JPS62185035A - Production of 2-indanone - Google Patents
Production of 2-indanoneInfo
- Publication number
- JPS62185035A JPS62185035A JP61024167A JP2416786A JPS62185035A JP S62185035 A JPS62185035 A JP S62185035A JP 61024167 A JP61024167 A JP 61024167A JP 2416786 A JP2416786 A JP 2416786A JP S62185035 A JPS62185035 A JP S62185035A
- Authority
- JP
- Japan
- Prior art keywords
- acid
- organic
- reaction
- hydrogen peroxide
- indene
- 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.)
- Pending
Links
- UMJJFEIKYGFCAT-UHFFFAOYSA-N indan-2-one Chemical compound C1=CC=C2CC(=O)CC2=C1 UMJJFEIKYGFCAT-UHFFFAOYSA-N 0.000 title claims abstract description 14
- 238000004519 manufacturing process Methods 0.000 title claims description 11
- MHAJPDPJQMAIIY-UHFFFAOYSA-N Hydrogen peroxide Chemical compound OO MHAJPDPJQMAIIY-UHFFFAOYSA-N 0.000 claims abstract description 23
- 239000003960 organic solvent Substances 0.000 claims abstract description 13
- 239000002253 acid Substances 0.000 claims abstract description 9
- 239000003054 catalyst Substances 0.000 claims abstract description 9
- 150000007524 organic acids Chemical class 0.000 claims abstract description 9
- 239000003513 alkali Substances 0.000 claims abstract description 8
- 229910052500 inorganic mineral Inorganic materials 0.000 claims abstract description 8
- 239000011707 mineral Substances 0.000 claims abstract description 8
- 125000000217 alkyl group Chemical group 0.000 claims abstract description 7
- 150000002469 indenes Chemical class 0.000 claims description 11
- 239000000203 mixture Substances 0.000 claims description 6
- 229910052739 hydrogen Inorganic materials 0.000 claims description 5
- 239000001257 hydrogen Substances 0.000 claims description 5
- 125000004435 hydrogen atom Chemical group [H]* 0.000 claims description 4
- 239000002904 solvent Substances 0.000 claims description 3
- 239000000126 substance Substances 0.000 claims 2
- 238000006243 chemical reaction Methods 0.000 abstract description 20
- YBYIRNPNPLQARY-UHFFFAOYSA-N 1H-indene Chemical compound C1=CC=C2CC=CC2=C1 YBYIRNPNPLQARY-UHFFFAOYSA-N 0.000 abstract description 14
- 238000000034 method Methods 0.000 abstract description 13
- 150000004967 organic peroxy acids Chemical class 0.000 abstract description 11
- YMWUJEATGCHHMB-UHFFFAOYSA-N Dichloromethane Chemical compound ClCCl YMWUJEATGCHHMB-UHFFFAOYSA-N 0.000 abstract description 7
- KWYUFKZDYYNOTN-UHFFFAOYSA-M Potassium hydroxide Chemical compound [OH-].[K+] KWYUFKZDYYNOTN-UHFFFAOYSA-M 0.000 abstract description 6
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 abstract description 6
- -1 etc. Chemical compound 0.000 abstract description 5
- 238000010438 heat treatment Methods 0.000 abstract description 5
- 150000002978 peroxides Chemical class 0.000 abstract description 5
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 abstract description 4
- VZGDMQKNWNREIO-UHFFFAOYSA-N tetrachloromethane Chemical compound ClC(Cl)(Cl)Cl VZGDMQKNWNREIO-UHFFFAOYSA-N 0.000 abstract description 4
- UOCLXMDMGBRAIB-UHFFFAOYSA-N 1,1,1-trichloroethane Chemical compound CC(Cl)(Cl)Cl UOCLXMDMGBRAIB-UHFFFAOYSA-N 0.000 abstract description 2
- SCYULBFZEHDVBN-UHFFFAOYSA-N 1,1-Dichloroethane Chemical compound CC(Cl)Cl SCYULBFZEHDVBN-UHFFFAOYSA-N 0.000 abstract description 2
- 239000007810 chemical reaction solvent Substances 0.000 abstract description 2
- 230000001590 oxidative effect Effects 0.000 abstract description 2
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 abstract 3
- HEDRZPFGACZZDS-UHFFFAOYSA-N Chloroform Chemical compound ClC(Cl)Cl HEDRZPFGACZZDS-UHFFFAOYSA-N 0.000 abstract 2
- XBDQKXXYIPTUBI-UHFFFAOYSA-N dimethylselenoniopropionate Natural products CCC(O)=O XBDQKXXYIPTUBI-UHFFFAOYSA-N 0.000 abstract 2
- 239000011369 resultant mixture Substances 0.000 abstract 2
- 150000001875 compounds Chemical class 0.000 abstract 1
- 235000019260 propionic acid Nutrition 0.000 abstract 1
- IUVKMZGDUIUOCP-BTNSXGMBSA-N quinbolone Chemical compound O([C@H]1CC[C@H]2[C@H]3[C@@H]([C@]4(C=CC(=O)C=C4CC3)C)CC[C@@]21C)C1=CCCC1 IUVKMZGDUIUOCP-BTNSXGMBSA-N 0.000 abstract 1
- 239000010410 layer Substances 0.000 description 9
- BDAGIHXWWSANSR-UHFFFAOYSA-N methanoic acid Natural products OC=O BDAGIHXWWSANSR-UHFFFAOYSA-N 0.000 description 8
- 238000007254 oxidation reaction Methods 0.000 description 6
- 239000002994 raw material Substances 0.000 description 6
- 235000010755 mineral Nutrition 0.000 description 5
- 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 4
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 4
- 235000019253 formic acid Nutrition 0.000 description 4
- 239000011541 reaction mixture Substances 0.000 description 4
- 238000003756 stirring Methods 0.000 description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 4
- WSLDOOZREJYCGB-UHFFFAOYSA-N 1,2-Dichloroethane Chemical compound ClCCCl WSLDOOZREJYCGB-UHFFFAOYSA-N 0.000 description 3
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 description 3
- 238000009835 boiling Methods 0.000 description 3
- GKIPXFAANLTWBM-UHFFFAOYSA-N epibromohydrin Chemical compound BrCC1CO1 GKIPXFAANLTWBM-UHFFFAOYSA-N 0.000 description 3
- JGJLWPGRMCADHB-UHFFFAOYSA-N hypobromite Inorganic materials Br[O-] JGJLWPGRMCADHB-UHFFFAOYSA-N 0.000 description 3
- 235000005985 organic acids Nutrition 0.000 description 3
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 2
- 229910000831 Steel Inorganic materials 0.000 description 2
- 239000006227 byproduct Substances 0.000 description 2
- 239000007795 chemical reaction product Substances 0.000 description 2
- 239000003795 chemical substances by application Substances 0.000 description 2
- 238000007796 conventional method Methods 0.000 description 2
- 230000007423 decrease Effects 0.000 description 2
- 150000002468 indanes Chemical class 0.000 description 2
- 239000012044 organic layer Substances 0.000 description 2
- 230000003647 oxidation Effects 0.000 description 2
- BWHMMNNQKKPAPP-UHFFFAOYSA-L potassium carbonate Chemical compound [K+].[K+].[O-]C([O-])=O BWHMMNNQKKPAPP-UHFFFAOYSA-L 0.000 description 2
- 229910000029 sodium carbonate Inorganic materials 0.000 description 2
- 239000010959 steel Substances 0.000 description 2
- KVCQTKNUUQOELD-UHFFFAOYSA-N 4-amino-n-[1-(3-chloro-2-fluoroanilino)-6-methylisoquinolin-5-yl]thieno[3,2-d]pyrimidine-7-carboxamide Chemical compound N=1C=CC2=C(NC(=O)C=3C4=NC=NC(N)=C4SC=3)C(C)=CC=C2C=1NC1=CC=CC(Cl)=C1F KVCQTKNUUQOELD-UHFFFAOYSA-N 0.000 description 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 1
- UIIMBOGNXHQVGW-DEQYMQKBSA-M Sodium bicarbonate-14C Chemical compound [Na+].O[14C]([O-])=O UIIMBOGNXHQVGW-DEQYMQKBSA-M 0.000 description 1
- 239000004280 Sodium formate Substances 0.000 description 1
- 238000010306 acid treatment Methods 0.000 description 1
- 229940030600 antihypertensive agent Drugs 0.000 description 1
- 239000002220 antihypertensive agent Substances 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- 238000013475 authorization Methods 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 239000012141 concentrate Substances 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 239000013078 crystal Substances 0.000 description 1
- 238000004821 distillation Methods 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000004880 explosion Methods 0.000 description 1
- 150000008282 halocarbons Chemical class 0.000 description 1
- QOSATHPSBFQAML-UHFFFAOYSA-N hydrogen peroxide;hydrate Chemical compound O.OO QOSATHPSBFQAML-UHFFFAOYSA-N 0.000 description 1
- QNXSIUBBGPHDDE-UHFFFAOYSA-N indan-1-one Chemical class C1=CC=C2C(=O)CCC2=C1 QNXSIUBBGPHDDE-UHFFFAOYSA-N 0.000 description 1
- 239000000543 intermediate Substances 0.000 description 1
- 239000012074 organic phase Substances 0.000 description 1
- 239000012071 phase Substances 0.000 description 1
- 239000006187 pill Substances 0.000 description 1
- 229910000027 potassium carbonate Inorganic materials 0.000 description 1
- WFIZEGIEIOHZCP-UHFFFAOYSA-M potassium formate Chemical compound [K+].[O-]C=O WFIZEGIEIOHZCP-UHFFFAOYSA-M 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- HLBBKKJFGFRGMU-UHFFFAOYSA-M sodium formate Chemical compound [Na+].[O-]C=O HLBBKKJFGFRGMU-UHFFFAOYSA-M 0.000 description 1
- 235000019254 sodium formate Nutrition 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 230000002269 spontaneous effect Effects 0.000 description 1
- 238000001256 steam distillation Methods 0.000 description 1
- 238000005292 vacuum distillation Methods 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
- 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]
本発明はインデン類にす2−インダノン類を製造する方
法に関する。DETAILED DESCRIPTION OF THE INVENTION [Industrial Field of Application] The present invention relates to a method for producing 2-indanones, which are indenes.
[従来の技術]
2−インダノン類は血圧降下剤等の医薬品の製造原料と
して重要であり、これまでにその製造法について種々報
告されている。例えば、インデンを原料とし、大過剰の
有機酸を溶媒として有機過酸を用いて酸化し、次いで鉱
酸中で加熱する方法(Org、 Syn、、 41.5
3(1,961))や、インデンに臭素水を反応させて
ブロムヒドリン体とし、次いでアルコール中でアルカリ
と反応させる方法(J、Arp、 Chew、 Soc
、、 57.2,022(1,935)及びJ、 ch
ew。[Prior Art] 2-indanones are important as raw materials for manufacturing pharmaceuticals such as antihypertensive agents, and various methods for their production have been reported so far. For example, a method in which indene is used as a raw material, oxidized using an organic peracid with a large excess of organic acid as a solvent, and then heated in a mineral acid (Org, Syn, 41.5
3 (1,961)), or a method in which indene is reacted with bromine water to form a bromohydrin, and then reacted with an alkali in alcohol (J, Arp, Chew, Soc.
,, 57.2,022 (1,935) and J, ch.
ew.
Soc、、 2,559(1,922) )等が知られ
て°いる。Soc, 2,559 (1,922)) etc. are known.
[発明が解決しようとする問題点]
しかしながら、これらのうらiyj者の有機過酸による
酸化法では、大過剰の有機酸、例えば蟻酸を溶媒として
使用するために製造コストの面で問題があり、しかし過
!iF[!とインデンを反応さUたまた、鉱酸処理に付
寸べき中間体を取り出寸ために反応混合物より蟻酸を留
去しなければイ5らず、これは未反応の過酸化物を高l
1lJfに濃縮することになって爆発等の危険性を伴な
うという重大な欠点を有している。他方、後者のブロム
ヒドリン法では、臭素水を使用するために+lI造コス
トの面や安全衛生の面で問題があり、しから副生成物の
発生により収率が低下するという欠点を有している。[Problems to be Solved by the Invention] However, these conventional oxidation methods using organic peracids have problems in terms of production cost because they use a large excess of organic acids, such as formic acid, as a solvent. But it's too late! iF[! In addition, in order to remove the intermediates to be subjected to the mineral acid treatment, formic acid must be distilled off from the reaction mixture, which removes unreacted peroxide at a high concentration.
It has a serious drawback in that it must be concentrated to 1 lJf, which poses a risk of explosion. On the other hand, the latter bromohydrin method uses bromine water, which poses problems in terms of production cost and safety and hygiene, and has the disadvantage that the yield decreases due to the generation of byproducts. .
本発明は未反応過酸化物を高濃度に濃縮することなり、
2−インダノン類を高い収率で得ることのできる製造方
法を提供することを目的とする。The present invention concentrates unreacted peroxide to a high concentration,
It is an object of the present invention to provide a manufacturing method that can obtain 2-indanones in high yield.
[問題点を解決するための手段]
本発明壱笠は、上記のような問題点を解決すべく鋭意検
討を行った結束、反応溶媒として非水溶性有機溶剤を用
い、アルカリ触媒の存在下に有機酸を加え、これらの混
合物に過酸化水素を滴下づることにより反応系内で右m
1stを発生させ、この反応系内で発生ずる有機過酸で
インデン類を酸化し、得られた中聞体を常法により鉱酸
と加熱することにより2−インダノン類が得られること
を見出し、本発明を完成したものである。[Means for Solving the Problems] The Ichikasa of the present invention is produced by using a water-insoluble organic solvent as the reaction solvent and in the presence of an alkali catalyst. By adding an organic acid and dropping hydrogen peroxide into the mixture, the right m
It was discovered that 2-indanones can be obtained by generating 1st, oxidizing indenes with the organic peracid generated in this reaction system, and heating the obtained mesomorph with mineral acid in a conventional manner, This completes the present invention.
本発明で使用する原料のインダン類としては、下記一般
式(I>
(式中、Rは水素または低級アルキル基を示す)で表わ
されるインダン又は低級アルキルインダンを挙げること
ができ、低級アルキル基としては、好ましくは炭素数1
〜3のアルキル基である。Examples of the raw material indanes used in the present invention include indanes or lower alkyl indanes represented by the following general formula (I> (in the formula, R represents hydrogen or a lower alkyl group), where the lower alkyl group is preferably has 1 carbon number
~3 alkyl group.
また、本発明で使用する非水溶性有機溶剤としては、使
用する有機酸及び反応系で生成する有機過酸に対して不
活性であり、実質的に水に溶解しない有機溶剤であれば
よく、例えばn−ヘキサジ、ベンビン、トルエン、塩化
メチレン、り[10ホルム、四塩化炭素、ジクロルエタ
ンあるいはトリクロルエタン等を挙げることができ、好
ましくは沸点100℃以下の低沸点ハロゲン化炭化水素
である。Further, the water-insoluble organic solvent used in the present invention may be any organic solvent as long as it is inert to the organic acid used and the organic peracid generated in the reaction system and is substantially insoluble in water. Examples include n-hexadi, bembin, toluene, methylene chloride, di[10]form, carbon tetrachloride, dichloroethane, and trichloroethane, and preferably a low-boiling halogenated hydrocarbon with a boiling point of 100°C or less.
さらに、本発明で使用するアルノJり触媒としては、例
えば水酸化ナトリウム、水酸化カリウム、炭酸ナトリウ
ム、炭酸カリウム、炭素水素ナトリウム、蟻酸ナトリウ
ム、蟻酸カリウム等を挙げることができる。このアルカ
リ触媒の使用量は、使用する原料のインデン類に対して
0.01〜0゜4当a、好ましくはo、i〜0.2当m
である。Furthermore, examples of the Alno-J catalyst used in the present invention include sodium hydroxide, potassium hydroxide, sodium carbonate, potassium carbonate, sodium bicarbonate, sodium formate, and potassium formate. The amount of this alkali catalyst to be used is 0.01 to 0.4 equivalents a, preferably o, i to 0.2 equivalents, based on the indenes used as raw materials.
It is.
このアルカリ触媒は酸化触媒として作用するもので、使
用しない場合には副生成物が増大し、反対に使用量がイ
ンデン類に対して0.4当虚を超えるときは原料の回収
母が増大し、いずれの場合も目的物である2−インダノ
ン類の収率が低下りる。This alkaline catalyst acts as an oxidation catalyst, and if it is not used, the amount of by-products will increase.On the other hand, if the amount used exceeds 0.4 equivalence to indenes, the amount of raw material recovered will increase. In either case, the yield of the target product, 2-indanones, decreases.
また、本発明で使用する有機酸としては、例えば蟻酸、
#l酸、プロピオンa!等の低級脂肪族モノカルボン酸
が好ましく、その使用Rは原料のインデン類に対して0
.5〜10当m、好ましくは1〜3当岳、である。In addition, examples of the organic acids used in the present invention include formic acid,
#l acid, propion a! Lower aliphatic monocarboxylic acids such as
.. It is 5 to 10 equivalents, preferably 1 to 3 equivalents.
本発明方法においては、上記インデン類、非水溶性有機
溶剤、アルカリ触媒及び右a酸の混合物° 巾に過酸化
水素を滴下して原−料のインデン類の酸化反応を行う。In the method of the present invention, hydrogen peroxide is added dropwise to the mixture of the indenes, a water-insoluble organic solvent, an alkali catalyst, and the right a acid to carry out the oxidation reaction of the raw indenes.
この目的で使用づ゛る過酸化水素としては、それが過酸
化水素そのものであっても、また、その水溶液(過酸化
水素水)であってもよいが、通常10〜90重固%過酸
化水素水、好ましくは20〜60重贋%過酸化水素水を
使用する。The hydrogen peroxide used for this purpose may be hydrogen peroxide itself or its aqueous solution (hydrogen peroxide solution), but it is usually 10 to 90% heavy solids peroxide. Hydrogen water, preferably 20 to 60% hydrogen peroxide water, is used.
この過酸化水素水の使用mは、原料のインデン類に対し
て0.5〜3当m、好ましくは161〜1゜5当mであ
る。The hydrogen peroxide solution used is 0.5 to 3 equivalents, preferably 161 to 1.5 equivalents, relative to the indenes as raw materials.
この過酸化水素水を上記混合物中に滴下して行うインデ
ン類の酸化反応は、その反応温度を通常O〜60℃、好
ましくは30〜40℃の範囲にするのがよく、従って、
過酸化水素水の滴下速度は反応温度が上記温度t!囲内
に維持される速度にするのがよい。さらに、このインデ
ン類の酸化反応は、過酸化水素の滴下終了後、撹拌を好
ましくは1〜10時間継続する。反応終了後、反応温度
を60’l上、例えば65〜80℃マーc 上fR,g
セ、反応系で生成した有機過酸を分解し、冷却後静置
して二層に分離させ、水層を除去する。なJ3、インデ
ン類の酸化反応生成物は、その大部分が有機溶剤層に溶
解しているが、水層にも少量溶解しているので、この水
層を反応に使用したと同じ有機溶剤で抽出し、回収する
のが望ましい。In the oxidation reaction of indenes carried out by dropping this hydrogen peroxide solution into the above mixture, the reaction temperature is usually in the range of 0 to 60°C, preferably 30 to 40°C.
The dropping rate of the hydrogen peroxide solution is such that the reaction temperature is above the temperature t! It is best to keep the speed within the range. Furthermore, in this oxidation reaction of indenes, stirring is preferably continued for 1 to 10 hours after the completion of dropping hydrogen peroxide. After the reaction is complete, increase the reaction temperature by 60'l, e.g. 65-80°C.
Second, the organic peracid produced in the reaction system is decomposed, and after cooling, it is allowed to stand to separate into two layers, and the aqueous layer is removed. J3, most of the oxidation reaction products of indenes are dissolved in the organic solvent layer, but a small amount is also dissolved in the water layer, so this water layer can be used in the same organic solvent used for the reaction. Preferably extracted and recovered.
次に、このようにして1!?られた有機溶剤層に鉱層、
例えば硫酸を加えて加熱し、目的とする下記一般式(I
I)
(式中、Rは水素または低級アルキル基を示す)で表さ
れる2−インダノン類、すなわら2−インダノン又は低
級アルキル置換2−インダノンを製造する。Next, do 1 like this! ? mineral layer in the organic solvent layer,
For example, by adding sulfuric acid and heating, the desired general formula (I
I) Produce 2-indanones represented by the formula (wherein R represents hydrogen or a lower alkyl group), ie, 2-indanone or lower alkyl-substituted 2-indanone.
この鉱酸を添加して行う加熱反応は通常70〜100℃
で0.5・〜2時間行う。有機溶剤の沸点が反応温度よ
り低い場合にはこの有機溶剤が留出した後所定の温度ま
で昇温する。反応終了後、有機相を分液し、これを例え
ば減圧蒸溜、水蒸気蒸溜等の適当な方法で分離精製する
。The heating reaction performed by adding this mineral acid is usually 70 to 100°C.
Do this for 0.5 to 2 hours. When the boiling point of the organic solvent is lower than the reaction temperature, the temperature is raised to a predetermined temperature after the organic solvent is distilled off. After the reaction is completed, the organic phase is separated and purified by an appropriate method such as vacuum distillation or steam distillation.
[実施例]
以下、実施例に塁いて、本発明方法を具体的に説明する
。[Example] Hereinafter, the method of the present invention will be specifically explained based on Examples.
実施例
インデン116gを1.2−ジクロルエタン3009に
溶解し、これに90重量%蟻酸153gと炭酸すトリウ
ム15gとを添加し、得られた混合物中に撹拌上反応温
度を30〜40℃に維持しながら35市■%過酸化水素
水130!Jを滴下し、滴下終了後35℃で6時間撹拌
を継続した。反応終了後、反応混合物の41ffを65
℃に上71させて30分間撹拌し、室温まで冷JJ]
L、て静置し、イ■1を分離して回収した。水層につい
ては1.2−ジクf−1ルエタン50gを使用して溶解
している反応生成物を回収し、」−2有IF!ffと合
せた。Example 116 g of indene was dissolved in 1,2-dichloroethane 3009, 153 g of 90% by weight formic acid and 15 g of sodium carbonate were added thereto, and the resulting mixture was stirred and the reaction temperature was maintained at 30 to 40°C. While 35 cities■% hydrogen peroxide solution 130! J was added dropwise, and after the completion of the addition, stirring was continued at 35°C for 6 hours. After the reaction is complete, 41ff of the reaction mixture is
Bring to 71°C, stir for 30 minutes, and cool to room temperature.]
The mixture was allowed to stand still, and ①1 was separated and collected. For the aqueous layer, 50 g of 1,2-dichloromethane was used to recover the dissolved reaction product, and the IF! Combined with ff.
次に、このようにして得られた有機層に15屯岳%VA
酸1.000グを加え、加熱しながら1.2−ジクロル
エタンを留去ざu、温度が100℃になったらその温度
で1時間撹拌を継続した。反応終了後、反応混合物を室
温まで冷却し、2−インダノンと1,2−ジクロルエタ
ンからなる有機層を分離して回収し、この右Ia層を1
7++m1llJで減圧蒸溜して2−インダノン95g
(収率72fflJri%、bp116〜118℃/1
7#1IllHO)を得た。Next, the organic layer obtained in this way was applied with 15% VA.
1.000 g of acid was added, 1,2-dichloroethane was distilled off while heating, and when the temperature reached 100°C, stirring was continued at that temperature for 1 hour. After the reaction was completed, the reaction mixture was cooled to room temperature, and an organic layer consisting of 2-indanone and 1,2-dichloroethane was separated and collected.
95g of 2-indanone distilled under reduced pressure with 7++mlJ
(Yield 72fflJri%, bp 116-118℃/1
7#1IllHO) was obtained.
[発明の効果]
本発明の方法によれば、有機過酸を反応系中で発生させ
ながら反応を進行させるので、反応の安全性が向上し、
反応終了後反応混合物を濃縮することなく未反応の過酸
化物を安全かつ容易に除去することができ、また有機酸
の使用段も従来の方法に比べて少なくてずみ、有機溶剤
も回収して再使用できるので製造コストの面でも極めて
有利である。しかも、本発明の方法によれば、従来の有
機過酸を使用する方法に比べて反応温度の制御が容易で
ある等その製造操作も改善される等、工業的に極めて有
用な製造方法である。[Effects of the Invention] According to the method of the present invention, the reaction proceeds while generating organic peracid in the reaction system, so the safety of the reaction is improved.
After the reaction is complete, unreacted peroxide can be removed safely and easily without concentrating the reaction mixture, and the number of steps for using organic acids is reduced compared to conventional methods, and organic solvents can also be recovered. Since it can be reused, it is extremely advantageous in terms of manufacturing costs. Moreover, the method of the present invention is an extremely useful manufacturing method industrially, as it is easier to control the reaction temperature and has improved manufacturing operations compared to conventional methods using organic peracids. .
特晶1出願人 新日鐵化学株式会社代 理 人
弁理士 成 瀬 勝 夫(外2名
)
手続ネit正書(自発)
昭和61年3月12日
特許庁長官 宇 賀 道 部 殿
1、事件の表示
昭和61年特許願第24167号
2、発明の名称
2−インダノン類の製造法
3、補正をする者
事件との閏゛係 特許出願人
住所 東京都中央区銀座五丁目13番16号名称 (6
64)新日鐵化学株式会礼
4、代理人 〒105 電話(433)4420住所
東京都港区新橋3丁目8番8号、上−ピル5階
5、補正により増加する発明の数 なし6、補正の対
象
補正の内容
(1)明m’a第2頁第8〜12行目を下記の通りに補
正する。Special Crystal 1 Applicant Nippon Steel Chemical Co., Ltd. Agent Patent Attorney Katsuo Naruse (2 others) Procedural Net Authorization (spontaneous) March 12, 1985 Commissioner of the Patent Office Michibe Uga 1, Display of the case 1986 Patent Application No. 24167 2, Name of the invention 2 - Process for producing indanones 3, Person making the amendment Interchange with the case Patent applicant address 13-16, Ginza 5-chome, Chuo-ku, Tokyo Name (6
64) Nippon Steel Chemical Co., Ltd. Rei 4, Agent 105 Telephone (433) 4420 Address
3-8-8 Shinbashi, Minato-ku, Tokyo, 5th Floor, 5th Pill, Number of inventions to be increased by the amendment None 6, Contents of the amendment subject to the amendment (1) Mei m'a, page 2, lines 8-12 Correct the eyes as follows.
f (Org、 Syn、、41.53(1961)
)や、インデンに臭素水を反応させてブロムヒドリン体
とし、次いでアルコール中でアルカリと反応させる方法
(J。f (Org, Syn, 41.53 (1961)
), or a method in which indene is reacted with bromine water to form a bromohydrin, and then reacted with an alkali in alcohol (J.
八m、 Chew、 Soc、、 57. 2,
022(1935)及σJ、 Chew。8m, Chew, Soc,, 57. 2,
022 (1935) and σJ, Chew.
Soc、、 2,559(1(122))等が知られテ
いル。j(2)明細書第5頁第17〜19行目に記載し
た[それが過酸化水素そのもの・・・・・・・・・であ
ってもよいが、Jを削除する。Soc, 2,559 (1 (122)) etc. are known. j (2) Described on page 5, lines 17 to 19 of the specification [It may be hydrogen peroxide itself, but J is deleted.
(3)明細書第7頁第11行目に記載した「相」をr層
jと補正する。(3) The "phase" described on page 7, line 11 of the specification is corrected to r layer j.
(4)明m棗第7頁第11行目(2箇所)及び第8頁第
14行目に記載した「焦面」をr蒸留jと補正する。(4) Correct the "focal plane" described in Ming Natsume, page 7, line 11 (two locations) and page 8, line 14, to r distillation j.
以上that's all
Claims (1)
されるインデン類を非水溶性有機溶剤を溶媒として、ア
ルカリ触媒の存在下に有機酸を加え、これらの混合物に
過酸化水素を滴下して酸化し、次いで鉱酸と加熱するこ
とを特徴とする下記一般式(II) ▲数式、化学式、表等があります▼(II) (式中、Rは水素または低級アルキル基を示す)で表わ
される2−インダノン類の製造法。[Claims] Indenes represented by the following general formula (I) ▲Mathematical formulas, chemical formulas, tables, etc. are available▼(I) (In the formula, R represents hydrogen or a lower alkyl group) in a water-insoluble organic solvent is used as a solvent, an organic acid is added in the presence of an alkali catalyst, hydrogen peroxide is added dropwise to the mixture to oxidize it, and then heated with a mineral acid. ▲Mathematical formula, chemical formula , tables, etc. ▼(II) Method for producing 2-indanones represented by (wherein R represents hydrogen or a lower alkyl group).
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP61024167A JPS62185035A (en) | 1986-02-07 | 1986-02-07 | Production of 2-indanone |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP61024167A JPS62185035A (en) | 1986-02-07 | 1986-02-07 | Production of 2-indanone |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS62185035A true JPS62185035A (en) | 1987-08-13 |
Family
ID=12130788
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP61024167A Pending JPS62185035A (en) | 1986-02-07 | 1986-02-07 | Production of 2-indanone |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS62185035A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN109232211A (en) * | 2018-11-06 | 2019-01-18 | 江苏师范大学 | A kind of synthetic method of 2- indone |
-
1986
- 1986-02-07 JP JP61024167A patent/JPS62185035A/en active Pending
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN109232211A (en) * | 2018-11-06 | 2019-01-18 | 江苏师范大学 | A kind of synthetic method of 2- indone |
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