Yellow phosphorus arsenic removing method
A yellow phosphorus and arsenic removal technology is applied in the field of yellow phosphorus purification and arsenic removal by oxidation, which can solve the problems of a large amount of mixed acid waste liquid, high production cost and large phosphorus loss.
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Embodiment 1-4
[0028] Embodiment 1-4 (example of the present invention):
[0029] Allocate 10 kilograms of water-phase oxidant described in table 1 in above-mentioned reactor (wherein basic oxidant is nitric acid, and oxidation enhancer is sodium bromate), adds 3 kilograms of technical grade yellow phosphorus, contains arsenic 85PPm before yellow phosphorus is handled, regulates The jacket heated the water temperature until the temperature of the reaction treatment solution reached 70°C and started to stir. The reaction was maintained at 70°C for 3 hours, the stirring was stopped, and the lower part of the yellow phosphorus for arsenic removal was removed.
[0030] It can be seen from Examples 1-4 that when the basic oxidant and the oxidation enhancer are added simultaneously, the removal rate of arsenic and the yield of yellow phosphorus are both high.
[0031] Table 1: Dearsenic conditions and results of Examples 1-4
[0032]
Embodiment 5—8
[0033] Embodiment 5-8 (example of the present invention):
[0034] In the reactor of embodiment 1, enter 10 kilograms of base oxidant nitric acid described in table 2, add 3 kilograms of industrial grade yellow phosphorus in the reactor, contain arsenic 85ppm before the yellow phosphorus is handled, regulate the temperature of jacket heating water, make reaction When the temperature of the solution reaches 70°C, stir and react for 30 minutes, then gradually add the oxidation enhancer sodium bromate within 1 hour, and react for 1 hour and 30 minutes under the condition of maintaining 70°C. The total reaction time for arsenic removal is still 3 hours. The lower part of the reactor removes arsenic and yellow phosphorus, and the final implementation results are shown in Table 2.
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