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Method for treating ammonia nitrogen in wastewater by using integrated process

A waste water treatment and combined process technology, applied in chemical instruments and methods, multi-stage water/sewage treatment, neutralized water/sewage treatment, etc., can solve the problems of unstable ammonia nitrogen in the effluent, unable to meet the discharge standards, etc., and achieve zero sewage The effect of emissions

Inactive Publication Date: 2013-03-13
CECEP L&T ENVIRONMENTAL TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0005] The present invention proposes a method for treating ammonia nitrogen in waste water using a combination process, the purpose of which is to use a combination process of chemical precipitation method + membrane treatment to overcome the shortcomings of the chemical treatment method that the ammonia nitrogen in the effluent is unstable and cannot be discharged up to the standard, and at the same time the membrane The advantages of treating low-concentration ammonia-nitrogen-containing wastewater, constant effluent quality, and high treatment efficiency are combined to reflect the advantages of the two processes and overcome the shortcomings of the two processes at the same time. It can achieve the standard discharge of ammonia nitrogen and heavy metals in the wastewater and meet GB8978- 96 "Integrated Sewage Discharge Standard" Class I Discharge Standard

Method used

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  • Method for treating ammonia nitrogen in wastewater by using integrated process

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Experimental program
Comparison scheme
Effect test

Embodiment 1

[0030] Embodiment 1: select the form of one-stage nanofiltration+one-stage reverse osmosis, reverse osmosis concentrated water is returned to sump, magnesium salt is selected magnesium sulfate for use, and phosphate is selected disodium hydrogen phosphate for use, n(N):n(P): n(Mg)=1:1.1:1.3, pH=9.5, nanofiltration clean water production rate=85%, operating pressure 1.4MPa, reverse osmosis clean water production rate=85%, operating pressure 1.6MPa;

[0031] Waste water quality: 2m 3 / h, pH=6.4, Mn 2+ Concentration 341mg / L, NH 4 + The concentration is 1080mg / L. The residence time in the stirring tank is 30min, and the residence time in the sedimentation tank is 6h. Under the above conditions, the effluent NH 4 + Concentration 9mg / L, Mn 2+ The concentration is 0.5mg / L.

Embodiment 2

[0032]Embodiment 2: select the form of one-stage nanofiltration+one-stage reverse osmosis, reverse osmosis concentrated water is returned to sump, magnesium salt selects magnesium sulfate for use, phosphate selects disodium hydrogen phosphate for use, n(N):n(P): n(Mg)=1:1.1:1.4, pH=9.5, nanofiltration clean water production rate=75%, operating pressure 1.2MPa, reverse osmosis clean water production rate=80%, operating pressure 1.4MPa;

[0033] Waste water quality: 2m 3 / h, pH=6.4, Mn 2+ Concentration 341mg / L, NH 4 + The concentration is 1080mg / L. The residence time in the stirring tank is 30min, and the residence time in the sedimentation tank is 6h. Under the above conditions, the effluent NH 4 + Concentration 6mg / L, Mn 2+ The concentration is 0.2mg / L.

Embodiment 3

[0034] Embodiment 3: Select the form of two-stage nanofiltration series connection + one-stage reverse osmosis, reverse osmosis concentrated water is returned to the sump, magnesium salt is selected magnesium chloride, and phosphate is selected disodium hydrogen phosphate, n(N):n(P): n(Mg)=1:1.1:1.3, pH=9.5, nanofiltration clean water production rate=85%, operating pressure 1.4MPa, reverse osmosis clean water production rate=90%, operating pressure 1.8MPa;

[0035] Waste water quality: 5m 3 / h, pH=6.4, Mn 2+ Concentration 341mg / L, NH 4 + The concentration is 1080mg / L. The residence time in the stirring tank is 30min, and the residence time in the sedimentation tank is 6h. Under the above conditions, the effluent NH 4 + Concentration 10mg / L, Mn 2+ The concentration is 0.3mg / L.

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Abstract

The invention relates to a method for treating ammonia nitrogen in wastewater by using an integrated process, and the method comprises a magnesium ammonium phosphate chemical precipitation process and a membrane treatment process and comprises the processing steps of collecting water, dosing, adjusting the pH (potential of Hydrogen) value, reacting, precipitating and filtering. The method has the technical characteristics that magnesium salt and phosphate are added during the dosing; a NaOH solution is added to regulate the pH to 8.5-10 during the adjustment; during the reaction, the wastewater retention time is greater than or equal to 30 minutes, the ammonia ion in the wastewater is fully reacted to generate magnesium ammonium phosphate precipitates and heavy metal ion is converted into hydroxide precipitates; the precipitation time is greater than or equal to 6 hours to realize solid-liquid separation during the precipitation; and the supernatant liquid enters a membrane treatment system, the reverse osmosis clear water can be directly discharged and the concentrated water returns to a water collecting tank or is subjected to nanofiltration. The method has the advantages that ammonia nitrogen-containing wastewater with various concentrations can be treated; heating is not needed in the treatment process; the ammonia nitrogen content in the effluent can meet the national first grade effluent standard; and the content of other pollutants such as heavy metals and the like in the effluent can be used for achieving the effluent standard. The method is suitable for treating low-biodegradability ammonia nitrogen-containing wastewater and the ammonia nitrogen-containing wastewater of factories without heat resources.

Description

technical field [0001] The invention belongs to the technical field of wastewater treatment, and in particular relates to a method for treating ammonia nitrogen in wastewater by using a combination process. Background technique [0002] With the increasing population and the rapid development of industry and agriculture, water pollution accidents occur frequently, posing serious harm to people and the environment. Many lakes and rivers cause water eutrophication due to excessive discharge of nitrogen and phosphorus, which seriously threatens human production, life and ecological balance. Ammonia nitrogen is one of the main factors causing water eutrophication. At present, incidents of heavy metal pollution in water occur frequently, which have a great impact on human health and safety. How to control ammonia nitrogen and heavy metal wastewater has become one of the main tasks in the field of water treatment, especially for the treatment of wastewater from mineral processing...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C02F9/04C02F1/66C02F1/44C02F1/52
Inventor 张翔宇余红辉朱彤李萌宋宝华杨剑魏刚姚一夫
Owner CECEP L&T ENVIRONMENTAL TECH
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