Method of separating and recovering ammonia from ammonia nitrogen wastewater
A technology for the separation and recovery of ammonia nitrogen wastewater, applied in the field of separation and recovery of ammonia, can solve the problems of expensive, unfeasible, and high cost of chemical products, and achieve the effects of simple process, avoiding secondary pollution, and easy operation
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Embodiment 1
[0037] Take NH 4 Cl concentration is 0.51mol / L cobalt chloride ammonium decomposition liquid 1.5m 3, its pH value is 8.1, according to 1.5 times of the stoichiometric number of ammonium metavanadate formed by the ammonium therein, stirring and adding sodium vanadate, reacting at -3°C for 8 hours, and filtering to obtain the ammonia nitrogen content of 13mg / L (<15ppm) Ammonia back liquid (ammonia nitrogen removal rate is 99.86%) and the ammonium metavanadate filter cake that moisture content is 6.5%, then convert the remaining vanadium into calcium vanadate stoichiometric number by 2.5 times and add chlorination Calcium, and adjust the pH of the solution to 10.5 with calcium oxide, stir at room temperature for 5 hours, filter the calcium salt precipitate filter cake and the vanadium-precipitated solution containing V≤1mg / L (1ppm), adjust the pH of the vanadium-precipitated solution to 7.8 and discharge it. The obtained calcium salt precipitate filter cake is leached with sodiu...
Embodiment 2
[0039] Take 3000mL of tungsten raffinate, which contains Na + , NH 4 + , SO 4 2- Etc., wherein ammonia nitrogen concentration is 630mg / L, and pH value is about 1.5, is converted into 25 times of stoichiometric number of ammonium vanadium heteropolyacid ammonium by ammonia nitrogen wherein and adds sodium phosphovanadium heteropolyacid (Na 12 PV 13 o 41 ·xH 2 (0), then add alkali to adjust the pH to 2.5~3.5, stir at room temperature for 3.5h, and filter to obtain ammonia nitrogen content after deamination (96.35% ammonia nitrogen removal rate) and ammonium enriched slag (phosphorous vanadium heteropoly ammonium acid filter cake). The resulting ammonium-enriched slag is thermally decomposed to obtain a vanadium-containing reagent. After the deamination, the liquid is first added with iron sulfate according to 5 times the stoichiometric number of the residual vanadium converted into ferric vanadate, and then alkali is added to adjust the pH to 4.2. For V<0.5mg / L vanadium ...
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