Zeolite modified macromolecule suspension biological carrier based wastewater reinforcement and nitrification process
A biological carrier and polymer technology, applied in biological water/sewage treatment, aerobic process treatment, sustainable biological treatment, etc., can solve the lack of enrichment of nitrifying bacteria functional design, restriction of nitrification effect, hydrophilicity and electrophilicity In order to achieve the effect of accelerating the growth rate of microbial attachment, improving the electrophilicity and hydrophilicity, and increasing the abundance
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Embodiment 1
[0018] 1) The reactor of this embodiment is a cylindrical device made of plexiglass, with an effective volume of 4L; 2) Control group: only 8-10g of zeolite powder (200 mesh) was added to the reactor for adsorption test; 3) Experimental group: The IFFAS reactor with zeolite-modified polymer suspended biological carrier, the dosage of the carrier is 30% of the effective volume of the reactor, and the sequential batch water feeding method is adopted. The concentration of the water in the reactor is 45mg / L, and the DO concentration is 2 -3mg / L. After each group of reactors operated for 6 hours, the effluent NH of the control group reactor 4 + -N concentration is 38.2mg / L, NH 4 + -N removal rate is 15%; the effluent NH of the experimental group reactor 4 + -N concentration is 0.9mg / L, NH 4 + -N removal rate was 98%.
Embodiment 2
[0020] 1) figure 1 It is a schematic diagram of the reaction device of this embodiment. Control group 1: activated sludge reactor, control group 2: IFFAS reactor with common carrier (the dosage of carrier is 30% of the effective volume of the reactor), experimental group: adding zeolite modified polymer suspended biological carrier The IFFAS reactor (carrier dosage is 30% of the effective volume of the reactor); 2) The sludge in the secondary sedimentation tank of the municipal sewage treatment plant is used to start the IFFAS reactor, and the sludge concentration in each reactor after inoculation is 2500mg / L; 3) The reactor adopts a continuous flow water inlet method, and the water flow rate is controlled to adjust the hydraulic retention time to 6 hours; an aeration plate is placed at the bottom of the reactor, and an external aeration device is connected to ensure the sludge and biological carrier. Fully fluidized and evenly distributed, and adjust the aeration rate throu...
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