Method for improving brine processing capability of brine preprocessor
A pre-processor, brine technology, applied in the direction of electrolysis components, electrolysis process, etc., can solve the problems of reducing water output and incomplete pre-treatment, etc.
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Embodiment 1
[0021] 1) After the light brine and steam condensate returned by electrolysis are mixed in the water distribution tank, they are pumped to the salt tank for salt conversion;
[0022] 2) Add refined agent A (caustic soda) and refined agent B (sodium hypochlorite) to the coarse saturated brine coming out of the salt tank when it flows through the baffle tank; enter the front reaction tank, the Mg content of the front reaction tank is 250ppm, and pump it to the pre-reaction tank after the reaction is completed. In the processor, the salt mud is removed according to the principle of stratification of insoluble substances with different specific gravity;
[0023] 3) After the desilting in the preprocessor is completed, 10% of the crude saturated brine flows back to the front reaction tank through the pipeline; 90% of the crude saturated brine flows into the rear reaction tank and adds refined preparation C (sodium carbonate), and after the reaction, enters the brine Membrane filter...
Embodiment 2
[0027] Others are the same as embodiment 1. The difference is:
[0028] The Mg content in the reaction tank before the primary brine section is 380ppm, the crude brine pump flow rate is increased by 30%, the preprocessor reflux regulating valve is 30% year-on-year, the preprocessor inlet membrane filter flow rate is kept constant, and the preprocessor outlet Mg is analyzed Content 18ppm, membrane filter outlet brine Ca+Mg<1ppm.
Embodiment 3
[0030] Others are the same as embodiment 1. The difference is: refining agent A is soda ash, refining agent B is sulfuric acid, and refining agent C is caustic soda.
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