A method for treating arsenic-containing polluted acid wastewater produced by smelting flue gas

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

Active Publication Date: 2017-07-11
JIANGXI UNIV OF SCI & TECH
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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 performance is poor, the clear liquid is easy to return to muddy, and the effluent is high-content Salt water cannot be reused; the treatment cost is high, and the treatment cost per ton of water is about 90 yuan
The vulcanization method is an effective method to recover and treat arsenic-containing wastewater, but the equipment is huge and occupies a large area; the pH value is adjusted repeatedly, the consumption of chemicals is large, and the treatment cost is high; there are many control indicators and difficult to operate and adjust; in order to ensure the heavy metal The removal rate often needs to add excessive sulfide. Excessive sulfide will generate hydrogen sulfide gas under acidic conditions, which is easy to cause secondary pollution. Hydrogen sulfide gas is highly toxic and easy to cause personal injury to field operators; the generated The heavy metal sulfides are very fine and difficult to separate from the liquid phase; the sludge particles are fine and difficult to dewater; the treated slag and water cannot be recycled and completely discarded, resulting in waste of resources; the treatment cost is high

Method used

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  • A method for treating arsenic-containing polluted acid wastewater produced by smelting flue gas
  • A method for treating arsenic-containing polluted acid wastewater produced by smelting flue gas
  • A method for treating arsenic-containing polluted acid wastewater produced by smelting flue gas

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0015] Embodiment 1: The composition of a certain smeltery sewage acid sample liquid is shown in Table 1:

[0016] Table 1 Water sample components

[0017]

[0018] Take 1L of this polluted acid for pretreatment to remove sulfate radicals, add 144.2g of anhydrous calcium chloride, stir at a speed of 600r / min, and react for 20min, while continuing to stir, add flocculant PAM2. 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, the arsenic content is less than 0.1%, which is not hazardous waste, and the removal rate of sulfate radical is 65.50%; the filtrate enters the pre-neutralization , slowly add lime to neutralize to pH = 0.5, stir at a speed of 600r / min, and react for 10min. While continuing to stir, add flocculant PAM1.5mg, stir at a medium speed of 120r / min for 4.5min, and stir at a slow speed of 30r / min for 10min. Stand still for 20 minutes, the filter res...

Embodiment 2

[0019] Embodiment 2: The composition of a certain smelter's sewage acid sample liquid is shown in Table 2:

[0020] Table 2 Water sample components

[0021]

[0022]Take 1L of this polluted acid for pretreatment to remove sulfate radicals, add the filtrate after neutralizing and removing arsenic for three times in Example 1, stir at a speed of 600r / min, and react for 40min, while continuing to stir, add 0.6mg of flocculant PAM at a medium speed of 120r / min stirring for 4.5min, slow speed 30r / min stirring for 10min, standing for 20min, and then solid-liquid separation; filter residue is mainly calcium sulfate, arsenic content is less than 0.1%, does not belong to hazardous waste, sulfate removal rate is 66.31%; filtrate Enter pre-neutralization, slowly add lime to neutralize to pH = 1, stirring speed 600r / min, time 10min to react, continue stirring while adding flocculant PAM2.0mg, medium speed 120r / min stirring 4.5min, slow speed 30r / min Stir for 10 minutes, let it stand ...

Embodiment 3

[0023] Embodiment 3: The composition of a certain smelter's sewage acid sample liquid is shown in Table 3:

[0024] Table 3 Water sample composition

[0025]

[0026] Take 1L of this polluted acid for pretreatment to remove sulfate radicals, add 201.9g of anhydrous calcium chloride, stir at a speed of 600r / min, and react for 60min, while continuing to stir, add flocculant PAM1. 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, the arsenic content is less than 0.1%, which is not hazardous waste, and the removal rate of sulfate radical is 78.23%; the filtrate enters the pre-neutralization , Slowly add lime to neutralize to pH = 1, stir at a speed of 600r / min, and react for 30min. While continuing to stir, add flocculant PAM0.6mg, stir at a medium speed of 120r / min for 4.5min, and stir at a slow speed of 30r / min for 10min. Stand still for 20 minutes, the filter res...

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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" (GB 5085.6-2007). 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 la...

Claims

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Application Information

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Patent Type & Authority Patents(China)
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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