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Technology for efficiently removing ammonia nitrogen from phosphorus-fluorine sewage containing ammonia nitrogen

An ammonia nitrogen and sewage technology, which is applied in the treatment field of phosphorus-containing fluorine ammonia nitrogen sewage, can solve the problems of limited wide application, the effect of removing ammonia nitrogen cannot meet the discharge standard, and the ammonia nitrogen cannot be removed in place, etc., and achieves the effect of widespread promotion value.

Inactive Publication Date: 2019-11-26
WENGFU (GRP) CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Existing literature shows that in order to maximize the removal rate of ammonia nitrogen, it is necessary to maintain the ratio n(NH 4 + ): n(Mg 2+ ): n(PO 4 3+ )=1:1.4:1, when the initial concentration is 200ppm, the effluent concentration is 18-30ppm, and the removal rate is about 88%. It is impossible to remove the ammonia nitrogen in place at one time, and a deep ammonia nitrogen removal process is required to remove the ammonia nitrogen in the water to the discharge standard within
The existing literatures all use one-time reaction to remove ammonia nitrogen, which makes the effect of removing ammonia nitrogen not meet the emission standards, which limits the wide application of this process

Method used

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  • Technology for efficiently removing ammonia nitrogen from phosphorus-fluorine sewage containing ammonia nitrogen
  • Technology for efficiently removing ammonia nitrogen from phosphorus-fluorine sewage containing ammonia nitrogen

Examples

Experimental program
Comparison scheme
Effect test

example 1

[0024] Measure 800ml of waste water containing phosphorus and ammonia nitrogen in a 1000mlA beaker, and analyze [NH 3 -N]348ppm, pH3.5, [P 5+ ]1100ppm, [F - ] 298ppm, add the pre-configured milk of lime into the beaker, adjust the pH to 6.8 while stirring, and react for 30 minutes, add a small amount of PAM solution (1‰) into the beaker, and wait for the slurry to settle for 10 minutes.

[0025] Pour the supernatant into a 1000ml B beaker with a volume of about 720ml, and analyze the supernatant [NH 3 -N]320ppm, pH6.5, [P 5+ ]720ppm, [F - ] 20ppm. Weigh 0.9 grams of industrial-grade MgO (MgO ≥ 85%), add 5.0 grams of water to adjust it to a solution state, pour it into the reaction slurry in the B beaker, and react for 1.5 hours under stirring.

[0026] After 1.5 hours, the pH value of the reaction slurry rose to 8.6, and a small amount of PAM solution (1‰) was added to the beaker. After the slurry settled for 10 minutes, the clear liquid was transferred to a 1000ml C beak...

example 2

[0030] Measure 800ml of waste water containing phosphorus and ammonia nitrogen in a 1000mlA beaker, and analyze [NH 3 -N]316ppm, pH3.1, [P 5+ ]1260ppm, [F - ]314ppm, add the pre-configured milk of lime into the beaker, adjust the pH to 6.2 while stirring, and react for 30 minutes, add a small amount of PAM solution (1‰) into the beaker, let the slurry settle for 10 minutes.

[0031] Pour the supernatant into a 1000ml B beaker, about 740ml in volume, and analyze the supernatant [NH 3 -N]289ppm, pH6.4, [P 5+ ]670ppm, [F - ] 32ppm. Weigh 0.9 grams of industrial grade MgO (MgO ≥ 85%), add 5.0 grams of water to adjust it to a solution state, pour it into the reaction slurry in the B beaker, and react for 1.5 hours under stirring.

[0032] After 1.5 hours, the pH value of the reaction slurry rose to 8.2, and a small amount of PAM solution (1‰) was added to the beaker. After the slurry settled for 10 minutes, the clear liquid was transferred to a 1000ml C beaker, and the clear l...

example 3

[0036] Measure 800ml of waste water containing phosphorus and ammonia nitrogen in a 1000mlA beaker, and analyze [NH 3 -N]350ppm, pH2.8, [P 5+ ]1354ppm, [F - ]426ppm, add the pre-configured milk of lime to the beaker, adjust the pH to 6.1 under stirring, and react for 30 minutes, add a small amount of PAM solution (1‰) to the beaker, and let the slurry settle for 10 minutes.

[0037] Pour the supernatant into a 1000ml B beaker with a volume of about 690ml, and analyze the supernatant [NH3 -N]326ppm, pH6.1, [P 5+ ]683ppm, [F - ] 29ppm. Weigh 0.9 grams of industrial grade MgO (MgO ≥ 85%), add 5.0 grams of water to adjust it to a solution state, pour it into the reaction slurry in the B beaker, and react for 1.5 hours under stirring.

[0038] After 1.5 hours, the pH value of the reaction slurry rose to 7.9. Add a small amount of lime milk to the beaker under stirring to raise the pH to 8.6. React for 30 minutes. Add a small amount of PAM solution (1‰) and wait for the slurry t...

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Abstract

The invention discloses a technology for efficiently removing ammonia nitrogen from phosphorus-fluorine sewage containing ammonia nitrogen. The technology can be combined with a traditional process for removing phosphorus and fluorine by using lime milk to efficiently and cheaply remove ammonia nitrogen in sewage and remove phosphorus and fluorine in water. The technology is obtained by optimizingand innovating a traditional chemical precipitation technology. The technology makes the ammonia nitrogen removal rate reach 97% or above and the content of ammonia nitrogen of effluent water controlled within 10 ppm when the ammonia nitrogen content of raw water is within 350 ppm, the effluent water meets the related requirements of Discharge Standard of Water Pollutants for Phosphate FertilizerIndustry (GB15580-2011), and the treatment cost can be controlled within 2 yuan / ton and is far lower than that of the traditional process. The P2O5 content in slag produced by the new technology is high, and the slag can be recycled as a composite fertilizer. The technology adopting a two-stage ammonia nitrogen removal process has the characteristics of low investment, low operation cost, simplicity in operation, and stability in operation, and is universally suitable for treating phosphorus-containing ammonia nitrogen wastewater in the phosphate fertilizer industry.

Description

technical field [0001] The invention relates to phosphate fertilizers, in particular to a treatment technology for phosphorus-containing, fluorine, ammonium and nitrogen sewage. Background technique [0002] Because the phosphate fertilizer industry generally involves ammonium phosphate and anhydrous hydrogen fluoride products, the phosphorus and fluoride wastewater in the phosphate fertilizer industry contains a relatively high concentration of ammonia nitrogen. Taking Wengfu Chemical Company as an example, the ammonia nitrogen content in the acidic phosphorus and fluorine wastewater reaches about 350ppm. The surrounding phosphorus and fluorine industry The ammonia nitrogen content in the wastewater was high. [0003] At present, the methods for removing ammonia nitrogen in phosphate wastewater include stripping method, membrane separation method, break point chlorination method, ion exchange method and chemical precipitation method. [0004] The stripping method is to adj...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C02F9/04C02F101/16
CPCC02F9/00C02F1/66C02F2001/007C02F1/5254C02F1/56C02F2101/16C02F2301/08
Inventor 杨尚松田仁道李永书
Owner WENGFU (GRP) CO LTD