Continuous production method of acephate
A technology of acephate linking and methamidophos is applied in the field of preparation of acephate continuous production, can solve the problems of no acephate continuous production and the like, achieves a high degree of automation, improved product output, and reduced waste water. Emission reduction effect
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Embodiment 2
[0032] First add 600kg of methamidophos solution by metering at the inlet of reaction pump 1.1, start reaction pump 1.1, slowly add 370kg of acetic anhydride at the inlet of reaction pump 1.1; after adding acetic anhydride, slowly drop 15kg of catalyst at the inlet of reaction pump 1.1 , and at the same time open the inlet and outlet valves of the circulating water of the cooler, and control the temperature of the reactor 1.2 at 50°C. After the dropwise addition is completed, keep warm at 50-60°C for 2 hours. After the base material is prepared, start continuous feeding production. The input amount of methamidophos solution is 1200kg / h, acetic anhydride is 740kg / h, catalyst is 30kg / h, and the reaction temperature is controlled at 50°C. , the reaction material overflows from the intermediate tank 1.3 into the insulation tank 1.4, and the temperature of the insulation tank is controlled at 50-60 ° C. The acylation solution of the material that is finally completed overflows from ...
Embodiment 3
[0041] Add 2000kg of acylation solution at the inlet of reaction pump 2.1, start reaction pump 2.1, add acylation solution and water (or mother liquor) at the inlet of reaction pump 2.1, control the addition of acylation solution 2000kg / h, water 1000L / h (or Mother liquor 2000L / h), open the brine import and export valve of cooler simultaneously, control reactor 2.2 temperature at 20 ℃. The hydrolyzate of the reacted material overflows from the intermediate tank 2.3 into the transfer tank 2.4, and the hydrolyzate is used as the raw material for the next process. The reaction yield is 99.3%.
[0042] 3. Neutralization and continuous production
[0043] 3.1 Embodiment 1
[0044] Add 2000kg of hydrolyzate to the inlet of reaction pump 3.1, start reaction pump 3.1, add hydrolyzate, solvent and ammonia gas at the inlet of reaction pump 3.1, control the addition of hydrolyzate to 4000kg / h, solvent 1000L / h, add ammonia to control PH Value at 9, open the brine import and export valve...
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