Method for sewage neutralization and efficient cyclic utilization of waste residue
A technology for sewage and waste residues, applied in the field of efficient recycling of sewage and waste residues, can solve the problems of waste of mineral resources, insignificant benefits, and high processing costs, and achieve the effects of improving comprehensive utilization of resources and increasing economic benefits.
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Embodiment 1
[0025] 1) Acidic wastewater neutralization treatment process
[0026] Acidic wastewater with a sulfuric acid concentration of 5% enters 4 stirring tanks connected in series, adding high-alkalinity calcium oxide slag produced after calcination to control pH = 7, fully aerating during the neutralization process, for 6 hours, and 5.5% after neutralization The thin slurry enters the thickener for thickening, the overflow returns to the acid purification process for use, and the high-concentration slurry enters the filter press dehydration process;
[0027] 2) Filter press dehydration
[0028] The high-concentration slurry is pumped into the filter press for pressing, filtration and dehydration, the filtrate is returned to the thickener, and the filter cake with a moisture content of 45% enters the rotary kiln baking process;
[0029] 3) Rotary kiln baking dehydration
[0030] The filter cake with a moisture content of 45% enters the rotary kiln through a belt conveyor, the rotar...
Embodiment 2
[0040] 1) Acidic wastewater neutralization treatment process
[0041] Acid wastewater with a sulfuric acid concentration of 10% enters 4 stirring tanks connected in series, and the high-basicity calcium oxide slag produced after calcination is added to control the pH=7, and the neutralization process is fully aerated for 7 hours, and after neutralization, 7% The thin slurry enters the thickener for thickening, the overflow returns to the acid purification process for use, and the high-concentration slurry enters the filter press dehydration process;
[0042] 2) Filter press dehydration
[0043] The high-concentration slurry is pumped into the filter press for pressing, filtration and dehydration, the filtrate is returned to the thickener, and the filter cake with a moisture content of 48% enters the rotary kiln baking process;
[0044] 3) Rotary kiln baking dehydration
[0045] The filter cake with a moisture content of 48% enters the rotary kiln through a belt conveyor. The...
Embodiment 3
[0055] 1) Acidic wastewater neutralization treatment process
[0056] Acidic wastewater with a sulfuric acid concentration of 15% enters 4 stirring tanks connected in series, adding high-basicity calcium oxide slag produced after calcination to control pH = 7, fully aerating during the neutralization process, for 8 hours, and 8% after neutralization The thin slurry enters the thickener for thickening, the overflow returns to the acid purification process for use, and the high-concentration slurry enters the filter press dehydration process;
[0057] 2) Filter press dehydration
[0058] The high-concentration slurry is pumped into the filter press for pressing, filtration and dehydration, the filtrate is returned to the thickener, and the filter cake with a moisture content of 50% enters the rotary kiln baking process;
[0059] 3) Rotary kiln baking dehydration
[0060] The filter cake with a moisture content of 50% enters the rotary kiln through a belt conveyor, the rotary k...
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