Stepped deep purification method of low-concentration arsenic waste water

A step-depth, low-concentration technology, applied in chemical instruments and methods, water pollutants, water/sewage treatment, etc., can solve the problem that the treatment indicators are easily affected by the external environment, do not meet the national environmental protection standards, and the calcium arsenate slag is stable In order to achieve clean production, improve the efficiency of solid-liquid separation, and reduce the amount of slag

Active Publication Date: 2019-12-20
ZIJIN MINING GROUP
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Problems solved by technology

At present, there are three main treatment methods for low-concentration arsenic-containing wastewater in various countries: iron salt method, adsorption method, and membrane separation. The iron salt method has the characteristics of simple treatment process and good treatment effect, but due to the low concentration of arsenic in water and few other impurities , so there are problems such as large consumption of chemicals, difficulty in solid-liquid separation, and poor stability of treatment indicators easily affected by the external environment; the adsorption method mainly uses resins, activated carbon, and biomass substrates loaded with iron salts (mainly iron hydroxide) As an adsorbent, it removes arsenic from the aqueous solution through the chelation or adsorption of iron ions, and achieves the purpose of deep purification. The post-resin regeneration conditions are harsh, the regeneration efficiency is low, and the service life of the resin is far lower than expected. Membrane separation has the characteristics of good separation effect and simple operation, but there are also problems that need to be solved, such as long pretreatment process and easy loss of membrane components. question
[0004] In order to solve the above problems, Chinese patent CN 201210260206.9 discloses "a method for purifying wastewater containing heavy metals and arsenic", which treats wastewater containing heavy metals and arsenic by adding sulfuric acid or soluble sulfate to the wastewater to supplement sulfate Then add reducing agent to reduce high-priced manganese, chromium, vanadium, etc. in wastewater, then add calcium carbonate to pre-adjust the pH value of the solution, and finally add lime to neutralize, so that harmful elements such as heavy metals and arsenic in wastewater can be precipitated and wrapped in In gypsum slag, but due to the poor stability of the calcium arsenate slag produced by it, it does not meet the national environmental protection standards; Chinese patent CN 207973618U discloses "a non-ferrous smelting flue gas purification dilute acid arsenic removal device", its processing object is non-ferrous smelting Flue gas, the reaction mechanism is to use sodium sulfide or hydrogen sulfide to react with arsenic in dilute acid to produce arsenic filter cake, and this device is mainly used to improve the reaction efficiency and strictly control the arsenic content of the solution after the sulfidation reaction to 30mg / L Below, it is obvious that the discharge is seriously exceeding the standard; Chinese patent CN201810956090.X discloses "an arsenic removal membrane for treating arsenic-containing wastewater in mines", which is an arsenic removal membrane with multiple functions prepared by using bamboo pulp fiber, glass fiber and eggshell powder And use this membrane to filter arsenic slag, the concentration of arsenic in the solution after filtration can reach 0.01mg / L, the membrane works by physical barrier and physicochemical adsorption; And the method of recycling”, which is to filter the high-arsenic polluted acid, membrane distillation, acid concentration and recovery of condensed water, the concentrated acid is reduced, cooled and precipitated arsenic trioxide, and then vulcanized to remove arsenic and heavy metals, although it is adopted stepwise treatment method, but there are problems such as the need for further harmless treatment of hazardous waste generated by different principles; Chinese patent CN201810008659. Invented a method for treating wastewater containing trivalent arsenic, which is to feed trivalent arsenic wastewater and ferric iron solution at the same time, adjust the pH value of the mixed solution to 1.41-2.45, stir at room temperature, and separate and precipitate. Sulfur-free genusite, Fe 6 (AsO 3 ) 4 (HAsO 3 )(OH) 4 4H 2 O, there are relatively harsh requirements on the ratio and concentration of the reactants, and the stability of the product-free hydroxyarsenite is unknown; The harmless treatment method of arsenic-containing slag liquid in chemical gold extraction process "The processing object is the high-concentration arsenic-containing slag liquid produced by the biological pre-oxidation-cyanide gold extraction process of arsenic-containing gold concentrate, and the goethite method (50~ 90°C, 2~4h) and ferrous salt enhanced aeration (control) for harmless treatment, although the effect of iron ions is used, there are problems such as inapplicability of the method

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Experimental program
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Embodiment 1

[0035] Initially, the low-concentration arsenic-containing wastewater (As 5mg / L) was treated with polyferric sulfate, and the mass ratio of iron to arsenic was 4 for primary arsenic removal, and then the low-concentration arsenic-containing wastewater was combined with primary arsenic removal bottom flow and deep arsenic removal bottom flow (control The iron / arsenic mass ratio is 20), stirred in the reaction tank for 30min, the stirring line speed is 2m / s, the pH detection device of the reaction tank is interlocked with the sulfuric acid or milk of lime metering peristaltic pump, so that the pH of the reaction is controlled at 7 ~9. Pump the preliminary arsenic removal slurry to the thickener, and at the same time add polyacrylamide polymer flocculants with a concentration of 0.1% to the feed barrel of the thickener, and control the amount of polyacrylamide polymer flocculants to 3g / t for preliminary removal Arsenic slag; the dense underflow part of preliminary arsenic removal...

Embodiment 2

[0037] Initially, the low-concentration arsenic-containing wastewater (As 3mg / L) was treated with polyaluminium chloride, and the primary arsenic removal was carried out at an aluminum / arsenic mass ratio of 7, and then the low-concentration arsenic-containing wastewater (As 3mg / L) was mixed with the primary arsenic removal underflow and deep arsenic removal underflow (control iron / arsenic mass ratio is 20), stir in the reaction tank for 20min, the stirring line speed is 2m / s, the pH detection device of the reaction tank is interlocked with the metering peristaltic pump of sulfuric acid or milk of lime for interlocking control, The pH of the reaction was controlled at 7-9. Pump the preliminary arsenic removal slag to the thickener, and at the same time add a polyacrylamide macromolecule flocculant with a concentration of 0.2% to the feed barrel of the thickener, and control the amount of polyacrylamide polymer flocculant to 5g / t for the preliminary arsenic removal slag; The den...

Embodiment 3

[0039] Initially, the low-concentration arsenic-containing wastewater (As 2mg / L) was used as a coagulant combined with ferric sulfate and polyaluminium chloride, and the mass ratio of iron (aluminum) / arsenic was 10 for primary arsenic removal, and then the low-concentration arsenic-containing wastewater ( As 2mg / L) and primary arsenic removal underflow and deep arsenic underflow (control iron / arsenic mass ratio is 30), stirred in the reaction tank for 10min, the stirring line speed was 1.0m / s, the pH detection device of the reaction tank and Sulfuric acid or milk of lime metering peristaltic pumps are interlocked to control the pH of the reaction at 7-9. Pump the preliminary arsenic removal slag to the thickener, and at the same time add polyacrylamide with a concentration of 0.1% to the feed barrel of the thickener, and control the amount of polyacrylamide to 8g / t dry preliminary arsenic removal slag; preliminary arsenic removal dense The underflow part is pumped to step (1),...

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Abstract

The invention relates to a stepped deep purification method of low-concentration arsenic waste water. The low-concentration arsenic waste water (1) is subjected to a primary arsenic removing and deeparsenic removing stepped treatment mode; at the initial stage of primary arsenic removal, a coagulant (8) is added to perform coagulation and then solid and liquid separation is conducted to obtain primary arsenic-removing bottom flow (3) and primary arsenic-removing overflow (4); during deep arsenic removal, iron salt (5) is added into the primary arsenic-removing overflow (4) to perform coagulation aeration and solid-liquid separation to obtain deep arsenic-removing bottom flow (6) and deep arsenic-removing overflow (7), the deep arsenic-removing overflow (7) is subjected to up-to-standard discharge; subsequently, the primary arsenic-removing bottom flow (3) and the deep arsenic-removing bottom flow (6) return to the primary arsenic removal to replace the coagulant (8); and the stepped deep purification method of the low-concentration arsenic waste water has the advantages that the arsenic concentration of the aqueous solution after treatment can be as low as 0.005 mg/L or below, themedicament consumption is low, the slag amount is small and the medicament efficacy is high, and is suitable for being applied to environmental protection and mine resource comprehensive utilizationindustry.

Description

technical field [0001] The invention relates to a step deep purification method of low-concentration arsenic-containing wastewater, which is suitable for the application in the industries of environmental protection and comprehensive utilization of mine resources. Background technique [0002] Non-ferrous metals and rare and precious metals are national strategic resources and occupy an important position in the national economy. The extraction of non-ferrous metals and rare and precious metals still mainly comes from the development of corresponding mineral resources. According to incomplete statistics, the development of non-ferrous metal mineral resources is the main source of arsenic pollution. This is because arsenic is a sulfur-friendly element. There are as many as 300 kinds of arsenic-containing minerals, and most of them are mixed with gold, copper, and lead in the form of sulfides. , zinc, tin, nickel, and cobalt ores, with the development of mineral resources, mi...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C02F9/04C02F101/10
CPCC02F9/00C02F1/5245C02F2101/103
Inventor 庄荣传王乾坤陈启斌沈青峰季常青肖琴王弘
Owner ZIJIN MINING GROUP
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