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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

Active Publication Date: 2018-12-07
CENT SOUTH UNIV +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, this method needs to add a large amount of phosphate and magnesium salt reagents, and also needs to add alkali to adjust the pH, the cost is high, and the regeneration method of the generated MAP is relatively harsh, which is not suitable for industrial applications.
[0009] In addition, it is well known that adding ammonia (ammonium) to vanadium-containing solution can form ammonium vanadate salt precipitation (ammonium vanadate, ammonium metavanadate and ammonium polyvanadate), but for a long time people have added ammonia (ammonium) to precipitate vanadium , and no one will add vanadium to precipitate ammonia (ammonium). This is because the ammonium vanadate salt has a certain solubility in water at room temperature, and the residual vanadium and ammonia nitrogen in the solution cannot directly meet the waste water discharge standard, and the chemical The products are relatively expensive, and simply adding vanadium to precipitate ammonia (ammonium) to treat ammonia nitrogen wastewater is technically unfeasible and economically uneconomical

Method used

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Examples

Experimental program
Comparison scheme
Effect test

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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PUM

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Abstract

The invention relates to a method of separating and recovering ammonia from ammonia nitrogen wastewater. The method comprises the following steps of: adding an excess vanadium-containing reagent to ammonia nitrogen wastewater; forcing ammonia nitrogen in the ammonia-nitrogen wastewater to be precipitated out in the form of ammonium salt by skillfully utilizing the common-ion effect generated by the vanadium-containing reagent, wherein the concentration of the ammonia nitrogen can be reduced to be less than or equal to 50mg / L; filtering to obtain ammonium enriched slag and a deaminated solution, and then adding a calcium-containing reagent or an iron-containing reagent to the deaminated solution so as to separate and recover the vanadium-containing reagent remaining therein, thereby causingV in the deaminated liquid to be less than or equal to 1mg / L; further decomposing the obtained ammonium enriched slag to obtain a product containing the vanadium reagent and ammonia (ammonium), thereby realizing the cyclic utilization of the vanadium-containing reagent in the ammonia-nitrogen wastewater treatment process and the resource treatment of ammonia-nitrogen wastewater to avoid the secondary pollution. The method has the advantages of simple process, simple operation, cleanness, environmental protection, economy, high efficiency and the like, and is suitable for industrial application of resource treatment of ammonia nitrogen wastewater.

Description

technical field [0001] The invention belongs to the fields of chemical industry and environmental protection, and in particular relates to a method for separating and recovering ammonia from ammonia nitrogen wastewater. Background technique [0002] Ammonia nitrogen is free ammonia (NH 3 ) and ammonium ions (NH 4 + ) in the form of nitrogen present in water. There are many sources of ammonia nitrogen in water. In addition to domestic sewage and landfill leachate, it also comes from the discharge of industrial wastewater such as iron and steel, oil refining, chemical fertilizers, leather tanning, petrochemicals, glass manufacturing, and feed production. Excessive ammonia nitrogen in the water body will lead to the proliferation of aquatic plants, blue-green algae and other organisms, destroying the ecological balance, causing a series of environmental problems, and seriously endangering ecological security. Under aerobic conditions, nitrosifying bacteria and nitrifying ba...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C02F9/04C02F11/10C01C1/02C02F101/16
CPCC01C1/026C02F1/5236C02F1/66C02F11/10C02F2101/16C02F2301/08Y02W10/40
Inventor 王学文王懿葛奇杜艳苹王明玉
Owner CENT SOUTH UNIV
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