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A method for the joint preparation of styrene oxide and benzaldehyde by heterogeneous catalytic epoxidation of styrene

A technology for epoxidizing styrene and styrene oxide, which is applied in the fields of oxidative preparation of carbonyl compounds, chemical recovery, organic chemistry, etc. It can solve the problems of unavoidable traces of organic chlorine, low conversion rate of toluene in one pass, and difficult control of reaction temperature and other problems, to achieve the effect of easy separation, obvious solvent effect and convenient operation

Active Publication Date: 2017-06-06
ZHEJIANG UNIV OF TECH
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  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0006] Benzaldehyde produced by traditional toluene chlorination and hydrolysis inevitably contains trace amounts of organic chlorine, which limits its application in pharmaceutical and spice industries
Patent CN 1876616 produces benzaldehyde by benzoate reduction method. Although the single-pass conversion rate and benzaldehyde selectivity of this method are very high, the reaction temperature must be above 300°C, which requires high energy consumption and high raw material costs.
Patent CN1068755 discloses a method for preparing benzaldehyde by gas-phase oxidation of toluene. Although this method is economical and environmentally friendly, and the selectivity of benzaldehyde is as high as 99%, the single-pass conversion rate of toluene is only 26%.
In addition, the gas-phase oxidation reaction of toluene is a strong exothermic reaction, and the reaction temperature is difficult to control. When the temperature is too high, benzaldehyde is easily over-oxidized to produce a series of by-products such as benzoic acid and carbon dioxide. In order to control the reaction temperature, it is necessary to increase equipment investment

Method used

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  • A method for the joint preparation of styrene oxide and benzaldehyde by heterogeneous catalytic epoxidation of styrene
  • A method for the joint preparation of styrene oxide and benzaldehyde by heterogeneous catalytic epoxidation of styrene
  • A method for the joint preparation of styrene oxide and benzaldehyde by heterogeneous catalytic epoxidation of styrene

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1-5

[0023] Examples 1-5: SiO with different n(Si / Ti) 2 -TiO 2 Combined Preparation of Styrene Oxide and Benzaldehyde by Composite Airgel Catalyzed Epoxidation of Styrene

[0024]Into five 50 mL two-necked round bottom flasks, add 0.25 g of catalysts with n(Si / Ti) of 5, 7, 9, 20, and 40 prepared above, 1.04 g (10 mmol) of styrene, N,N- With 10 g of dimethylformamide, the flask was reacted at a constant temperature in an oil bath at 60°C and refluxed for 6 h while stirring continuously. 10 ml (10 mmol) of 30% hydrogen peroxide was added at a constant speed by a micro-sampling pump, and the dropping time was 0.5 h. After the reaction, the catalyst was separated by filtration, and the filtrate was analyzed by gas chromatography. The filtrate was rectified, and the fractions at 180°C and 190°C were taken respectively to obtain styrene oxide and benzaldehyde in sequence. The product was qualitatively analyzed by GC-MS (CP-3800 / Saturn2000 gas / mass spectrometer, capillary column: CP-SI...

Embodiment example 6~9

[0028] Implementation Cases 6~9: SiO with Different Catalyst Consumption 2 -TiO 2 Combined Preparation of Styrene Oxide and Benzaldehyde by Composite Airgel Catalytic Epoxidation of Styrene

[0029] Choose SiO with n(Si / Ti) = 9 2 -TiO 2 Composite airgel was used as catalyst, and 0.15 g, 0.25 g, 0.35 g and 0.45 g were weighed respectively (the mass ratios of substrate styrene and catalyst were 6.7:1, 4:1, 2.9:1, 2.2:1) and released into four 50mL two-necked flasks, and other operating conditions were the same as in Examples 1 to 5. The reaction results are shown in Table 2.

[0030] Table 2 Effect of different catalyst dosage on epoxidation reaction

[0031]

[0032] As can be seen from Table 2, the catalyst dosage increases, the styrene conversion rate improves, the styrene oxide selectivity and the benzaldehyde selectivity all improve, but when the catalyst dosage exceeds 0.35 g, the styrene conversion rate, epoxybenzene Ethane selectivity and benzaldehyde selectivit...

Embodiment example 10~12

[0033] Implementation Cases 10~12: Different n(H 2 o 2 / styrene) under the epoxidation of styrene to jointly prepare the result of styrene oxide and benzaldehyde

[0034] Choose SiO with n(Si / Ti) = 9 2 -TiO 2 Composite aerogels were used as catalysts, and n(H 2 o 2 / styrene) is 0.5, 1 and 2 30% hydrogen peroxide, and other reaction conditions are with embodiment 1~5. The results are shown in Table 3.

[0035] Table 3 Different n(H 2 o 2 / styrene) on the epoxidation reaction

[0036]

[0037] As can be seen in table 3, along with the increase of hydrogen peroxide consumption, styrene conversion % improves, styrene oxide selectivity % and benzaldehyde selectivity % change little, but when n(H 2 o 2 / styrene) exceeds 1, the % increase of styrene conversion rate is not obvious. In order to control the self-decomposition degree of hydrogen peroxide and reduce the danger in the production process, preferably n(H 2 o 2 / styrene) is 0.5~1:1.

[0038] Implementation Ca...

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Abstract

The invention relates to a method for jointly preparing styrene oxide and benzaldehyde by heterogeneous catalytic epoxidized styrene and belongs to the technical field of preparation of fine chemical products. The method comprises the following steps: taking styrene as a substrate, taking N, N-dimethylformamide as a reaction solvent, taking 30 percent of hydrogen peroxide by weight as an oxidizing agent, performing the epoxidation of olefin under the action of an SiO2-TiO2 composite aerogel catalyst, controlling the reaction temperature to be 40-80 DEG C, controlling the reaction time to be 4-10 hours, performing rectifying treatment on reaction liquid after the completion of reaction, and respectively taking fractions of 180 DEG C and 190 DEG C to obtain the styrene oxide and the benzaldehyde in sequence. According to the method, with the adoption of the SiO2-TiO2 composite aerogel catalyst, an expensive template agent is not required, the high-temperature roasting treatment is not required, the preparation is simple, and the cost is low; the catalyst can be reused for multiple times after separation, the operation is convenient, and is environment-friendly, the economic benefit is high, and the sum of the selectivity of the obtained styrene oxide and the selectivity of the obtained benzaldehyde is more than 99 percent.

Description

technical field [0001] The invention belongs to the technical field of preparation of fine chemical products, and specifically relates to a heterogeneous catalytic reaction for joint preparation of styrene oxide and benzene with mild reaction conditions, simple catalyst preparation and easy separation from the reaction solution, convenient product post-treatment, and less environmental pollution. formaldehyde method. Background technique [0002] Styrene oxide, also known as styrene oxide, is a fine chemical that can be used as an epoxy resin diluent, UV-absorber, flavor enhancer, and is also an important intermediate in organic synthesis, pharmaceutical industry, and fragrance industry Body, which is mainly obtained by epoxidation of styrene. [0003] Industrially, the production of styrene oxide adopts the traditional haloalcohol method and the direct oxidation method of peroxyacid. The former has many by-products and serious equipment corrosion, while the latter has expe...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C07D303/04C07D301/12C07C47/54C07C45/28B01J21/08
CPCY02P20/584
Inventor 姜剑锋张波邓冰心
Owner ZHEJIANG UNIV OF TECH