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Novel process for reclaiming waste water containing CN- and NH3 or NH4-

A waste water and acid waste water technology, which is applied in the new process field of resource recycling containing CN- and NH3 or NH4+ waste water, can solve the problems of no export value, cannot be reused, and high processing cost, and achieves low equipment investment and operating costs, absorption and absorption. The effect of improved recycling efficiency and process economy

Active Publication Date: 2008-10-01
BEIJING ZIGUANG YINGLI CHEM TECH CO LTD +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Its disadvantages are: when the cyanide concentration is high, the consumption of chemical reagents is large, and the operating cost is high
The disadvantage is: H 2 o 2 More expensive, higher processing costs
The ion exchange method has low investment, simple process and convenient operation. However, the regeneration of the resin is difficult. If the ammonia is blown off and regenerated, it will be released into the atmosphere and cause secondary pollution. If the ammonia blown out is absorbed by water, the dilute ammonia water obtained It cannot be reused and has no export value
[0008] In summary, for the CN - and NH 3 or NH 4 + For wastewater, the existing single treatment technology has various deficiencies in the separate treatment, or it can only deal with the CN in the wastewater. - or NH 3 / NH 4 + , or the consumption of chemical reagents is large, and the energy consumption is high

Method used

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  • Novel process for reclaiming waste water containing CN- and NH3 or NH4-

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0023] According to the flow process shown in Figure 1, the high-salt cyanuric chloride-containing ammonium-containing sodium formate wastewater (containing CN - : 800mg / L, NH 4 + -N: 1200mg / L, NaCl: 200000mg / L, HCOONa: 1200mg / L, pH: 8.0) sent to the decyanation tower, added hydrochloric acid to adjust the pH value to 2.0, and the gas-liquid ratio was 250:1 (m 3 / m 3 ) air is blown off, and the air entrained with HCN after the blow off returns to the decyanation tower after the sodium hydroxide solution absorbs HCN. After stripping, the concentration of cyanide in the wastewater dropped from 800mg / L at the beginning to 20mg / L, and the stripping rate was 97.5%. The total amount of cyanide in the absorption tower was 7640mg, and the absorption rate was 97.4%.

[0024] The waste water that comes out from the decyanation tower adds sodium hydroxide to adjust the pH value to 11.5, and sends it into the deamination tower with a gas-liquid ratio of 900:1 (m 3 / m 3 ) air to blow ...

Embodiment 2

[0027] According to the flow process shown in Figure 1, the high-salt cyanuric chloride-containing ammonium-containing sodium formate wastewater (containing CN - : 800mg / L, NH 4 - -N: 1200mg / L, NaCl: 200000mg / L, HCOONa: 1200mg / L, pH: 8.0) sent to the decyanation tower, added hydrochloric acid to adjust the pH value to 6.0, and the gas-liquid ratio was 250:1 (m 3 / m 3 ) air is blown off, and the air entrained with HCN after the blow off returns to the decyanation tower after the sodium hydroxide solution absorbs HCN. After stripping, the concentration of cyanide in the wastewater dropped from 800mg / L at the beginning to 40mg / L, and the stripping rate was 95%. The total amount of cyanide in the absorption tower was 7334mg, and the absorption rate was 96.5%.

[0028] Add sodium hydroxide to the wastewater from the decyanation tower to adjust the pH value to 10.5, and send it to the deamination tower with a gas-liquid ratio of 900:1 (m 3 / m 3 ) air to blow off, the entrained ...

Embodiment 3

[0031] According to the process shown in Figure 1, CN will be included - : 800mg / L, CaCl 2 : 20000mg / L, NH 4 Cl: 8000mg / L, pH: 3.0 waste water is sent to the decyanation tower, and the gas-liquid ratio is 200:1 (m 3 / m 3 ) air is blown off, and the air entrained with HCN after the blow off returns to the decyanation tower after the potassium hydroxide solution absorbs HCN. After stripping, the concentration of cyanide in the wastewater dropped from 800mg / L at the beginning to 10mg / L, and the stripping rate was 98.8%. The total amount of cyanide in the absorption tower was 7750mg, and the absorption rate was 98.1%.

[0032] The waste water that comes out from the decyanation tower adds calcium hydroxide to adjust the pH value to 11.5, and sends it into the deamination tower with a gas-liquid ratio of 1000:1 (m 3 / m 3 ) air to blow off, the entrained NH after blow off 3 The air absorbs NH by acetic acid 3 Then return to the deamination tower. After stripping, the concent...

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Abstract

The invention relates to a method for separating HCN and NH3 for reclamation or realizing standardized discharge from wastewater solution that contains CN<-> and NH3 or NH4<+>, particularly relates to a new technique of resource cyclic utilization of high-salt cyanide and ammonium bearing wastewater, which is represented by cyanuric chloride industry, thus opening a new way of resource cyclic utilization of the high-salt cyanide and ammonium bearing wastewater, which is represented by cyanuric chloride, and providing a totally new clean production technology with simple technique, investment-saving and low operation fee and resource cyclic used feature of the integrated utilization of wastewater that contains the CN<-> and NH3 or NH4<+>.

Description

technical field [0001] The present invention relates to a kind of from containing CN - and NH 3 or NH 4 + Separation and recovery of HCN and NH from wastewater solution 3 The method of post-reuse or up-to-standard discharge, especially involving high-salt CN - and NH 3 or NH 4 + A new technology for resource recycling of waste water. Background technique [0002] After nearly 20 years of development, China's cyanuric chloride industry has begun to take shape, and has formed a production capacity of 60,000-80,000 tons per year. However, because the traditional sodium cyanide method is used for production, there are problems such as long process flow, high material consumption, and a large amount of high-concentration sodium chloride wastewater containing impurities such as ammonium, cyanide, and sodium formate. Due to the high concentration of sodium chloride, it is difficult to treat the wastewater by biodegradation process, and it is also difficult to remove the am...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C02F9/04C02F1/74C01C3/02C01C1/02
Inventor 尹应武冯天瀚谢增勇朱宇同李瑞
Owner BEIJING ZIGUANG YINGLI CHEM TECH CO LTD
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