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
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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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