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Method for preparing tetraenol from production waste liquid of 1-chloro prenyl

A kind of chloroisoamylene, carbopentaenol technology, applied in hydrolysis preparation, organic chemistry and other directions, to achieve considerable economic and social benefits, reduce production costs, reduce pollution effects

Inactive Publication Date: 2011-05-04
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0008] The invention provides a method for preparing carbopentenol from the production waste liquid of 1-chloroisoamyl, the production waste liquid is produced in the production process of preparing 1-chloroisoamyl from isoprene, by Processes such as elimination and hydrolysis reaction and separation are made isopentenol and 3-methyl butenol by this production waste liquid, the technical problem to be solved is to improve the utilization value of this production waste liquid, and reduce the pollution to environment, in order to Make up for the shortcomings of existing technology

Method used

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  • Method for preparing tetraenol from production waste liquid of 1-chloro prenyl
  • Method for preparing tetraenol from production waste liquid of 1-chloro prenyl
  • Method for preparing tetraenol from production waste liquid of 1-chloro prenyl

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Experimental program
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Effect test

Embodiment 1~12

[0032] The test raw material is the production waste liquid produced by the process of obtaining 1-chloroisopentene from isoprene through hydrogen chloride addition reaction, isomerization reaction and product refining, which contains 70.5wt% of dichloroisopentane, Other components are a small amount of chlorinated isopentene, isoprene, and some other chlorinated organic compounds.

[0033] In a 1.0-L reaction kettle equipped with a mechanical stirring device, a spherical condenser and a thermometer, 100 grams of the above-mentioned test raw materials were put in. Weigh the required amount of water, inorganic strong base and catalyst, dissolve the inorganic strong base into water, and then put the aqueous alkali solution and catalyst into the reaction kettle. The reaction was carried out after the temperature was gradually raised to the set value under stirring, and the reaction was completed within the set time. The reactant was cooled down, left to stand for stratification,...

Embodiment 13~22

[0044] After mixing the oil phase materials obtained in Examples 1 to 12, three steps of rectification are carried out in sequence, and the first to third steps of rectification correspond to process 3) to process 5) in the above technical scheme, respectively.

[0045] 1) The first step of rectification:

[0046] A thermometer and a rectifying column were installed in a three-necked flask with a capacity of 1 L, the rectifying column was filled with packing, and the theoretical plate number of the rectifying column was 30. The oil phase material obtained in the above-mentioned embodiments 1~12 is rectified and separated in this rectification device, and the tower bottom material and the tower top material are obtained respectively;

[0047] 2) Second step rectification:

[0048] A thermometer and a rectifying column were installed in a three-necked flask with a capacity of 1 L, the rectifying column was filled with packing, and the theoretical plate number of the rectifying ...

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Abstract

The invention relates to a method for preparing pentacarbonyl alcohol from the production waste liquid of 1-chloro prenyl. The method comprises the following steps of: (1) adding water and inorganic alkali to production waste liquid, carrying out an elimination reaction and a hydrolysis reaction under normal pressure under the existence of a catalyst so that dichloropentane in the production waste liquid generates the pentacarbonyl alcohol, wherein the catalyst is selected from one of benzyl triethylammonium chloride, eunatrol and Nal; (2) standing and layering a reaction product in the process (1) and taking out an oil-phase material; (3) distilling and separating the oil-phase material obtained in the process (2); (4) distilling and separating a tower kettle material obtained in the process (3) and condensing a tower top material to obtain a refined prenol product; and (5) distilling and separating the tower top material obtained in the process (3) and obtaining a refined 3-methyl butenol product from the tower kettle material. The invention greatly improves the utilization values of the production waste liquid generated in a process for preparing the 1-chloro prenyl from the isoprene, lessens the environmental pollution and has remarkable economic and social benefits.

Description

technical field [0001] The present invention relates to a kind of utilization method of the production waste liquid of preparing 1-chloroisoprene from isoprene, in particular to the preparation of prenol and 3-isoprenol from the production waste liquid through processes such as elimination reaction, hydrolysis reaction and separation. The method of methyl butenol. Background technique [0002] Using isoprene as a starting material to prepare linalool is the main process route for artificial synthesis of linalool at present. Isoprene is added with hydrogen chloride to generate 1-chloroisoamylene and 3-chloroisoamylene, wherein 3-Chloroisoamylene is then converted to 1-chloroisoamylene by isomerization. 1-Chloroisoamylene is then synthesized into methylheptenone through condensation reaction, and finally linalool is synthesized through acetylenic, hydrogenation and other procedures. A certain amount of dichloroisopentane can be produced when hydrogen chloride is added to obt...

Claims

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Application Information

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IPC IPC(8): C07C29/09C07C33/03
Inventor 郭世卓黄勇孙春水谢家明方玲
Owner CHINA PETROLEUM & CHEM CORP