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A kind of catalyst and application thereof of isopentenyl acetate transesterification to prepare prenyl alcohol

A technology of isopentenyl acetate and isopentenyl acetate, which is applied in the field of catalyst and its reaction process, can solve the problems of uncontinuous reaction, harsh reaction conditions, long process route, etc., and achieve a simple, environmentally friendly, pollution-free and reaction process. The effect of mild conditions and simple material requirements

Active Publication Date: 2021-04-09
DALIAN INST OF CHEM PHYSICS CHINESE ACAD OF SCI
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0005] The three relatively mature process routes have their own advantages and disadvantages: (1) the isobutylene method requires a large investment in equipment, harsh reaction conditions, and high production costs
(2) The isoprene method has rich sources of raw materials, obvious production cost advantages, and a gentle reaction process, but the boiling point of isoprene is low, the gas phase reaction is not easy to control, and the vapor toxicity is relatively high, and HCl is extremely corrosive to equipment
(3) Acetone method, acetylene raw material cost is high, process route is long, product yield is low, production cost rises
[0007] At present, the isopentenol reaction carried out by the researchers all adopts the tank reactor, which cannot be continuously reacted, and focuses on the research of the catalyst.
Although some effective catalysts have been invented, they are still unsatisfactory for industrial applications

Method used

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  • A kind of catalyst and application thereof of isopentenyl acetate transesterification to prepare prenyl alcohol

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0024] Take 0.1%Ir-5%Fe / 20%CeO 2 / SiO 2 as a catalyst. The mass ratio of the reaction raw material isopentenyl acetate to methanol is 1:9, the raw material injection volume is 2mL / min, 2g catalyst is added, the reaction temperature is 130°C, and H 2 Pressurize to 2Mpa, and pass through H all the time during the reaction 2 And the gas volumetric space velocity is 1000h -1 , The reaction time is 40h.

Embodiment 2

[0026] The reaction raw material was changed to the mass ratio of prenyl acetate and ethanol to be 1:9, the reaction temperature was changed to 150° C., and other conditions were the same as in Example 1.

Embodiment 3

[0028] Take 1%Ir-5%Fe / 30%CeO 2 / SiO 2 as a catalyst. The mass ratio of the reaction raw materials isopentenyl acetate and butanol is 1:7, the raw material injection volume is 3mL / min, 3g catalyst is added, the reaction temperature is 170°C, and H 2 Pressurize to 2Mpa, and pass through H all the time during the reaction 2 And the gas volumetric space velocity is 1000h -1 , The reaction time is 50h.

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Abstract

The invention relates to a catalyst for preparing isopentenol through transesterification of isopentenyl acetate and a reaction process thereof. The method uses isopentenyl acetate and normal alcohol as reaction raw materials, and under the action of a solid acid as a catalyst, isopentenyl alcohol and certain acetate are transesterified. The normal alcohols include methanol, ethanol, propanol and butanol, and the corresponding certain acetates are methyl acetate, ethyl acetate, propyl acetate and butyl acetate. Described this solid acid catalyst adopts IrFe / CeO 2 / SiO 2 as a catalyst system. It is particularly pointed out that an important reaction process step to obtain a high-yield target product (≥90%) is to first feed H in the reaction process. 2 for a period of time, and then switch to N 2 . The invention has the obvious advantages of low economic and environmental costs, easy separation of products, simple post-treatment, etc., and has good application prospects.

Description

technical field [0001] The invention relates to a catalyst for preparing isopentenol through transesterification of isopentenyl acetate and a reaction process thereof. Background technique [0002] Pyrethroid fine chemicals are widely used biomimetic insecticides that emerged at the end of the last century. In January 2007, my country introduced five highly toxic and high-residue organophosphorus pesticides such as methamidophos in all regions of the country. Completely banned, pyrethroid pesticides have been vigorously advocated and promoted by the state, and have been considered as the star of hope to replace highly toxic and high-residue organophosphorus pesticides, accounting for more than half of the total usage of urban sanitation pesticides . Today, new insecticide chemicals have been formed after carbamate, organophosphorus, and organochlorine biomimetic insecticides, which is another phased achievement in the historical development of pesticides. It has outstanding ...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J23/89B01J37/02B01J37/08C07C29/128C07C33/025C07C67/03C07C69/14
CPCB01J23/002B01J23/894B01J37/0201B01J37/088B01J2523/00C07C29/1285C07C67/03C07C33/025C07C69/14B01J2523/3712B01J2523/41B01J2523/827B01J2523/842
Inventor 王爱琴苗治理孙永南梁观峰张涛
Owner DALIAN INST OF CHEM PHYSICS CHINESE ACAD OF SCI
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