Method for recycling waste sulfuric acid in chlor-alkali industry
A technology for chlor-alkali industry and waste sulfuric acid, which is applied in the direction of alkali metal sulfite/sulfite, chemical instruments and methods, alkali metal compounds, etc., and can solve the problems of limited improvement effect, low economic benefit, and poor operability, etc. problems, achieve the effect of simple operation, simple and feasible process, and eliminate risks
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Embodiment 1
[0035] A method for recycling waste sulfuric acid in the chlor-alkali industry, comprising the following steps:
[0036] (1) at 6.3m 3 Add deionized water into the enamel reaction kettle, turn on the stirrer, then weigh the chlor-alkali industrial waste sulfuric acid (76.5%), slowly add it into the reaction kettle through a diaphragm pump, and then slowly add potassium hydroxide solution (30%) under stirring , the percentage by weight of the added chlor-alkali industrial waste sulfuric acid, deionized water, and potassium hydroxide solution is 25.05%, 2.33% and 72.62%. After adding, a mixed solution is formed and a white precipitate is separated out. The pH of the mixed solution is controlled at 6.5. The reaction process The chlorine gas removed in the process is transported to the alkali washing tower by the induced draft fan, and is absorbed by caustic soda to generate sodium hypochlorite;
[0037] (2) Add deionized water to the neutralization kettle, make the product in st...
Embodiment 2
[0041] A method for recycling waste sulfuric acid in the chlor-alkali industry, comprising the following steps:
[0042] (1) at 6.3m 3 Add deionized water into the enamel reaction kettle, turn on the agitator, then weigh the chlor-alkali industrial waste sulfuric acid (76.5%), slowly add it into the reaction kettle through a diaphragm pump, and then slowly add potassium hydroxide solution (48%) under stirring , the percentage by weight of the added chlor-alkali industrial waste sulfuric acid, deionized water, and potassium hydroxide solution is 33.25%, 6.5% and 60.25%. After adding, a mixed solution is formed and a white precipitate is separated out. The pH of the mixed solution is controlled at 6.5. The reaction process The chlorine gas removed in the process is transported to the alkali washing tower by the induced draft fan, and is absorbed by caustic soda to generate sodium hypochlorite;
[0043] (2) Add deionized water to the neutralization kettle, make the product in st...
Embodiment 3
[0047] A method for recycling waste sulfuric acid in the chlor-alkali industry, comprising the following steps:
[0048] (1) at 6.3m 3 Add deionized water into the enamel reaction kettle, turn on the agitator, then weigh the chlor-alkali industrial waste sulfuric acid (75.1%), slowly add it into the reaction kettle through a diaphragm pump, and then slowly add potassium hydroxide solution (30%) under stirring , the percentage by weight of the added chlor-alkali industrial waste sulfuric acid, deionized water, and potassium hydroxide solution is 25.44%, 1.85% and 72.71%. After adding, a mixed solution is formed and a white precipitate is separated out, and the pH of the mixed solution is controlled at 7. The reaction process The chlorine gas removed in the process is transported to the alkali washing tower by the induced draft fan, and is absorbed by caustic soda to generate sodium hypochlorite;
[0049] (2) Add deionized water to the neutralization kettle, make the product in...
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