JPH04364138A - Production of hydroquinone or 2-cyclohexen-1-one-4-hydroperoxide - Google Patents
Production of hydroquinone or 2-cyclohexen-1-one-4-hydroperoxideInfo
- Publication number
- JPH04364138A JPH04364138A JP23177791A JP23177791A JPH04364138A JP H04364138 A JPH04364138 A JP H04364138A JP 23177791 A JP23177791 A JP 23177791A JP 23177791 A JP23177791 A JP 23177791A JP H04364138 A JPH04364138 A JP H04364138A
- Authority
- JP
- Japan
- Prior art keywords
- cyclohexenone
- hydroquinone
- hydroperoxide
- production
- cyclohexen
- 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.)
- Withdrawn
Links
- QIGBRXMKCJKVMJ-UHFFFAOYSA-N Hydroquinone Chemical compound OC1=CC=C(O)C=C1 QIGBRXMKCJKVMJ-UHFFFAOYSA-N 0.000 title claims abstract description 40
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 7
- FWFSEYBSWVRWGL-UHFFFAOYSA-N cyclohex-2-enone Chemical compound O=C1CCCC=C1 FWFSEYBSWVRWGL-UHFFFAOYSA-N 0.000 claims abstract description 17
- MYMOFIZGZYHOMD-UHFFFAOYSA-N Dioxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 claims abstract description 10
- 229910001882 dioxygen Inorganic materials 0.000 claims abstract description 6
- 239000007791 liquid phase Substances 0.000 claims description 5
- 150000002432 hydroperoxides Chemical class 0.000 claims description 2
- SYGXAMNYMMEKSS-UHFFFAOYSA-N cyclohex-2-en-1-one hydrogen peroxide Chemical compound OO.O=C1CCCC=C1 SYGXAMNYMMEKSS-UHFFFAOYSA-N 0.000 abstract description 10
- MHAJPDPJQMAIIY-UHFFFAOYSA-N Hydrogen peroxide Chemical compound OO MHAJPDPJQMAIIY-UHFFFAOYSA-N 0.000 abstract description 5
- 239000012442 inert solvent Substances 0.000 abstract 1
- 238000000034 method Methods 0.000 description 10
- 238000006243 chemical reaction Methods 0.000 description 9
- ISWSIDIOOBJBQZ-UHFFFAOYSA-N Phenol Chemical compound OC1=CC=CC=C1 ISWSIDIOOBJBQZ-UHFFFAOYSA-N 0.000 description 7
- 239000007864 aqueous solution Substances 0.000 description 7
- 238000000354 decomposition reaction Methods 0.000 description 7
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 5
- 238000007254 oxidation reaction Methods 0.000 description 5
- PAYRUJLWNCNPSJ-UHFFFAOYSA-N Aniline Chemical compound NC1=CC=CC=C1 PAYRUJLWNCNPSJ-UHFFFAOYSA-N 0.000 description 4
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 description 4
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 4
- 230000002378 acidificating effect Effects 0.000 description 4
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 description 3
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 description 3
- XTVVROIMIGLXTD-UHFFFAOYSA-N copper(II) nitrate Chemical compound [Cu+2].[O-][N+]([O-])=O.[O-][N+]([O-])=O XTVVROIMIGLXTD-UHFFFAOYSA-N 0.000 description 3
- 239000011261 inert gas Substances 0.000 description 3
- 230000003647 oxidation Effects 0.000 description 3
- 230000001590 oxidative effect Effects 0.000 description 3
- 239000001301 oxygen Substances 0.000 description 3
- 229910052760 oxygen Inorganic materials 0.000 description 3
- 239000012071 phase Substances 0.000 description 3
- 239000000243 solution Substances 0.000 description 3
- 239000002904 solvent Substances 0.000 description 3
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical group CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 description 2
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 2
- 229910002651 NO3 Inorganic materials 0.000 description 2
- NHNBFGGVMKEFGY-UHFFFAOYSA-N Nitrate Chemical compound [O-][N+]([O-])=O NHNBFGGVMKEFGY-UHFFFAOYSA-N 0.000 description 2
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 description 2
- 239000002253 acid Substances 0.000 description 2
- 238000004458 analytical method Methods 0.000 description 2
- 229910052786 argon Inorganic materials 0.000 description 2
- 239000012298 atmosphere Substances 0.000 description 2
- -1 benzene Chemical class 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- 239000003054 catalyst Substances 0.000 description 2
- 150000001875 compounds Chemical class 0.000 description 2
- ORTQZVOHEJQUHG-UHFFFAOYSA-L copper(II) chloride Chemical compound Cl[Cu]Cl ORTQZVOHEJQUHG-UHFFFAOYSA-L 0.000 description 2
- OPQARKPSCNTWTJ-UHFFFAOYSA-L copper(ii) acetate Chemical compound [Cu+2].CC([O-])=O.CC([O-])=O OPQARKPSCNTWTJ-UHFFFAOYSA-L 0.000 description 2
- 230000002349 favourable effect Effects 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 238000004817 gas chromatography Methods 0.000 description 2
- VCJMYUPGQJHHFU-UHFFFAOYSA-N iron(3+);trinitrate Chemical compound [Fe+3].[O-][N+]([O-])=O.[O-][N+]([O-])=O.[O-][N+]([O-])=O VCJMYUPGQJHHFU-UHFFFAOYSA-N 0.000 description 2
- BDAGIHXWWSANSR-UHFFFAOYSA-N methanoic acid Natural products OC=O BDAGIHXWWSANSR-UHFFFAOYSA-N 0.000 description 2
- VLKZOEOYAKHREP-UHFFFAOYSA-N n-Hexane Chemical compound CCCCCC VLKZOEOYAKHREP-UHFFFAOYSA-N 0.000 description 2
- 229910052757 nitrogen Inorganic materials 0.000 description 2
- 239000000047 product Substances 0.000 description 2
- AZQWKYJCGOJGHM-UHFFFAOYSA-N 1,4-benzoquinone Chemical compound O=C1C=CC(=O)C=C1 AZQWKYJCGOJGHM-UHFFFAOYSA-N 0.000 description 1
- QEEPPWQOVJWUBC-UHFFFAOYSA-N 1-hydroperoxycyclohexene Chemical compound OOC1=CCCCC1 QEEPPWQOVJWUBC-UHFFFAOYSA-N 0.000 description 1
- JHWIEAWILPSRMU-UHFFFAOYSA-N 2-methyl-3-pyrimidin-4-ylpropanoic acid Chemical compound OC(=O)C(C)CC1=CC=NC=N1 JHWIEAWILPSRMU-UHFFFAOYSA-N 0.000 description 1
- OSWFIVFLDKOXQC-UHFFFAOYSA-N 4-(3-methoxyphenyl)aniline Chemical compound COC1=CC=CC(C=2C=CC(N)=CC=2)=C1 OSWFIVFLDKOXQC-UHFFFAOYSA-N 0.000 description 1
- 229910021591 Copper(I) chloride Inorganic materials 0.000 description 1
- XDTMQSROBMDMFD-UHFFFAOYSA-N Cyclohexane Chemical compound C1CCCCC1 XDTMQSROBMDMFD-UHFFFAOYSA-N 0.000 description 1
- CWYNVVGOOAEACU-UHFFFAOYSA-N Fe2+ Chemical compound [Fe+2] CWYNVVGOOAEACU-UHFFFAOYSA-N 0.000 description 1
- 229910021578 Iron(III) chloride Inorganic materials 0.000 description 1
- GRYLNZFGIOXLOG-UHFFFAOYSA-N Nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 description 1
- LSNNMFCWUKXFEE-UHFFFAOYSA-N Sulfurous acid Chemical compound OS(O)=O LSNNMFCWUKXFEE-UHFFFAOYSA-N 0.000 description 1
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 description 1
- 235000011054 acetic acid Nutrition 0.000 description 1
- MCDLETWIOVSGJT-UHFFFAOYSA-N acetic acid;iron Chemical compound [Fe].CC(O)=O.CC(O)=O MCDLETWIOVSGJT-UHFFFAOYSA-N 0.000 description 1
- 150000007513 acids Chemical class 0.000 description 1
- 150000001298 alcohols Chemical class 0.000 description 1
- 150000001338 aliphatic hydrocarbons Chemical class 0.000 description 1
- 229910000147 aluminium phosphate Inorganic materials 0.000 description 1
- 150000004945 aromatic hydrocarbons Chemical class 0.000 description 1
- XTKDAFGWCDAMPY-UHFFFAOYSA-N azaperone Chemical compound C1=CC(F)=CC=C1C(=O)CCCN1CCN(C=2N=CC=CC=2)CC1 XTKDAFGWCDAMPY-UHFFFAOYSA-N 0.000 description 1
- 239000006227 byproduct Substances 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- RFKZUAOAYVHBOY-UHFFFAOYSA-M copper(1+);acetate Chemical compound [Cu+].CC([O-])=O RFKZUAOAYVHBOY-UHFFFAOYSA-M 0.000 description 1
- OXBLHERUFWYNTN-UHFFFAOYSA-M copper(I) chloride Chemical compound [Cu]Cl OXBLHERUFWYNTN-UHFFFAOYSA-M 0.000 description 1
- ARUVKPQLZAKDPS-UHFFFAOYSA-L copper(II) sulfate Chemical compound [Cu+2].[O-][S+2]([O-])([O-])[O-] ARUVKPQLZAKDPS-UHFFFAOYSA-L 0.000 description 1
- 229910000366 copper(II) sulfate Inorganic materials 0.000 description 1
- SPTHWAJJMLCAQF-UHFFFAOYSA-M ctk4f8481 Chemical group [O-]O.CC(C)C1=CC=CC=C1C(C)C SPTHWAJJMLCAQF-UHFFFAOYSA-M 0.000 description 1
- 229940076286 cupric acetate Drugs 0.000 description 1
- 229960003280 cupric chloride Drugs 0.000 description 1
- 229940045803 cuprous chloride Drugs 0.000 description 1
- 238000010790 dilution Methods 0.000 description 1
- 239000012895 dilution Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000002360 explosive Substances 0.000 description 1
- 229960002089 ferrous chloride Drugs 0.000 description 1
- 239000011790 ferrous sulphate Substances 0.000 description 1
- 235000003891 ferrous sulphate Nutrition 0.000 description 1
- 235000019253 formic acid Nutrition 0.000 description 1
- 235000011167 hydrochloric acid Nutrition 0.000 description 1
- 239000003112 inhibitor Substances 0.000 description 1
- 229910052500 inorganic mineral Inorganic materials 0.000 description 1
- 239000003456 ion exchange resin Substances 0.000 description 1
- 229920003303 ion-exchange polymer Polymers 0.000 description 1
- NMCUIPGRVMDVDB-UHFFFAOYSA-L iron dichloride Chemical compound Cl[Fe]Cl NMCUIPGRVMDVDB-UHFFFAOYSA-L 0.000 description 1
- RBTARNINKXHZNM-UHFFFAOYSA-K iron trichloride Chemical compound Cl[Fe](Cl)Cl RBTARNINKXHZNM-UHFFFAOYSA-K 0.000 description 1
- BAUYGSIQEAFULO-UHFFFAOYSA-L iron(2+) sulfate (anhydrous) Chemical compound [Fe+2].[O-]S([O-])(=O)=O BAUYGSIQEAFULO-UHFFFAOYSA-L 0.000 description 1
- RUTXIHLAWFEWGM-UHFFFAOYSA-H iron(3+) sulfate Chemical compound [Fe+3].[Fe+3].[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O RUTXIHLAWFEWGM-UHFFFAOYSA-H 0.000 description 1
- PVFSDGKDKFSOTB-UHFFFAOYSA-K iron(3+);triacetate Chemical compound [Fe+3].CC([O-])=O.CC([O-])=O.CC([O-])=O PVFSDGKDKFSOTB-UHFFFAOYSA-K 0.000 description 1
- 229910000359 iron(II) sulfate Inorganic materials 0.000 description 1
- 229910000360 iron(III) sulfate Inorganic materials 0.000 description 1
- 150000002576 ketones Chemical class 0.000 description 1
- 238000004811 liquid chromatography Methods 0.000 description 1
- 239000011707 mineral Substances 0.000 description 1
- 235000010755 mineral Nutrition 0.000 description 1
- 229910017604 nitric acid Inorganic materials 0.000 description 1
- 239000012299 nitrogen atmosphere Substances 0.000 description 1
- 150000007524 organic acids Chemical class 0.000 description 1
- 235000005985 organic acids Nutrition 0.000 description 1
- 239000007800 oxidant agent Substances 0.000 description 1
- 238000010979 pH adjustment Methods 0.000 description 1
- 235000011007 phosphoric acid Nutrition 0.000 description 1
- 238000006116 polymerization reaction Methods 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 229910052719 titanium Inorganic materials 0.000 description 1
- 239000010936 titanium Substances 0.000 description 1
- JOXIMZWYDAKGHI-UHFFFAOYSA-N toluene-4-sulfonic acid Chemical compound CC1=CC=C(S(O)(=O)=O)C=C1 JOXIMZWYDAKGHI-UHFFFAOYSA-N 0.000 description 1
Landscapes
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
Description
【0001】0001
【産業上の利用分野】本発明は、2−シクロヘキセン−
1−オン(以下シクロヘキセノンと略す)を液相酸化す
ることからなるヒドロキノンまたは2−シクロヘキセン
−1−オン−4−ヒドロペルオキシド(以下シクロヘキ
セノンヒドロペルオキシドと略す)の製造法に関するも
のである。ヒドロキノンは写真現像剤、染料、酸化およ
び重合防止剤として利用される。[Industrial Field of Application] The present invention relates to 2-cyclohexene-
The present invention relates to a method for producing hydroquinone or 2-cyclohexen-1-one-4-hydroperoxide (hereinafter referred to as cyclohexenone hydroperoxide), which comprises liquid phase oxidation of 1-one (hereinafter referred to as cyclohexenone). Hydroquinone is utilized as a photographic developer, dye, oxidation and polymerization inhibitor.
【0002】0002
【従来の技術】ヒドロキノンの製造法としては従来より
(1)ジイソプロピルベンゼンヒドロペルオキシドを酸
分解する方法(特公昭56−27498号公報)(2)
フェノールをケトンの存在下、過酸化水素で酸化する方
法(特公昭55−16492号公報及び特公昭55−1
6493号公報)
(3)アニリンを硫酸と重クロム酸ソーダで酸化してp
−ベンゾキノンとし、亜硫酸を加え還元する方法等があ
る。[Prior Art] Conventional methods for producing hydroquinone include (1) a method of acid decomposition of diisopropylbenzene hydroperoxide (Japanese Patent Publication No. 56-27498); (2)
A method of oxidizing phenol with hydrogen peroxide in the presence of a ketone (Japanese Patent Publication No. 16492/1982 and Japanese Patent Publication No. 55/1983)
(3) Oxidize aniline with sulfuric acid and sodium dichromate to form p
- There is a method of reducing benzoquinone and adding sulfite.
【0003】0003
【発明が解決しようとする課題】上記(1)、(2)の
方法は工業化されているが、(1)の方法は多段階プロ
セスであるとともに、副生成物としてアセトンがヒドロ
キノンの2当量も生成してしまう。(2)の方法は、酸
化剤として過酸化水素を用いるので、安全性確保のため
多くの注意、工夫を必要とする。さらに(3)の方法は
アニリンを酸化した後、さらに還元してヒドロキノンに
するという多段階プロセスである。いずれにしても工業
的に有利とは言えない。[Problems to be Solved by the Invention] Methods (1) and (2) above have been industrialized, but method (1) is a multi-step process, and the by-product is acetone, which is equivalent to 2 equivalents of hydroquinone. It will generate. Since method (2) uses hydrogen peroxide as an oxidizing agent, much care and effort is required to ensure safety. Furthermore, method (3) is a multi-step process in which aniline is oxidized and then further reduced to hydroquinone. In any case, it cannot be said that it is industrially advantageous.
【0004】0004
【課題を解決するための手段】本発明者らは、ヒドロキ
ノンを得る方法を鋭意検討した結果、驚くべきことにシ
クロヘキセノンを液相にて、分子状酸素を用い酸化する
ことによりヒドロキノンまたはシクロヘキセノンヒドロ
ペルオキシドを一段で合成できることを見出し、本発明
を完成するに至った。[Means for Solving the Problems] As a result of intensive study on a method for obtaining hydroquinone, the present inventors surprisingly found that hydroquinone or cyclohexenone can be obtained by oxidizing cyclohexenone in a liquid phase using molecular oxygen. We have discovered that hydroperoxides can be synthesized in one step, and have completed the present invention.
【0005】即ち、本発明は、シクロヘキセノンを液相
において分子状酸素により酸化することを特徴とするヒ
ドロキノンまたはシクロヘキセノンヒドロペルオキシド
の製造法である。以下、本発明を説明する。本発明に用
いるシクロヘキセノンは、シクロヘキセニルヒドロペル
オキシドを各種分解触媒で分解して高収率で得ることが
できる。(特開昭58−13538号公報、特開昭58
−72532号公報)。That is, the present invention is a method for producing hydroquinone or cyclohexenone hydroperoxide, which is characterized by oxidizing cyclohexenone with molecular oxygen in a liquid phase. The present invention will be explained below. Cyclohexenone used in the present invention can be obtained in high yield by decomposing cyclohexenyl hydroperoxide with various decomposition catalysts. (Unexamined Japanese Patent Publication No. 58-13538, Unexamined Japanese Patent Application No. 58-13538
-72532).
【0006】シクロヘキセノンは、単独もしくは適当な
溶媒に溶解した油相状態で用いても良い。溶媒としては
本発明の条件下で不活性な溶媒、たとえばアルコール類
、ベンゼン等の芳香族炭化水素、n−ヘキサン、シクロ
ヘキサン等の脂肪族炭化水素などが挙げられる。本発明
は、シクロヘキセノンの酸化を液相において分子状酸素
により行うことを特徴とする。反応を行う時の酸素の形
態としては、酸素ガス、空気、またはこれらを窒素、ア
ルゴン等の不活性ガスで希釈したものを用いる。シクロ
ヘキセノンの爆発範囲をはずす意味で、シクロヘキセノ
ンの限界酸素濃度以下に不活性ガスで希釈した混合ガス
を用いるのが好ましい。Cyclohexenone may be used alone or in the form of an oil phase dissolved in a suitable solvent. Examples of the solvent include solvents that are inert under the conditions of the present invention, such as alcohols, aromatic hydrocarbons such as benzene, and aliphatic hydrocarbons such as n-hexane and cyclohexane. The present invention is characterized in that cyclohexenone is oxidized in a liquid phase using molecular oxygen. The form of oxygen used in the reaction is oxygen gas, air, or a dilution of these with an inert gas such as nitrogen or argon. In order to remove the explosive range of cyclohexenone, it is preferable to use a mixed gas diluted with an inert gas to a concentration below the limit oxygen concentration of cyclohexenone.
【0007】反応圧力について、特に制限はないが反応
系中酸素量を増加させるという意味で、加圧下で行うこ
とが好ましい。反応温度については50〜300℃、好
ましくは100〜200℃で行われる。低温ほどシクロ
ヘキセノンヒドロペルオキシドの生成に有利になり、高
温ほどヒドロキノンの生成に有利になる。[0007] There are no particular restrictions on the reaction pressure, but it is preferable to carry out the reaction under increased pressure in order to increase the amount of oxygen in the reaction system. The reaction temperature is 50 to 300°C, preferably 100 to 200°C. The lower the temperature, the more favorable the formation of cyclohexenone hydroperoxide, and the higher the temperature, the more favorable the formation of hydroquinone.
【0008】上記のヒドロキノンと共に生成するシクロ
ヘキセノンヒドロペルオキシドは以下に示す分解処理に
よりヒドロキノンに変換することができる。分解触媒と
しては、酸性水溶液を用いる。酸性水溶液とはpHが7
以下の水溶液であり、好ましくはpHが3以下の水溶液
が用いられる。pH調節のため使用される化合物として
は、硫酸、硝酸、塩酸、リン酸等の鉱酸、酢酸、ギ酸、
パラトルエンスルホン酸等の有機酸、硫酸第一鉄、硫酸
第二鉄、硝酸第一鉄、硝酸第二鉄、塩化第一鉄、塩化第
二鉄、酢酸第一鉄、酢酸第二鉄、硫酸第一銅、硫酸第二
銅、硝酸第一銅、硝酸第二銅、塩化第一銅、塩化第二銅
、酢酸第一銅、酢酸第二銅等の塩、イオン交換樹脂など
が用いられる。またこれら化合物の使用量としては、水
溶液のpHが7以下、好ましくは3以下になる限り特に
制限はない。シクロヘキセノンヒドロペルオキシド含有
の油相と酸性水溶液との混合割合としては、体積比で酸
性水溶液1に対して油相0.01〜50倍、好ましくは
0.1〜10倍である。Cyclohexenone hydroperoxide produced together with the above hydroquinone can be converted to hydroquinone by the decomposition treatment described below. An acidic aqueous solution is used as the decomposition catalyst. An acidic aqueous solution has a pH of 7.
The following aqueous solutions are used, preferably those having a pH of 3 or less. Compounds used for pH adjustment include mineral acids such as sulfuric acid, nitric acid, hydrochloric acid, phosphoric acid, acetic acid, formic acid,
Organic acids such as para-toluenesulfonic acid, ferrous sulfate, ferric sulfate, ferrous nitrate, ferric nitrate, ferrous chloride, ferric chloride, ferrous acetate, ferric acetate, sulfuric acid Salts such as cuprous, cupric sulfate, cuprous nitrate, cupric nitrate, cuprous chloride, cupric chloride, cuprous acetate, cupric acetate, and ion exchange resins are used. The amount of these compounds to be used is not particularly limited as long as the pH of the aqueous solution is 7 or less, preferably 3 or less. The mixing ratio of the oil phase containing cyclohexenone hydroperoxide and the acidic aqueous solution is 0.01 to 50 times, preferably 0.1 to 10 times, the oil phase per volume of the acidic aqueous solution.
【0009】分解処理の際の雰囲気は特に制限はないが
、シクロヘキセノンヒドロペルオキシドの複次反応を避
ける意味で窒素もしくはアルゴン等の不活性ガス雰囲気
下で行うことが好ましい。分解温度については、50〜
300℃、好ましくは70〜150℃で行われる。The atmosphere during the decomposition treatment is not particularly limited, but it is preferably carried out under an inert gas atmosphere such as nitrogen or argon in order to avoid multiple reactions of cyclohexenone hydroperoxide. Regarding the decomposition temperature, 50~
It is carried out at 300°C, preferably 70-150°C.
【0010】0010
【実施例】以下実施例により本発明を説明する。[Examples] The present invention will be explained below with reference to Examples.
【0011】[0011]
【実施例1】シクロヘキセノン1.0g(10.4mm
ol)をSUS−316製反応器中に入れ、6%のO2
/N2 混合ガスを50kg/cm3 (O2 ;1
.6mmol)の加圧下で吹き込み、150℃の温度で
、1時間、酸化した。酸化反応液中の生成物をガスクロ
マトグラフィーにより分析した結果、ヒドロキノン0.
016g(0.15mmol)、フェノール0.004
g(0.004mmol)が確認された。仕込みシクロ
ヘキセノンに対するヒドロキノン収率1.44%、フェ
ノール収率0.04%であった。[Example 1] Cyclohexenone 1.0g (10.4mm
ol) into a SUS-316 reactor and 6% O2
/N2 mixed gas at 50kg/cm3 (O2;1
.. 6 mmol) under pressure and oxidized at a temperature of 150° C. for 1 hour. As a result of analyzing the product in the oxidation reaction solution by gas chromatography, it was found that 0.0% of hydroquinone was detected.
016g (0.15mmol), phenol 0.004
g (0.004 mmol) was confirmed. The hydroquinone yield was 1.44% and the phenol yield was 0.04% based on the charged cyclohexenone.
【0012】0012
【実施例2〜4】表1に示す条件に変える以外は、実施
例1と同じ操作で反応を行った。その結果を表1に示す
。Examples 2 to 4 Reactions were carried out in the same manner as in Example 1, except that the conditions were changed to those shown in Table 1. The results are shown in Table 1.
【0013】[0013]
【実施例5】シクロヘキセノン5g(52.1mmol
)をチタン製反応器中に入れ、、純酸素を10kg/c
m3 (O2 ;20mmol)の加圧下で吹き込み、
70℃の温度で13時間、酸化した。ガスクロマトグラ
フィー及びヨードメトリー分析の結果、ヒドロキノン0
.14g(1.27mmol)、フェノール0.009
g(0.10mmol)、シクロヘキセノンヒドロペル
オキシド0.33g(2.55mmol)が確認された
。[Example 5] Cyclohexenone 5g (52.1mmol
) was placed in a titanium reactor, and pure oxygen was added at 10 kg/c.
m3 (O2; 20 mmol) under pressure,
Oxidation was carried out at a temperature of 70° C. for 13 hours. As a result of gas chromatography and iodometry analysis, hydroquinone was found to be 0.
.. 14g (1.27mmol), phenol 0.009
g (0.10 mmol) and 0.33 g (2.55 mmol) of cyclohexenone hydroperoxide were confirmed.
【0014】この酸化反応液5gとpHが2のFeSO
4 水溶液5mlを、窒素雰囲気下70℃で4時間反応
させた。ヨードメトリー分析の結果、反応停止時にはシ
クロヘキセノンヒドロペルオキシドは完全に分解してい
た。分解処理後反応液中の生成物を液体クロマトグラフ
ィーで分析した結果、ヒドロキノン0.39g(3.5
7mmol)、フェノール0.014g(0.15mm
ol)が確認された。仕込みシクロヘキセノンに対する
ヒドロキノン収率6.8%、フェノール収率0.29%
であった。[0014] 5 g of this oxidation reaction solution and FeSO with a pH of 2
4 5 ml of the aqueous solution was reacted at 70° C. for 4 hours under a nitrogen atmosphere. As a result of iodometry analysis, cyclohexenone hydroperoxide was completely decomposed by the time the reaction was stopped. As a result of analyzing the product in the reaction solution after decomposition treatment by liquid chromatography, it was found that 0.39 g (3.5
7 mmol), phenol 0.014 g (0.15 mmol), phenol 0.014 g (0.15 mmol)
ol) was confirmed. Hydroquinone yield 6.8%, phenol yield 0.29% based on charged cyclohexenone
Met.
【0015】[0015]
【表1】[Table 1]
【0016】[0016]
【発明の効果】シクロヘキセノンを原料とし、新規で、
かつ簡便な一段階製造法でヒドロキノンまたはシクロヘ
キセノンヒドロペルオキシドを合成することができる。[Effect of the invention] Using cyclohexenone as a raw material, it is a new,
Moreover, hydroquinone or cyclohexenone hydroperoxide can be synthesized by a simple one-step production method.
Claims (1)
において分子状酸素により酸化することを特徴とするヒ
ドロキノンまたは2−シクロヘキセン−1−オン−4−
ヒドロペルオキシドの製造法。1. Hydroquinone or 2-cyclohexen-1-one-4-, characterized in that 2-cyclohexen-1-one is oxidized with molecular oxygen in a liquid phase.
Method for producing hydroperoxides.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP23177791A JPH04364138A (en) | 1990-09-21 | 1991-09-11 | Production of hydroquinone or 2-cyclohexen-1-one-4-hydroperoxide |
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2-249986 | 1990-09-21 | ||
JP24998690 | 1990-09-21 | ||
JP23177791A JPH04364138A (en) | 1990-09-21 | 1991-09-11 | Production of hydroquinone or 2-cyclohexen-1-one-4-hydroperoxide |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH04364138A true JPH04364138A (en) | 1992-12-16 |
Family
ID=26530087
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP23177791A Withdrawn JPH04364138A (en) | 1990-09-21 | 1991-09-11 | Production of hydroquinone or 2-cyclohexen-1-one-4-hydroperoxide |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH04364138A (en) |
-
1991
- 1991-09-11 JP JP23177791A patent/JPH04364138A/en not_active Withdrawn
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