Continuous flow synthesis process of tert-amyl hydroperoxide

A technology of tert-amyl hydroperoxide and hydrogen peroxide is applied in the preparation of peroxy compounds, the preparation of organic compounds, organic chemistry and other directions, and can solve the problems of increasing waste water, increasing the difficulty of post-treatment, and long total reaction time, etc. Achieve the effect of reducing the production of by-products, shortening the total reaction time, and optimizing the reaction temperature

Active Publication Date: 2021-02-26
LINZIZHENGHUA ACCESSORY INGREDIENT ZIBO
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0003] From the prior art, it can be seen that the existing synthesis techniques of tert-amyl hydroperoxide (TAHP) all have amplification effects in different degrees, leading to industrial scale-up It will consume a lot of manpower and material resources and there are many uncertainties; there are also problems with the reliability of the process after amplification, and the product quality is unstable and difficult to control; at the same time, the production process lacks flexibility and has potential safety risks; The total reaction time is too long, and the yield is not high, which reduces the production efficiency, which increases the difficulty of industrialization
The inability to achieve mass production limits its application
[0004] Chinese patent CN101298429A discloses a production method of di-tert-butyl peroxide, which mixes a certain concentration of sulfuric acid, hydrogen peroxide and phosphotungstic acid, Add tert-butanol to the mixed solution to react to obtain a mixture of tert-butyl hydroperoxide and di-tert-butyl hydroperoxide. This method adds phosphotungstic acid and stabilizers, which increases the cost and difficulty of post-treatment, and the product It is a mixture of tert-butyl hydroperoxide and di-tert-butyl peroxide, which needs to be separated by pressurized distillation, which increases the processing cost. In addition, the method uses 35% concentrated sulfuric acid, which increases the waste water after reaction.

Method used

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  • Continuous flow synthesis process of tert-amyl hydroperoxide
  • Continuous flow synthesis process of tert-amyl hydroperoxide
  • Continuous flow synthesis process of tert-amyl hydroperoxide

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0033] The integrated continuous flow reactor adopts a unitized structure, which includes a premixing unit, an esterification unit and a quenching unit in sequence. Use a constant flow pump to transport sulfuric acid and hydrogen peroxide to the premixing unit for reaction to generate peroxymonosulfuric acid; then use a constant flow pump to transport tert-amyl alcohol to the esterification unit. Alcohol reacts to obtain a reaction solution; the reaction solution further flows into the quenching unit to quench the reaction, collect the reaction mother liquor, and separate layers to obtain tert-amyl hydroperoxide, its mass spectrum is as follows figure 1 , the peak data of tert-amyl hydroperoxide in the figure are shown in Table 8. The consumption of raw material, the reaction temperature of each unit, product purity and yield are shown in Table 1, wherein T 1 , T 2 , T 3 represent the temperature of premix unit, esterification unit and quenching unit respectively.

[0034]...

Embodiment 2

[0037] Reaction process is with embodiment 1, and the consumption of raw material, the reaction temperature of each unit, product purity and yield are shown in Table 2, wherein T 1 , T 2 , T 3 represent the temperature of premix unit, esterification unit and quenching unit respectively.

[0038] Table 2 The amount of raw materials, the reaction temperature of each unit, product purity and yield data table

[0039]

Embodiment 3

[0041] Reaction process is with embodiment 1, and the consumption of raw material, the reaction temperature of each unit, product purity and yield are shown in Table 3, wherein T 1 , T 2 , T 3 represent the temperature of premix unit, esterification unit and quenching unit respectively.

[0042] Table 3 The amount of raw materials, the reaction temperature of each unit, product purity and yield data table

[0043]

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Abstract

The invention relates to the technical field of chemistry and chemical engineering, in particular to a continuous flow synthesis process of tert-amyl hydroperoxide. The continuous flow synthesis process of tert-amyl hydroperoxide comprises the following steps: in an integrated continuous flow reactor, reacting sulfuric acid with hydrogen peroxide to generate peroxymonosulfuric acid; and carrying out esterification reaction on peroxymonosulfuric acid and tert-amyl alcohol, and quenching to obtain tert-amyl hydroperoxide. By adopting the synthesis process, the reaction process is optimized, thegeneration of byproducts is reduced, the product quality is stable, the product yield is improved, the product yield is 99% or above, and the purity is 91% or above; the total reaction time is less than or equal to 180s. Compared with the traditional production process, the reaction temperature is greatly increased, the total reaction time is greatly shortened, the product index is stable and thereproducibility is good.

Description

technical field [0001] The invention relates to the technical field of chemistry and chemical engineering, in particular to a continuous flow synthesis process of tert-amyl hydroperoxide. Background technique [0002] Organic peroxides are derivatives after one or two hydrogen atoms in the hydrogen peroxide molecule are replaced by organic groups, and its general formula is R-O-O-R. At present, the industrial organic synthesis oxidants mainly include tert-amyl hydroperoxide (TAHP) and the like. Tert-amyl hydroperoxide (TAHP), also known as t-amyl hydroperoxide, is a commonly used initiator for free radical reactions. It is characterized by good thermal stability, safe use, and easy control; below 50 °C, its The activity has no obvious change within three months, and there is no need for high-cost frozen storage, and can be used in the fields of emulsion polymerization, water phase polymerization, solidification and graft polymerization. TAHP is also widely used in styrene ...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07C407/00C07C409/04
CPCC07C407/00C07C409/04
Inventor 陈唐建翟志强薛育宴马赳高陶蕾娟王跟泉孔祥伦
Owner LINZIZHENGHUA ACCESSORY INGREDIENT ZIBO
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