Method for biologically removing phosphorus by using acid produced by mixing municipal sludge and organic wastes
A technology for organic waste and biological phosphorus removal, applied in biological sludge treatment, chemical instruments and methods, biological water/sewage treatment, etc., can solve problems such as less research
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Embodiment 1
[0017] Embodiment 1, a method of mixing municipal sludge and organic waste to produce acid for biological phosphorus removal, the steps are as follows:
[0018] (1) Put wastewater, organic waste and settled anaerobic sludge from the sewage treatment plant into the reactor, the weight ratio of anaerobic sludge to organic waste is 1:2, and use sodium bicarbonate to adjust the materials in the reactor pH to 6;
[0019] (2) Put the material in the reactor for 5 hours for pretreatment, and quickly fill the reactor with N after the pretreatment 2 To remove the air in the reactor, maintain the anaerobic state in the reactor, and treat for 3 h ;
[0020] (3) Put NH into the reactor 4 Cl and KH 2 PO 4 As a nitrogen source, control the material NH in the reactor +3 – The N content is 25mg / L, the material temperature is 20°C, and the circulation pump is used for anaerobic circulation for 200h, aeration for 5h, and drainage after 14-h of static settlement.
Embodiment 2
[0021] Embodiment 2, a method of mixing municipal sludge and organic waste to produce acid for biological phosphorus removal, the steps are as follows:
[0022] (1) Put wastewater, organic waste and settled anaerobic sludge from the sewage treatment plant into the reactor, the weight ratio of anaerobic sludge to organic waste is 1: 3, and use sodium bicarbonate to adjust the material in the reactor pH to 7;
[0023] (2) Put the materials in the reactor for 10 h for pretreatment, and quickly fill the reactor with N after the pretreatment 2 To remove the air in the reactor, keep the anaerobic state in the reactor, and treat for 6 h ;
[0024] (3) Put NH into the reactor 4 Cl and KH 2 PO 4 As a nitrogen source, control the material NH in the reactor +3 – The N content is 35mg / L, the material temperature is 25°C, the circulation pump is used for anaerobic circulation for 220 hours, aeration for 7 hours, and drainage after 16 hours of static settlement.
Embodiment 3
[0025] Embodiment 3, a method of mixing municipal sludge and organic waste to produce acid for biological phosphorus removal, the steps are as follows:
[0026] (1) Put wastewater, organic waste and settled anaerobic sludge from the sewage treatment plant into the reactor, the weight ratio of anaerobic sludge to organic waste is 1:2.5, and use sodium bicarbonate to adjust the materials in the reactor pH to 6.5;
[0027] (2) Put the material in the reactor for 5 hours for pretreatment, and quickly fill the reactor with N after the pretreatment 2 To remove the air in the reactor, keep the anaerobic state in the reactor, and treat for 4h ;
[0028] (3) Put NH into the reactor 4 Cl and KH 2 PO 4 As a nitrogen source, control the material NH in the reactor +3 – The N content is 30mg / L, the material temperature is 20°C, the circulation pump is used for anaerobic circulation for 215 hours, aeration for 6 hours, and drainage after 15 hours of static settlement.
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