Method for treating and cycling light salt brine containing sodium carbonate and sodium hypochlorite
A technology of sodium hypochlorite and sodium carbonate, applied in chemical instruments and methods, multi-stage water/sewage treatment, water/sludge/sewage treatment, etc., can solve the problem that sodium chloride and sodium carbonate cannot be effectively used and increase the amount of wastewater treatment in enterprises The amount and treatment cost and other issues can be solved to achieve the effects of saving waste water treatment cost and raw material cost, easy operation and environmental protection
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Embodiment 1
[0027] (1) 1000kg of light brine containing sodium carbonate and sodium hypochlorite (see Table 1 for specific components and content) produced by the hydrogen chloride catalytic oxidation chlorine production device is delivered to the baffle tank, and adding a weight concentration in the baffle tank is a 31% hydrochloric acid solution , adjust the pH to 8, transport to the reaction kettle, the stirring of the reaction kettle is in the normal open state, and the temperature of the solution in the tower kettle is maintained at 40°C through the jacketed hot water, and the reaction is carried out for 240 minutes, so that the sodium hypochlorite is decomposed. The solution is pumped to the middle tank;
[0028] (2) Adding the sodium hydroxide solution that the weight concentration is 32% in the middle tank, adjust the pH to 12, and add anhydrous sodium sulfite, react for 15 minutes, and the treatment solution obtained (see Table 1 for specific components and contents) is delivered ...
Embodiment 2
[0043] (1) 1000kg of light brine containing sodium carbonate and sodium hypochlorite (see Table 3 for specific components and content) produced by the hydrogen chloride catalytic oxidation chlorine production device is delivered to the baffle tank, and the hydrochloric acid solution that is 31% by weight is added in the baffle tank , adjust the pH to 8.5, transport to the reactor, the reactor is in the normal state of stirring, and the temperature of the solution in the tower kettle is maintained at 60°C through the jacketed hot water, and react for 180 minutes to make the sodium hypochlorite decompose. The solution is pumped to the middle tank;
[0044] (2) Adding the sodium hydroxide solution that the weight concentration is 32% in the intermediate tank, adjust the pH to 11, and add anhydrous sodium sulfite, react for 15 minutes, and the treatment solution obtained (see Table 3 for specific components and contents) is delivered to In the reactor after the brine section; wher...
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