This invention relates to a high NH4 content + ‑N, high NO3 — -N and high F — The high-efficiency, low-consumption treatment process for photovoltaic
wastewater involves initially removing
fluoride from the
wastewater, which then enters a synergistic short-
cut denitrification tank. Through the synergistic effect of heterotrophic short-
cut denitrification and
sulfur autotrophic short-
cut denitrification in the tank, NO3... — -N denitrification reaction controlled at NO2 — This step, involving the addition of
nitrogen (N), avoids full-scale denitrification by combining the
effluent from short-cut denitrification with high NH4 levels. + -N
silane wastewater is mixed in an intermediate tank and then undergoes efficient denitrification via an anaerobic
ammonia oxidation (AAO) reactor. The
effluent from the AAO reactor enters the MABR (Maintenance-Based
Bioreactor) tank. The unique
layered structure of the MABR
biofilm ensures that
nitrification / short-cut
nitrification, AAO, and denitrification / short-cut denitrification reactions occur in the same reactor, achieving deep denitrification and removal of residual COD. This process achieves acid-base balance during the
biochemical reactions, saving 100% of the acid and alkali dosage.
Sludge production is only 10% of that of traditional denitrification processes under the same load, significantly reducing operating costs.