JPH0530821B2 - - Google Patents
Info
- Publication number
- JPH0530821B2 JPH0530821B2 JP28727889A JP28727889A JPH0530821B2 JP H0530821 B2 JPH0530821 B2 JP H0530821B2 JP 28727889 A JP28727889 A JP 28727889A JP 28727889 A JP28727889 A JP 28727889A JP H0530821 B2 JPH0530821 B2 JP H0530821B2
- Authority
- JP
- Japan
- Prior art keywords
- reaction
- vinyl acetate
- compound
- alkali
- acetylation reaction
- 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 - Fee Related
Links
- XTXRWKRVRITETP-UHFFFAOYSA-N Vinyl acetate Chemical compound CC(=O)OC=C XTXRWKRVRITETP-UHFFFAOYSA-N 0.000 claims description 21
- -1 acetyl compound Chemical class 0.000 claims description 21
- 238000006640 acetylation reaction Methods 0.000 claims description 21
- 238000000034 method Methods 0.000 claims description 18
- 150000002989 phenols Chemical class 0.000 claims description 17
- 239000003513 alkali Substances 0.000 claims description 15
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 11
- 239000002904 solvent Substances 0.000 claims description 9
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 claims description 6
- IAZDPXIOMUYVGZ-UHFFFAOYSA-N Dimethylsulphoxide Chemical compound CS(C)=O IAZDPXIOMUYVGZ-UHFFFAOYSA-N 0.000 claims description 6
- ZMXDDKWLCZADIW-UHFFFAOYSA-N N,N-Dimethylformamide Chemical compound CN(C)C=O ZMXDDKWLCZADIW-UHFFFAOYSA-N 0.000 claims description 6
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 claims description 6
- 125000002887 hydroxy group Chemical group [H]O* 0.000 claims description 6
- 238000006386 neutralization reaction Methods 0.000 claims description 6
- 229910052700 potassium Inorganic materials 0.000 claims description 6
- 239000011591 potassium Substances 0.000 claims description 6
- ISWSIDIOOBJBQZ-UHFFFAOYSA-N Phenol Chemical compound OC1=CC=CC=C1 ISWSIDIOOBJBQZ-UHFFFAOYSA-N 0.000 claims description 5
- 150000003839 salts Chemical class 0.000 claims description 5
- 238000000926 separation method Methods 0.000 claims description 4
- IKHGUXGNUITLKF-XPULMUKRSA-N acetaldehyde Chemical compound [14CH]([14CH3])=O IKHGUXGNUITLKF-XPULMUKRSA-N 0.000 claims description 3
- 229910021529 ammonia Inorganic materials 0.000 claims description 3
- 239000007788 liquid Substances 0.000 claims description 3
- 238000004519 manufacturing process Methods 0.000 claims description 3
- 238000001953 recrystallisation Methods 0.000 claims description 3
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 claims description 2
- WHXSMMKQMYFTQS-UHFFFAOYSA-N Lithium Chemical compound [Li] WHXSMMKQMYFTQS-UHFFFAOYSA-N 0.000 claims description 2
- FXHOOIRPVKKKFG-UHFFFAOYSA-N N,N-Dimethylacetamide Chemical compound CN(C)C(C)=O FXHOOIRPVKKKFG-UHFFFAOYSA-N 0.000 claims description 2
- 229910052728 basic metal Inorganic materials 0.000 claims description 2
- 125000003178 carboxy group Chemical group [H]OC(*)=O 0.000 claims description 2
- 125000001309 chloro group Chemical group Cl* 0.000 claims description 2
- 229910052744 lithium Inorganic materials 0.000 claims description 2
- 230000000737 periodic effect Effects 0.000 claims description 2
- 229910052701 rubidium Inorganic materials 0.000 claims description 2
- IGLNJRXAVVLDKE-UHFFFAOYSA-N rubidium atom Chemical compound [Rb] IGLNJRXAVVLDKE-UHFFFAOYSA-N 0.000 claims description 2
- 229910052708 sodium Inorganic materials 0.000 claims description 2
- 239000011734 sodium Substances 0.000 claims description 2
- BVKZGUZCCUSVTD-UHFFFAOYSA-L Carbonate Chemical compound [O-]C([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-L 0.000 claims 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-M hydroxide Chemical compound [OH-] XLYOFNOQVPJJNP-UHFFFAOYSA-M 0.000 claims 1
- 230000003472 neutralizing effect Effects 0.000 claims 1
- 238000000746 purification Methods 0.000 claims 1
- 238000006243 chemical reaction Methods 0.000 description 26
- WFDIJRYMOXRFFG-UHFFFAOYSA-N Acetic anhydride Chemical compound CC(=O)OC(C)=O WFDIJRYMOXRFFG-UHFFFAOYSA-N 0.000 description 18
- 239000002253 acid Substances 0.000 description 8
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 description 6
- KWYUFKZDYYNOTN-UHFFFAOYSA-M Potassium hydroxide Chemical compound [OH-].[K+] KWYUFKZDYYNOTN-UHFFFAOYSA-M 0.000 description 6
- 230000002378 acidificating effect Effects 0.000 description 6
- 239000012345 acetylating agent Substances 0.000 description 5
- IKHGUXGNUITLKF-UHFFFAOYSA-N Acetaldehyde Chemical compound CC=O IKHGUXGNUITLKF-UHFFFAOYSA-N 0.000 description 4
- 239000003518 caustics Substances 0.000 description 4
- 230000000694 effects Effects 0.000 description 4
- 239000000203 mixture Substances 0.000 description 4
- 125000000218 acetic acid group Chemical group C(C)(=O)* 0.000 description 3
- 239000006227 byproduct Substances 0.000 description 3
- 239000007795 chemical reaction product Substances 0.000 description 3
- 238000003756 stirring Methods 0.000 description 3
- DNIAPMSPPWPWGF-GSVOUGTGSA-N (R)-(-)-Propylene glycol Chemical class C[C@@H](O)CO DNIAPMSPPWPWGF-GSVOUGTGSA-N 0.000 description 2
- WETWJCDKMRHUPV-UHFFFAOYSA-N acetyl chloride Chemical compound CC(Cl)=O WETWJCDKMRHUPV-UHFFFAOYSA-N 0.000 description 2
- 239000012346 acetyl chloride Substances 0.000 description 2
- 238000007796 conventional method Methods 0.000 description 2
- 238000005260 corrosion Methods 0.000 description 2
- 230000007797 corrosion Effects 0.000 description 2
- 239000013078 crystal Substances 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 235000011118 potassium hydroxide Nutrition 0.000 description 2
- 239000000047 product Substances 0.000 description 2
- QTBSBXVTEAMEQO-UHFFFAOYSA-M Acetate Chemical compound CC([O-])=O QTBSBXVTEAMEQO-UHFFFAOYSA-M 0.000 description 1
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 1
- 229920002472 Starch Polymers 0.000 description 1
- GSEJCLTVZPLZKY-UHFFFAOYSA-N Triethanolamine Chemical compound OCCN(CCO)CCO GSEJCLTVZPLZKY-UHFFFAOYSA-N 0.000 description 1
- 230000000397 acetylating effect Effects 0.000 description 1
- 230000021736 acetylation Effects 0.000 description 1
- 125000003118 aryl group Chemical group 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 150000004649 carbonic acid derivatives Chemical class 0.000 description 1
- 239000003054 catalyst Substances 0.000 description 1
- 238000002425 crystallisation Methods 0.000 description 1
- 230000008025 crystallization Effects 0.000 description 1
- 238000004821 distillation Methods 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- IXCSERBJSXMMFS-UHFFFAOYSA-N hydrogen chloride Substances Cl.Cl IXCSERBJSXMMFS-UHFFFAOYSA-N 0.000 description 1
- 229910000041 hydrogen chloride Inorganic materials 0.000 description 1
- 230000007062 hydrolysis Effects 0.000 description 1
- 238000006460 hydrolysis reaction Methods 0.000 description 1
- 150000004679 hydroxides Chemical class 0.000 description 1
- 230000007935 neutral effect Effects 0.000 description 1
- 230000009972 noncorrosive effect Effects 0.000 description 1
- 150000002894 organic compounds Chemical class 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 235000019698 starch Nutrition 0.000 description 1
- 238000003786 synthesis reaction Methods 0.000 description 1
Landscapes
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Description
産業上の利用分野
本発明は酢酸ビニルをアセチル化剤としてフエ
ノール類化合物をアセチル化してアセチル化合
物、即ち、芳香族の酢酸エステルを製造する方法
に関する。この方法は簡便、迅速、低温でアセチ
ル化し、従来の無水酢酸または塩化アセチルを使
用し、そして酸性反応生成物を生成する方法に比
べて、耐腐食性反応設備を不要にする利点があ
る。
従来の技術
これまで、酢酸ビニルを使用したアセチル化反
応は澱粉類のアセチル化反応の文献(米国特許第
3022189号、同第3081296号、同第3318868号、同
第4038482号、同第2731496号)に見られるが、こ
の酸性ヒドロキシ基を持つフエノール類化合物の
アセチル反応の記述はなく、この優れた効果を応
用した例は未だ文献に発表されていない。
発明が解決しようとする課題
フエノール類化合物と一般の脂肪族アルコール
類化合物とがやゝ異なるところは、両者とも同じ
ようにヒドロキシ基を含んでいるが、前者は電離
されて酸性を帯び、故に、ヒドロキシ基のアセチ
ル化反応は脂肪族アルコール類化合物よりも困難
であることが知られている。より高い反応温度
と、より強酸性触媒を必要とし、このために反応
装置の材質の要求も過酷な条件を必要とし、生成
物の成分も複雑となる。
工業用でもつとも用いられるアセチル化剤は無
水酢酸と塩化アセチルが主であり、この2種類共
に水分に敏感で後者がもつとも甚だしく、故に加
水分解を避けなければならない。反応後前者は1
モルの酢酸を生成し、後者は塩化水素を生成し、
前者は蒸留によつて分離しなければならない。故
に、設備費用がかゝり、後者は水分による装置の
厳重な腐食性および公害を非常に注意しなければ
ならない。
課題を解決するための手段
本発明者等は、従来の欠点を克服すべく検討し
た結果、フエノール類化合物をアルカリで中和し
て塩にし、160℃以下の温度で酢酸ビニルを用い
てアセチル化反応させることにより、アセチル化
合物を効率よく製造する方法を見いだし、本発明
を完成させたものである。
本発明は酢酸ビニルの使用により、反応後の副
産物には腐食性はなく、揮発性のアセトアルデヒ
ドとなる。アセトアルデヒドは簡単に主要生成物
から分離できるほか、回収して多くの有機化合物
の合成に使用される。
反応中、このフエノール類化合物の酸性を抑制
するために、先にアルカリでフエノール類化合物
を中和してヒドロキシ塩にしてその親核性を増
し、更に中性酢酸ビニルエステルの反応能力を増
すため、結果において大部分のフエノール類化合
物は効率よく対応するアセチル化合物に導くこと
ができる。
本発明は、アセチル化反応するにあたり、ま
ず、フエノール類化合物をアルカリで中和するも
のである。
本発明のフエノール化合物としては、フエノー
ル以外に、例えば、クロル基、ヒドロキシ基、カ
ルボキシ基を有するフエノールを用いることがで
きる。使用することができるアルカリとしては、
周期律表の第族の塩基性金属塩、即ち、リチウ
ム、ナトリウム、カリウム、ルビジウムの水酸化
物または炭酸塩、および有機アミン化合物あるい
はアンモニア等を挙げることができる。中和に使
用するアルカリとフエノール類化合物のモル比は
0.5ないし2.5であることが好ましい。
アセチル化反応の際の酢酸ビニルの使用量は、
フエノール類化合物に対してモル比で1:10、好
ましくは、1:5の範囲を選ぶことができる。
アセチル化反応は溶媒中で行うことが好まし
く、例えば、水、ジメチルスルホキシド
(DMSO)、ジメチルホルムアミド、ジメチルア
セトアミド等を使用することができる。反応を行
うにあたつて、溶媒とフエノール類化合物との重
量比は2ないし8であることが好ましい。アセチ
ル化反応を行うには、反応温度は前述した如く
160℃以下、0℃以上であり、反応をより効率よ
く行うには、10℃ないし110℃、より好ましくは、
20℃ないし70℃の反応温度で行われる。反応はま
た、加圧下で行うことが望ましく、1ないし10気
圧、より好ましくは、1ないし3気圧を選択する
ことである。
以上の如くして生成されるアセチル化合物は、
副成されるアセトアルデヒドを蒸発させることに
より、また、水等の溶媒と固液分離により分離、
再結晶することで精製し、取得することができ
る。
例えば、第1図に示すような装置を配置して、
反応から取得までを実施することができる。
この装置において、フエノール類化合物とアル
カリとは、中和タンクN1にて塩を形成し、反応
タンクR1に送られ、酢酸ビニルと混ざりアセチ
ル化反応が行われる。副成するアセトアルデヒド
は、熱交換器E1およびE2を経て回収される。
一方、得られた粗アセチル化合物は、中和タンク
(沈殿タンク)N2に送られて、サンでアルカリ
を取り除かれ、遠心分離器S1にて固液分離した
後、再結晶のために結晶タンクC1に導かれ、そ
の結晶を遠心分離器S2にて分離し、精製アセチ
ル化合物として得ることができる。
実施例
以下、実施例により本発明を更に詳しく説明す
る。因に、実施例1はアセチル化剤としての酢酸
ビニルと無水酢酸との反応率と選択率について比
較を行つたものである。また、実施例2、実施例
3、実施例4および実施例5は、それぞれ酢酸ビ
ニルの使用量、アルカリおよびその使用量と水の
使用量に対する反応の影響について示したもので
ある。更に、実施例6は、水、その他の溶媒で試
みた場合、実施例7は、フエノールおよび他のフ
エノール類化合物を用いた場合の結果を示すもの
である。
実施例 1
酢酸ビニルと無水酢酸を別々にアセチル化剤と
して使用し、パラオキシ安息香酸のアセチル化反
応を観察した。反応条件は以下の通りである。
酢酸ビニル:100gのパラオキシ安息香酸と81g
の苛性カリを400mlの水に撹拌しながら加え、
均一に溶解後、酢酸ビニル80mlを加え22時間反
応した。
無水酢酸:100gのパラオキシ安息香酸に120mlの
酢酸と120mlの無水酢酸を加え、125〜130℃で
撹拌しながら2時間反応した。
表1にこの2種類のアセチル化剤の反応結果を
示す。
INDUSTRIAL APPLICATION FIELD The present invention relates to a method for producing an acetyl compound, that is, an aromatic acetate, by acetylating a phenol compound using vinyl acetate as an acetylating agent. This method is simple, rapid, performs acetylation at low temperatures, and has the advantage of eliminating the need for corrosion-resistant reaction equipment over conventional methods that use acetic anhydride or acetyl chloride and produce acidic reaction products. Conventional technology Until now, the acetylation reaction using vinyl acetate has been reported in the literature on the acetylation reaction of starches (US Patent No.
No. 3022189, No. 3081296, No. 3318868, No. 4038482, No. 2731496), but there is no description of the acetyl reaction of phenolic compounds having this acidic hydroxyl group, and there is no description of this excellent effect. Application examples have not yet been published in the literature. Problems to be Solved by the Invention The difference between phenolic compounds and general aliphatic alcohol compounds is that both contain hydroxy groups in the same way, but the former are ionized and become acidic, so It is known that the acetylation reaction of hydroxy groups is more difficult than that of aliphatic alcohol compounds. They require higher reaction temperatures and stronger acidic catalysts, which require harsher reactor material requirements and result in more complex product compositions. The acetylating agents that are commonly used in industry are mainly acetic anhydride and acetyl chloride, both of which are sensitive to moisture, and the latter is extremely sensitive to moisture, so hydrolysis must be avoided. The former is 1 after the reaction
produces moles of acetic acid, the latter produces hydrogen chloride,
The former must be separated by distillation. Therefore, the equipment costs are high, and the latter must be very careful about the severe corrosion and pollution of the equipment due to moisture. Means for Solving the Problems As a result of studies to overcome the conventional drawbacks, the present inventors neutralized a phenol compound with an alkali to form a salt, and acetylated it using vinyl acetate at a temperature of 160°C or less. The present invention was completed by discovering a method for efficiently producing acetyl compounds through reaction. Due to the use of vinyl acetate in the present invention, the by-product after the reaction is non-corrosive and becomes volatile acetaldehyde. Acetaldehyde is easily separated from the main product and can be recovered and used in the synthesis of many organic compounds. During the reaction, in order to suppress the acidity of this phenolic compound, the phenolic compound is first neutralized with an alkali and converted into a hydroxy salt to increase its nucleophilicity, and further to increase the reaction ability of the neutral vinyl acetate ester. As a result, most of the phenolic compounds can be efficiently converted to the corresponding acetyl compounds. In the present invention, a phenol compound is first neutralized with an alkali in carrying out an acetylation reaction. As the phenol compound of the present invention, in addition to phenol, for example, phenol having a chloro group, a hydroxy group, or a carboxy group can be used. Alkali that can be used include:
Mention may be made of basic metal salts of group of the periodic table, ie, hydroxides or carbonates of lithium, sodium, potassium, rubidium, and organic amine compounds or ammonia. The molar ratio of alkali and phenolic compounds used for neutralization is
It is preferably 0.5 to 2.5. The amount of vinyl acetate used in the acetylation reaction is
The molar ratio to the phenolic compound can be selected in the range of 1:10, preferably 1:5. The acetylation reaction is preferably carried out in a solvent, and for example, water, dimethyl sulfoxide (DMSO), dimethylformamide, dimethylacetamide, etc. can be used. In carrying out the reaction, the weight ratio of the solvent to the phenolic compound is preferably 2 to 8. To carry out the acetylation reaction, the reaction temperature is as described above.
The temperature is 160°C or lower and 0°C or higher, and in order to carry out the reaction more efficiently, the temperature is 10°C to 110°C, more preferably,
The reaction temperature is 20°C to 70°C. The reaction is also desirably carried out under pressure, with a pressure of 1 to 10 atm, more preferably 1 to 3 atm being selected. The acetyl compound produced as above is
By evaporating the by-produced acetaldehyde, and separating it from solvents such as water by solid-liquid separation,
It can be purified and obtained by recrystallization. For example, by arranging a device as shown in Figure 1,
It is possible to carry out everything from reaction to acquisition. In this apparatus, the phenol compound and the alkali form a salt in the neutralization tank N1, and the salt is sent to the reaction tank R1, where it is mixed with vinyl acetate and subjected to an acetylation reaction. Acetaldehyde, which is produced as a by-product, is recovered via heat exchangers E1 and E2.
On the other hand, the obtained crude acetyl compound is sent to a neutralization tank (precipitation tank) N2, the alkali is removed with a sanator, and after solid-liquid separation is performed in a centrifuge S1, crystallization tank C1 is used for recrystallization. The crystals can be separated in a centrifuge S2 to obtain a purified acetyl compound. Examples Hereinafter, the present invention will be explained in more detail with reference to Examples. Incidentally, in Example 1, the reaction rate and selectivity of vinyl acetate and acetic anhydride as acetylating agents were compared. In addition, Examples 2, 3, 4, and 5 show the influence of the reaction on the amount of vinyl acetate used, the amount of alkali used, and the amount of water used, respectively. Furthermore, Example 6 shows the results when water and other solvents were used, and Example 7 shows the results when phenol and other phenolic compounds were used. Example 1 Vinyl acetate and acetic anhydride were used separately as acetylating agents, and the acetylation reaction of paraoxybenzoic acid was observed. The reaction conditions are as follows. Vinyl acetate: 100g paraoxybenzoic acid and 81g
of caustic potash is added to 400 ml of water with stirring,
After uniformly dissolving, 80 ml of vinyl acetate was added and reacted for 22 hours. Acetic anhydride: 120 ml of acetic acid and 120 ml of acetic anhydride were added to 100 g of paraoxybenzoic acid, and the mixture was reacted for 2 hours with stirring at 125-130°C. Table 1 shows the reaction results of these two types of acetylating agents.
【表】
実施例 2
100gのパラオキシ安息香酸と81gの苛性カリ
を400mlの水を加えて溶かし、酢酸ビニルを加え
て2時間反応した。表2に酢酸ビニル使用量と反
応の影響を示す。[Table] Example 2 100 g of paraoxybenzoic acid and 81 g of caustic potassium were dissolved in 400 ml of water, vinyl acetate was added, and the mixture was reacted for 2 hours. Table 2 shows the amount of vinyl acetate used and the influence of the reaction.
【表】
実施例 3
100gのパラオキシ安息香酸と表3のモル比の
苛性カリを加え、400mlの水に溶解した後、200ml
の酢酸ビニルを加えて2時間反応した。表3にア
ルカリ使用量と反応の影響を示す。[Table] Example 3 Add 100g of paraoxybenzoic acid and caustic potassium in the molar ratio shown in Table 3, dissolve in 400ml of water, and then add 200ml of
of vinyl acetate was added and reacted for 2 hours. Table 3 shows the amount of alkali used and the influence of the reaction.
【表】
実施例 4
パラオキシ安息香酸と各種のアルカリについて
実施例2と同様に行つた。表4にアルカリの種類
と反応の影響を示す。[Table] Example 4 The same procedure as in Example 2 was conducted using paraoxybenzoic acid and various alkalis. Table 4 shows the type of alkali and its influence on the reaction.
【表】
実施例 5
100gのパラオキシ安息香酸と81gの苛性カリ
に表5の通りの量の水を加え撹拌して溶解した
後、200mlの酢酸ビニルを加えて2時間反応した。
表5に水量と反応の影響を示す。[Table] Example 5 100 g of paraoxybenzoic acid and 81 g of caustic potassium were added to water in the amount shown in Table 5 and dissolved by stirring, and then 200 ml of vinyl acetate was added and reacted for 2 hours.
Table 5 shows the influence of water amount and reaction.
【表】
実施例 6
100gのパラオキシ安息香酸と120mlのトリエタ
ノールアミンを各種の溶剤にそれぞれ溶かし、
328ml酢酸ビニルと反応した。表6に各種溶剤に
対するアセチル化反応の影響を示す。[Table] Example 6 Dissolve 100g of paraoxybenzoic acid and 120ml of triethanolamine in various solvents,
Reacted with 328ml vinyl acetate. Table 6 shows the influence of acetylation reactions on various solvents.
【表】
実施例 7
各種のフエノール化合物(1モル)と表7の量
の苛性カリを加え、苛性カリの4倍量の水を加え
て溶かし、これに1.2モルの酢酸ビニルを加えて
室温で反応した。表7に各フエノール化合物のア
セチル化反応の結果を示す。[Table] Example 7 Various phenol compounds (1 mol) and the amount of caustic potassium shown in Table 7 were added, 4 times the amount of water as the amount of caustic potash was added to dissolve it, 1.2 mol of vinyl acetate was added thereto, and the mixture was reacted at room temperature. . Table 7 shows the results of the acetylation reaction of each phenol compound.
【表】
発明の効果
本発明の第1の効果は、低温でフエノール類化
合物のアセチル化反応が進行させることができる
ことにある。
本発明の第2の効果は、アセチル化反応が簡便
で反応生成物が反応条件下で分離でき、従来の方
法におけるような不要な酸性副産物を生成しない
ことである。
第3の効果は、低温反応条件と非酸性反応生成
物のため、設備に高価な材料を必要としないこと
である。
このような効果は工業的に実施する場合におい
て非常に有利な条件である。[Table] Effects of the Invention The first effect of the present invention is that the acetylation reaction of phenolic compounds can proceed at low temperatures. A second advantage of the present invention is that the acetylation reaction is simple, the reaction products can be separated under the reaction conditions, and unnecessary acidic by-products are not produced as in conventional methods. The third advantage is that the equipment does not require expensive materials due to the low temperature reaction conditions and non-acidic reaction products. Such effects are very advantageous conditions for industrial implementation.
第1図は本発明の方法を実施するための製造方
法の例を示すフローチヤート。
E1,E2……熱交換器、R1……反応タン
ク、N1……中和タンク、S1,S2……遠心分
離器、C……結晶タンク。
FIG. 1 is a flowchart showing an example of a manufacturing method for carrying out the method of the present invention. E1, E2... Heat exchanger, R1... Reaction tank, N1... Neutralization tank, S1, S2... Centrifugal separator, C... Crystal tank.
Claims (1)
にし、160℃以下の温度で酢酸ビニルを用いてア
セチル化反応させることを特徴とするアセチル化
合物の製造方法。 2 アセチル化反応を10℃ないし110℃で行う請
求項1記載の方法。 3 アセチル化反応を20℃ないし70℃で行う請求
項1記載の方法。 4 アセチル化反応を1ないし10気圧下で行う請
求項1記載の方法。 5 アセチル化反応を1ないし3気圧下で行う請
求項1記載の方法。 6 使用する酢酸ビニル対フエノール類化合物の
モル比を1:10にて行う請求項1記載の方法。 7 使用する酢酸ビニル対フエノール類化合物の
モル比を1:5にて行う請求項1記載の方法。 8 使用するアルカリが周期律表の第族の塩基
性金属塩、有機アミン化合物またはアンモニアで
ある請求項1記載の方法。 9 使用するアルカリがリチウム、ナトリウム、
カリウム、ルビジウムの水酸化物もしくは炭酸塩
またはアンモニアである請求項1記載の方法。 10 中和に使用するアルカリとフエノール類化
合物のモル比が0.5ないし2.5である請求項1記載
の方法。 11 中和およびアセチル化反応を溶媒中で行う
請求項1記載の方法。 12 溶剤が水、ジメチルスルホキシド、ジメチ
ルホルムアミド、ジメチルアセトアミドである請
求項1記載の方法。 13 溶媒に対するフエノール類化合物の重量比
が2ないし8である請求項11記載の方法。 14 フエノール類化合物がフエノールまたはク
ロル基、ヒドロキシ基、カルボキシ基を有するフ
エノールである請求項1記載の方法。 15 フエノール類化合物をアルカリで中和して
塩にし、160℃以下の温度で酢酸ビニルを用いて
アセチル化反応させ、副成したアセトアルデヒド
を蒸発、分離し、生成物のアセチル化合物を固液
分離により分離、再結晶し、精製することを特徴
とするアセチル化合物の取得方法。[Scope of Claims] 1. A method for producing an acetyl compound, which comprises neutralizing a phenol compound with an alkali to form a salt, and subjecting it to an acetylation reaction using vinyl acetate at a temperature of 160° C. or lower. 2. The method according to claim 1, wherein the acetylation reaction is carried out at 10°C to 110°C. 3. The method according to claim 1, wherein the acetylation reaction is carried out at 20°C to 70°C. 4. The method according to claim 1, wherein the acetylation reaction is carried out under 1 to 10 atmospheres. 5. The method according to claim 1, wherein the acetylation reaction is carried out under 1 to 3 atmospheres. 6. The method according to claim 1, wherein the molar ratio of vinyl acetate to phenolic compound used is 1:10. 7. The method according to claim 1, wherein the molar ratio of vinyl acetate to phenolic compound used is 1:5. 8. The method according to claim 1, wherein the alkali used is a basic metal salt of group of the periodic table, an organic amine compound or ammonia. 9 The alkali used is lithium, sodium,
2. The method according to claim 1, wherein the hydroxide or carbonate of potassium, rubidium or ammonia is used. 10. The method according to claim 1, wherein the molar ratio of the alkali and phenolic compound used for neutralization is 0.5 to 2.5. 11. The method according to claim 1, wherein the neutralization and acetylation reactions are carried out in a solvent. 12. The method according to claim 1, wherein the solvent is water, dimethylsulfoxide, dimethylformamide, or dimethylacetamide. 13. The method according to claim 11, wherein the weight ratio of the phenolic compound to the solvent is from 2 to 8. 14. The method according to claim 1, wherein the phenolic compound is phenol or a phenol having a chloro group, a hydroxy group, or a carboxy group. 15 Neutralize the phenolic compound with an alkali to form a salt, perform an acetylation reaction using vinyl acetate at a temperature below 160°C, evaporate and separate the by-produced acetaldehyde, and separate the acetyl compound as a product by solid-liquid separation. A method for obtaining an acetyl compound, characterized by separation, recrystallization, and purification.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP28727889A JPH03153647A (en) | 1989-11-02 | 1989-11-02 | Preparation and aquisition of acetyl compound |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP28727889A JPH03153647A (en) | 1989-11-02 | 1989-11-02 | Preparation and aquisition of acetyl compound |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH03153647A JPH03153647A (en) | 1991-07-01 |
| JPH0530821B2 true JPH0530821B2 (en) | 1993-05-11 |
Family
ID=17715332
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP28727889A Granted JPH03153647A (en) | 1989-11-02 | 1989-11-02 | Preparation and aquisition of acetyl compound |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH03153647A (en) |
-
1989
- 1989-11-02 JP JP28727889A patent/JPH03153647A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPH03153647A (en) | 1991-07-01 |
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