JPS62258331A - Method for producing 3-alkenylcatechol - Google Patents
Method for producing 3-alkenylcatecholInfo
- Publication number
- JPS62258331A JPS62258331A JP61102270A JP10227086A JPS62258331A JP S62258331 A JPS62258331 A JP S62258331A JP 61102270 A JP61102270 A JP 61102270A JP 10227086 A JP10227086 A JP 10227086A JP S62258331 A JPS62258331 A JP S62258331A
- Authority
- JP
- Japan
- Prior art keywords
- compound
- aqueous solution
- copper
- catalyst
- 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.)
- Granted
Links
- 238000004519 manufacturing process Methods 0.000 title claims description 10
- 238000006243 chemical reaction Methods 0.000 claims abstract description 34
- 150000001875 compounds Chemical class 0.000 claims abstract description 25
- 239000005749 Copper compound Substances 0.000 claims abstract description 19
- 150000001880 copper compounds Chemical class 0.000 claims abstract description 19
- 239000003054 catalyst Substances 0.000 claims abstract description 16
- 239000007864 aqueous solution Substances 0.000 claims abstract description 15
- 125000003118 aryl group Chemical group 0.000 claims abstract description 9
- 230000003301 hydrolyzing effect Effects 0.000 claims abstract description 5
- 229910052757 nitrogen Inorganic materials 0.000 claims description 7
- 125000004433 nitrogen atom Chemical group N* 0.000 claims description 4
- 125000004430 oxygen atom Chemical group O* 0.000 claims description 4
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 abstract description 12
- KWYUFKZDYYNOTN-UHFFFAOYSA-M Potassium hydroxide Chemical compound [OH-].[K+] KWYUFKZDYYNOTN-UHFFFAOYSA-M 0.000 abstract description 9
- 239000003513 alkali Substances 0.000 abstract description 6
- 239000002184 metal Substances 0.000 abstract description 5
- 229910052751 metal Inorganic materials 0.000 abstract description 5
- 235000011121 sodium hydroxide Nutrition 0.000 abstract description 4
- 235000011118 potassium hydroxide Nutrition 0.000 abstract description 3
- 239000002994 raw material Substances 0.000 abstract description 3
- 239000000126 substance Substances 0.000 abstract description 3
- 239000013522 chelant Substances 0.000 abstract description 2
- 239000005725 8-Hydroxyquinoline Substances 0.000 abstract 1
- 230000003113 alkalizing effect Effects 0.000 abstract 1
- 239000007795 chemical reaction product Substances 0.000 abstract 1
- 239000002917 insecticide Substances 0.000 abstract 1
- 229960003540 oxyquinoline Drugs 0.000 abstract 1
- MCJGNVYPOGVAJF-UHFFFAOYSA-N quinolin-8-ol Chemical compound C1=CN=C2C(O)=CC=CC2=C1 MCJGNVYPOGVAJF-UHFFFAOYSA-N 0.000 abstract 1
- 238000006460 hydrolysis reaction Methods 0.000 description 9
- ISWSIDIOOBJBQZ-UHFFFAOYSA-N Phenol Chemical compound OC1=CC=CC=C1 ISWSIDIOOBJBQZ-UHFFFAOYSA-N 0.000 description 8
- 239000000571 coke Substances 0.000 description 8
- 229910000831 Steel Inorganic materials 0.000 description 7
- 239000010959 steel Substances 0.000 description 7
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 5
- WEVYAHXRMPXWCK-UHFFFAOYSA-N methyl cyanide Natural products CC#N WEVYAHXRMPXWCK-UHFFFAOYSA-N 0.000 description 5
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 4
- 229910021591 Copper(I) chloride Inorganic materials 0.000 description 4
- 229910052802 copper Inorganic materials 0.000 description 4
- 239000010949 copper Substances 0.000 description 4
- 150000004699 copper complex Chemical class 0.000 description 4
- OXBLHERUFWYNTN-UHFFFAOYSA-M copper(I) chloride Chemical compound [Cu]Cl OXBLHERUFWYNTN-UHFFFAOYSA-M 0.000 description 4
- 229940045803 cuprous chloride Drugs 0.000 description 4
- 238000000034 method Methods 0.000 description 4
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 239000000203 mixture Substances 0.000 description 3
- 239000000243 solution Substances 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- PLSMJPHVSIUHKS-UHFFFAOYSA-N 3-(2-methylprop-1-enyl)benzene-1,2-diol Chemical compound CC(C)=CC1=CC=CC(O)=C1O PLSMJPHVSIUHKS-UHFFFAOYSA-N 0.000 description 2
- QPLDLSVMHZLSFG-UHFFFAOYSA-N Copper oxide Chemical compound [Cu]=O QPLDLSVMHZLSFG-UHFFFAOYSA-N 0.000 description 2
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 2
- KYQCOXFCLRTKLS-UHFFFAOYSA-N Pyrazine Chemical compound C1=CN=CC=N1 KYQCOXFCLRTKLS-UHFFFAOYSA-N 0.000 description 2
- 239000002253 acid Substances 0.000 description 2
- 125000003342 alkenyl group Chemical group 0.000 description 2
- 125000000217 alkyl group Chemical group 0.000 description 2
- 125000004429 atom Chemical group 0.000 description 2
- 229910052799 carbon Inorganic materials 0.000 description 2
- 125000003178 carboxy group Chemical group [H]OC(*)=O 0.000 description 2
- YCIMNLLNPGFGHC-UHFFFAOYSA-N catechol Chemical compound OC1=CC=CC=C1O YCIMNLLNPGFGHC-UHFFFAOYSA-N 0.000 description 2
- 239000003518 caustics Substances 0.000 description 2
- 230000000052 comparative effect Effects 0.000 description 2
- 239000013078 crystal Substances 0.000 description 2
- 230000007423 decrease Effects 0.000 description 2
- 125000001475 halogen functional group Chemical group 0.000 description 2
- 125000005843 halogen group Chemical group 0.000 description 2
- 230000007062 hydrolysis Effects 0.000 description 2
- 125000002887 hydroxy group Chemical group [H]O* 0.000 description 2
- -1 j-sulfonaphthylamine Chemical compound 0.000 description 2
- LPYUENQFPVNPHY-UHFFFAOYSA-N methoxycatechol Natural products COC1=CC=CC(O)=C1O LPYUENQFPVNPHY-UHFFFAOYSA-N 0.000 description 2
- 125000000449 nitro group Chemical group [O-][N+](*)=O 0.000 description 2
- 238000001556 precipitation Methods 0.000 description 2
- YGSDEFSMJLZEOE-UHFFFAOYSA-N salicylic acid Chemical compound OC(=O)C1=CC=CC=C1O YGSDEFSMJLZEOE-UHFFFAOYSA-N 0.000 description 2
- 125000000020 sulfo group Chemical group O=S(=O)([*])O[H] 0.000 description 2
- 125000004191 (C1-C6) alkoxy group Chemical group 0.000 description 1
- FLBAYUMRQUHISI-UHFFFAOYSA-N 1,8-naphthyridine Chemical compound N1=CC=CC2=CC=CN=C21 FLBAYUMRQUHISI-UHFFFAOYSA-N 0.000 description 1
- VGVRPFIJEJYOFN-UHFFFAOYSA-N 2,3,4,6-tetrachlorophenol Chemical class OC1=C(Cl)C=C(Cl)C(Cl)=C1Cl VGVRPFIJEJYOFN-UHFFFAOYSA-N 0.000 description 1
- QPKNFEVLZVJGBM-UHFFFAOYSA-N 2-aminonaphthalen-1-ol Chemical compound C1=CC=CC2=C(O)C(N)=CC=C21 QPKNFEVLZVJGBM-UHFFFAOYSA-N 0.000 description 1
- ZBJJDYGJCNTNTH-UHFFFAOYSA-N Betahistine mesilate Chemical group CS(O)(=O)=O.CS(O)(=O)=O.CNCCC1=CC=CC=N1 ZBJJDYGJCNTNTH-UHFFFAOYSA-N 0.000 description 1
- WKBOTKDWSSQWDR-UHFFFAOYSA-N Bromine atom Chemical group [Br] WKBOTKDWSSQWDR-UHFFFAOYSA-N 0.000 description 1
- KXDHJXZQYSOELW-UHFFFAOYSA-M Carbamate Chemical compound NC([O-])=O KXDHJXZQYSOELW-UHFFFAOYSA-M 0.000 description 1
- 241000283986 Lepus Species 0.000 description 1
- 241001106041 Lycium Species 0.000 description 1
- 229910002651 NO3 Inorganic materials 0.000 description 1
- NHNBFGGVMKEFGY-UHFFFAOYSA-N Nitrate Chemical compound [O-][N+]([O-])=O NHNBFGGVMKEFGY-UHFFFAOYSA-N 0.000 description 1
- PCNDJXKNXGMECE-UHFFFAOYSA-N Phenazine Natural products C1=CC=CC2=NC3=CC=CC=C3N=C21 PCNDJXKNXGMECE-UHFFFAOYSA-N 0.000 description 1
- QAOWNCQODCNURD-UHFFFAOYSA-L Sulfate Chemical compound [O-]S([O-])(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-L 0.000 description 1
- 239000004480 active ingredient Substances 0.000 description 1
- 125000003282 alkyl amino group Chemical group 0.000 description 1
- 125000004390 alkyl sulfonyl group Chemical group 0.000 description 1
- 125000003277 amino group Chemical group 0.000 description 1
- 229960004050 aminobenzoic acid Drugs 0.000 description 1
- 125000003710 aryl alkyl group Chemical group 0.000 description 1
- AXCZMVOFGPJBDE-UHFFFAOYSA-L calcium dihydroxide Chemical compound [OH-].[OH-].[Ca+2] AXCZMVOFGPJBDE-UHFFFAOYSA-L 0.000 description 1
- 239000000920 calcium hydroxide Substances 0.000 description 1
- 229910001861 calcium hydroxide Inorganic materials 0.000 description 1
- 235000011116 calcium hydroxide Nutrition 0.000 description 1
- DUEPRVBVGDRKAG-UHFFFAOYSA-N carbofuran Chemical compound CNC(=O)OC1=CC=CC2=C1OC(C)(C)C2 DUEPRVBVGDRKAG-UHFFFAOYSA-N 0.000 description 1
- 125000004432 carbon atom Chemical group C* 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 229910052801 chlorine Inorganic materials 0.000 description 1
- 125000001309 chloro group Chemical group Cl* 0.000 description 1
- 210000000078 claw Anatomy 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- BERDEBHAJNAUOM-UHFFFAOYSA-N copper(I) oxide Inorganic materials [Cu]O[Cu] BERDEBHAJNAUOM-UHFFFAOYSA-N 0.000 description 1
- JZCCFEFSEZPSOG-UHFFFAOYSA-L copper(II) sulfate pentahydrate Chemical compound O.O.O.O.O.[Cu+2].[O-]S([O-])(=O)=O JZCCFEFSEZPSOG-UHFFFAOYSA-L 0.000 description 1
- 229960004643 cupric oxide Drugs 0.000 description 1
- KRFJLUBVMFXRPN-UHFFFAOYSA-N cuprous oxide Chemical compound [O-2].[Cu+].[Cu+] KRFJLUBVMFXRPN-UHFFFAOYSA-N 0.000 description 1
- 229940112669 cuprous oxide Drugs 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-M hydroxide Chemical compound [OH-] XLYOFNOQVPJJNP-UHFFFAOYSA-M 0.000 description 1
- 239000011261 inert gas Substances 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000004811 liquid chromatography Methods 0.000 description 1
- 239000007791 liquid phase Substances 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- 239000011259 mixed solution Substances 0.000 description 1
- JESXATFQYMPTNL-UHFFFAOYSA-N mono-hydroxyphenyl-ethylene Natural products OC1=CC=CC=C1C=C JESXATFQYMPTNL-UHFFFAOYSA-N 0.000 description 1
- 238000006386 neutralization reaction Methods 0.000 description 1
- 239000012299 nitrogen atmosphere Substances 0.000 description 1
- QJGQUHMNIGDVPM-UHFFFAOYSA-N nitrogen group Chemical group [N] QJGQUHMNIGDVPM-UHFFFAOYSA-N 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- FJKROLUGYXJWQN-UHFFFAOYSA-N papa-hydroxy-benzoic acid Natural products OC(=O)C1=CC=C(O)C=C1 FJKROLUGYXJWQN-UHFFFAOYSA-N 0.000 description 1
- 150000004686 pentahydrates Chemical class 0.000 description 1
- 239000000575 pesticide Substances 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- GGOZGYRTNQBSSA-UHFFFAOYSA-N pyridine-2,3-diol Chemical compound OC1=CC=CN=C1O GGOZGYRTNQBSSA-UHFFFAOYSA-N 0.000 description 1
- 239000011541 reaction mixture Substances 0.000 description 1
- 230000035484 reaction time Effects 0.000 description 1
- 229960004889 salicylic acid Drugs 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 125000001424 substituent group Chemical group 0.000 description 1
- 229910052717 sulfur Inorganic materials 0.000 description 1
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/50—Improvements relating to the production of bulk chemicals
- Y02P20/52—Improvements relating to the production of bulk chemicals using catalysts, e.g. selective catalysts
Landscapes
- Catalysts (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明は3−アルケニルカテコールの製造法に関するも
のである。更に詳しくは一一ノ馬ロー4−フルケニルフ
ェノールをアルカリ水溶i中、銅化合物触媒の存在下、
加水分解することにより3−アルケニルカテコールを製
造する方法の改良に関するものである。DETAILED DESCRIPTION OF THE INVENTION [Industrial Field of Application] The present invention relates to a method for producing 3-alkenylcatechol. More specifically, Ichinomaro 4-flukenylphenol was dissolved in alkaline water in the presence of a copper compound catalyst,
The present invention relates to an improvement in a method for producing 3-alkenylcatechol by hydrolysis.
3−アルケニルカテコール例えば3−イソブテニルカテ
コールはλ、−−ジメチルーー13−ジヒドロベンゾ−
7−フラニルメチルカルバメート、すなわちカルボフラ
ンの名で知られている殺虫剤原体の中間体として重要な
化合物である。3-Alkenylcatechol For example, 3-isobutenylcatechol is λ, --dimethyl-13-dihydrobenzo-
7-furanylmethyl carbamate, which is an important compound as an intermediate for the pesticide active ingredient known as carbofuran.
従来3−アルケニルカテコール例えば3−インブテニル
カテコールの製法としてコークコロ−6−インブテニル
フェノールを塩化第一銅の存在下苛性ソーダ水溶液で加
水分解する方法が知られている(特開昭!rg−17’
AJ39号)。Conventionally, as a method for producing 3-alkenylcatechol, such as 3-imbutenylcatechol, a method is known in which coro-6-inbutenylphenol is hydrolyzed with an aqueous solution of caustic soda in the presence of cuprous chloride (JP-A-Show! RG-17'
AJ No. 39).
しかしながら該方法は、クロルフェノール類の加水分解
反応速度が遅<i’to−irocの高い反応温度を必
要とし、かつ触媒としての銅化合物を多量に使用する必
要があるため、高温反応によるカテコール類の選択性の
低下が起こり。However, this method requires a high reaction temperature such that the hydrolysis reaction rate of chlorophenols is slow <i'to-iroc, and it is necessary to use a large amount of copper compound as a catalyst. A decrease in selectivity occurs.
又、高い反応圧力、銅化合物の還元析出の問題、更には
銅使用量が多いことによる経済性の低下など工業的に必
ずしも有利な方法とはいえない。In addition, this method is not necessarily industrially advantageous because of problems such as high reaction pressure, reduction and precipitation of copper compounds, and lower economic efficiency due to the large amount of copper used.
本発明者はツーハロー6−アルケニルフェノールを銅化
合物触媒の存在下加水分解して3−アルケニルカテコー
ルを製造する方法について鋭意検討した結果ある種の金
属に対してキレート作用をもつ化合物を存在させること
によシ顕著に加水分解反応速度が増大し、よって、反応
温度の低温化、触媒量の低減が達成できることを見い出
した。As a result of extensive research into a method for producing 3-alkenylcatechol by hydrolyzing two-halo 6-alkenylphenol in the presence of a copper compound catalyst, the present inventor has determined to include a compound that has a chelating effect on certain metals. It has been found that the hydrolysis reaction rate is significantly increased, and therefore the reaction temperature can be lowered and the amount of catalyst can be reduced.
本発qの要旨uニーハロ−6−アルヶニルフェノールを
アルカリ水溶液中、銅化合物触媒の存在下加水分解する
ことにより3−アルケニルカテコールを製造する方法に
おいて反応系に芳香環中及び/または芳香環に直結した
位置に酸素原子及び/または窒素原子を有する二連配位
化合物を存在させることを特徴とする3−アルケニルカ
テコールの製造法に存する。Summary of this project qU In a method for producing 3-alkenylcatechol by hydrolyzing ni-halo-6-alkanylphenol in an alkaline aqueous solution in the presence of a copper compound catalyst, aromatic rings and/or aromatic rings are present in the reaction system. The present invention relates to a method for producing 3-alkenylcatechol, characterized by the presence of a double coordination compound having an oxygen atom and/or a nitrogen atom at a position directly connected to the 3-alkenylcatechol.
以下、本発明を更に詳細に説明する。The present invention will be explained in more detail below.
本発明の反応原料であるツーハロー6−アルケニルフェ
ノールは、下記一般式(I)で表わされる。Two-halo 6-alkenylphenol, which is a raw material for the reaction of the present invention, is represented by the following general formula (I).
(式中、Xはハロゲン原子、 R’、R”及びRAは同
−又は相異なシ水素原子、C1〜C8のアルキル基を表
わす。)
一般式(1)で表わされる化合物の具体例としては、コ
ーククロー6−イソプテニルフエノー/l/、J−フa
モー t、−インブテニルフェノール。(wherein, , coke claw 6-isoptenylphenol/l/, J-fa
Mot, -inbutenylphenol.
ニークロロ−6−ビニルフェノール、ニーブロモー6−
ビニルフェノール、コーク−ロー6一プロベニルフェノ
ール、コープクモ−6−プロペニルフェノール、コーク
クロー6−プテニルフエノール、コシプロモー4−プ?
ニルフエノール、ニークロロ−6−(コーンチル−l−
ブテニル)フェノール、ニープロモー1.−(2−メチ
ル−t−7’テニル)フェノール、ニークロロ−6−(
ニーエチルーl−ブテニル)フェノール、−一プロモ−
6−(2−エチル−7−ブテニル)フェノール、ニーク
ロローb−(/−メチル−7−ブテニル)フェノール、
コーブロ%−t、−(t−メチル−l−ブテニル)フェ
ノール、ニークロロ−&−(/−エチル−インブテニル
)フェノール、コープロモ−4−(t−エチル−インブ
テニル)フェノール等が挙げられるが、好ましくはアル
ケニル基の炭素数が−〜6でXが塩素原子又は臭素原子
のものであり。Nichloro-6-vinylphenol, Nibromo-6-
Vinylphenol, Coco-Cro-6-probenylphenol, Coco-Cro-6-propenylphenol, Coco-Cro-6-Ptenylphenol, Cocypromo-4-P?
Nilphenol, dichloro-6-(cornyl-l-
butenyl) phenol, kneepromo1. -(2-methyl-t-7'tenyl)phenol, nichloro-6-(
Niethyl-l-butenyl)phenol, -promo-
6-(2-ethyl-7-butenyl)phenol, nichlorob-(/-methyl-7-butenyl)phenol,
Cobro%-t, -(t-methyl-l-butenyl)phenol, nichloro-&-(/-ethyl-inbutenyl)phenol, copromo-4-(t-ethyl-inbutenyl)phenol, etc. are mentioned, but preferably The alkenyl group has - to 6 carbon atoms, and X is a chlorine atom or a bromine atom.
特KJ−クロロ−6−インプテニルフエノールが好まし
い。Particularly preferred is KJ-chloro-6-imptenylphenol.
本発明で触媒として使用する銅化合物は一価銅化合物、
二価銅化合物のいずれでもよく例えば硫酸鋼、硝酸鋼、
塩化第二鋼、塩化第一銅、酸化第二銅、亜酸化銅、水酸
化鋼などが挙げられる。これらの銅化合物の使用量は通
常ニーハロー6−アルケニルフェノール1モルIC対し
て銅として0.00/−/グラム原子、好ましくはo、
oi〜0.2グラム原子である。The copper compounds used as catalysts in the present invention are monovalent copper compounds,
Any divalent copper compound may be used, such as sulfate steel, nitrate steel,
Examples include chlorinated steel, cuprous chloride, cupric oxide, cuprous oxide, and hydroxide steel. The amount of these copper compounds used is usually 0.00/-/gram atom of copper per 1 mol IC of nihalo-6-alkenylphenol, preferably o,
oi ~ 0.2 gram atom.
前記一般式CI)で表わされる2−ハロー6−アルケニ
ルフェノールの加水分解反応は、アルカリ水溶液中で行
なわれる。アルカリとしては苛性ソーダ、苛性カリ、水
酸化カルシウム等が挙げられるが苛性ソーダ、苛性カリ
が好ましい。The hydrolysis reaction of the 2-halo-6-alkenylphenol represented by the general formula CI) is carried out in an alkaline aqueous solution. Examples of the alkali include caustic soda, caustic potash, and calcium hydroxide, with caustic soda and caustic potash being preferred.
その使用iはコー^−ロー6−アルケニルフェノールに
対してコ〜ざ倍モル、好ましくは一〜参倍モルである。The amount used is 1 to 1 times the mole, preferably 1 to 1 times the amount of co^-rho-6-alkenylphenol.
苛性アルカリは通常アルカリ水溶液として反応系に添加
するが、添加する苛性アルカリ水溶液の濃度は通常O,
S〜20直量暢であり、好ましくは一〜10重量秀であ
る。Caustic alkali is usually added to the reaction system as an alkaline aqueous solution, and the concentration of the added caustic alkali aqueous solution is usually O,
S~20 weight strength, preferably 1~10 weight strength.
本Q明でld、2−ハロ−6−アルケニルフェノール、
銅化合物触媒及びアルカリ水溶液からなる反応系に、芳
香環中及び/または芳香環に直結した位置に酸素原子及
び/または窒素原子を有する二連配位化合物を存在させ
ることを必須の要件とする。In this Q, ld, 2-halo-6-alkenylphenol,
It is an essential requirement that a double coordination compound having an oxygen atom and/or a nitrogen atom in an aromatic ring and/or in a position directly connected to an aromatic ring be present in a reaction system consisting of a copper compound catalyst and an aqueous alkali solution.
芳香族中及び/ま九は芳香環に直結した位置に酸素原子
及び/ま九は窒素原子を有する二連配位化合物としては
例えばj−ヒドロキシキノリン、g−アミノキノリン、
ナフチリジン、j−スルホナフチルアミン、ざ−アミノ
ナフトール、l−ヒドロキシフェナジン、 !、!’−
ジピリジル、 u、!’−ジピリジルアミン、 2.2
’−ジピリジルエーテル、 J、!’−ジピリジルチオ
エーテル、ユ、2′−ジピリジルケトン、ビビラジン、
J、J −ビス(ニーピリジル)ピラジン、l、IQ−
7エナンスロリン、ニーヒドロキシビリジン1、コーア
ミノビリジン、コーヒドロキシメチルピリジン、0−ア
ミノフェノール、0−アミノ安息香酸、カテコール、メ
トキシカテコール、サリチル酸、J−(4(−ピラゾリ
ル)−アミノプロピオン酸などが挙げられる。これらの
化合物はさらにC,%C,のアルキル基、C,S−C,
のアルケニル基+ C,〜CIoのアラルキル基、ヒド
ロキシル基、C1〜C6のアルコキシ基、アミノ基、C
5〜C2のアルキルアミ7基、スルホ基、C1〜C4の
アルキルスルホニル基、ニトロ基、ハロゲン原子、カル
ボキシ基等の置換基、好ましくはC1〜C5のアルキル
基、ヒドロキシ基、スルホ基、ニトロ基、ハロゲン原子
、カルボキシ基等で置換されていてもよい。かかる化合
物としては1例えばコータチル−t−ヒドロキシキノリ
ン、ψ、t−ジヒドロキシキノリン、ダーアルコキシー
j−ヒドロキシキノリン、!−アミノーt−ヒドロキシ
キノリン%j−スルホ−j−ヒドロキシキノリン、!−
ニトローt−ヒドロキシ中ノリン、j−10ローj−ヒ
ドロヤシキノ1.)ン、コーカルポキシーt−ヒドロキ
シキノリン、j17−ジクロル−g−ヒドロキシキノリ
ン、コーカルボキシー弘、t−ジヒドロキシキノリン等
が挙げられる。本発明の二車配位化合物のうち、錯体を
形成し九際、中心金属とのキレートがj〜6員環を形成
する化合物が特に好ましい。Examples of divalent coordination compounds having an oxygen atom and/or a nitrogen atom in the aromatic group and in a position directly connected to the aromatic ring include j-hydroxyquinoline, g-aminoquinoline,
Naphthyridine, j-sulfonaphthylamine, aminonaphthol, l-hydroxyphenazine, ! ,! '−
Dipyridyl, u! '-dipyridylamine, 2.2
'-dipyridyl ether, J,! '-dipyridyl thioether, 2'-dipyridyl ketone, bivirazine,
J, J-bis(neepyridyl)pyrazine, l, IQ-
Examples include 7-enanthroline, dihydroxypyridine 1, co-aminopyridine, co-hydroxymethylpyridine, 0-aminophenol, 0-aminobenzoic acid, catechol, methoxycatechol, salicylic acid, J-(4(-pyrazolyl)-aminopropionic acid) These compounds further contain an alkyl group of C, %C, C, S-C,
alkenyl group + C, ~CIo aralkyl group, hydroxyl group, C1-C6 alkoxy group, amino group, C
Substituents such as 5 to C2 alkylamino groups, sulfo groups, C1 to C4 alkylsulfonyl groups, nitro groups, halogen atoms, carboxy groups, preferably C1 to C5 alkyl groups, hydroxy groups, sulfo groups, nitro groups, It may be substituted with a halogen atom, a carboxy group, etc. Such compounds include, for example, cortacyl-t-hydroxyquinoline, ψ,t-dihydroxyquinoline, d-alkoxyj-hydroxyquinoline,! -amino-t-hydroxyquinoline% j-sulfo-j-hydroxyquinoline,! −
Nitro t-Hydroxy Norin, J-10 Rho J-Hydroyashikino 1. ), cocarboxy t-hydroxyquinoline, j17-dichloro-g-hydroxyquinoline, cocarboxylic acid, t-dihydroxyquinoline, and the like. Among the bivalent coordination compounds of the present invention, compounds in which a complex is formed and the chelate with the central metal forms a j- to six-membered ring are particularly preferred.
これらの二車配位化合物は反応系内で触媒である銅化合
物とある量論関係をもつで錯体を形配位化合物の使用量
は銅化合物に対して0,07〜700倍モル、好ましく
は1〜コO倍モル必要である。These two-wheel coordination compounds have a certain stoichiometric relationship with the copper compound as a catalyst in the reaction system, so they form a complex.The amount of the coordination compound used is 0.07 to 700 times the amount of the copper compound, preferably 1 to 0 times the mole is required.
尚、本発明に於ては、銅化合物触媒と二車配位化合物を
夫々単独で反応系に添加する代わシに、銅化合物と二車
配位化合物により生成する銅錯体をあらかじめ公知の方
法〔例えばg−ヒドロキシキノリンの場合Sp@atr
o Chlm、Aeta g(iqs6)/ ]により
製造し、反応系に添加してもよい。In the present invention, instead of adding the copper compound catalyst and the two-wheel coordination compound alone to the reaction system, the copper complex formed by the copper compound and the two-wheel coordination compound is prepared in advance by a known method [ For example, in the case of g-hydroxyquinoline, Sp@atr
o Chlm, Aeta g(iqs6)/] and may be added to the reaction system.
本発明の加水分解反応は通常100〜コ00C1好まし
くは13θ〜/70cで行なわれる。The hydrolysis reaction of the present invention is usually carried out at a temperature of 100 to 00C1, preferably 13θ to 70C.
圧力は反応混合物を液相に保持することができる圧力で
あればよく1通常、常圧又は、加水分解反応の自己発生
圧力下あるいは窒素等の不活性ガス加圧下で実施され、
前記温度の場合には約t−tqkg/cd!である。反
応温度があまり低くすぎると反応速度が遅く、逆にあま
シ高すぎると反応系中の銅−二車配位化合物錯体が不安
定となり銅が析出するばかりか目的とするJ−アルケニ
ルカテコールの収率も低下するので好ましくない。また
反応時間は通常0.5〜io時間程度である。The pressure may be any pressure that can maintain the reaction mixture in a liquid phase.1 Usually, the reaction is carried out at normal pressure, under the self-generated pressure of the hydrolysis reaction, or under the pressure of an inert gas such as nitrogen,
At the above temperature, about t-tqkg/cd! It is. If the reaction temperature is too low, the reaction rate will be slow; on the other hand, if the reaction temperature is too high, the copper-binary coordination compound complex in the reaction system will become unstable, leading to precipitation of copper and impeding the yield of the target J-alkenylcatechol. This is not preferable because the rate also decreases. Further, the reaction time is usually about 0.5 to io hours.
本発明の反応においては反応途中で反応系内の銅錯体化
合物よシごく一部の銅が金属鋼として析出し、これが反
応器に付着することもあるがこれを防止するためには反
応装置として1反応器合物と接する内壁面をフッ素樹脂
で構成したものを用いることが望ましい。In the reaction of the present invention, a small amount of copper may precipitate as metal steel from the copper complex compound in the reaction system during the reaction, and this may adhere to the reactor. 1. It is desirable to use one in which the inner wall surface in contact with the reactor is made of fluororesin.
反応終了後の混合物は通常、常圧まで降圧したのち金属
鋼が析出していればこれを濾過によシ分離する。p液は
PHり以下にすることKよ1)J−アルケニルカテコー
ルを含む結晶またはオイル層及び水層を形成させ、次い
でこれを分離したのち結晶またはオイル層は必要に応じ
て、再結晶または蒸溜することにより目的とするJ−ア
ルケニルカテコールを回収することができる。またJ−
アルケニルカテコールを分離し念水層からは中和等の通
常の方法によυ銅錯体及び/または過剰の二車配位化合
物が回収され、ニーハロー6−アルケニルフエツールノ
加水分解の触媒または反応系に存在させる二車配位化合
物として再使用することもできる。After the reaction is completed, the pressure of the mixture is usually lowered to normal pressure, and if metal steel is precipitated, it is separated by filtration. The pH of the p-liquid should be lower than 1) Form a crystal or oil layer containing J-alkenylcatechol and an aqueous layer, then separate this, and then recrystallize or distill the crystal or oil layer as necessary. By doing so, the target J-alkenylcatechol can be recovered. Also J-
The alkenylcatechol is separated, and the υ copper complex and/or the excess divalent coordination compound are recovered from the aqueous layer by a conventional method such as neutralization, and are used as a catalyst or reaction system for the hydrolysis of nihalo6-alkenylfetool. It can also be reused as a dicared coordination compound present in
次に本発明を実施例によシ更に詳細に説明するが、本発
明はその要旨を超えない限り以下の実施例に限定される
ものではない。Next, the present invention will be explained in more detail with reference to examples, but the present invention is not limited to the following examples unless it exceeds the gist thereof.
実施例1
シキノリン0.190fをこのアルカリ水溶液に添加し
!θ〜60Cで溶解させ念。硫酸銅五水塩O,ユ!0?
を水コ―に溶解した水溶液を上記t−ヒドロキシキノリ
ンのアルカリ水溶液に攪拌下添加しO,S時間攪拌を続
は次いでコーク四ロー6−インプテニルフエノール、7
.A s tヲ添加し溶解させたのち808製加圧反応
器内部を窒素置換した。/jj″−/j4℃に温度調節
した油浴に上記SUS製加圧反応器を浸してS時間加熱
攪拌させた。反応終了後反応液を窒素雰囲気下、3j%
塩酸り―を含む水溶液コQ−に添加し遊離した油状物を
ベンゼン/ T HF −/(体積比)の混合液コOt
dで抽出し抽出物な液体クロマトグラフィーで定量した
結果コーク四ロー6−インプテニルフエノールの転換率
はgosでありJ−イソブテニルカテコールノ収率は6
1チであった。Example 1 0.190f of Shiquinoline was added to this alkaline aqueous solution! Make sure to dissolve at θ~60C. Copper sulfate pentahydrate O, yu! 0?
An aqueous solution prepared by dissolving t-hydroxyquinoline in water coke was added to the above alkaline aqueous solution of t-hydroxyquinoline under stirring, and the mixture was stirred for O, S hours.
.. After adding Ast and dissolving it, the inside of the 808 pressurized reactor was purged with nitrogen. /jj''-/jThe SUS pressurized reactor was immersed in an oil bath whose temperature was adjusted to 4°C and heated and stirred for S hours. After the reaction was completed, the reaction solution was heated to 3j% under a nitrogen atmosphere.
Add the liberated oil to an aqueous solution containing hydrochloric acid (Q) and add it to a mixed solution of benzene/THF/(volume ratio).
As a result of extracting and quantifying the extract by liquid chromatography, the conversion rate of Coke 4-6-imptenylphenol was gos, and the yield of J-isobutenylcatechol was 6.
It was 1ch.
比較例1
実施例1においてt−ヒドロキシキノリンを除いたほか
は全〈実施例1と同様に反応を実施した結果コーク四ロ
ー6−インプテニルフエノールの転換率はコチであり3
−イソブテニルカテコールの収率はi%にすぎなかった
。このことによ)g−ヒドロキシキノリンの反応速度に
およぼす効果が非常に大きいことが判った。Comparative Example 1 The reaction was carried out in the same manner as in Example 1 except that t-hydroxyquinoline was removed. As a result, the conversion rate of Coke 4-row 6-imptenylphenol was
- The yield of isobutenylcatechol was only i%. It was found that the effect of g-hydroxyquinoline on the reaction rate was very large.
実施例2〜6
表−!記載のj−ヒドロキシキノリン誘導体を1#ic
酸鋼五水塩に対しコ倍モル使用した以外は実施例1と同
様にしてコーク四ロー6−インプテニルフエノールの加
水分解を行なった。結果を表−1に示した。Examples 2-6 Table-! 1#ic of the j-hydroxyquinoline derivative described above.
Coke tetralo 6-imptenylphenol was hydrolyzed in the same manner as in Example 1, except that twice the mole of acid steel pentahydrate was used. The results are shown in Table-1.
表−l
実施例ク
コ、2′−ジピリジルアミン0.J I J 54をア
セトニトリル20−に溶解したのち塩化第1銅0.09
9 fl−を添加し室温で1時間攪拌し、次いで減圧下
アセトニトリルを溜去しコ、コ′−ジピリジルアミンの
銅錯体を調製した。Table-l Example Lycium, 2'-dipyridylamine 0. After dissolving J I J 54 in 20 - acetonitrile, cuprous chloride 0.09
9 fl- was added and stirred at room temperature for 1 hour, and then acetonitrile was distilled off under reduced pressure to prepare a copper complex of co,co'-dipyridylamine.
5O8−,31&展加圧反応器中で9 !r % Na
OHコ、2り?を水5sccに溶解し、次いでコーク四
ロー6−インプテニルフエノール3.6り?ヲ添加、溶
解した。このコークロロー!−−イソ7”fニルフェノ
ールのアルカリ水溶液に前記銅錯体を添加したのちSU
s製加圧反応器を窒゛累置換し、該反応器を/gO−/
l/Cに温度調節した油浴に浸して3時間加熱攪拌した
。反応終了後、反応液を実施例1と同様に処理したとこ
ろコーク四ロー6−インプテニルフエノールの転換率は
9s%、3−インブテニルフェノールの収率は67チで
あった。5O8-, 31 & 9 in a pressurized reactor! r%Na
OH, two? was dissolved in 5 scc of water, and then 3.6 cc of Coke 4-row 6-imptenylphenol was added. Added and dissolved. This corroro! --After adding the copper complex to an alkaline aqueous solution of iso7''f-nylphenol, SU
A pressurized reactor manufactured by S was repeatedly replaced with nitrogen, and the reactor was
The mixture was immersed in an oil bath whose temperature was adjusted to 1/C and heated and stirred for 3 hours. After the reaction was completed, the reaction solution was treated in the same manner as in Example 1, and the conversion rate of Coke 4-6-inputenylphenol was 9s%, and the yield of 3-inbutenylphenol was 67s%.
実施例ff −/り、比較例コ
銅化合物として塩化第一銅を使用し1表−一記載の二車
配位化合物を所定量使用した以外は実施例1と同様にし
てコークコロ−6−インブテニルフェノールの加水分解
反応を行なった。Example ff - / Comparative Example Coke coro-6-imbu was prepared in the same manner as in Example 1, except that cuprous chloride was used as the copper compound and a predetermined amount of the two-wheel coordination compound listed in Table 1 was used. The hydrolysis reaction of tenylphenol was carried out.
結果を表−コに示した。The results are shown in Table C.
本発明によれば、−一ハロー6−アルケニルフェノール
をアルカリ水溶液中、銅化合物触媒の存在下加水分解す
ることによりJ−アルケニルカテコールを製造する方法
に於て1反応系に特定の二車配位化合物を存在させるこ
とにより。According to the present invention, in a method for producing J-alkenylcatechol by hydrolyzing -1-halo-6-alkenylphenol in an alkaline aqueous solution in the presence of a copper compound catalyst, a specific bivalent coordination is provided in one reaction system. By having a compound present.
加水分解反応速度が著しく増大し、よって少ない触媒量
でも高転換率及び高収率で目的とするJ−アルケニルカ
テコールを取得することが可能である。The hydrolysis reaction rate is significantly increased, and therefore it is possible to obtain the desired J-alkenylcatechol at a high conversion rate and high yield even with a small amount of catalyst.
出願人 三菱化成工業株式会社 代理人 弁理士 長谷用 − (ほか1名)Applicant: Mitsubishi Chemical Industries, Ltd. Agent: Patent Attorney Hase - (1 other person)
Claims (1)
水溶液中、銅化合物触媒の存在下加水分解することによ
り3−アルケニルカテコールを製造する方法において反
応系に、芳香環中及び/または芳香環に直結した位置に
酸素原子及び/または窒素原子を有する二座配位化合物
を存在させることを特徴とする3−アルケニルカテコー
ルの製造法(1) In a method for producing 3-alkenylcatechol by hydrolyzing 2-halo-6-alkenylphenol in an alkaline aqueous solution in the presence of a copper compound catalyst, it is directly connected to the aromatic ring and/or to the reaction system. A method for producing 3-alkenylcatechol, characterized by the presence of a bidentate compound having an oxygen atom and/or nitrogen atom at the position
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP61102270A JPH07108872B2 (en) | 1986-05-02 | 1986-05-02 | Process for producing 3-alkenylcatechol |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP61102270A JPH07108872B2 (en) | 1986-05-02 | 1986-05-02 | Process for producing 3-alkenylcatechol |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS62258331A true JPS62258331A (en) | 1987-11-10 |
| JPH07108872B2 JPH07108872B2 (en) | 1995-11-22 |
Family
ID=14322905
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP61102270A Expired - Lifetime JPH07108872B2 (en) | 1986-05-02 | 1986-05-02 | Process for producing 3-alkenylcatechol |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH07108872B2 (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH04338348A (en) * | 1991-05-13 | 1992-11-25 | Mitsubishi Kasei Corp | Method for producing catechols |
-
1986
- 1986-05-02 JP JP61102270A patent/JPH07108872B2/en not_active Expired - Lifetime
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH04338348A (en) * | 1991-05-13 | 1992-11-25 | Mitsubishi Kasei Corp | Method for producing catechols |
Also Published As
| Publication number | Publication date |
|---|---|
| JPH07108872B2 (en) | 1995-11-22 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| PL128067B1 (en) | Method of manufacture of diaryl ethers | |
| JPH01308245A (en) | Production of benoic acid and salt thereof | |
| JPH0739366B2 (en) | Method for producing o-hydroxy-benzaldehyde | |
| US4048236A (en) | Process for preparing o-alkoxy-p-allylphenols | |
| JPS61282355A (en) | Manufacture of 4,4'-dinitrostilbene-2,2'-disulfonate | |
| JPH07108872B2 (en) | Process for producing 3-alkenylcatechol | |
| JPS5828259B2 (en) | Method for producing phloroglucin and its derivatives | |
| JPH04334334A (en) | Production method of catechols | |
| JPS6078948A (en) | Production of iminodiacetate | |
| JP3784865B2 (en) | Method for producing 4,4'-bis (chloromethyl) biphenyl | |
| JP3278945B2 (en) | Method for producing parafluorophenol | |
| JPS6245A (en) | Production of 2,3,4,5-tetrafluorobenzoic acid | |
| RU2155185C1 (en) | Method of preparing partially fluorinated benzoic acids | |
| JPS6399029A (en) | Hydrolysis of aromatic iodide | |
| CN110713434B (en) | Intermediate of compound with anticancer activity, preparation method and application thereof | |
| US2948737A (en) | Process for the production of thiophene carboxylic acids | |
| US3657343A (en) | Preparation of ynamines and phenylacetamides | |
| JPH04338348A (en) | Method for producing catechols | |
| WO2000069825A1 (en) | Process for preparing tribromomethylsulfonylpyridine | |
| JPS6159614B2 (en) | ||
| JPS61200938A (en) | Manufacture of 4,4'_dihydroxydiphenyl ether | |
| JPH0338537A (en) | Synthesis of biphenyl-4,4'-diol | |
| JPS5929659A (en) | Preparation of thiosalicylic acid and dithiosalicylic acid | |
| SU441702A1 (en) | Method for producing ethylene glycol esters | |
| JPH0334947A (en) | Production of dihydric phenols |