JPH0211565A - Preparation of metachloroperbenzoic acid - Google Patents
Preparation of metachloroperbenzoic acidInfo
- Publication number
- JPH0211565A JPH0211565A JP16444988A JP16444988A JPH0211565A JP H0211565 A JPH0211565 A JP H0211565A JP 16444988 A JP16444988 A JP 16444988A JP 16444988 A JP16444988 A JP 16444988A JP H0211565 A JPH0211565 A JP H0211565A
- Authority
- JP
- Japan
- Prior art keywords
- peroxide
- reaction
- metachlorobenzoyl
- alcohol
- inert 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.)
- Granted
Links
- LULAYUGMBFYYEX-UHFFFAOYSA-N metachloroperbenzoic acid Natural products OC(=O)C1=CC=CC(Cl)=C1 LULAYUGMBFYYEX-UHFFFAOYSA-N 0.000 title claims abstract description 41
- NHQDETIJWKXCTC-UHFFFAOYSA-N 3-chloroperbenzoic acid Chemical compound OOC(=O)C1=CC=CC(Cl)=C1 NHQDETIJWKXCTC-UHFFFAOYSA-N 0.000 title claims description 18
- 238000002360 preparation method Methods 0.000 title description 2
- YMWUJEATGCHHMB-UHFFFAOYSA-N Dichloromethane Chemical compound ClCCl YMWUJEATGCHHMB-UHFFFAOYSA-N 0.000 claims abstract description 30
- 238000006243 chemical reaction Methods 0.000 claims abstract description 30
- MHAJPDPJQMAIIY-UHFFFAOYSA-N Hydrogen peroxide Chemical compound OO MHAJPDPJQMAIIY-UHFFFAOYSA-N 0.000 claims abstract description 23
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims abstract description 20
- 150000008044 alkali metal hydroxides Chemical class 0.000 claims abstract description 12
- 239000012442 inert solvent Substances 0.000 claims abstract description 6
- 239000008346 aqueous phase Substances 0.000 claims abstract description 5
- XSTXAVWGXDQKEL-UHFFFAOYSA-N Trichloroethylene Chemical group ClC=C(Cl)Cl XSTXAVWGXDQKEL-UHFFFAOYSA-N 0.000 claims abstract description 3
- UBOXGVDOUJQMTN-UHFFFAOYSA-N trichloroethylene Natural products ClCC(Cl)Cl UBOXGVDOUJQMTN-UHFFFAOYSA-N 0.000 claims abstract description 3
- 125000003236 benzoyl group Chemical group [H]C1=C([H])C([H])=C(C([H])=C1[H])C(*)=O 0.000 claims description 13
- HEDRZPFGACZZDS-UHFFFAOYSA-N Chloroform Chemical compound ClC(Cl)Cl HEDRZPFGACZZDS-UHFFFAOYSA-N 0.000 claims description 6
- 238000000034 method Methods 0.000 claims description 6
- 238000004519 manufacturing process Methods 0.000 claims description 4
- VZGDMQKNWNREIO-UHFFFAOYSA-N tetrachloromethane Chemical compound ClC(Cl)(Cl)Cl VZGDMQKNWNREIO-UHFFFAOYSA-N 0.000 claims description 4
- 238000002156 mixing Methods 0.000 claims description 3
- SCYULBFZEHDVBN-UHFFFAOYSA-N 1,1-Dichloroethane Chemical compound CC(Cl)Cl SCYULBFZEHDVBN-UHFFFAOYSA-N 0.000 claims description 2
- 150000008282 halocarbons Chemical class 0.000 claims description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims 1
- 229910052799 carbon Inorganic materials 0.000 claims 1
- 150000002978 peroxides Chemical class 0.000 abstract description 19
- 239000000047 product Substances 0.000 abstract description 19
- 239000002904 solvent Substances 0.000 abstract description 8
- 150000001875 compounds Chemical class 0.000 abstract description 5
- 239000006227 byproduct Substances 0.000 abstract description 2
- FKLJPTJMIBLJAV-UHFFFAOYSA-N Compound IV Chemical compound O1N=C(C)C=C1CCCCCCCOC1=CC=C(C=2OCCN=2)C=C1 FKLJPTJMIBLJAV-UHFFFAOYSA-N 0.000 abstract 1
- 239000000203 mixture Substances 0.000 abstract 1
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 24
- KWYUFKZDYYNOTN-UHFFFAOYSA-M Potassium hydroxide Chemical compound [OH-].[K+] KWYUFKZDYYNOTN-UHFFFAOYSA-M 0.000 description 18
- DKGAVHZHDRPRBM-UHFFFAOYSA-N Tert-Butanol Chemical compound CC(C)(C)O DKGAVHZHDRPRBM-UHFFFAOYSA-N 0.000 description 14
- 230000000052 comparative effect Effects 0.000 description 11
- -1 methyl metachlorobenzoate Chemical compound 0.000 description 11
- 150000004965 peroxy acids Chemical class 0.000 description 7
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 6
- 238000004458 analytical method Methods 0.000 description 6
- 239000000243 solution Substances 0.000 description 6
- 239000003381 stabilizer Substances 0.000 description 6
- 239000007864 aqueous solution Substances 0.000 description 5
- 239000013078 crystal Substances 0.000 description 5
- CSNNHWWHGAXBCP-UHFFFAOYSA-L Magnesium sulfate Chemical compound [Mg+2].[O-][S+2]([O-])([O-])[O-] CSNNHWWHGAXBCP-UHFFFAOYSA-L 0.000 description 4
- 238000005516 engineering process Methods 0.000 description 4
- 230000035484 reaction time Effects 0.000 description 4
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 description 3
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 description 3
- 125000004432 carbon atom Chemical group C* 0.000 description 3
- 239000007806 chemical reaction intermediate Substances 0.000 description 3
- 230000007423 decrease Effects 0.000 description 3
- 239000002994 raw material Substances 0.000 description 3
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 2
- LRHPLDYGYMQRHN-UHFFFAOYSA-N N-Butanol Chemical compound CCCCO LRHPLDYGYMQRHN-UHFFFAOYSA-N 0.000 description 2
- KFSLWBXXFJQRDL-UHFFFAOYSA-N Peracetic acid Chemical compound CC(=O)OO KFSLWBXXFJQRDL-UHFFFAOYSA-N 0.000 description 2
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- 239000007844 bleaching agent Substances 0.000 description 2
- 238000009835 boiling Methods 0.000 description 2
- 238000001816 cooling Methods 0.000 description 2
- XPPKVPWEQAFLFU-UHFFFAOYSA-N diphosphoric acid Chemical compound OP(O)(=O)OP(O)(O)=O XPPKVPWEQAFLFU-UHFFFAOYSA-N 0.000 description 2
- 238000004821 distillation Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 150000002148 esters Chemical class 0.000 description 2
- 229910052943 magnesium sulfate Inorganic materials 0.000 description 2
- 235000019341 magnesium sulphate Nutrition 0.000 description 2
- 125000005395 methacrylic acid group Chemical group 0.000 description 2
- 150000004967 organic peroxy acids Chemical class 0.000 description 2
- 238000007254 oxidation reaction Methods 0.000 description 2
- 238000003786 synthesis reaction Methods 0.000 description 2
- GLVYLTSKTCWWJR-UHFFFAOYSA-N 2-carbonoperoxoylbenzoic acid Chemical compound OOC(=O)C1=CC=CC=C1C(O)=O GLVYLTSKTCWWJR-UHFFFAOYSA-N 0.000 description 1
- WHIHIKVIWVIIER-UHFFFAOYSA-N 3-chlorobenzoyl chloride Chemical compound ClC(=O)C1=CC=CC(Cl)=C1 WHIHIKVIWVIIER-UHFFFAOYSA-N 0.000 description 1
- NSXJEEMTGWMJPY-UHFFFAOYSA-N 9-[3-(3-carbazol-9-ylphenyl)phenyl]carbazole Chemical compound C12=CC=CC=C2C2=CC=CC=C2N1C1=CC(C=2C=CC=C(C=2)N2C3=CC=CC=C3C3=CC=CC=C32)=CC=C1 NSXJEEMTGWMJPY-UHFFFAOYSA-N 0.000 description 1
- 239000004342 Benzoyl peroxide Substances 0.000 description 1
- OMPJBNCRMGITSC-UHFFFAOYSA-N Benzoylperoxide Chemical compound C=1C=CC=CC=1C(=O)OOC(=O)C1=CC=CC=C1 OMPJBNCRMGITSC-UHFFFAOYSA-N 0.000 description 1
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 1
- CERQOIWHTDAKMF-UHFFFAOYSA-N Methacrylic acid Chemical compound CC(=C)C(O)=O CERQOIWHTDAKMF-UHFFFAOYSA-N 0.000 description 1
- CTQNGGLPUBDAKN-UHFFFAOYSA-N O-Xylene Chemical compound CC1=CC=CC=C1C CTQNGGLPUBDAKN-UHFFFAOYSA-N 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 230000002378 acidificating effect Effects 0.000 description 1
- 239000003905 agrochemical Substances 0.000 description 1
- 150000004945 aromatic hydrocarbons Chemical class 0.000 description 1
- 235000019400 benzoyl peroxide Nutrition 0.000 description 1
- 239000012295 chemical reaction liquid Substances 0.000 description 1
- 239000003153 chemical reaction reagent Substances 0.000 description 1
- 238000004587 chromatography analysis Methods 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- CVTVRXGPXQVJAU-UHFFFAOYSA-N dioxiran-3-ol Chemical compound OC1OO1 CVTVRXGPXQVJAU-UHFFFAOYSA-N 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 238000006735 epoxidation reaction Methods 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 239000012847 fine chemical Substances 0.000 description 1
- 238000007710 freezing Methods 0.000 description 1
- 230000008014 freezing Effects 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 239000000543 intermediate Substances 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- CERQOIWHTDAKMF-UHFFFAOYSA-M methacrylate group Chemical group C(C(=C)C)(=O)[O-] CERQOIWHTDAKMF-UHFFFAOYSA-M 0.000 description 1
- 125000002496 methyl group Chemical group [H]C([H])([H])* 0.000 description 1
- MGFYIUFZLHCRTH-UHFFFAOYSA-N nitrilotriacetic acid Chemical compound OC(=O)CN(CC(O)=O)CC(O)=O MGFYIUFZLHCRTH-UHFFFAOYSA-N 0.000 description 1
- 239000012071 phase Substances 0.000 description 1
- 230000009257 reactivity Effects 0.000 description 1
- 238000004904 shortening Methods 0.000 description 1
- 238000007086 side reaction Methods 0.000 description 1
- 230000001629 suppression Effects 0.000 description 1
- 239000008096 xylene Substances 0.000 description 1
Landscapes
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
Description
【発明の詳細な説明】
(産業上の利用分野)
有機過酸の中でも特にメタクロロ過安息香酸は有機合成
反応においてエポキシ化反応、バイヤー・ビリガー酸化
反応、N−オキシド化等に使用することができ医・農薬
等の精密化学品から、!l化剤、漂白剤として広く用い
られている。又、有機過酸の多くは不安定であり長期間
の保存が出来ないのに対して、メタクロロ過安息香酸は
室温下でも非常に安定な結晶であるため取り扱いがし易
く。[Detailed Description of the Invention] (Industrial Application Field) Among organic peracids, metachloroperbenzoic acid can be used in organic synthesis reactions, such as epoxidation reactions, Bayer-Villiger oxidation reactions, and N-oxidation reactions. From fine chemicals such as medicine and agricultural chemicals! It is widely used as a bleaching agent and a bleaching agent. Additionally, many organic peracids are unstable and cannot be stored for long periods of time, whereas metachloroperbenzoic acid is a very stable crystal even at room temperature, making it easy to handle.
室温下で保管しても数ケ月間は純度低下がほとんどない
、又、その反応性においても、過酢酸、モノ過フタル酸
などに比較して数々の利点が見出されている6以上2本
発明はメタクロロ過安息香酸の製造技術を確立し、広く
一般に供しようとするものである。There is almost no decrease in purity even when stored at room temperature for several months, and in terms of reactivity, numerous advantages have been found compared to peracetic acid, monoperphthalic acid, etc. The purpose of the invention is to establish a technology for producing metachloroperbenzoic acid and to make it widely available to the public.
(従来の技術)
メタクロロ安息香酸クロライドを原料とするメタクロロ
過安息香酸の製造技術に関しては米国特許jI3231
605号、3232979号、3485869号等にお
いてメタクロロ安息香酸クロライドをt−ブチルアルコ
ールの存在下で過酸化水素、水酸化ナトリウム又は水酸
化カリウムと反応することにより得られるとされている
。上記いずれの特許もt−ブチルアルコールを使用する
点に特徴があり減圧留去してt−ブチルアルコールを除
き製品を得ている。しかしながらt−ブチルアルコール
の沸点は82.5℃(760mmHg)と高く、融点も
25.6℃であるため熱的に不安定な反応液である過酸
水溶液からt−ブチルアルコールを留去することは危険
又は困難を伴う、又。(Prior art) Regarding the production technology of metachloroperbenzoic acid using metachlorobenzoic acid chloride as a raw material, US Patent jI3231
No. 605, No. 3232979, No. 3485869, etc., it is said that it is obtained by reacting metachlorobenzoic acid chloride with hydrogen peroxide, sodium hydroxide, or potassium hydroxide in the presence of t-butyl alcohol. All of the above patents are characterized in that t-butyl alcohol is used, and products are obtained by removing t-butyl alcohol by distillation under reduced pressure. However, t-butyl alcohol has a high boiling point of 82.5°C (760 mmHg) and a melting point of 25.6°C, so it is difficult to distill t-butyl alcohol from a peracid aqueous solution, which is a thermally unstable reaction liquid. involves danger or difficulty;
米国特許13462480号においては生成した過酸が
不安定であるためニトリロトリ#酸のような特殊な安定
剤の存在下に当該過酸を製造するとしている。又、ソ連
国の文献Zh、 P r i k 1 。In US Pat. No. 1,346,2480, since the peracid produced is unstable, the peracid is produced in the presence of a special stabilizer such as nitrilotriacid. Also, Soviet literature Zh, P r i k 1.
Khim、、1986.59 (2)、388−91に
おいても安定剤であるオキシエチリデンニリン酸の存在
下で反応条件を検討し過酸純度85〜90%の製品を得
たとの報告があるが、製品中に反応中間体であるメタク
ロロ過酸化ベンゾイルが含まれるとされている。Khim, 1986.59 (2), 388-91 also reported that the reaction conditions were investigated in the presence of oxyethylidene diphosphoric acid as a stabilizer and a product with a peracid purity of 85 to 90% was obtained. The product is said to contain benzoyl metachloroperoxide, a reaction intermediate.
(発明が解決しようとする問題点)
即ち、従来の技術においては過酸が反応液中で不安定で
ある為、特殊な安定剤を添加する必要があり、又、多量
にアルコールを使用することによりメタクロロ安息香酸
のエステルが生成し、収率が低下するばかりではなく、
a品の純度を低下させる問題がある。又、従来の技術に
おいては使用しているアルコールの沸点が高かったり、
凝固点が高かったりして、アルコールの留去に危険を伴
う等の問題がある。(Problems to be solved by the invention) That is, in the conventional technology, since peracid is unstable in the reaction solution, it is necessary to add a special stabilizer, and a large amount of alcohol is used. This not only results in the formation of esters of metachlorobenzoic acid, but also reduces the yield.
There is a problem of lowering the purity of product a. In addition, in conventional technology, the boiling point of the alcohol used is high,
There are problems such as the high freezing point, which makes it dangerous to distill off the alcohol.
(問題点を解決するための手段及び作用)本発明者らは
前述の問題点を解決する方法を鋭意研究した結果、メタ
クロロ安息香酸クロライド(1)をアルカリ金属水酸化
物(II)、過酸化水素(■)、炭素数3以下のアルコ
ール(rV)及びメタクロロ過酸化ベンゾイルの可溶な
不活性溶剤を混合して反応する際に(ff): (1
)を2.5:1から5.5:1のモル比で使用し、
(III) :(1)を4=1から6:1のモル比で
使用し(IV)を水性相に対し25〜50重景%使重量
、ft応湿温度5〜25℃反応することを特徴とするメ
タクロロ過安息香酸の製造方法を見出し本発明を完成す
るに至った。(Means and effects for solving the problems) As a result of intensive research into methods for solving the above-mentioned problems, the present inventors found that metachlorobenzoic acid chloride (1) was converted into alkali metal hydroxide (II), peroxidized When reacting by mixing hydrogen (■), an alcohol having 3 or less carbon atoms (rV), and an inert solvent in which metachlorobenzoyl peroxide is soluble (ff): (1
) in a molar ratio of 2.5:1 to 5.5:1,
(III): (1) is used in a molar ratio of 4=1 to 6:1, and (IV) is used in an amount of 25 to 50% by weight with respect to the aqueous phase, and the reaction temperature is 5 to 25°C. The inventors discovered a characteristic method for producing metachloroperbenzoic acid and completed the present invention.
以下アルカリ金属水酸化物として水酸化カリウム、炭素
数3以下のアルコールとしてメタノールを使用した場合
について反応式を記述して本発明をさらに詳しく説明す
る。The present invention will be described in more detail below by describing a reaction formula for the case where potassium hydroxide is used as the alkali metal hydroxide and methanol is used as the alcohol having 3 or less carbon atoms.
2 CI C,H4C0C1+ 2 KOH+H,
0x(1) (n) CII
I)→CI CmH4C0−00−OCCaH4Cl(
メタクロロ過酸化ベンゾイル)
+2 K Cl + 2 Hz○ ・・・(A)CI
CaH4G O−00−OCCaHaC1+2KO
H+H!0.−)2CIC,H,C0−00に+2H,
O・ ・ (B)
副反応
CI Ca H4COCl + CH10H+ K O
H→CI Ca H4CO−OCHl + K Cl
+ H! 0(メタクロロ安息香酸メチル) ・・
・ (C)メタクロロ過安息香酸は反応(A)、(B)
式をへて合成されていることは公知であり式(A)。2 CI C, H4C0C1+ 2 KOH+H,
0x(1) (n) CII
I)→CI CmH4C0-00-OCCaH4Cl(
benzoyl metachloroperoxide) +2 K Cl + 2 Hz○ ... (A) CI
CaH4G O-00-OCCaHaC1+2KO
H+H! 0. -) 2CIC, H, +2H to C0-00,
O・・(B) Side reaction CI Ca H4COCl + CH10H+ K O
H→CI Ca H4CO-OCHL + K Cl
+H! 0 (methyl metachlorobenzoate)...
・(C) Metachloroperbenzoic acid reacts with (A) and (B)
It is known that the compound is synthesized through the formula (A).
(B)よりメタクロロ安息香酸クロライドに対する水酸
カリウム及び過酸化水素の理論モル比は(III):
(ff): (1)=1:2:1である。又。From (B), the theoretical molar ratio of potassium hydroxide and hydrogen peroxide to metachlorobenzoic acid chloride is (III):
(ff): (1)=1:2:1. or.
(B)式の反応においてはアルコール存在下でないと当
量的に反応が進行しにくいことは過安息香酸の例におい
て文献Tetrahedron、23.3327 (1
967)に記載がある。ところがメタクロロ過安息香酸
の合成反応においてアルコールのみを添加した場合には
製品中に反応中間体であるメタクロロ過酸化ベンゾイル
が数%残存してくる。これはメタクロロ過酸化ベンゾイ
ルが水性反応液に不溶で厘応しにくい為である。そこで
本発明ではメタクロロ過酸化ベンゾイルの可溶な溶媒で
かつ反応液中で不活性なものを添加することにより、製
品中へ残存するメタクロロ過酸化ベンゾイル量を減少し
得ることを見出した。又。In the reaction of formula (B), it is difficult to proceed equivalently unless in the presence of an alcohol, as shown in the literature Tetrahedron, 23.3327 (1
967). However, when only alcohol is added in the synthesis reaction of metachloroperbenzoic acid, several percent of benzoyl metachloroperoxide, which is a reaction intermediate, remains in the product. This is because benzoyl metachloroperoxide is insoluble and difficult to react with the aqueous reaction solution. Therefore, in the present invention, it has been discovered that the amount of metachlorobenzoyl peroxide remaining in the product can be reduced by adding a solvent in which metachlorobenzoyl peroxide is soluble and inert in the reaction solution. or.
同時にアルコール添加量もψなく出来る為、副圧力(C
)式も進行しにりく、副生成物であるメタクロロ安息香
酸メチル等のエステルの生成も抑制出来る1次に本発明
においてはメタクロロ安息香酸クロライド(1)に対す
るアルカリ金属水酸化物(n)及び過酸化水素(III
)のモル比を理論値に対していずれも過剰量で下記の特
定範囲、すなわち(n): (1)=2.5: 1か
ら5.5:1のモル比となるアルカリ金属水酸化物を眉
い。At the same time, since the amount of alcohol added can be done without ψ, the secondary pressure (C
) formula is slow to proceed, and the formation of esters such as methyl metachlorobenzoate, which are by-products, can be suppressed.Firstly, in the present invention, the alkali metal hydroxide (n) and peroxide relative to metachlorobenzoic acid chloride (1) can be suppressed. Hydrogen oxide (III
) of an alkali metal hydroxide having a molar ratio in the following specific range in excess of the theoretical value, that is, (n): (1) = 2.5: 1 to 5.5: 1. frowned.
(III): (1)=4 : 1から6=1のモル
比となる過酸化水素を用いることにより、取率向上、w
J生成物の抑利2厘応時間の原線等の本発明の目的が達
成出来る。又、ここでいう炭素数3以下のアルコールと
はメタノール、エタノール又はプロパツールを言い、添
加量としては反応液中の水性相の25〜50重量%使用
することで目的は達成出来る。又、前述のメタクロロ過
酸化ベンゾイルの可溶な溶媒とはジクロロメタン、クロ
ロホルム。(III): By using hydrogen peroxide at a molar ratio of (1)=4:1 to 6=1, the yield can be improved, w
The objectives of the present invention, such as the suppression of the J product and the raw material of the reaction time, can be achieved. Moreover, the alcohol having 3 or less carbon atoms here refers to methanol, ethanol, or propatool, and the purpose can be achieved by using the alcohol in an amount of 25 to 50% by weight of the aqueous phase in the reaction solution. Further, the solvents in which benzoyl metachloroperoxide is soluble are dichloromethane and chloroform.
四塩化炭素、ジクロロエタン、トリクロロエチレンなど
のハロゲン化炭化水素類、又はベンゼン。Halogenated hydrocarbons such as carbon tetrachloride, dichloroethane, trichloroethylene, or benzene.
トルエン、キシレンなどの芳瞥族炭化水素票が上げられ
る。メタクロロ過酸化ベンゾイルに対する溶解性や溶媒
留去の容易性の面から添加量としては上記アルコールの
添加量よりも若干多く使用すれば本発明の目的は達成出
来る。又、従来から特に問題とされていた過酸の安定剤
はニトリロトリ酢酸やオキシエチリデンニリン酸のごと
き特殊な安定剤を使用しなくても安価で手に入る硫酸マ
グネシウムなどで十分である。この理由は2本発明がメ
タクロロ安息香酸クロライドに対して十分過剰量のアル
カリ金属水酸化物及び過酸化水素を使用している点とメ
タクロロ過酸化ベンゾイルの可溶な溶媒を添加している
為、短時間で反応を終了することが出来る為と思われる
0本発明者らの検討によると従来から知られた反応方法
においてはメタクロロ過酸化ベンゾイルが反応液に溶解
しにくい為9式(B)の反応が遅くメタクロロ過酸化ベ
ンゾイルの残存量を2%以下とする為には数時間反応す
る必要があり、その間に過酸が分解して純度低下を起こ
す、又2本発明においては反応中間体であるメタクロロ
過酸化ベンゾイルが溶剤により可溶化さ九ているため反
応時間は短くてすむ。Aromatic hydrocarbons such as toluene and xylene are cited. The object of the present invention can be achieved if the amount of alcohol added is slightly larger than the amount of alcohol mentioned above in terms of solubility in benzoyl metachloroperoxide and ease of solvent distillation. In addition, as a stabilizer for peracid, which has been a particular problem in the past, magnesium sulfate, which is available at low cost, is sufficient without using special stabilizers such as nitrilotriacetic acid or oxyethylidene diphosphoric acid. This is because the present invention uses a sufficiently excessive amount of alkali metal hydroxide and hydrogen peroxide relative to metachlorobenzoyl chloride, and the addition of a solvent in which metachlorobenzoyl peroxide is soluble. This seems to be because the reaction can be completed in a short time.According to the study by the present inventors, in the conventionally known reaction method, benzoyl metachloroperoxide is difficult to dissolve in the reaction solution, so the reaction of Formula 9 (B) The reaction is slow and it is necessary to react for several hours in order to reduce the residual amount of metachlorobenzoyl peroxide to 2% or less, during which time the peracid decomposes and causes a decrease in purity. Since some metachlorobenzoyl peroxide is solubilized by the solvent, the reaction time is short.
例えば反応時間2〜4時間の間にメタクロロ過酸化ベン
ゾイル残量は2%以下となり1反応がほぼ完結している
ことが分る。For example, during the reaction time of 2 to 4 hours, the remaining amount of benzoyl metachloroperoxide becomes 2% or less, indicating that one reaction is almost completed.
(発明の効果)
本発明のメタクロロ過安息香酸の製造方法は前述のごと
く構成されている為、以下に示すようないくつかの利点
を有している。(Effects of the Invention) Since the method for producing metachloroperbenzoic acid of the present invention is configured as described above, it has several advantages as shown below.
第一は本発明においては反応中間体であるメタクロロ過
酸化ベンゾイルの可溶な溶媒を添加しているため、高収
率で而も短い時間で反応を終了できる。又、そのために
特殊な安定剤を添加する必要もない。First, in the present invention, since a solvent in which benzoyl metachloroperoxide, which is a reaction intermediate, is soluble is added, the reaction can be completed in a high yield and in a short time. Moreover, there is no need to add special stabilizers for this purpose.
第二ハメタクロロ過酸化ベンゾイルの可溶な溶媒の添加
により、アルコール使用量を従来知られた方法に比較し
て減少することが出来たため、メタクロロ安息香酸エス
テルの削成を大幅に抑制出来る。By adding a solvent in which secondary metachlorobenzoyl peroxide is soluble, the amount of alcohol used can be reduced compared to conventionally known methods, and therefore the removal of metachlorobenzoic acid ester can be significantly suppressed.
第三は反応試剤の使用量を特定範囲で行なうと収率向上
、W1生戒物の抑制1反応時間の短縮等の本発明の目的
が達成出来る。Thirdly, by using the amount of the reaction reagent within a specific range, the objectives of the present invention, such as improving the yield, suppressing W1 raw materials, and shortening the reaction time, can be achieved.
第四はt−ブチルアルコールを使用していない為に、t
−ブチルアルコールの留去に伴う危険性等の問題がない
。Fourth, since t-butyl alcohol is not used, t-butyl alcohol is not used.
- There are no problems such as danger associated with distilling off butyl alcohol.
(実施例)
次に実施例及び比較例を挙げて説明するが、いずれも例
示のためのものであって本発明をそれらのみに限定する
ものではない。(Example) Next, an example and a comparative example will be given and explained, but all are for illustrative purposes and the present invention is not limited to them.
(実施例1)
温度計、かくはん機(パドル式3枚羽根)及び冷却用バ
スを備えたILのフラスコに30%水酸化カリウム水溶
液70.5g、35%過酸化水素水溶液61.1g+ジ
クロロメタン70g*メタノール46g及び硫酸マグネ
シウム0.5gを混合し10℃に冷却した後メタクロロ
安息香酸クロライド22g(蒸留品)を投入し、かくは
ん下で。(Example 1) In an IL flask equipped with a thermometer, stirrer (paddle type 3 blades), and cooling bath, 70.5 g of 30% potassium hydroxide aqueous solution, 61.1 g of 35% hydrogen peroxide aqueous solution + 70 g of dichloromethane* After mixing 46 g of methanol and 0.5 g of magnesium sulfate and cooling to 10°C, 22 g of metachlorobenzoic acid chloride (distilled product) was added and stirred.
2時間反応を行なった0反応終了後、20%硫酸280
gを投入し、ジクロロメタン280gを加えメタクロロ
過安息香酸を酸性下でジクロロメタン相へ抽出した0次
にロータリー・エバポレータにて抽出液からジクロロメ
タンを減圧留去して針状結晶の製品20.1gを得た。After the reaction was completed for 2 hours, 20% sulfuric acid 280
280 g of dichloromethane was added and metachloroperbenzoic acid was extracted into the dichloromethane phase under acidic conditions. Next, dichloromethane was distilled off from the extract under reduced pressure using a rotary evaporator to obtain 20.1 g of a needle-shaped crystal product. Ta.
この製品はヨードメトリー法により94.3%のメタク
ロ口過安息IP!2を含んでいた。又、i!!体クロマ
トグラフィーによる分析でメタクロロ過酸化ベンゾイル
は0゜1%、メタクロロ安息香酸メチルは1.4%の含
有量であった。尚、製品収率は92.6%であった。This product has 94.3% methacrylic acid based on the iodometry method! It contained 2. Also, i! ! Analysis by body chromatography revealed that the content of metachlorobenzoyl peroxide was 0.1% and the content of methyl metachlorobenzoate was 1.4%. Note that the product yield was 92.6%.
(実施例2)
実施例1における30%水酸化カリウム水溶液のかわり
に3o%水酸化ナトリウム水溶液50゜3gを用いた以
外は実施例1と全く同様に反応を行ない針状結晶の製品
20.2gを得た0分析結果はメタクロ口過安息香12
95.1%、メタクロロ過酸化ベンゾイルは0.2%、
メタクロロ安息香酸メチルは1.0%の含有量であった
。尚、I1品数取率93.1%であった。(Example 2) The reaction was carried out in exactly the same manner as in Example 1, except that 50.3 g of a 30% sodium hydroxide aqueous solution was used instead of the 30% potassium hydroxide aqueous solution in Example 1, and 20.2 g of a needle-shaped crystal product was obtained. The obtained 0 analysis result is methacrylate perbenzoin 12
95.1%, metachlorobenzoyl peroxide 0.2%,
The content of methyl metachlorobenzoate was 1.0%. Incidentally, the I1 item count rate was 93.1%.
(実施例3)
実施例1におけるジクロロメタンのかわりにクロロホル
ムを使用した以外は実施例1と全く同様に反応を行ない
針状結晶の製品20.1gを得た。(Example 3) The reaction was carried out in exactly the same manner as in Example 1, except that chloroform was used instead of dichloromethane in Example 1, and 20.1 g of a needle-like crystal product was obtained.
分析結果はメタクロロ過安息香酸93.2%、メタクロ
ロ過酸化ベンゾイルは0.9%、メタクロロ安息香酸メ
チルは1.2%の含有量であった。The analysis results showed that the content of metachloroperbenzoic acid was 93.2%, the content of metachlorobenzoyl peroxide was 0.9%, and the content of methyl metachlorobenzoate was 1.2%.
尚、製品収率は92.6%であった。Note that the product yield was 92.6%.
(実施例4)
実施例1におけるメタノールのかわりにエタノールを使
用した以外は実施例1と全く同様に反応を行なった。そ
の結果針状結晶の製品19.agを得た6分析結果はメ
タクロロ過安息香酸86゜0%、メタクロロ過酸化ベン
ゾイルは1.7%。(Example 4) The reaction was carried out in exactly the same manner as in Example 1 except that ethanol was used instead of methanol in Example 1. The result is a needle-shaped crystal product19. The results of the 6 analysis obtained for ag were 86.0% metachloroperbenzoic acid and 1.7% metachlorobenzoyl peroxide.
メタクロロ安息香酸エチルは0.9%の含有量であった
。尚、II品数取率88.9%であった。The content of ethyl metachlorobenzoate was 0.9%. Furthermore, the acceptance rate of II items was 88.9%.
(実施例5〜6)および(比較例1〜2)次に反応温度
を変えた以外は実施例1と同等の条件で反応した実施例
及び比較例について結果を表1.にまとめた。(Examples 5 to 6) and (Comparative Examples 1 to 2) Next, Table 1 shows the results for Examples and Comparative Examples that were reacted under the same conditions as Example 1 except that the reaction temperature was changed. summarized in.
表 1 。Table 1.
送量以外は実施例1と同等の方法で実験した実施例につ
いて結果を表 2.にまとめた。Table 2 shows the results of an experiment conducted in the same manner as in Example 1 except for the feeding amount. summarized in.
表 2 。Table 2.
FAはメタクロ口過安息香11.MCBPOはメタクロ
ロ過酸化ベンゾイルを意味する0表 1゜の結果の様に
反応温度の高い比較例2ではメタクロロ過安息香酸が分
解し純度低下が著しいのに対して2反応温度の低いO”
Cでは中間体であるメタクロロ過酸化ベンゾイルの残存
が多く反応が遅い。FA is methacrylic hyperbenzoin 11. MCBPO means metachlorobenzoyl peroxide.As shown in the results in Table 1, in Comparative Example 2 where the reaction temperature was high, metachloroperbenzoic acid decomposed and the purity decreased markedly.
In C, a large amount of the intermediate metachlorobenzoyl peroxide remains and the reaction is slow.
(実施例7〜13)
次に過酸化水素及びアルカリ金属水酸化物の仕(比較例
3〜9)
次に過酸化水素及びアルカリ金属水酸化物の仕込量以外
は実施例1と同等の方法で実験した比較例について結果
を表 3.にまとめた。(Examples 7 to 13) Next, the preparation of hydrogen peroxide and alkali metal hydroxide (Comparative Examples 3 to 9) Next, the same method as in Example 1 except for the amount of hydrogen peroxide and alkali metal hydroxide added. Table 3 shows the results for comparative examples tested in 3. summarized in.
表 の製品への混入が極端に少ないことが分る。table It can be seen that the amount of contamination in the product is extremely low.
(実施例14〜17)及び(比較例10〜13)次に、
メタノールの添加量以外は実施例1と同等の方法で反応
を行なった所、各々実施例及び比較例とも18〜21g
の製品が得られた。各々実施例及び比較例の製品分析結
果を表 4.にまとめた。(Examples 14 to 17) and (Comparative Examples 10 to 13) Next,
The reaction was carried out in the same manner as in Example 1 except for the amount of methanol added, and the amount was 18 to 21 g for both the Example and Comparative Example.
of products were obtained. Table 4 shows the product analysis results of Examples and Comparative Examples. summarized in.
表 4 。Table 4.
表 2.及び表 3.においてm:n:xは過酸化水素
:アルカリ金属水酸化物:メタクロロ安息香酸クロライ
ドのモル比を意味する。又、PAはメタクロロ過安息香
酸、MCBPOはメタクロロ過酸化ベンゾイルを意味す
る0表 3.よりMCBPOの残量が比較例3〜9にお
いては20%以上あり1表 2.における実施例7〜1
3においては2%以下で島り、実施例においてMCBP
OPAはメタクロロ過安息香酸、MCBPOはメタクロ
ロ過酸化ベンゾイル、MBはメタクロロ安息香酸メチル
を意味する。ここで言うメタノール量は反応液中の水性
相に対する重量%で示す0表4、よりメタノール添加量
が20%以下ではメック00過酸化ベンゾイルが多く残
存し、メタノール添加量が60%ではメタクロロ過安息
香酸純度が低下すると同時にメタクロロ安息香酸メチル
が多く生成するすることが分る。Table 2. and Table 3. m:n:x means the molar ratio of hydrogen peroxide:alkali metal hydroxide:metachlorobenzoic acid chloride. Also, PA means metachloroperbenzoic acid and MCBPO means metachlorobenzoyl peroxide.Table 3. Therefore, the remaining amount of MCBPO was 20% or more in Comparative Examples 3 to 9. Examples 7-1 in
In No. 3, the island was 2% or less, and in the example, MCBP
OPA means metachloroperbenzoic acid, MCBPO means metachlorobenzoyl peroxide, and MB means methyl metachlorobenzoate. The amount of methanol referred to here is expressed in weight% with respect to the aqueous phase in the reaction solution.Table 4 shows that when the amount of methanol added is 20% or less, a large amount of MEC 00 benzoyl peroxide remains, and when the amount of methanol added is 60%, methanol peroxide remains. It can be seen that as the acid purity decreases, more methyl metachlorobenzoate is produced.
(比較例14)
実施例1において反応時に添加したジクロロメタンを添
加しない以外は実施例1と全く同様に反応を行なった。(Comparative Example 14) The reaction was carried out in exactly the same manner as in Example 1, except that dichloromethane, which was added during the reaction in Example 1, was not added.
その結果製品19.4gを得た。As a result, 19.4 g of product was obtained.
分析結果はメタクロ口過安息香!151.2%、メタク
ロロ過酸化ベンゾイル30.7%、メタクロロ安息香酸
メチル4.1%であった0反応時にジクロロメタンを添
加しない場合はメタクロロ過安息香酸純度が低く、メタ
クロロ過酸化ベンゾイル及びメタクロロ安息香酸メチル
が多く生成していることが分った。The analysis results are methacrylic hyperbenzoin! 151.2%, benzoyl metachloroperoxide 30.7%, and methyl metachlorobenzoate 4.1%.0 If dichloromethane is not added during the reaction, the purity of metachloroperbenzoic acid is low, and the purity of benzoyl metachloroperoxide and methyl metachlorobenzoate is low. It was found that a large amount of methyl was produced.
Claims (2)
リ金属水酸化物(II)、過酸化水素(III)、炭素数3
以下のアルコール(IV)及びメタクロロ過酸化ベンゾイ
ルの可溶な不活性溶剤を混合して反応する際に(II):
( I )を2.5:1から5.5:1のモル比で使用し
、(III):( I )を4:1から6:1のモル比で使用
し(IV)を水性相に対し25〜50重量%使用し、反応
温度5〜25℃で反応することを特徴とするメタクロロ
過安息香酸の製造方法。(1) Metachlorobenzoic acid chloride (I) is combined with alkali metal hydroxide (II), hydrogen peroxide (III), and carbon number 3
When reacting by mixing the following alcohol (IV) and an inert solvent in which benzoyl metachloroperoxide is soluble (II):
(I) was used in a molar ratio of 2.5:1 to 5.5:1, (III): (I) was used in a molar ratio of 4:1 to 6:1 and (IV) was added to the aqueous phase. A method for producing metachloroperbenzoic acid, which comprises using 25 to 50% by weight of metachloroperbenzoic acid and reacting at a reaction temperature of 5 to 25°C.
としてジクロロメタン、クロロホルム、四塩化炭素、ジ
クロロエタン、トリクロロエチレンなどのハロゲン化炭
化水素類を用いる特許請求の範囲第1項記載の方法。(2) The method according to claim 1, in which halogenated hydrocarbons such as dichloromethane, chloroform, carbon tetrachloride, dichloroethane, and trichloroethylene are used as the inert solvent in which benzoyl metachloroperoxide is soluble.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP16444988A JP2684385B2 (en) | 1988-06-30 | 1988-06-30 | Method for producing metachloroperbenzoic acid |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP16444988A JP2684385B2 (en) | 1988-06-30 | 1988-06-30 | Method for producing metachloroperbenzoic acid |
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JPH0211565A true JPH0211565A (en) | 1990-01-16 |
JP2684385B2 JP2684385B2 (en) | 1997-12-03 |
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ID=15793382
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS63115811A (en) * | 1986-11-01 | 1988-05-20 | Osaka Eyazoole Kogyo Kk | Depilatory agent |
-
1988
- 1988-06-30 JP JP16444988A patent/JP2684385B2/en not_active Expired - Fee Related
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS63115811A (en) * | 1986-11-01 | 1988-05-20 | Osaka Eyazoole Kogyo Kk | Depilatory agent |
JPH0764712B2 (en) * | 1986-11-01 | 1995-07-12 | 大阪エヤ−ゾル工業株式会社 | Hair remover |
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