Treatment method of arsenium-containing polluted acid wastewater generated by smelting flue gas

A technology of polluted acid wastewater and smelting flue gas, applied in water/sewage multi-stage treatment, water/sludge/sewage treatment, chemical instruments and methods, etc., can solve the problems of high investment, complicated process and waste of resources, etc. The effect of good treatment effect, simple operation and low consumption

Active Publication Date: 2015-12-16
JIANGXI UNIV OF SCI & TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0004] Lime-iron salt method and sulfidation method are mostly used in smelters to treat arsenic-containing wastewater. The amount of raw materials and slag in the lime-iron salt method is very large, which makes material transportation difficult; the limestone pretreatment equipment is huge, occupies a large area, and the investment is high. Poor; complex process, huge equipment, high cost of neutralization and anti-neutralization, large consumption of flocculants; valuable metals in slag are depleted and cannot be recovered, resulting in waste of resources; the main component of neutralized slag after dehydration is gypsum And iron arsenic salt, containing other heavy metal basic salts (Cu(OH)2, Zn(OH)2, etc.), at the current stage, it is difficult to recover the useful metals in it, and the production cost is high. In order not to cause secondary pollution, it must Properly dispose of the neutralized slag, which is usually landfilled in a permanent slag site (according to national regulations, the slag is a hazardous waste); the effluent water quality is not easy to control to meet the standard, the floc settlement

Method used

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  • Treatment method of arsenium-containing polluted acid wastewater generated by smelting flue gas
  • Treatment method of arsenium-containing polluted acid wastewater generated by smelting flue gas
  • Treatment method of arsenium-containing polluted acid wastewater generated by smelting flue gas

Examples

Experimental program
Comparison scheme
Effect test

Example Embodiment

[0015] Example 1: The composition of the acid sample liquid from a smelter is shown in Table 1:

[0016] Table 1 Water sample composition

[0017]

[0018] Take 1L of this dirty acid for pretreatment to remove sulfate, add 144.2g of anhydrous calcium chloride, stir at 600r / min, and react for 20min. While continuing to stir, add flocculant PAM2.5mg, and stir at medium speed of 120r / min for 4.5 min, stirring at a slow speed of 30r / min for 10min, standing for 20min, and then performing solid-liquid separation; the filter residue is mainly calcium sulfate with an arsenic content of less than 0.1%, which is not a hazardous waste, and the sulfate removal rate is 65.50%; the filtrate enters pre-neutralization , Slowly add lime to neutralize to pH=0.5, stir at 600r / min, and react for 10min. While continuing to stir, add flocculant PAM1.5mg, medium speed 120r / min for 4.5min, slow speed 30r / min for 10min, Let stand for 20 minutes, the filter residue is mainly calcium sulfate, the content of...

Example Embodiment

[0019] Example 2: The composition of the acid sample liquid from a smelter is shown in Table 2:

[0020] Table 2 Water sample composition

[0021]

[0022] Take 1L of this dirty acid for pretreatment to remove sulfate, add the filtrate after three neutralization and removal of arsenic in Example 1, stirring at 600r / min, for 40min to react, while continuing to stir, add 0.6mg of flocculant PAM, medium speed 120r Stirring for 4.5min at 30r / min, stirring at a slow speed of 30r / min for 10min, standing for 20min, and then performing solid-liquid separation; the filter residue is mainly calcium sulfate with an arsenic content of less than 0.1%, which is not a hazardous waste, and the sulfate removal rate is 66.31%; filtrate Enter pre-neutralization, slowly add lime to neutralize to pH=1, stirring speed 600r / min, time 10min for reaction, while continuing to stir, add flocculant PAM2.0mg, medium speed 120r / min stirring 4.5min, slow speed 30r / Min stirring for 10 minutes, standing for 20 m...

Example Embodiment

[0023] Example 3: The composition of the acid sample liquid from a smelter is shown in Table 3:

[0024] Table 3 Water sample composition

[0025]

[0026] Take 1L of this dirty acid for pretreatment to remove sulfate, add 201.9g of anhydrous calcium chloride, stir at 600r / min, and react for 60min. While continuing to stir, add flocculant PAM1.5mg, and stir at a medium speed of 120r / min for 4.5 min, stirring at a slow speed of 30r / min for 10 min, standing for 20 min, and then performing solid-liquid separation; the filter residue is mainly calcium sulfate with an arsenic content of less than 0.1%, which is not a hazardous waste, and the sulfate removal rate is 78.23%; the filtrate enters the pre-neutralization , Slowly add lime to neutralize to pH=1, the stirring speed is 600r / min, the reaction time is 30min, while continuing to stir, add the flocculant PAM 0.6mg, the medium speed 120r / min stirs for 4.5min, the slow speed 30r / min stirs for 10min, Let stand for 20 minutes, the filt...

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Abstract

The invention relates to a treatment method of arsenium-containing polluted acid wastewater generated by smelting flue gas, which comprises the following steps: pretreatment for sulfate removal; preneutralization; primary neutralization; secondary neutralization; tertiary neutralization; and circulating treatment. The pretreatment for sulfate removal, preneutralization and primary neutralization are sequentially operated to remove the sulfates and fluorine in the system in the precipitation form, wherein the removal rate is up to 95% or above, and the precipitate arsenium content is less than 0.1%. The secondary neutralization can enable more than 85% of the Cu, Fe, Pb, Zn and other metals to form a hydroxide precipitate, so that the high-content metals can be recycled. The tertiary neutralization can enable more than 95% of As to be enriched in the filter residue in the forms of calcium arsenate and calcium arsenite and to be recycled. The method can not generate unmanageable neutralization slag to form secondary pollution, and uses fewer reagents in the whole process; the calcium chloride only needs to be purchased at the time of starting; the operating process can be satisfied by circulation; and the method only consumes small amounts of lime and flocculant, is simple to operate, and has the advantages of low cost and favorable treatment effect.

Description

technical field [0001] The invention belongs to the technical field of wastewater treatment, and in particular relates to a method for treating arsenic-containing polluted acid wastewater produced by smelting flue gas. Background technique [0002] On October 1, 2007, the State Environmental Protection Administration and the State Administration of Quality Supervision, Inspection and Quarantine jointly promulgated the "Identification of Hazardous Waste Identification Standards for Toxic Substance Content" (GB5085.6-2007). According to relevant laws and regulations, this standard has the effect of mandatory execution. The standard clearly stipulates that when the total mass fraction of one or more highly toxic substances or carcinogens in solid waste is greater than or equal to 0.1%, the solid waste is classified as hazardous waste and must be managed as hazardous waste according to law. [0003] The acid wastewater produced by washing copper smelting flue gas contains a lar...

Claims

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Application Information

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IPC IPC(8): C02F9/10C02F101/20
Inventor 吴速英张大超肖隆文陈云嫩代振鹏朱清江
Owner JIANGXI UNIV OF SCI & TECH
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