A method for synergistic and low-consumption removal of multi-pollutants in nitrogen fertilizer wastewater
A technology for pollutants and waste water, applied in the direction of water pollutants, chemical instruments and methods, water/sewage multi-stage treatment, etc., can solve the problems of high cost and high energy consumption, reduce energy consumption and material consumption, and improve process applicability Effects on sex and flexibility
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specific Embodiment approach 1
[0016] Specific embodiment one: the collaborative low-consumption method of this embodiment removes multi-pollutants in nitrogenous fertilizer wastewater, comprising the following steps:
[0017] 1. Nitrogen fertilizer wastewater is pumped into the anaerobic digestion reactor directly or after pretreatment. The reactor is a sealed sequencing batch reactor (SBR) with mechanical stirring and a gas collection device at the top; the reaction cycle is: Water for 0.5-1h, stirring for 20-24h, standing still for 0.5-1h, draining for 0.5-1h, water exchange ratio of 60%-80%; during operation, the temperature in the anaerobic digestion reactor is 20-40°C, and the pH is 7.0 ~8.0, the sludge concentration is 7000~9000mg / L; at this stage, 60~80% of organic matter and 70~90% of sulfur-containing pollutants in the wastewater are under the action of methanogenic bacteria and sulfate reducing bacteria in the sludge be removed;
[0018] 2. The effluent from the anaerobic digestion reactor enter...
specific Embodiment approach 2
[0020] Specific embodiment two: the difference between this embodiment and specific embodiment one is the pretreatment described in step one, when the anaerobic digestion section effluent COD of step one is higher than 80mg / L, enable the forward osmosis unit, first Low-concentration nitrogen fertilizer wastewater is concentrated; others are the same as the specific embodiment one.
specific Embodiment approach 3
[0021] Specific embodiment three: the difference between this embodiment and specific embodiment two is that the forward osmosis unit uses a cellulose triacetate (CTA) membrane with a thickness of 50-80 μm and a pore size of 0.2-0.35 nm as the permeable membrane; mol / L NaCl is used as the driving solution, and the concentration ratio is controlled at 2 to 5 times; the others are the same as in the second embodiment.
[0022] In this embodiment, the waste water is concentrated by relying on the pressure difference on both sides of the permeable membrane as the driving force.
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