Method for resource treatment of phosphatized sludge
A technology of phosphating sludge and disposal method, applied in sludge treatment, chemical instruments and methods, water/sludge/sewage treatment, etc., can solve the problems of difficult treatment of phosphating wastewater and high treatment cost, and achieve low treatment cost , high processing efficiency, and the effect of resource utilization
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[0041] Example 1
[0042] Using the present invention to treat the phosphating sludge produced by a surface treatment enterprise in Jiangsu, the operating conditions are as follows: waste sulfuric acid with an acid concentration of 10% is used, and the dosage ratio of the phosphating sludge and the waste sulfuric acid (all in each embodiment) is: 1:5, the stirring and mixing time is 1h, after the reaction, the filter residue is pressure filtered and sent to the cement factory to make cement; the filtrate is added with a self-configured precipitant, and the proportion of the precipitant is NaOH:EDTA:FeSO 4 = 2:3:0.5, the dosage of the precipitant is 0.3% of the filtrate, and the reaction time is 1h; after passing through the anion exchange resin, the saturated resin is eluted with a rate of 1.4 volume column / hour, and in the eluent Add 10% slaked lime, react for 1.5h, and the reaction pH is 6 to form a phosphate pigment.
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[0043] Example 2
[0044] Using the invention to treat the phosphating sludge of a chemical enterprise in Anhui, the operating conditions are as follows: waste sulfuric acid with an acid concentration of 5% is used, the dosage ratio of phosphating sludge and waste sulfuric acid is 1:15, and the stirring and mixing time is 2h After the reaction, the filter residue is pressure filtered and sent to the cement factory to make cement; the filtrate is added with a self-configured precipitant, and the proportion of the precipitant is NaOH:EDTA:FeSO 4= 6:1:1, the dosage of the precipitant is 1.2% of the filtrate, and the reaction time is 1.5h; after passing through the anion exchange resin, the saturated adsorption resin is eluted at a rate of 1.8 volumes of column / hour, and in the eluent. Add 15% slaked lime, react for 2 hours, and the reaction pH is 7 to form phosphate pigment.
Example Embodiment
[0045] Example 3
[0046] Using the invention to treat the phosphating sludge of a stainless steel production enterprise in Anhui, the operating conditions are as follows: waste sulfuric acid with an acid concentration of 20% is used, the dosage ratio of the phosphating sludge and the waste sulfuric acid is 1:3, and the stirring and mixing time is 1.5h, after the reaction, the filter residue is pressure filtered and sent to the cement factory for making cement; the filtrate is added with a self-configured precipitant, and the proportion of the precipitant is NaOH:EDTA:FeSO 4 =3:2:0.8, the dosage of the precipitant is 1.5% of the filtrate, and the reaction time is 0.5h; after passing through the anion exchange resin, the saturated resin is eluted with a rate of 1.2 volume column / hour, and in the eluent Add 20% of slaked lime, react for 2.5 hours, and the reaction pH is 8 to form a phosphate pigment.
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