Method for treating high concentration ammonia nitrogen waste water
A technology of ammonia nitrogen wastewater and treatment method, which is applied in biological water/sewage treatment, water/sludge/sewage treatment, sustainable biological treatment, etc., can solve the problem of low ammonia nitrogen concentration and organic matter content, and achieve the effect of reducing the number of times.
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Embodiment 1
[0026] Nitrifying bacteria are enriched by intermittent activated sludge method. The activated sludge is taken from the sludge at the outlet of the secondary settling tank in the wastewater treatment workshop of the refinery, and inoculated into the enrichment reactor with an inoculation amount of 30v%, with a total volume of 3L , and then add the enrichment medium, wherein the composition of the enrichment medium used is (NH 4 ) 2 SO 4 , FeSO 4 ·7H 2 O, MgSO 4 ·7H 2 O, NaCl, CaCl 2 and KH 2 PO 4 , the concentration is as follows: NH 4 + -N initial concentration is 150mg / L, final concentration is 1000mg / L; Fe 2+ The concentration is 12mg / L; Mg 2+ The concentration is 18mg / L; Na + The concentration is 800mg / L; Ca 2+ The concentration is 16mg / L; KH 2 PO 4 The concentration is 260mg / L. During the enrichment process, NaHCO 3 Control pH. The culture conditions are: temperature: 24°C; pH=6.0-7.5; SV: 15%-20%; DO: 10mg L -1 . One cycle per day, water intake time ...
Embodiment 2
[0029] Nitrifying bacteria are enriched by intermittent activated sludge method. The activated sludge is taken from the outlet sludge of the secondary settling tank in the wastewater treatment workshop of the refinery, and inoculated into the enrichment reactor with an inoculum of 22v%, with a total volume of 3L , and then add the enriched culture solution, wherein the composition of the enriched culture solution used is the same as in Example 1, but the concentration is different, specifically as follows: NH 4 + -N initial concentration is 100mg / L, final concentration is 550mg / L; Fe 2+ The concentration is 6mg / L; Mg 2 + The concentration is 10mg / L; Na + The concentration is 300mg / L; Ca 2+ The concentration is 8mg / L; KH 2 PO 4 The concentration is 100mg / L. During the enrichment process, NaHCO 3 Control pH. The culture conditions are: temperature: 25°C; pH=6.0-7.5; SV: 15%-25%; DO: 5mg·L -1 . 2 cycles per day, water intake time is 10 minutes, aeration is 11 hours, na...
Embodiment 3
[0032] Nitrifying bacteria are enriched by intermittent activated sludge method. The activated sludge is taken from the outlet sludge of the catalyst wastewater treatment workshop and inoculated in the enrichment reactor with an inoculation amount of 28v%. The total volume is 3L, and then the enriched Collect culture fluid, wherein the enrichment culture fluid composition used is the same as embodiment 1, but the concentration is different, specifically as follows: NH 4 + -N initial concentration is 180mg / L, final concentration is 800mg / L; Fe 2+ The concentration is 10mg / L; Mg 2+ The concentration is 12mg / L; Na + The concentration is 500mg / L; Ca 2+ The concentration is 10mg / L; KH 2 PO 4 The concentration is 200mg / L. During the enrichment process, NaHCO 3 Control pH. The culture conditions are: temperature: 28°C; pH=6.0-8.5; SV: 15%-20%; DO: 8mg·L -1 . One cycle per day, water intake time is 30 minutes, aeration is 22.5 hours, natural settlement is 40 minutes, superna...
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