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Technology for treating waste water containing ammonia nitrogen

An ammonia nitrogen wastewater and a treatment process technology, which is applied in the field of ammonia nitrogen-containing wastewater treatment technology, can solve problems such as inability to timely and accurately determine, ammonia nitrogen concentration exceeding the standard, low reuse value, etc., and achieves reduced monitoring workload, fewer regeneration times, and convenient desorption. Effect

Inactive Publication Date: 2009-12-23
JIANGXI UNIV OF SCI & TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0004] The traditional ion exchange method cannot timely and accurately determine the leakage point of the effluent (when the concentration of ammonia nitrogen in the effluent reaches 15mg / L, the feeding must be stopped, otherwise the discharge cannot meet the standard), resulting in the concentration of ammonia nitrogen in the effluent exceeding the standard and cannot be recycled. , and due to the NH adsorbed by the exchange resin 4 + Too little, resulting in NH in the desorption solution during desorption (regeneration) 4 + If the concentration is too low, the reuse value is not high, and further treatment is required, so the treatment cost is high

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0020] Embodiment 1: ion exchange column Φ 40 * 300mm, built-in 001 * 7 (strongly acidic styrene series cation exchange resin) dry resin 275g, the waste water that ammonia nitrogen concentration is 810mg / L enters from the exchange column top with 50mL / min flow rate, when When the feed reaches 14.1L, it is detected that the pH value of the effluent is 7, that is, the feed is stopped, and the remaining liquid is ejected with deionized water, and the total volume of the effluent is 15.6L, of which the volume of the first part of the effluent is 5.2L. After analysis, the concentration of ammonia nitrogen is 10mg / L (in line with the first-class emission standard of 15mg / L), and the discharge meets the standard. The volume of the latter part of the effluent is 10.2L. After analysis, the concentration of ammonia nitrogen is 87mg / L. This effluent enters another exchange column (the same specification is Φ40×300mm, and contains 275g of 001×7 dry resin) at the same flow rate. 10.2L of th...

Embodiment 2

[0022] Embodiment 2: The ion exchange column is the same as Example 1. Firstly, 0.4L of wastewater with an ammonia nitrogen concentration of 31400mg / L was introduced from the top of the exchange column at 30mL / min, and then deionized water was used to push out the remaining liquid, so that the total volume of the effluent was 0.7L, of which the volume of the first part of the effluent was It is 100mL, and the concentration of ammonia nitrogen after analysis is 12mg / L (in line with the first-class discharge standard of 15mg / L), and the discharge meets the standard. The volume of the latter part of the effluent is 600mL, and the ammonia nitrogen concentration is 105mg / L after analysis. The effluent enters another exchange column at the same flow rate (the same specification is Φ40×300mm, and contains 275g of 001×7 dry resin). After the 600mL solution enters , the effluent (600mL) was analyzed for an ammonia nitrogen concentration of 13mg / L. Continue to quantitatively enter 0.4L...

Embodiment 3

[0024] Embodiment 3: with embodiment 1. The difference is that the two exchange columns are connected in series and fed continuously, that is, the wastewater with an ammonia nitrogen concentration of 810mg / L enters from the top of the first exchange column at a flow rate of 50mL / min, and the effluent directly enters the top of the second exchange column and After being adsorbed by the resin, it flows out from the bottom of the column. When the first exchange column was fed to 15L, the feed was stopped, and deionized water was used to push the remaining liquid into the second exchange column. At this moment, the first exchange column is transferred to the desorption (regeneration) operation, and the second exchange column continues to enter the waste water with an ammonia nitrogen concentration of 810mg / L from the top at a flow rate of 40mL / min. The effluent with a volume of 15L in the front part flowing out from the second exchange column, after analysis, the concentration of...

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Abstract

The invention relates to the technology for treating waste water containing ammonia nitrogen and recovering ammonia in the industries, in particular to a technology for treating waste water containing ammonia nitrogen. In the conventional ion exchange method, the effulent liquid can not be recycled due to the over standard of ammonia and nitrogen of the effulent liquid caused by the untimely and inaccurate judgment of effulent liquid perforation points, the recycling value is low due to the low concentration of NH4 in stripping liquid, the ammonia nitrogen is required to be treated and the treatment cost is higher. The technology for treating waste water containing ammonia nitrogen comprises the following steps: waste water containing ammonia nitrogen is injected into a first exchange column filled with cation exchange resin, the material liquid effuses from the outlet of the first exchange column after being absorbed by the cation exchange resin and then flows into a second exchange column filled with cation exchange resin for further absorption, and the ammonia nitrogen concentration of the effluent liquid from the outlet of the second exchange column is less than 15 mg / L. The technology has low cost, and can comprehensively recover ammonia and continuously discharge by meeting the standards or recycle the waste water.

Description

technical field [0001] The invention relates to the treatment of various types of ammonia-nitrogen-containing wastewater in industry and the comprehensive recovery technology of ammonia, in particular to a treatment process of ammonia-nitrogen-containing wastewater in the wet smelting of tungsten and rare earth. Background technique [0002] At present, there is a large amount of ammonia emissions in the fields of industry and agriculture, especially the wet smelting of tungsten and rare earths uses a large amount of reagents containing ammonia and nitrogen, which makes the amount and concentration of ammonia nitrogen-containing wastewater in the process large, and most of the wastewater cannot be returned. Recycling, and only after high-cost treatment can the emission meet the standard. [0003] Nitrogen is a nutrient in water bodies. When the amount of ammonia nitrogen in the water body is excessive, it will cause eutrophication of the water body, causing aquatic plants s...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C02F9/02B01J20/34C01C1/16C01C1/02C02F1/04C02F9/10C02F1/42C02F1/66
Inventor 郭永忠罗仙平严群李健昌封丹黄俊文赖华
Owner JIANGXI UNIV OF SCI & TECH
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