline earth metal. The compound (II) can be obtained by adding an aqueous solution of sulfuric acid, hydrochloric acid or the like thereto.
また、得られた化合物( I I )は、その純度を向上させるために、反応液等から、 抽出、 晶析、 蒸留等の精製操作に付してもよい。 The obtained compound (II) may be subjected to a purification operation such as extraction, crystallization, or distillation from the reaction solution or the like in order to improve the purity.
本発明の製造方法は、簡易であり、 安価であり、 安全性にも優れる、 工業的に適 した製造方法である。 化合物(I I) は、 ポリアミド改質剤、 ポリエステル改質剤、 化粧品基剤、 ポリ エステルまたはポリアミドの原料等の用途に有用である。 The production method of the present invention is an industrially suitable production method that is simple, inexpensive, and excellent in safety. Compound (II) is useful for applications such as polyamide modifiers, polyester modifiers, cosmetic bases, and raw materials for polyesters or polyamides.
発明を実施するための最良の形態 BEST MODE FOR CARRYING OUT THE INVENTION
実施例 1 : 2 , 5—ジェチルアジピン酸の合成 Example 1: Synthesis of 2,5-getyl adipic acid
2, 5—ジェチル一 3, 4—ジヒドロ一 2H—ピラン一 2—メタノール 2,5-Jetyl-1,3,4-dihydro-1H-pyran-1-2-methanol
.170. 0 g (1. 0mo l) 、 水酸化ナトリウム (関東化学株式会社製) 170. 0 g (2. 4mo 1 )および流動パラフィン 60 S (中央化成株式会社製) 200 gを還流器、圧力コントロール弁および温度コントロール可能な電熱炉を備 えた 1 Lニッケル製ォ一トクレーブに仕込み、 1. 0 MP a以下で加熱攪拌した。 発生する水素ガスをガスメ一夕一で測定し、反応の進行をチェックしながら 220 〜230°Cにて、 10時間反応させた。反応後、 2, 5—ジェチルアジピン酸ニナ トリウム塩を含む反応液を 100°C以下まで冷却し、 蒸留水 400 gに溶解させ、 さらに 30 %硫酸 420 gを滴下することにより析出した粗 2 , 5—ジェチルアジ ピン酵を濾取した。得られた粗 2, 5ージェチルアジピン酸をメチルイソブチルケ トン 300 m 1に溶解し、水洗後、 60 °Cにて減圧濃縮することにより 2, 5—ジ ェチルアジピン酸を含む残渣 183 gを得た。この残渣を n—へキサンより結晶化 することにより、 白色結晶の 2, 5—ジェチルアジピン酸 170 g (収率 85%) を得た。得られた 2, 5—ジェチルアジピン酸の物性値を以下に示す。 .170.0 g (1.0 mol), sodium hydroxide (manufactured by Kanto Chemical Co., Ltd.) 170.0 g (2.4 mol 1) and liquid paraffin 60 S (manufactured by Chuo Kasei Co., Ltd.) 200 g It was charged into a 1 L nickel autoclave equipped with a pressure control valve and an electric furnace capable of controlling the temperature, and heated and stirred at 1.0 MPa or less. The generated hydrogen gas was measured overnight, and the reaction was carried out at 220 to 230 ° C. for 10 hours while checking the progress of the reaction. After the reaction, the reaction solution containing 2,5-getyl sodium adipic acid salt was cooled to 100 ° C or less, dissolved in 400 g of distilled water, and further precipitated by adding dropwise 420 g of 30% sulfuric acid. , 5-Jetyl adipine yeast was collected by filtration. The obtained crude 2,5-diethyladipate was dissolved in 300 ml of methyl isobutyl ketone, washed with water, and concentrated under reduced pressure at 60 ° C to obtain 183 g of a residue containing 2,5-diethyladipate. Obtained. The residue was crystallized from n-hexane to obtain 170 g (yield: 85%) of white crystals of 2,5-getyladipic acid. The physical property values of the obtained 2,5-getyladipic acid are shown below.
^-NM (400MHz、 CDC 13、 TMS) δ ( iii) : 0. 90 (t, 6H) 、 1. 48— 1. 63 (m, 8H) 、 2. 23 - 2, 25 (m, 2 H) 13C - NMR ( 100MHz、 CDC 13、 TMS) δ ( m) : 1 1. 92、 25. 81、 30. 38、 47. 55、 177. 23 ^ -NM (400MHz, CDC 1 3 , TMS) δ (iii): 0. 90 (t, 6H), 1. 48- 1. 63 (m, 8H), 2. 23 - 2, 25 (m, 2 H) 13 C - NMR (100MHz , CDC 1 3, TMS) δ (m): 1 1. 92, 25. 81, 30. 38, 47. 55, 177. 23
GC-MS (CI) : (ジメチルエステル体へと誘導した後、 分析) GC-MS (CI): (Analysis after derivation to dimethyl ester)
保持時間 8. 50分 (m/z) : 230 (M+ 1) Retention time 8.50 minutes (m / z): 230 (M + 1)
保持時間 8. 60分 (m/z) : 230 (M+ 1) Retention time 8.60 minutes (m / z): 230 (M + 1)
GC—MS分析条件およびジメチルエステル体調製法 GC-MS analysis conditions and dimethyl ester preparation method
カラム:キヤビラリ一カラム CP- Wax 58 (FFAP) CB (GLサイエンス社 製) (25mx0.2 m) Column: Capillary column CP-Wax 58 (FFAP) CB (GL Science) (25mx0.2m)
カラム温度: 100°Cで 1分保持後、 8°C/分で 270°Cまで昇温 ■ . Column temperature: After holding at 100 ° C for 1 minute, raise the temperature to 270 ° C at 8 ° C / min.
注入温度: 270°C 検出器温度: 280°C Injection temperature: 270 ° C Detector temperature: 280 ° C
サンプルをベンゼン /メタノール (3/7容量/容量) 溶液に溶解後、 トリメチル シリルジァゾメタン (10%n—へキサン,溶液) を加え室温で 30分間、 攪拌する ことによりジメチルエステル体溶液を調製した。 After dissolving the sample in a benzene / methanol (3/7 volume / volume) solution, add trimethylsilyldiazomethane (10% n-hexane, solution) and stir at room temperature for 30 minutes to remove the dimethyl ester solution. Prepared.
実施例 2 : 2, 5—ジェチルアジピン酸の合成 Example 2: Synthesis of 2,5-getyladipate
原料を 2, 5—ジェチルテトラヒドロピラン一 2—メタノール 172. 0 g (1. Omo 1)、 水酸化カリウム (関東化学株式会社製) 99. 0 g (3. 0 mo 1)および流動パラフィン 60 S (中央化成株式会社製) 200 gに変更する 以外は実施例' 1と同様な操作を行い、 白色結晶の 2, 5—ジェチルアジピン酸 158 g (収率 79%) を得た。 ' 実施例 3 : 2, 5—ジェチルアジピン酸の合成 The starting materials were 2,5-diethyltetrahydropyran-1-methanol 172.0 g (1. Omo 1), potassium hydroxide (manufactured by Kanto Chemical Co., Ltd.) 99.0 g (3.0 mo 1) and liquid paraffin 60 The same operation as in Example '1 was carried out except that S (manufactured by Chuo Kasei Co., Ltd.) was changed to 200 g, to give 158 g (yield 79%) of white crystals of 2,5-getyladipic acid. '' Example 3: Synthesis of 2,5-diethyladipate
原料を 2, 5—ジェチル一 3, 4—ジヒドロー 2 H—ピラン一 2—カルボアルデ ヒド' 168. 0 g ( 1. Omo 1)、 水酸化力リウム (関東化学株式会社製) 99. 0 g (3. Omo 1) および流動パラフィン 60 S (中央化成株式会社製) 200 gに変更する以外は実施例 1と同様な操作を行い、 白色結晶の 2 , 5—ジェ チルアジビン酸 131 g (収率 65%) を得た。 The raw materials were 2,5-tetraethyl-1,4-dihydro-2H-pyran-1-2-carboaldehyde '168.0 g (1.0 Omo 1), hydroxide hydroxide (Kanto Chemical Co., Ltd.) 99.0 g ( 3. Omo 1) and liquid paraffin 60 S (manufactured by Chuo Kasei Co., Ltd.) were changed to 200 g, and the same operation as in Example 1 was carried out to obtain 131 g of 2,5-getylazivic acid as white crystals (yield 65 %).
参考例 1 : 2, 5—ジェチルー 3, 4—ジヒドロ— 2 H—ピラン一 2—カルボアル デヒドの合成 Reference Example 1: Synthesis of 2,5-diethyl-3,4-dihydro-2H-pyran-1-2-carbaldehyde
攪拌チヅプを入れた内容積 10 Omlのォートクレーブに 2—ェチルァク口レ イン 50g (Aldri c h社製、 純度 85%)を加え、 150〜160°Cにて 8 時間反応させた。 次いで、 反応液を減圧蒸留に付すことにより、 82〜84°C/ 50 Paの留分として 2, 5—ジェチル一 3, 4—ジヒドロー 2 H—ピラン一 2— カルボアルデヒド 36. 8 gが得られた (収率 87%) 。 To an autoclave having an internal volume of 10 Oml and containing a stirring chip was added 50 g of 2-ethyl acetate (Aldrich, purity: 85%), and the mixture was reacted at 150 to 160 ° C for 8 hours. Then, the reaction mixture was subjected to distillation under reduced pressure to obtain 36.8 g of 2,5-getyl-1,3,4-dihydro-2H-pyran-1-carbaldehyde as a fraction at 82 to 84 ° C./50 Pa. (Yield 87%).
参考例 2 : 23 5—ジェチルテ.トラヒドロピラン一 2—メタノールの合成 Reference Example 2:. 2 3 5 Jechirute synthesis tiger tetrahydropyran one 2- methanol
攪拌チヅプを入れた内容積 10 Omlのォ一トクレーブに、 2, 5—ジェチル一 3, 4—ジヒドロ一 2 H—ピラン一 2—カルボアルデヒド 10. Ogおよびスポン ジニッケル触媒(日揮化学株式会社製 N—113) 0. 3 gを加え、 水素圧 2. 0 MPa、 温度 150°Cで、 6時間、 反応させた。反応終了後、 反応液よりスポンジ 二ッケル触媒を濾別し、得られた濾液をシリカゲルカラムクロマトグラフィー [溶 媒: n—へキサン/酢酸ェチル二 9ノ1 (容量比) ] に付すことにより、 2, 5- ジェチルテトラヒドロピラン一 2—メタノール 9.8 gが得られた(収率 98%)o 参考例 3 : 2, 5—ジェチル一 3, 4—ジヒドロ一 2 H—ピラン一 2—メタノール の合成 In a photoclave containing a stirring chip and having an internal volume of 10 Oml, 2,5-dimethyl-1,3,4-dihydro-12H-pyran-12-carbaldehyde 10. Og and sponge nickel catalyst (Nikki Chemical Co., Ltd. —113) 0.3 g was added, and the mixture was reacted at a hydrogen pressure of 2.0 MPa and a temperature of 150 ° C for 6 hours. After the completion of the reaction, the sponge nickel catalyst was filtered off from the reaction solution, and the obtained filtrate was subjected to silica gel column chromatography [solvent: n-hexane / ethyl acetate (volume ratio)] to give a solution. twenty five- 9.8 g of getyltetrahydropyran-12-methanol was obtained (98% yield) .o Reference Example 3: Synthesis of 2,5-diethyl-1,3,4-dihydro-12H-pyran-12-methanol
攪拌チヅプ¾入れた内容積 100mlのオートクレープに、 2, 5—ジェチル一 3, 4ージヒドロ一 2 H—ピラン一 2—カルボアルデヒド 10. 0 §"ぉょぴ〇11ー 〇 系触媒 (11八1 311八^"製、 0202 P) 0. 5 gを加え、 水素圧 2. 0 MP a、温度 130 °Cで 5時間反応させた。反応終了後、 反応液より C u— C r系 触媒を濾別し、得られた濾液をシリカゲルカラムクロマトグラフィー [溶媒: n— へキサン/酢酸ェチル =9Z1 (容量比) ] に付すことにより、 2, 5—ジェチル 一 3, 4—ジヒドロ一2H—ピラン一 2—メタノール 9. 6 gが得られた (収率 95%) 。 In a 100 ml autoclave containing a stirring chip, 2,5-diethyl-1,3,4-dihydro-1 2 H-pyran-1-carbaldehyde 10.0 § "ぉ 11-〇-based catalyst (118 0.52 g, manufactured by 1 311 octane ", and reacted at a hydrogen pressure of 2.0 MPa and a temperature of 130 ° C. for 5 hours. After completion of the reaction, the Cu—Cr system catalyst was separated from the reaction solution by filtration, and the obtained filtrate was subjected to silica gel column chromatography [solvent: n-hexane / ethyl acetate = 9Z1 (volume ratio)]. 9.6 g of 2,5-diethyl-1,3,4-dihydro-1H-pyran-12-methanol was obtained (yield 95%).
産業上の利用可能性 Industrial applicability
本発明により、 ポリアミ ド改質剤、 ポリエステル改質剤、 化粧品基剤、 ポリエス テルまたはポリアミ ドの原料等の用途に有用である分岐アジピン酸の工業的に適 した製造方法が提供される。 According to the present invention, there is provided an industrially suitable method for producing a branched adipic acid which is useful for applications such as a polyamide modifier, a polyester modifier, a cosmetic base, a polyester or a polyamide raw material, and the like.
Claims
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2005504918A JPWO2004069780A1 (en) | 2003-02-10 | 2004-02-10 | Process for producing branched adipic acid |
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| JP2003-032090 | 2003-02-10 | ||
| JP2003032090 | 2003-02-10 |
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| WO2004069780A1 true WO2004069780A1 (en) | 2004-08-19 |
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| PCT/JP2004/001403 Ceased WO2004069780A1 (en) | 2003-02-10 | 2004-02-10 | Process for production of adipic acids having side chains |
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| JP (1) | JPWO2004069780A1 (en) |
| TW (1) | TW200418753A (en) |
| WO (1) | WO2004069780A1 (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2008080613A1 (en) * | 2006-12-29 | 2008-07-10 | Abbott Laboratories Vascular Enterprises Limited | Medical devices comprising a modified polyamide |
| US8389646B2 (en) | 2007-05-10 | 2013-03-05 | Abbott Laboratories Vascular Enterprises Limited | Medical devices comprising a co-polymer of a modified polyamide and a polycarbonate |
| US8492484B2 (en) | 2007-05-10 | 2013-07-23 | Abbott Laboratories Vascular Enterprises Limited | Medical devices comprising a co-polymer of a polyamide and a polycarbonate diamine |
Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH07258148A (en) * | 1994-03-23 | 1995-10-09 | Kuraray Co Ltd | Method for producing 3-methylglutaric acid |
| JPH10316610A (en) * | 1997-05-13 | 1998-12-02 | Daicel Chem Ind Ltd | Oxidation of ethers |
-
2004
- 2004-02-09 TW TW93102889A patent/TW200418753A/en unknown
- 2004-02-10 JP JP2005504918A patent/JPWO2004069780A1/en not_active Withdrawn
- 2004-02-10 WO PCT/JP2004/001403 patent/WO2004069780A1/en not_active Ceased
Patent Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH07258148A (en) * | 1994-03-23 | 1995-10-09 | Kuraray Co Ltd | Method for producing 3-methylglutaric acid |
| JPH10316610A (en) * | 1997-05-13 | 1998-12-02 | Daicel Chem Ind Ltd | Oxidation of ethers |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2008080613A1 (en) * | 2006-12-29 | 2008-07-10 | Abbott Laboratories Vascular Enterprises Limited | Medical devices comprising a modified polyamide |
| US8304498B2 (en) | 2006-12-29 | 2012-11-06 | Abbott Laboratories Vascular Enterprises Limited | Medical devices comprising a modified polyamide |
| CN101611075B (en) * | 2006-12-29 | 2014-06-25 | 雅培血管企业有限公司 | Medical devices containing modified polyamides |
| US8389646B2 (en) | 2007-05-10 | 2013-03-05 | Abbott Laboratories Vascular Enterprises Limited | Medical devices comprising a co-polymer of a modified polyamide and a polycarbonate |
| US8492484B2 (en) | 2007-05-10 | 2013-07-23 | Abbott Laboratories Vascular Enterprises Limited | Medical devices comprising a co-polymer of a polyamide and a polycarbonate diamine |
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| Publication number | Publication date |
|---|---|
| JPWO2004069780A1 (en) | 2006-05-25 |
| TW200418753A (en) | 2004-10-01 |
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