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Method for preparing 5-tert butyl meta-xylene by adopting tubular reactor

A technology of tubular reactor and m-xylene, which is applied in the direction of chemical instruments and methods, catalytic reactions, condensation between hydrocarbons and non-hydrocarbons, etc., can solve the problems of difficult loading and unloading, and reduce post-processing Pressure, simple and clear operation, and the effect of reducing the generation of by-products

Inactive Publication Date: 2019-03-01
濮阳市欧亚化工科技有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Benefits of technology

This patented technology describes a new way to prepare 1 -terti- butyl m metoimme (BMIM). By mixing certain chemical substance called BMOX and trioxane together at once, this mixture becomes very effective when producing desired products like pentaerythritoltetone or trimellitol. Compared to other methods that involve multiple steps such as distillations or crystallization processes, these techniques have advantages including faster processing times, increased productivity due to less material handling, lower energy consumption compared to existing methods, and fewer harmful waste streams produced from conventional methods. Additionally, there's no need for complicated operations because they only require one step instead of three.

Problems solved by technology

This patented technical solution involves making certain compounds from 2-dimethoxy-5-(trimethyl)phenol (TMP). However this process causes side mixing between two molecules called monomers during its formation. To prevent these issues, it suggests adding another substance like tertiary butanamine or pentaerythritol into one end of the vessel containing both materials beforehand. These modifications help increase efficiency while reducing pressure drop caused by turbulence inside the system.

Method used

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Examples

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Effect test

Embodiment 1

[0018] A kind of method that adopts tubular reactor to prepare 5-tert-butyl m-xylene that the present invention proposes comprises the following steps:

[0019] S1. Preparation of auxiliary catalyst: Weigh 3 parts by weight of barium titanate, 1 part by weight of 4-chloropyridine, 0.6 parts by weight of 4-(trifluoromethyl)pyridine, 2 parts by weight of nickel oxide, and 2.5 parts by weight of anhydrous copper sulfate , 8 parts by weight of silica sol with a solid content of 25%, 14 parts by weight of ethanol solution with a mass fraction of 25% for subsequent use, 4-chloropyridine, 4-(trifluoromethyl)pyridine and anhydrous copper sulfate are added to the mass successively In an ethanol solution with a fraction of 25%, after heating up to 30°C, ultrasonically oscillate to disperse and mix to obtain a mixed solution, mix and grind barium titanate and nickel oxide to 170 mesh, then add them to the mixed solution, continue to oscillate and disperse evenly, and finally raise the tem...

Embodiment 2

[0023] A kind of method that adopts tubular reactor to prepare 5-tert-butyl m-xylene that the present invention proposes comprises the following steps:

[0024] S1. Preparation of auxiliary catalyst: Weigh 4 parts by weight of barium titanate, 1.4 parts by weight of 4-chloropyridine, 0.9 parts by weight of 4-(trifluoromethyl)pyridine, 3 parts by weight of nickel oxide, and 3.5 parts by weight of anhydrous copper sulfate , 12 parts by weight of silica sol with a solid content of 25%, 20 parts by weight of ethanol solution with a mass fraction of 25% for subsequent use, 4-chloropyridine, 4-(trifluoromethyl)pyridine and anhydrous copper sulfate are added to the mass successively In an ethanol solution with a fraction of 25%, after heating up to 40°C, ultrasonically oscillate to disperse and mix to obtain a mixed solution, mix and grind barium titanate and nickel oxide to 210 mesh, then add them to the mixed solution, continue to oscillate and disperse evenly, and finally raise the...

Embodiment 3

[0028] A kind of method that adopts tubular reactor to prepare 5-tert-butyl m-xylene that the present invention proposes comprises the following steps:

[0029]S1. Preparation of auxiliary catalyst: weigh 5 parts by weight of barium titanate, 1.8 parts by weight of 4-chloropyridine, 1.2 parts by weight of 4-(trifluoromethyl)pyridine, 4 parts by weight of nickel oxide, and 4.5 parts by weight of anhydrous copper sulfate , 15 parts by weight of silica sol with a solid content of 25%, 24 parts by weight of ethanol solution with a mass fraction of 25% for subsequent use, 4-chloropyridine, 4-(trifluoromethyl)pyridine and anhydrous copper sulfate are added to the mass successively In an ethanol solution with a fraction of 25%, after heating up to 50°C, ultrasonically oscillate to disperse and mix to obtain a mixed solution, mix and grind barium titanate and nickel oxide to 250 mesh, then add them to the mixed solution, continue to oscillate and disperse evenly, and finally raise the ...

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PUM

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Abstract

The invention discloses a method for preparing 5-tert butyl meta-xylene by adopting a tubular reactor. The method comprises the following steps: S1, preparing an auxiliary catalyst; S2, mixing the auxiliary catalyst with aluminum trichloride, thus preparing a compound catalyst; mixing the compound catalyst with meta-xylene, thus obtaining a raw material A; using tert-butyl chloride as a raw material B, and feeding the raw material A and the raw material B for reacting by respectively adopting two feeding modes; S3, carrying out aftertreatment on a reaction solution after completing reaction, thus obtaining a 5-tert butyl meta-xylene finished product. According to the method disclosed by the invention, the reaction time is greatly shortened, the conversion rate is remarkably increased, generation of byproducts is reduced, the method has the advantages that operation is simple and clear and is safe and reliable, the yield of the prepared 5-tert butyl meta-xylene is up to 95 percent or above and is increased by 20 percent or above than the yield of a traditional technology, and the problems that during a stirring process of a traditional tank reactor, influence of backmixing appears,and charging and discharging are difficult are solved.

Description

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Claims

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Application Information

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Owner 濮阳市欧亚化工科技有限公司
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