Preparation of alpha-tetralone by two-step catalysis method

A technology of tetralone and tetralone, which is applied in the field of preparation of α-tetralone by a two-step catalytic method, can solve problems such as difficult separation, low selectivity of α-tetralone, and toxic dosage of catalyst.

Inactive Publication Date: 2009-09-30
HUNAN UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The consumption of main and auxiliary catalysts in this process is large and the cost is high; moreover, the chromium salt is poisonous and difficult to separate from the product, polluting the product and the environment
In addition to α-tetralone, the oxidation product of molecular oxygen oxidation tetralone also contains a large amount of α-tetralin hydroperoxide and α-tetralinol, and the selectivity of α-tetralone is not high
Wherein α-tetralinol has a great adverse effect on the subsequent use of α-tetralone, and the boiling point of α-tetralinol and α-tetralone is very close, so it is difficult to separate
U.S. Patent No. 4,175,098 has reported in DMF solvent, with chromium salt and N, N-dialkyl amides compound catalytic oxidation α-tetralin prepares the method for α-tetralone; This method will use solvent, and catalyzer is poisonous And the consumption is large, the cost is high
U.S. Patent No. 4,283,352 has reported a kind of technology that non-catalyzed oxidation prepares α-tetralone; The oxidation process of this method does not use catalyst, makes reaction time very long, and the ketone-alcohol ratio of gained product is not high

Method used

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  • Preparation of alpha-tetralone by two-step catalysis method
  • Preparation of alpha-tetralone by two-step catalysis method
  • Preparation of alpha-tetralone by two-step catalysis method

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0013] The metalloporphyrin with general formula (I) structure is dissolved in the 50ml tetralin, and the concentration of metalloporphyrin is 14.75ppm, R 1 = Cl, R 2 =R 3 =H, M=Fe, X=Cl. Air was introduced at a gas velocity of 300ml / min. React at 90 DEG C for 8 hours, the conversion rate of tetralin is 15.32%, the selectivity of α-tetralin hydroperoxide is 89.88%, the total selection of α-tetralin hydroperoxide and α-tetralone The sex is 95.37%. Take 24.40g of oxidizing solution, drop into 30ml FeSO 4 ·7H 2 Aqueous solution of O (dissolved with 0.86g of FeSO 4 ·7H 2 O), ice-water bath controls the temperature in the reaction process at about 0°C, and adds dropwise under stirring, and after 30 minutes, the dropwise addition is completed, and continues to stir and stir for 60 minutes. Hydrogen peroxide is almost completely decomposed into α-tetralone, and the total selectivity of α-tetralone is 95.31%.

Embodiment 2

[0015] The metalloporphyrin with general formula (I) structure is dissolved in the 50ml tetralin, and the concentration of metalloporphyrin is 14.75ppm, R 1 = Cl, R 2 =R 3 =H, M=Co, X=Cl. Feed into air with 300ml / min gas velocity, react at 90 ℃ for 8 hours, the transformation rate of tetralin is 34.22%, and α-tetrahydronaphthalene hydroperoxide selectivity is 83.36%, α-tetralin hydroperoxide and α-tetralone with an overall selectivity of 95.40%. Take 28.94g of oxidizing solution, drop into 30ml of CuCl aqueous solution (dissolved with 0.36g of CuCl), control the temperature in the reaction process at about 0°C in an ice-water bath, add drop by drop under stirring, after 30min dropwise addition, continue to stir for 60min, After vacuum filtration and separation treatment, the α-tetralin hydroperoxide in the oxidation solution is almost completely decomposed into α-tetralone, and the total selectivity of α-tetralone is 94.66%.

Embodiment 3

[0017] The metalloporphyrin with general formula (I) structure is dissolved in the 50ml tetralin, and the concentration of metalloporphyrin is 29.50ppm, R 1 = Cl, R 2 =R 3 =H, M=Co, X=Cl. Feed into air with 300ml / min gas velocity, react 4 hours at 90 ℃, the transformation rate of tetralin is 25.02%, and the α-tetralin hydroperoxide selectivity is 83.09%, α-tetralin hydroperoxide and α-tetralone with an overall selectivity of 94.27%. Take 25.00g of oxidizing solution, drop into 30ml of FeSO 4 ·7H 2 O aqueous solution (dissolved with 0.9g of FeSO 4 ·7H 2 0), the ice-water bath controls the temperature in the reaction process at about 0°C, and it is added dropwise under stirring, and the dropwise addition is completed in 30 minutes, and the stirring is continued for 60 minutes. Hydrogen oxide is almost completely decomposed into α-tetralone, and the total selectivity of α-tetralone is 94.26%.

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Abstract

The invention discloses a novel method for preparing alpha-tetralone by using tetrahydronaphthalene as a raw material. The method comprises the following two steps: a first step, under the condition without solvent and assistant, 1 to 20 atm (absolute pressure) of air or oxygen or mixed gas of oxygen and inert gases is introduced, the reaction temperature is between 60 and 150 DEG C, monometallic porphyrin of general formula (I) or (II) and mu-O-bimetallic porphyrin or solid carriers thereof are used as a catalyst, the concentration of the catalyst is 1 to 80 ppm, the reaction time is 1 to 12 hours, and oxidized mixed solution containing high alpha-tetrahydronaphthalene peroxide and alpha-tetralone can be selectively obtained; and a second step, the alpha-tetrahydronaphthalene peroxide in the oxidized mixed solution obtained in the first step is high selectively and directionally decomposed into the alpha-tetralone by using transition metal salt as a catalyst. In the step of catalytic decomposition, the molar ratio of transition metal irons to the alpha-tetrahydronaphthalene peroxide is 1:1-100, and the reaction temperature is between 0 and 100 DEG C. The method has the advantages of short reaction time, mild reaction conditions, little using amount of the catalyst, high conversion rate and good selectivity of a target product; and the used catalyst is environment-friendly and has no corrosion to equipment.

Description

(1) Technical field [0001] The invention relates to a method for preparing α-tetralone by a two-step catalytic method. In the first step, under the catalysis of metalloporphyrin, tetralin is selectively oxidized by air or oxygen to α-tetralin hydroperoxide and α-tetralone; in the second step, transition metal ions are used to catalyze the decomposition of the first step to produce The α-tetralin hydroperoxide, thereby highly selectively prepares α-tetralone. (2) Background technology [0002] α-tetralone is an important intermediate in the production of many medicines. At present, the industry mainly adopts the production process of using chromium salt as the main catalyst and pyridine compounds as auxiliary catalysts to catalyze the air oxidation of tetralone. This kind of process requires a large amount of main and auxiliary catalysts and high cost; moreover, the chromium salt is poisonous and difficult to separate from the product, polluting the product and the environme...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07C49/637C07C45/36B01J31/22B01J31/28
Inventor 阳卫军郭灿城曹军
Owner HUNAN UNIV
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