Wastewater treatment method using magnetism biological carrier and magnetic separation technique
A sewage treatment method and biological carrier technology, applied in biological water/sewage treatment, magnetic field/electric field water/sewage treatment, sustainable biological treatment, etc., can solve the difficulty of carrier stripping, high energy consumption of recirculation and complex operation and management and other issues, to achieve the effect of improving recycling efficiency, reducing operating costs, and good economic benefits
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Embodiment 1
[0019] Make the density 1.04g / cm 3 , the magnetic biological carrier with a particle size of 0.043-0.076mm was put into the aeration tank, and the magnetic biological carrier was made of Fe 3 o 4 Magnetic particles and polyethylene resin synthesis. If excess sludge is generated, the sludge and water can be separated by wet drum type permanent magnet weak magnetic field magnetic separator, and then put into the carrier stripping separator to realize the separation of sludge and magnetic carrier. After magnetic separation, the magnetic The carrier is put back into the reactor to realize the recovery and reuse of the magnetic carrier. When the addition amount is 4g / L, the hydraulic retention time is 4h, the aeration rate is 50L / h, and the superficial air velocity is 1.8m 3 / (m 2 h), when the reflux ratio of the mixed solution is 3, the COD removal rate of the effluent can reach 93.8% after testing.
Embodiment 2
[0021] Make the density 1.11g / cm 3 , the magnetic biological carrier with a particle size of 0.076-0.16 mm is put into the aeration tank, and the magnetic biological carrier body is synthesized by magnetite and polyethylene resin. If excess sludge is generated, the sludge and water can be separated by wet drum type permanent magnet weak magnetic field magnetic separator, and then put into the carrier stripping separator to realize the separation of sludge and magnetic carrier. After magnetic separation, the magnetic The carrier is put back into the reactor to realize the recovery and reuse of the magnetic carrier. When the addition amount is 10g / L, the hydraulic retention time is 3h, the aeration rate is 100L / h, and the superficial air velocity is 3.5m 3 / (m 2 .h), when the reflux ratio of the mixed solution is 2, the COD removal rate of the effluent can reach 98.2% after testing.
Embodiment 3
[0023] Make the density 1.20g / cm 3 , The magnetic biological carrier with a particle size of 0.043-0.076mm is put into the aeration tank, and the magnetic biological carrier is synthesized by magnetite particles and polypropylene resin. If excess sludge is generated, the sludge and water can be separated by wet drum type permanent magnet weak magnetic field magnetic separator, and then put into the carrier stripping separator to realize the separation of sludge and magnetic carrier. After magnetic separation, the magnetic The carrier is put back into the reactor to realize the recovery and reuse of the magnetic carrier. When the addition amount is 7g / L, the hydraulic retention time is 3.5h, the aeration rate is 80L / h, and the superficial air velocity is 2.8m 3 / (m 2 h), when the reflux ratio of the mixed solution is 5, the COD removal rate of the effluent can reach 98.0% after testing.
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