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Method for preparing benzaldehyde by oxidizing toluene

A technology for benzaldehyde and toluene, applied in the field of toluene oxidation to prepare benzaldehyde, can solve the problems of small market of benzyl alcohol acetate, low conversion rate of single-stage reactor, uneconomical industrial production, etc. Separation, less waste liquid and less residue

Inactive Publication Date: 2013-05-29
申广照
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  • Summary
  • Abstract
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  • Claims
  • Application Information

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Problems solved by technology

In the Chinese patent No. CN101607867 in 2009, the method of connecting multi-stage oxidation reactor and gas-liquid separator in series was adopted, the conversion rate of toluene reached over 95%, and the total selectivity of benzaldehyde and benzyl alcohol reached over 50%. , but the conversion rate of the single-stage reactor is low and the energy consumption is high
In the above-mentioned method for preparing benzaldehyde by direct liquid-phase oxidation of toluene, all can not ensure that benzaldehyde has high selectivity while satisfying the high conversion rate of toluene; adopt organic acid to improve the situation, but increase the separation process and the introduction of other impurities
[0007] In 2004, the Chinese patent No. CN1528726 disclosed a method for preparing benzaldehyde by liquid-phase oxidation of aromatic hydrocarbon side chains in an acidic or neutral ionic liquid and acetic acid mixed solvent, at 115-120°C Oxidation of toluene, when the conversion rate of toluene was 42%, the selectivity of benzaldehyde was 48%, and the selectivity of benzyl alcohol acetate was 58%. This method uses a large amount of expensive ionic liquid and acetic acid solvent, which greatly increases the production cost , and the separation of products is relatively difficult, and the market for the benzyl alcohol acetate produced at the same time is not large, and further processing is required to recycle benzyl alcohol and acetic acid, and industrial production is uneconomical
[0008] In summary, there is not yet a method for the production of benzaldehyde that is simple in reaction, energy-saving and environmentally friendly, and product and solvent are easy to separate and recycle, and the conversion rate of toluene in the reaction and the selectivity of benzaldehyde are higher at the same time

Method used

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  • Method for preparing benzaldehyde by oxidizing toluene
  • Method for preparing benzaldehyde by oxidizing toluene
  • Method for preparing benzaldehyde by oxidizing toluene

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Embodiment 1

[0024] In the present embodiment, the method for preparing benzaldehyde by oxidation of toluene is as follows, in a 500ml reactor, add solvent benzyl benzoate 240g, toluene 60g and catalyst cobalt benzoate 3.0g, start stirring, feed air so that the absolute pressure in the reactor is 0.3MPa, then turn on the heating to heat the reaction liquid to 180-185°C, the air flow rate is 0.4L / min, and the absolute pressure of the reactor is kept at 0.35MPa. Separation, toluene returns to the reactor, and water is treated as waste liquid. React for 6 hours, turn off the air to cool. Quantitative analysis by gas chromatography showed that the reaction liquid contained 28.6 g of toluene, 28.3 g of benzaldehyde, 3.2 g of benzyl alcohol and 4.2 g of benzoic acid, the conversion rate of toluene was 52.3%, and the selectivity of benzaldehyde was 78.3%. After the reaction solution separates toluene, benzaldehyde, benzyl alcohol and benzoic acid by distillation, the mother liquor containing ben...

Embodiment 2

[0026] Add 280g of solvent benzyl benzoate, 20g of toluene, 3.0g of cobalt benzoate, and 1.0g of manganese benzoate into a 500ml reactor, start stirring, react under normal pressure, feed air at a flow rate of 0.2L / min, and heat until the reaction The temperature is 225-230°C, and the mixed solution of benzyl benzoate, catalyst and toluene is added at a flow rate of 30g / h. The content of toluene in the mixed solution is 30%, and the reaction solution is continuously released to keep the liquid level in the reactor at a constant temperature. Beginning height, the reaction liquid distillation that emits is separated out benzaldehyde, benzyl alcohol and benzoic acid, remaining benzyl benzoate and catalyst mother liquor are purified and then add 30% raw material toluene to mix and return to with the flow velocity of 30g / h In the reactor; Stop adding the mixed solution of fresh benzyl benzoate, catalyst and toluene simultaneously. The gas phase on the reaction liquid contains tolue...

Embodiment 3

[0028] Add 500g of solvent benzyl benzoate, 40g of toluene, 6.0g of cobalt benzoate, 1.0g of manganese benzoate, and 0.5g of nickel benzoate into an 800ml bubble column reactor, and react under normal pressure with an air flow rate of 0.2L / min, be heated to reaction temperature and be 220-225 ℃, add the mixed solution of benzyl benzoate, catalyzer and toluene with the flow rate of 30g / h, toluene content is 30% in the mixed solution, constantly emit reaction solution to make the liquid in the reactor The position is kept at the initial height, and the reaction liquid distilled to separate benzaldehyde, benzyl alcohol and benzoic acid, and the remaining benzyl benzoate and catalyst mother liquor are purified and added with 30% raw material toluene to mix and with a flow rate of 30g / h Return in the reactor; Stop adding the mixed solution of fresh benzyl benzoate, catalyst and toluene simultaneously. The gas phase on the reaction liquid contains toluene, benzaldehyde and water, a...

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Abstract

The invention relates to a method for preparing benzaldehyde by oxidizing toluene. Currently, no method for producing the benzaldehyde has simple reactions as well as high toluene percent conversion and benzaldehyde selectivity. The raw materials comprise 1-59% of toluene, 0.005-5% of master catalyst, oxygen source and 40-98% of benzyl benzoate, wherein the mol ratio of oxygen molecules in the oxygen source to toluene is (0.3-3):1, and the master catalyst is one or more than two of cobalt ions, manganese ions, vanadium ions and nickel ions. The method comprises the following steps: mixing the toluene, master catalyst and benzyl benzoate in a reactor; at the temperature of 140-300 DEG C and under the absolute pressure of 0.05-1.0 Mpa, introducing the oxygen source into the mixed liquor to react for more than 2 hours; and refining the mixed liquor to obtain the benzaldehyde. The toluene percent conversion is higher than 30%, and the benzaldehyde selectivity is higher than 70%. The invention has the advantages of simple reaction, energy conservation, environmental protection, easy separation of products and solvent, and high toluene percent conversion and benzaldehyde selectivity.

Description

technical field [0001] The invention relates to a method for preparing benzaldehyde, in particular to a method for preparing benzaldehyde by oxidation of toluene. Background technique [0002] Benzaldehyde is an important fine chemical product, which is widely used in industrial fields such as medicine, dyestuff, fragrance, pesticide and materials. The production method of preparing benzaldehyde disclosed now mainly contains following three kinds: toluene chlorination hydrolysis method, benzoic acid (ester) reduction method and toluene direct oxidation method, wherein the toluene direct oxidation method comprises gas phase method and liquid phase method. [0003] Chlorine is inevitably contained in the benzaldehyde produced by the traditional chlorination and hydrolysis of toluene, while benzaldehyde used in industries such as medicine and spices cannot contain chlorine, so the benzaldehyde produced by the chlorination and hydrolysis of toluene is The scope of application h...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C07C47/54C07C45/36
Inventor 申广照文维
Owner 申广照