Amino benzene analog waste water biological treatment method
A technology for biological treatment and wastewater, applied in sustainable biological treatment, biological water/sewage treatment, water/sludge/sewage treatment, etc., can solve the problem of inability to apply fluidized bed reactor, etc., and achieve good economic benefits and environment. Benefit, low wear rate, waste reduction effect
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Embodiment 1
[0021] In the SBR reactor with an effective volume of 1.3L, large-porous cross-linked polystyrene white balls were used as immobilized microbial carriers. The carrier volume was 4% of the effective volume of the reactor. After 20-30 days of microbial immobilization, the synthetic A stable biofilm is formed on a macroporous polymer carrier. The test wastewater is simulated p-toluidine wastewater, whose pH value is adjusted to 5-10, and nitrogen and phosphorus nutrients are added to make the wastewater COD 1100mg / L and p-toluidine concentration 327mg / L. Add 0.8L waste water to the reactor in each batch, and the water inflow mode is instantaneous water inflow. At 25°C, when the aeration rate is 0.6L / min, after aeration for 360 minutes, sediment for 30 minutes and drain. The COD in the effluent is 10.5mg / L, the concentration of p-toluidine is less than 0.5mg / L, and the concentration of ammonia nitrogen is 20mg / L.
Embodiment 2
[0023] In the SBR reactor described in Example 1, macroporous cross-linked polystyrene white balls accounting for 6% of the effective volume were added as immobilized microorganism carriers. After 20-30 days of microorganism immobilization, a stable biofilm is formed on the synthetic macroporous polymer carrier. The test wastewater is simulated p-aminophenol production wastewater, whose pH value is adjusted to 5-10, and nitrogen and phosphorus nutrients are added to make the wastewater COD 2300mg / L and p-aminophenol concentration 648mg / L. The amount of water inflow and the way of water inflow are the same as in Example 1. At 15°C, when the aeration rate is 0.9L / min, after aeration for 420 minutes, sediment for 120 minutes and drain. The COD in the effluent was 16.4mg / L, the concentration of p-aminophenol was less than 0.5mg / L, and the concentration of ammonia nitrogen was 23.9mg / L.
Embodiment 3
[0025] In the SBR reactor described in Example 1, macroporous anion exchange resin D301 accounting for 10% of the effective volume was added as the immobilized microorganism carrier. After 20-30 days of microorganism immobilization, a stable biofilm is formed on the synthetic macroporous polymer carrier. Test waste water, water intake and water intake mode are the same as embodiment 1. At 10°C, when the aeration rate is 0.9L / min, after aeration for 480 minutes, sediment for 90 minutes and drain. The COD in the effluent is 17.1mg / L, the concentration of p-toluidine is less than 0.5mg / L, and the concentration of ammonia nitrogen is 24.1mg / L.
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