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A method for treating vanadium industrial wastewater with semi-dry flue gas desulfurization ash

A technology for industrial wastewater and desulfurization ash, applied in multi-stage water treatment, water/sewage treatment, chemical instruments and methods, etc., can solve the problems of incomplete discharge, low treatment efficiency, high treatment cost, etc., and solve secondary pollution And the problem of land occupation, good treatment effect and high economic value

Active Publication Date: 2019-04-26
NORTHEASTERN UNIV LIAONING
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Although these methods have certain effects, there are generally problems such as high treatment cost, low treatment efficiency, easy to produce secondary pollution and failure to fully meet the discharge standards.

Method used

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  • A method for treating vanadium industrial wastewater with semi-dry flue gas desulfurization ash
  • A method for treating vanadium industrial wastewater with semi-dry flue gas desulfurization ash
  • A method for treating vanadium industrial wastewater with semi-dry flue gas desulfurization ash

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0034] The pH of vanadium industrial wastewater is 1, the total chromium concentration is 4500 mg / L, the hexavalent chromium concentration is 3800 mg / L, the pentavalent vanadium concentration is 200 mg / L, and the ammonia nitrogen (NH 3 -N) concentration 4000mg / L; introduce vanadium industrial wastewater into the reduction reaction tank, stir and add semi-dry FGD ash; the amount of semi-dry FGD ash added is 10% of the total mass of vanadium and chromium in vanadium industrial wastewater times; the XRD pattern of semi-dry flue gas desulfurization ash is as follows figure 2 shown;

[0035] Add inorganic acid to adjust the pH=1.0 of all materials in the reduction reaction tank, and then reduce the reaction for 30min under stirring conditions to reduce the high valence state of vanadium and chromium to low valence state; the inorganic acid is sulfuric acid;

[0036] After the reduction reaction is completed, it is left to stand for precipitation for 2 hours, and the primary super...

Embodiment 2

[0042] The method is the same as in Example 1, except that:

[0043] (1) The pH of vanadium industrial wastewater is 2, the total chromium concentration is 4200 mg / L, the hexavalent chromium concentration is 3600 mg / L, the pentavalent vanadium concentration is 150 mg / L, and the ammonia nitrogen (NH 3 -N) concentration 3600mg / L; introduce vanadium industrial wastewater into the reduction reaction tank, stir and add semi-dry FGD ash; the amount of semi-dry FGD ash added is 8% of the total mass of vanadium and chromium in vanadium industrial wastewater times;

[0044] (2) Add inorganic acid to adjust the pH=2.0 of all materials in the reduction reaction tank, and then react under stirring conditions for 20min; the inorganic acid is hydrochloric acid;

[0045] (3) After the reduction reaction is completed, stand for precipitation for 1.5h;

[0046] (4) Introduce the primary mixed solution into the neutralization and sedimentation tank, add sodium hydroxide to adjust pH=7.0, stir...

Embodiment 3

[0052] The method is the same as in Example 1, except that:

[0053] (1) The pH of vanadium industrial wastewater is 2, the total chromium concentration is 3800 mg / L, the hexavalent chromium concentration is 3400 mg / L, the pentavalent vanadium concentration is 100 mg / L, and the ammonia nitrogen (NH 3 -N) concentration of 3200mg / L; introduce vanadium industrial wastewater into the reduction reaction tank, stir and add semi-dry FGD ash; the amount of semi-dry FGD ash added is 6% of the total mass of vanadium and chromium in vanadium industrial wastewater times;

[0054] (2) Add inorganic acid to adjust the pH=2.0 of all materials in the reduction reaction tank, and then react under stirring conditions for 15 minutes; the inorganic acid is nitric acid;

[0055] (3) After the reduction reaction is completed, stand for precipitation for 1h;

[0056] (4) Introduce the primary mixed solution into the neutralization and sedimentation tank, add sodium hydroxide to adjust pH=8.0, stir...

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Abstract

The invention discloses a method for treating vanadium industrial wastewater by the aid of semi-dry flue gas desulfurization ash. The method includes steps of (1), adding the semi-dry flue gas desulfurization ash into the vanadium industrial wastewater; (2), adding inorganic acid into the vanadium industrial wastewater to regulate a pH (potential of hydrogen) value of the vanadium industrial wastewater and stirring the inorganic acid and the vanadium industrial wastewater to obtain mixtures; (3), allowing the mixtures to stand still, separating supernatant from precipitates, carrying out pressure filtration on the precipitates to obtain calcium sulfate and mixing filter liquid and the supernatant with each other to obtain first mixed liquid; (4), adding sodium hydroxide into the first mixed liquid, stirring the first mixed liquid and the sodium hydroxide to obtain second mixed liquid, adding flocculating agents into the second mixed liquid and continuing to stir the flocculating agents and the second mixed liquid to obtain third mixed liquid; (5), allowing the third mixed liquid to stand still, separating supernatant from precipitates, carrying out pressure filtration on the precipitates to form chromium-containing green mud and mixing filter liquid and the supernatant with each other to obtain fourth mixed liquid; (6), leading the fourth mixed liquid into an ammonia nitrogen precipitating tank, stirring the fourth mixed liquid, adding magnesium salt and phosphate into the fourth mixed liquid to obtain fifth mixed liquid, regulating a pH value of the fifth mixed liquid and then continuing to stir the fifth mixed liquid; (7), allowing the fifth mixed liquid to stand still and separating supernatant from precipitates. The method has the advantages that semi-dry desulfurization solid waste can be recycled, accordingly, the wastewater treatment cost can be reduced, the problems of secondary pollution and land occupation of semi-dry desulfurization ash can be solved, and the method has high environmental benefits, economic benefits and social benefits.

Description

technical field [0001] The invention belongs to the technical field of waste water and solid waste treatment, and in particular relates to a method for treating vanadium industrial waste water with semi-dry flue gas desulfurization ash. Background technique [0002] Vanadium is known as a metal "vitamin" and is widely used in metallurgy, chemical industry and other industries as alloy additives and catalysts in organic chemicals. At present, the production process of its main product vanadium pentoxide is mostly sodium roasting process. The process is: vanadium slag crushing - sodium roasting - water leaching of vanadium - leachate purification - acid ammonium salt vanadium - melting; this process produces a large amount of highly polluted acidic wastewater, which is characterized by high salinity, large discharge and high heavy metal content , according to the requirements of "GB 26452-2011 Vanadium Industrial Pollutant Discharge Standard", the total chromium, hexavalent ch...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C02F9/04C01F11/46C01G37/02C05B17/00
CPCC01F11/46C01G37/02C01P2002/72C02F1/52C02F1/5236C02F1/56C02F1/586C02F1/66C02F1/70C02F9/00C02F2301/08C05B17/00
Inventor 薛向欣方得安廖翔
Owner NORTHEASTERN UNIV LIAONING
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