Short-range preprocessing method for cutting effluent
A cutting waste liquid and pretreatment technology, which is applied in water/sewage treatment, chemical instruments and methods, special compound water treatment, etc. High-efficiency demulsification, convenient oil-water separation, and simple operation for problems such as high oil content
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Embodiment 1
[0014] Take 1000ml of cutting waste fluid produced by mechanical processing, its initial COD value is 68000mg / L, and its initial pH is 7.3. With sulfuric acid, the pH value of the waste liquid is adjusted to 3, and 6g of ferrous sulfate heptahydrate (0.0216molFeSO 4 ·7H 2 O), aerate and stir to dissolve, slowly add 24g of 30% hydrogen peroxide (containing 0.212mol H 2 o 2 ), reacted for 2h, left to separate after the reaction, and skimmed off the slick oil. Add Ca(OH) to the supernatant 2 , the pH of the solution was adjusted to 8, and then 10 mg of anionic PAM was added, stirred for 5 minutes, precipitated for 20 minutes, and the sediment was separated and filtered under pressure. After the above steps, the COD removal rate of the waste liquid is 95.4%.
Embodiment 2
[0016] Take 1000ml of cutting waste fluid produced by mechanical processing, its initial COD value is 88000mg / L, and its initial pH is 7.5. With sulfuric acid, the pH value of the waste liquid is adjusted to 3.5, and 7g ferrous sulfate heptahydrate (0.0252mol FeSO 4 ·7H 2 O), aerated and stirred to dissolve, slowly added 16.8g of 30% hydrogen peroxide (containing 0.148mol H 2 o 2 ), reacted for 2h, left to separate after the reaction, and skimmed off the slick oil. Add Ca(OH) to the supernatant 2 , the pH of the solution was adjusted to 8.5, and then 20 mg of anionic PAM was added, stirred for 5 minutes, precipitated for 20 minutes, and the sediment was separated and filtered under pressure. After the above steps, the COD removal rate of the waste liquid is 96.2%.
Embodiment 3
[0018] Take 1000ml of cutting waste fluid produced by mechanical processing, its initial COD value is 172620mg / L, and its initial pH is 9. With sulfuric acid, the pH value of the waste liquid is adjusted to 3.5, and 9g ferrous sulfate heptahydrate (0.0324mol FeSO 4 ·7H 2 O), aerate and stir to dissolve, slowly add 45g of 30% hydrogen peroxide (containing 0.4mol H 2 o 2 ), reacted for 2.5h, left to separate after the reaction, and skimmed off the slick oil. Add Ca(OH) to the supernatant 2 , the pH of the solution was adjusted to 9, then 20 mg of anionic PAM was added, stirred for 7 minutes, precipitated for 25 minutes, the sediment was separated, and the sediment was subjected to pressure filtration. After the above steps, the COD removal rate of the waste liquid is 90.2%.
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