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A process for treating ammonia nitrogen wastewater using gaseous membrane

An ammonia nitrogen wastewater, gaseous membrane technology, applied in the direction of degassed water/sewage treatment, water/sewage treatment, water/sewage multi-stage treatment, etc. Shorten the service life and other problems, to avoid the permeation distillation, improve the stripping efficiency, and improve the service life.

Active Publication Date: 2022-01-28
江西铜鼓有色冶金化工有限责任公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0005] However, in the gaseous membrane deamination process, not only ammonia molecules enter the absorption liquid through the membrane wall, but also water molecules enter the absorption liquid through the micropores on the membrane wall (associated osmotic distillation), resulting in rapid expansion of the absorption liquid volume, As a result, the absorption solution is diluted, and the higher the acid and salt concentration in the absorption solution, the more serious the osmotic distillation of water, so it is difficult to obtain the expected by-product, that is, a high-concentration ammonium salt solution
Chinese patent CN106186492A overcomes the accompanying osmotic distillation problem by keeping the temperature difference between the wastewater and the absorption liquid at 10-20°C, increasing the ammonia nitrogen concentration in the wastewater to 1000-10000mg / L, and adding electrolytes to the wastewater, but the temperature difference in this method Difficult to control, both sides quickly reach temperature balance, and high concentration of ammonia nitrogen affects the stability of gaseous membrane modules, resulting in easy pollution and shortened service life, which limits its popularization and application

Method used

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  • A process for treating ammonia nitrogen wastewater using gaseous membrane
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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0048] The type of waste water is condensed concentrated ammonia water with an ammonia nitrogen content of 10000mg / L, and a compound decolorizing agent is added according to the ratio of g / mL to 10:10000. The compound decolorizing agent is composed of calcium hydroxide, sodium hydroxide, activated carbon and fly ash according to the weight It is obtained by mixing 3:2:3:1. Then add the heavy metal scavenger HMC-M1 according to the solid-liquid ratio g / mL of 2:10000, stir at a speed of 200r / min for 40min, and then filter and ultrafilter in sequence. The pH of the pretreated wastewater is 11, and it is sent to the stripping tower. The waste heat and steam in the production are used to heat the air blown by the blower. The hot air is continuously blown into the wastewater, and the ammonia nitrogen in it is stripped into ammonia gas. Through the hydrochloric acid absorption tower, it is converted into ammonium chloride. The concentration of ammonia nitrogen in the waste water aft...

Embodiment 2

[0051] The type of wastewater is cleaning APT wastewater with an ammonia nitrogen content of 5000mg / L. According to the ratio of solid to liquid g / mL of 15:10000, a composite decolorizing agent is added. The composite decolorizing agent is composed of calcium hydroxide, sodium hydroxide, activated carbon and fly ash according to the weight It is obtained by mixing 3:2:3:2. Then add the heavy metal scavenger according to the solid-liquid ratio g / mL of 3:10000, stir at a speed of 300r / min for 35min, and then filter and ultrafilter in sequence. The pH of the pretreated wastewater is 12, and it is sent to the stripping tower. The waste heat and steam in the production are used to heat the air blown by the blower. The hot air is continuously blown into the wastewater, and the ammonia nitrogen in it is stripped into ammonia gas. Through the hydrochloric acid absorption tower, it is converted into ammonium chloride. The concentration of ammonia nitrogen in the stripped wastewater wa...

Embodiment 3

[0054] The type of waste water is condensed concentrated ammonia water with an ammonia nitrogen content of 20000mg / L, and a compound decolorizing agent is added according to the solid-liquid ratio g / mL of 20:10000. The compound decolorizing agent is composed of calcium hydroxide, sodium hydroxide, activated carbon and fly ash according to the weight It is obtained by mixing 4:2:3:1. Then add the heavy metal scavenger according to the solid-liquid ratio g / mL of 2.5:10000, stir at a speed of 500r / min for 30min, and then filter and ultrafilter in sequence. The pH of the pretreated wastewater is 11, and it is sent to the stripping tower. The waste heat and steam in the production are used to heat the air blown by the blower. The hot air is continuously blown into the wastewater, and the ammonia nitrogen in it is stripped into ammonia gas. Through the hydrochloric acid absorption tower, it is converted into ammonium chloride. The concentration of ammonia nitrogen in the stripped w...

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Abstract

The invention relates to a process for treating ammonia-nitrogen wastewater by using a gaseous membrane. The steps include: pre-treating high-concentration ammonia-nitrogen wastewater with a composite decolorizer and a heavy metal scavenger, sending it to a blow-off tower for ammonia-nitrogen removal, and the blown-off ammonia gas enters hydrochloric acid The absorption tower generates ammonium chloride; the waste water after stripping treatment is mixed with low-concentration ammonia nitrogen waste water to obtain waste liquid, and the pH of the waste liquid is adjusted to above 10.5, and then ultrafiltration is performed, and the waste liquid and absorption liquid after ultrafiltration enter In the gaseous membrane module, the flow rate and temperature are controlled to remove ammonia nitrogen, and ammonium salt solution and waste liquid with ammonia nitrogen content lower than 10mg / L are obtained; the ammonium salt solution is sent to the stripping tower after adjusting the pH value, and then passed through the hydrochloric acid absorption tower, Ammonium chloride is obtained. The ammonia nitrogen removal rate of this method exceeds 99%, and the waste liquid after treatment meets the discharge standard. During the process, the gaseous membrane has good stability, does not produce osmotic distillation of water, and the process of the gaseous membrane can be continuously carried out, which is beneficial to industrial implementation.

Description

technical field [0001] The invention belongs to the field of ammonia nitrogen wastewater treatment, and in particular relates to a process for treating ammonia nitrogen wastewater by using a gaseous membrane. Background technique [0002] In recent years, with the rapid development of petrochemical, coal chemical, fine chemical, fertilizer, pharmaceutical, metallurgy, electronics and other industries, the daily discharge of ammonia nitrogen wastewater has been increasing. Ammonia nitrogen in wastewater is an important substance for water eutrophication and environmental pollution, which affects water quality and human health, and also causes a huge waste of resources. Therefore, the country requires ammonia nitrogen-containing wastewater to be removed using ammonia nitrogen removal technology, and can only be discharged after reaching the "Comprehensive Wastewater Discharge Standard". [0003] At present, the most common ammonia nitrogen removal technologies include biologi...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C02F9/04B01D53/78B01D53/58C02F101/16
CPCB01D53/58B01D53/78C02F9/00C02F1/20C02F1/66C02F1/444C02F2101/16Y02A50/20
Inventor 刘恒嵩戴征文唐美春
Owner 江西铜鼓有色冶金化工有限责任公司