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Method for separating mixtures containing anthracene alkylation reaction products

A separation method, an alkylation technology, applied in the field of separation, can solve the problems that the separation technology of anthracene alkylation reaction product system has not been reported yet, and achieve the effect of reducing the difficulty of operation, improving the purity and the total yield

Active Publication Date: 2021-08-06
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

[0007] From the reports of the prior art, the separation technology of the anthracene alkylation reaction product system has not been reported yet

Method used

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  • Method for separating mixtures containing anthracene alkylation reaction products
  • Method for separating mixtures containing anthracene alkylation reaction products
  • Method for separating mixtures containing anthracene alkylation reaction products

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preparation example Construction

[0043] In the present invention, the conditions and methods for the anthracene alkylation can be carried out in a conventional manner in the art. Usually, the preparation method of alkyl anthracene comprises: in the presence of a catalyst, a raw material liquid containing anthracene and an alkylation solvent is contacted with an alkylating agent to carry out an alkylation reaction. Wherein, the raw material of alkylation reaction is anthracene, and the alkylation solvent is the inert organic solvent that can dissolve anthracene, for example, can be C 6 -C 12 The paraffins or cycloalkanes of benzene can also be one-, two- or multiple-substituents of benzene, wherein, the substituents in the one-, two- or multiple-substituents of benzene are C 1 -C 4 One or more of the alkyl and halogen elements; more preferably, the alkylation solvent is a benzene substitute; most preferably, the alkylation solvent is 1,3,5-trimethylbenzene.

[0044] In the present invention, the substance t...

Embodiment 1

[0067] The liquid acid methanesulfonic acid is used as a catalyst for the alkylation reaction. In a 300ml stirred reactor, 46g of anthracene, 80ml of mesitylene, and 3ml of methanesulfonic acid were charged. After sealing the reaction kettle, start the stirring and temperature rise control program, the speed is set to 1000 rpm, and the temperature is 165°C. After the kettle temperature reached the set value, 2-methyl-2-butene was introduced into the kettle through a feed pump, the total amount of feed was 15.1 g, and the feed rate was 0.66 g / min. When the olefin feed was completed, the reaction conditions were kept constant, and the reaction was continued for 270 minutes before the reaction was terminated. Methanesulfonic acid was removed by sedimentation and separation, and a small amount of material in the kettle was taken out for chromatographic analysis. The same experimental conditions were carried out 5 times, and the materials were collected to provide raw materials f...

Embodiment 2

[0073] The alkylation reaction was carried out according to the method of Example 1, except that the method for separating the mixture of the alkylation reaction products included: the operating temperature of the atmospheric distillation system was 165° C., and the solvent trimethylbenzene was distilled off. Then raise the temperature of the atmospheric distillation device to 220° C., send the molten solid material into the melting crystallizer, and feed the cooling medium to start cooling and crystallization. The cooling rate was 1.0°C / h, the crystallization temperature was 197°C, the amount of anthracene added as seed crystal accounted for 1% by weight of the mass of the molten mixture, and the crystal growth time was controlled at 1.5h. After the crystallization process is over, the uncrystallized feed liquid is discharged and sent to the vacuum distillation system. Slowly heat up and sweat the crystals in the crystallizer, the temperature rise rate is 0.6°C / h, the sweatin...

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Abstract

The invention relates to the technical field of anthracene alkylation reaction separation technology, and discloses a method for separating a mixture containing anthracene alkylation reaction products. The separation method includes separating a stream containing anthracene, an alkylation solvent and a series of alkylanthracene products, Wherein, the separation method includes: alkylation solvent separation, melting crystallization and multi-stage vacuum distillation. Through the fusion crystallization-multistage vacuum distillation coupling separation technology proposed by the present invention, the operational difficulty of the separation process of anthracene-series alkylanthracene products can be significantly reduced, and the purity and total yield of target products can be improved.

Description

technical field [0001] The present invention relates to a separation method, in particular to a separation method of a mixture containing anthracene alkylation reaction product. Background technique [0002] Hydrogen peroxide is an important green basic chemical with a high degree of industrial relevance. Since 2008, my country has become the largest country in the production of hydrogen peroxide, and its consumption in 2015 has exceeded 10 million t / a ( at 27.5%). At present, the process technology for producing hydrogen peroxide at home and abroad is mainly the anthraquinone method. The 2-alkylanthraquinone in this process is used as the "carrier" of the process, which directly affects the quality and output of hydrogen peroxide. The phthalic anhydride method is the main method to produce 2-alkylanthraquinones, but this process has serious environmental pollution problems. To produce 1t of ethylanthraquinone, it needs to consume 1.76t of anhydrous AlCl 3 and 4.2t fuming...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C07C7/00C07C15/24
Inventor 郑博费建奇宗保宁朱振兴郄思远潘智勇唐晓津田龙胜胡立峰毛俊义刘铮
Owner CHINA PETROLEUM & CHEM CORP