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Technology for removing mercury in contaminated acid wastewater

A technology for the removal of polluted acid wastewater, applied in the field of lead and zinc smelting, can solve the problems of inability to treat suspended particulate mercury and colloidal mercury in water, Hg fluctuation of polluted acid wastewater, low Hg compliance rate of wastewater, etc., and achieves simple production control. Easy to operate, improve the cohesion effect, and the effect of high Hg compliance rate

Inactive Publication Date: 2016-09-21
BAIYIN NONFERROUS GROUP
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  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

And with the change of ore source, the mercury in the zinc concentrate fluctuates greatly, resulting in a large fluctuation of Hg in the sewage acid wastewater, which brings great difficulty to the subsequent wastewater treatment
[0003] General treatment methods of polluted acid wastewater: such as figure 2 As shown, the main method for treating mercury in sewage acid wastewater in China is the vulcanization-neutralization precipitation method. The general treatment process is as follows figure 1 As shown, there are problems in the traditional vulcanization-neutralization method: the vulcanization-neutralization precipitation method can only remove ionic mercury in water, but cannot treat suspended particulate mercury and colloidal mercury in water, and the Hg compliance rate of treated wastewater is low and unstable. In particular, it cannot meet the requirement that the Hg standard of the current effluent wastewater has dropped from the original 0.05mg / L to the current 0.03mg / L

Method used

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  • Technology for removing mercury in contaminated acid wastewater
  • Technology for removing mercury in contaminated acid wastewater
  • Technology for removing mercury in contaminated acid wastewater

Examples

Experimental program
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Effect test

Embodiment 1

[0022] (1) The total mercury concentration generated during the sulfuric acid dynamic wave washing process is 20mg / L, and the volume is 33m 3 The dirty acid wastewater is pumped into the reaction tank, and the mass percent concentration is added to be 5%, and the volume is 4.18L metered KMnO 4 React for 15-20 minutes, then add the Baume degree to 3-4, the volume is 8m 3 Lime milk reacted for 10 minutes, adjusted pH value to 3-4, Hg in wastewater 2+ When the ion concentration is 20mg / L, add sodium sulfide with a mass percentage concentration of 5% and a volume of 14.63L, and react for 30-45 minutes.

[0023] (2) Add flocculant polyacrylamide with a mass per thousand concentration of 3‰ and a volume of 1-1.5L to the pulp after mercury removal, and pump the liquid into a plate-and-frame filter after reacting for 5 minutes to obtain filtrate and filter residue. The Hg content in the filtrate is less than 0.03mg / L, and the mercury content in the filter residue is 0.264%, which is...

Embodiment 2

[0025] (1) The total mercury concentration produced during the sulfuric acid dynamic wave washing process is 650mg / L, and the volume is 33m 3 The dirty acid wastewater is pumped into the reaction tank, and the mass percentage concentration is 5%, and the volume is 136L of KMnO 4 React for 15-20 minutes, then add the Baume degree to 3-4, the volume is 8 m 3 Lime milk reacted for 10 minutes, adjusted pH value to 3-4, Hg in wastewater 2+ When the ion concentration is 650mg / L, add sodium sulfide with a concentration of 5% and a volume of 475L, and react for 30-45 minutes.

[0026] (2) Add flocculant polyacrylamide with a mass per thousand concentration of 3‰ and a volume of 1-1.5L to the pulp after mercury removal, and pump the liquid into a plate-and-frame filter after reacting for 5 minutes to obtain filtrate and filter residue. The Hg content in the filtrate is less than 0.03mg / L, and the mercury content in the filter residue is 7.82%, which is comprehensively recovered.

Embodiment 3

[0028] (1) The total mercury concentration produced during the sulfuric acid dynamic wave washing process is 2000mg / L, and the volume is 33m 3 The dirty acid wastewater is pumped into the reaction tank, and the mass percentage concentration is 5%, and the volume is 418L of KMnO 4 React for 15-20 minutes, then add the Baume degree to 3-4, the volume is 8m 3 Lime milk reacted for 10 minutes, adjusted pH value to 3-4, Hg in wastewater 2+ When the ion concentration is 2000mg / L, add sodium sulfide with a mass percentage concentration of 5% and a volume of 1463L, and react for 30-45 minutes.

[0029] (2) Add flocculant polyacrylamide with a mass per thousand concentration of 3‰ and a volume of 1-1.5L to the pulp after mercury removal, and pump the liquid into a plate-and-frame filter after reacting for 5 minutes to obtain filtrate and filter residue. The Hg content in the filtrate is less than 0.03mg / L, and the mercury in the filter residue is 20.33%, which is comprehensively reco...

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Abstract

The invention discloses a technology for removing mercury in contaminated acid wastewater. The method specifically comprises the following steps of pumping contaminated acid wastewater produced in a sulfuric acid dynamic wave scrubbing process into a reaction tank, adding a strong oxidant KMnO4, then adding lime milk for reaction, and then adding sodium sulphide for reaction; adding a flocculating agent, namely polyacrylamide into ore pulp after mercury removal, pumping the liquid into a plate and frame filter after the reaction to obtain filter liquor and filter residues, wherein the content of Hg in the obtained filter liquor is detected to be less than 0.03mg / L, and the content of the mercury in the filter residues is 0.264 to 20.33 percent, and collecting the filter residues. By adopting the technology provided by the invention to treat contaminated acid produced in the sulfuric acid dynamic wave scrubbing process of the lead and zinc smelting industry to remove the Hg, the wastewater discharging reaches the standard, the operation is simple and reliable, and a production field test result shows that the novel technology is feasible technically. By using the technology in production practice for two years, the problem that the Hg in the contaminated acid produced by lead and zinc smelting does not reach the standard is thoroughly solved. By adopting the technology provided by the invention to remove the mercury, the fact that the Hg of discharge water is less than or equal to 0.03mg / L is guaranteed, and a method through which the discharge reaches the standard is realized.

Description

technical field [0001] The invention belongs to the technical field of lead-zinc smelting, relates to the removal of mercury from polluted acid produced in the sulfuric acid dynamic wave washing process, and in particular to a process for removing mercury from polluted acid wastewater. Background technique [0002] The source and characteristics of dirty acid wastewater: dirty acid wastewater comes from sulfuric acid dynamic wave washing in the process of lead-zinc smelting, and has the characteristics of high Hg, high F and high COD. In particular, the Hg concentration is generally 20-2000mg / L, mainly in the form of suspended particulate mercury, ionic mercury, and colloidal mercury, with elemental mercury, monovalent mercury, and divalent mercury in the valence state. And with the change of ore source, the mercury in the zinc concentrate fluctuates greatly, resulting in a large fluctuation of Hg in the sewage acid wastewater, which brings great difficulty to the subsequent...

Claims

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Application Information

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IPC IPC(8): C02F9/04C02F101/20
CPCC02F1/001C02F1/5236C02F1/56C02F1/66C02F1/72C02F9/00C02F2101/20
Inventor 段宏志马菲菲刘向东赵贵俊魏银春师晓军王新文焦晓斌王丽娟张昱琛
Owner BAIYIN NONFERROUS GROUP
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