Organic waste water processing method with synchronously carbon, nitrogen and sulfur removal in one reactor
A technology for organic wastewater treatment and organic wastewater, applied in chemical instruments and methods, water/sewage multi-stage treatment, water/sludge/sewage treatment, etc., can solve the problems of low treatment efficiency, high operating cost, complex process, etc. Achieve high processing efficiency and save floor space
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specific Embodiment approach 1
[0016] Specific implementation mode one: see figure 1 , the organic wastewater treatment method for synchronous removal of carbon, nitrogen and sulfur in a reactor described in this embodiment comprises the following steps:
[0017] Step 1, using only one fluidized bed reactor 3 organic wastewater carbon, nitrogen and sulfur synchronous removal integrated equipment to treat wastewater; the wastewater (wastewater to be treated) is mainly polluted by sulfate, nitrate and organic matter Sulfur-nitrogen-containing organic wastewater with a mass ratio of sulfur to nitrogen of 0.5-5 and a mass ratio of COD to N of 3-8;
[0018] Step 2. Cultivate granular sludge: First, add activated sludge into the fluidized bed reactor 3; then, introduce the waste water to be treated into the fluidized bed reactor 3, and the volume load of the influent in N shall not exceed 2.0kgN / m 3 d, keep the temperature in the fluidized bed reactor 3 at 20-35°C, the hydraulic retention time (HRT) 4h-16h, an...
specific Embodiment approach 2
[0022] Specific embodiment two: In step one of this embodiment, the sulfur-nitrogen mass ratio is 2-2.5, and the sulfur-nitrogen-containing organic wastewater with a COD and N mass ratio of 3-8, wherein the sulfur-nitrogen mass ratio is 2.5, COD to N mass ratio is 5.0, nitrate volume load is 1.5kgN / m 3 When d, the removal effect is the best, and the removal rate of sulfate, nitrate and organic matter reaches 98%, 98% and 80% respectively. Other steps are the same as in the first embodiment.
specific Embodiment approach 3
[0023] Specific implementation method three: In step two of this embodiment, the trace element solution contains 500 mg of H per liter. 3 BO 3 , 500mg of ZnCl 2 , 500mg of (NH 4 ) 6 Mo 7 o 24 4H 2 O, 500mg of NiCl·6H 2 O, 500mg of AlCl 3 ·6H 2 O, 500mg of CoCl 2 ·6H 2 O, 500mg of CuSO 4 ·5H 2 O, 1000mg of NaSeO 3 ·5H 2 O, 1500mg of FeCl 3 ·6H 2 O, 5000mg of MnCl 2 4H 2 O and 5 ml of a 37% HCl solution. The addition of trace elements can promote and strengthen the formation of granular sludge, shortening the formation time of granular sludge by half a month. Other steps are the same as in the first embodiment.
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