Continuous production method of multi-kettle serial triazine herbicide

A technology of multi-reactor series connection and production method, applied in the direction of organic chemistry, can solve the problems of low cost performance, slow reaction titration speed, low load of a single set, etc., achieve high degree of process automation, strong continuity of production process, good The effect of social and economic benefits

Inactive Publication Date: 2019-04-16
SHANDONG NORMAL UNIV
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  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

The inventors have found that the problems of the existing technology are: one, the reaction temperature is not easy to control, because the heat transfer area of ​​the jacket is relatively small and the heat of reaction is relatively large, so the reaction drop rate cannot be fast, otherwise the side reactions will be aggravated; the other is the low production capacity , due to the limitation of the drop rate, it takes about 18-24 hours for the sequencing batch reaction to complete the whole process; the third is that there are many side reactions, because the temperature cannot be accurately controlled, operating factors, local overconcentration and other factors cause many side reactions, and the product purity Poor; Fourth, there are many intermittent production equipment, complicated operation, and low labor efficiency. It is inevitable that there will be quality fluctuations caused by manual operation errors
[0004] The process of using microreactors to synthesize triazine herbicides reported in China, due to the low load of a single set of microreactors, will cause a large investment and low cost performance for this 10,000-ton product
[0005] In CN201710663765.7, a mixer and a tubular reactor are used to synthesize the triazine herbicide atrazine. Although it can be produced continuously, there is no back-mixing process in the reaction process. The best effect may not be achieved; in addition, the water phase of the first stage of reaction is not separated between the first stage of reaction and the second stage of reaction in the whole process, and the impurities and unreacted materials in it are easy to be carried into the next stage, resulting in the increase of impurities

Method used

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  • Continuous production method of multi-kettle serial triazine herbicide
  • Continuous production method of multi-kettle serial triazine herbicide
  • Continuous production method of multi-kettle serial triazine herbicide

Examples

Experimental program
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Effect test

Embodiment 1

[0090] Embodiment 1: The multi-pot continuous production method of atrazine

[0091] (1) Charge a certain amount of nitrogen in the batching kettle 1 for replacement, cyanuric chloride and toluene are added to the batching kettle in a ratio of 1:5 by mass ratio, fully dissolved to obtain a toluene solution of cyanuric chloride;

[0092] (2) the above-mentioned prepared cyanuric chloride solution passes through precooler 2 according to the flow rate of 6000kg / hour (wherein cyanuric chloride 1000kg / hour), and the material outlet temperature of control precooler 2 is at 5-7 ℃, and The precisely metered 70% aqueous solution of isopropylamine is fully mixed in the mixer 3 and enters a reactor 4, and the flow rate of the aqueous solution of isopropylamine is controlled at 460kg / hour.

[0093] (3) One-stage reactor 4 (reactor volume 5m 3 ) The reaction solution enters the heat exchanger 5 through the pump (the material outlet temperature is controlled at 13-15°C) for extracorporeal ...

Embodiment 2

[0100] Embodiment 2: the multi-reactor series continuous production method of simazine

[0101] (1) Charge a certain amount of nitrogen in the batching kettle 1 for replacement, cyanuric chloride and toluene are added to the batching kettle in a ratio of 1:5 by mass ratio, fully dissolved to obtain a toluene solution of cyanuric chloride;

[0102] (2) the above-mentioned prepared cyanuric chloride solution passes through precooler 2 according to the flow rate of 6000kg / hour (wherein cyanuric chloride 1000kg / hour), and the material outlet temperature of control precooler 2 is at 5-7 ℃, and The precisely metered 70% aqueous solution of isopropylamine is fully mixed in the mixer 3 and enters a reactor 4, and the flow rate of the aqueous solution of monoethylamine is controlled at 350 kg / hour.

[0103] (3) One-stage reactor 4 (reactor volume 5m 3 ) The reaction solution enters the heat exchanger 5 through the pump (the material outlet temperature is controlled at 8-10°C) for extr...

Embodiment 3

[0110] Embodiment 3: the continuous production method of terbutyline in series with multiple reactors

[0111] (1) Charge a certain amount of nitrogen in the batching kettle 1 for replacement, cyanuric chloride and toluene are added to the batching kettle in a ratio of 1:5 by mass ratio, fully dissolved to obtain a toluene solution of cyanuric chloride;

[0112] (2) the above-mentioned prepared cyanuric chloride solution passes through precooler 2 according to the flow rate of 6000kg / hour (wherein cyanuric chloride 1000kg / hour), and the material outlet temperature of control precooler 2 is at 5-7 ℃, and The precisely metered 70% aqueous solution of tert-butylamine is fully mixed in the mixer 3 and enters the first-stage reactor 4, and the flow rate of the aqueous solution of tert-butylamine is controlled at 566.5 kg / hour.

[0113] (3) One-stage reactor 4 (reactor volume 5m 3 ) The reaction liquid enters the heat exchanger 5 through the pump (the material outlet temperature is...

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Abstract

The invention relates to a continuous production method of a multi-kettle serial triazine herbicide. A metered cyanuric chloride solution is pre-cooled and mixed with alkylamine R1 in a mixer to entera first-stage reaction kettle, continuous discharging is conducted, after a heat exchanger is passed, the cyanuric chloride solution is neutralized with alkali in the mixer and enters a first-stage neutralization kettle, after a reaction is completed, the cyanuric chloride solution passes through a continuous water separator and the heat exchanger and is mixed with alkylamine R2 in the mixer to enter a second-stage reaction kettle, the continuous discharging is conducted, after the cyanuric chloride solution passes through the heat exchanger, the cyanuric chloride solution is mixed with the alkali in the mixer to enter a second-stage neutralization kettle, after the neutralization, a aqueous phase is separated by a continuous layerer, a solvent is removed, and drying is conducted to obtain a triazine product. The production method has the advantages of high productivity, good production stability, high efficiency, high product quality and the like, is particularly suitable for technical transformation of existing production enterprises, has a low transformation cost, basically does not add novel reaction equipment, and is easily mastered by existing enterprises.

Description

technical field [0001] The invention belongs to the field of chemical synthesis, and in particular relates to a method for continuously producing triazine herbicides in series with multiple reactors. Background technique [0002] Triazine herbicides are one of the traditional herbicides introduced in the 1950s, and their herbicidal activity was discovered in 1952 by the Swiss company Geigy. It acts by inhibiting photosynthesis of plants by targeting D1 protein through photosynthetic system II (PSII). After years of experimentation, a series of triazine herbicides have been developed. Among them, zinc herbicides are used in large amounts. Two chlorine atoms in trimeric chlorine are replaced by two alkylamine groups to form zinc herbicides. Usually, these alkylamine groups include ethylamine, isopropylamine, cyclic Propylamino, tert-butylamino, etc. Representative zinc herbicides include atrazine (atrazine), simazine, terbuthine, permethazine, and the like. This kind of he...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07D251/50
CPCC07D251/50
Inventor 陈冬梅张金娥毕研迎
Owner SHANDONG NORMAL UNIV
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