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Production process of tertiary amyl benzene

A tert-amylbenzene, production process technology, applied in the field of tert-amylbenzene production process, can solve problems such as poor dissolution of aluminum trichloride, intensified isomerization reaction, excessive concentration of reaction catalyst, etc.

Inactive Publication Date: 2009-12-23
葛秀龙
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The reaction catalyst represented by aluminum trichloride plays a catalytic role in the tert-amylbenzene synthesis process, and at the same time, it has an isomerization effect on the tert-amyl structure, and because the dissolution of aluminum trichloride in the reaction system is not good, It is prone to the phenomenon that the concentration of local reaction catalyst is too large, which intensifies the occurrence of isomerization reaction
AlCl is used alone in the traditional process 3 or use AlCl 3 and H 2 SO 4 Diacids are used as catalysts. Due to the rearrangement of tert-amyl groups in the F-C reaction process, a large number of sec-amylbenzene isomers are produced, which has the disadvantage of low yield.

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0008] Add 71.92ml benzene (0.803mol) and 2.5gAlCl to the 500ml four-necked bottle 3 and 7.5gFeCl 3 , lower the temperature to 5°C, then dropwise add 10.8g (0.123mol) of tert-amyl alcohol, and finish the dropwise addition for 1h. After the dropwise addition, continue to react at 5°C for 6h, add 100g of water for hydrolysis, stand to separate the layers, separate the organic layer, and then Wash once with water, separate layers, absorb water with calcium chloride, remove benzene, and distill under reduced pressure to obtain 15.1 g of tert-amylbenzene with a content of 99.1% (GC).

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PUM

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Abstract

The invention discloses a production process of tertiary amyl benzene which is prepared by F-C alkylation of benzene and tertiary amyl alcohol. The production process comprises the following steps of: adding 6.53mol of benzene, 0.15mol of AlCl3 and 0.38mol of FeCl3 in a four-opening bottle, reducing the temperature to 0 to 5 DEG C, then adding 1mol of tertiary amyl alcohol by dropping for 1 hour, continuing reaction for 6 hours at the temperature of 0 to 5 DEG C after the dropwise adding, adding water for hydrolysis, standing and layering, separating the organic horizon, washing with water again, layering, absorbing water with calcium chloride, debenzolizing and conducting pressure reduction and distillation, thus obtaining the tertiary amyl benzene. In the production process, lewis acid AlCl3 and FeCl3 are used as catalysts, and the use amount of AlCl3 is reduced properly, thus avoiding the defects caused by only adopting AlCl3 or adopting two acids of AlCl3 and H2SO4 as the catalysts, leading the yield of tertiary amyl benzene to reach 90 percent and the content of isomer to be less than 0.2 percent.

Description

technical field [0001] The invention relates to the field of chemical raw material production, in particular to a production process of tert-amylbenzene. Background technique [0002] Tert-amylbenzene, also known as dimethylethylphenylmethane and p-amylbenzene, is a raw material for organic synthesis and can be used as a new working carrier for medicine, liquid crystal materials and hydrogen peroxide. The molecular formula of tert-amylbenzene is C 11 h 16 , Prepared by F-C alkylation of benzene and tert-amyl alcohol. The technical key of the tert-amylbenzene synthesis process is to control the ratio of isomers in the product. The reaction catalyst represented by aluminum trichloride plays a catalytic role in the tert-amylbenzene synthesis process, and at the same time, it has an isomerization effect on the tert-amyl structure, and because the dissolution of aluminum trichloride in the reaction system is not good, It is prone to the phenomenon that the concentration of lo...

Claims

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Application Information

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IPC IPC(8): C07C15/02C07C2/86B01J27/128
CPCY02P20/52
Inventor 葛秀龙
Owner 葛秀龙
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