A system and method for three-dimensional electrolytic removal of ammonia nitrogen in a liquid-solid fluidized bed to realize wastewater reuse
A fluidized bed and three-dimensional electric technology, which is applied in the fields of chemical industry and environmental protection, can solve the problems of particle electrode anode catalytic coating wear, low performance of unipolar particle electrodes, low effect of unipolar particle electrodes, etc., and achieve pollution-free economy properties, promoting decomposition, and inhibiting wear
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Embodiment 1
[0066] combine figure 1 , a liquid-solid fluidized bed three-dimensional electrolytic ammonia nitrogen removal system used in this embodiment to realize wastewater reuse, including a filtering section 1, a spraying section 2, an electrolysis section 3 and a water quality adjustment section 4;
[0067] Filtration section 1 includes gravity settling tank 1-1, settling tank blowdown valve 1-2, filter inlet pump 1-3, filter 1-4 and filter blowdown valve 1-5;
[0068] Spray section 2 includes spray tower 2-1, spray tower drain valve 2-2, spray pump 2-3, catalyst tank 2-4, catalyst feed valve 2-5, catalyst feed pump 2-6, Induced fan 2-7 and spray tower feed pump 2-8;
[0069] Electrolysis section 3 includes DC power supply 3-1, electrolyzer feed pump 3-2, plate and frame electrolyzer 3-3, fluidized bed electrolysis inlet valve 3-4, fluidized bed electrolyzer 3-5, fluidized bed electrolyzer Liquid outlet valve 3-6, gas-liquid separation tank 3-7 and separation tank drain valve 3-8;...
Embodiment 2
[0078] In this embodiment, the method of removing ammonia nitrogen by three-dimensional electrolysis of the liquid-solid fluidized bed described in Embodiment 1 to realize the reuse of wastewater includes the following steps:
[0079] The ammonia nitrogen waste water is sent to the gravity settling tank 1-1, and after gravity settling, the supernatant and sludge are obtained; the sludge is discharged through the settling tank blowdown valve 1-2 and sent for treatment; the supernatant is sent in through the filter inlet pump 1-3 In the filter 1-4, the filtered clear liquid and filtered sludge are obtained; the filtered sludge is discharged through the filter sewage valve 1-5 and sent for processing; a part of the filtered clear liquid is sent to the spray tower 2 through the spray tower feeding pump 2-8 -1; another part of the filtered clear liquid is sent into the regulating tank 4-2 through the raw water pump 4-4 of the regulating tank; the catalyst in the catalyst tank 2-4 pa...
Embodiment 3
[0082] In this embodiment, the printing and dyeing wastewater of a certain enterprise is used as the treatment object, and the treatment capacity is 15m 3 / h, the initial value of ammonia nitrogen is 10000. In the spraying section 2, the catalyst is a sodium chloride solution, and the amount of the catalyst added is 2% of the mass of the ammonia nitrogen wastewater. The water flow in the plate and frame electrolyzer 3-3 is in parallel structure, and the current is in series structure. The anode in the plate and frame electrolytic cell 3-3 is a titanium electrode coated with platinum, ruthenium, iridium, tantalum, tin, antimony and manganese; the cathode is a titanium electrode; the distance between the anode and cathode is 2mm; the current density of the anode is 800A / m 2 . The built-in electrode in the plate-frame electrolytic cell 3-3 adopts an integrated bipolar plate structure, and the coated titanium electrode adopts a single-sided active coating. In the fluidized bed ...
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