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Method for comprehensively utilizing vanadium slag

A vanadium slag and leaching slag technology, applied in the field of comprehensive utilization of vanadium slag, can solve the problems of large industrial waste gas, large material consumption, long process flow, etc., achieve reduced material consumption, high comprehensive yield, and shortened process flow Effect

Inactive Publication Date: 2014-10-29
PANZHIHUA IRON & STEEL RES INST OF PANGANG GROUP
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Problems solved by technology

[0005] Since the beginning of this century, there are some defects in the vanadium extraction process of converter vanadium slag roasting-leaching: (1) The process flow is long and the material consumption is large; (2) A large amount of industrial waste gas is produced, polluting the atmosphere; (3) Vanadium slag Poor comprehensive utilization of resources
This process has a good leaching effect for raw materials with high calcium content, but the roasting process is complicated, the process is long, and a large amount of harmful gases are generated during the production process, which pollutes the environment;
[0008] (3) Chinese patent 201010514573.8 "A method for extracting vanadium by wet method using vanadium-containing titanium converter slag" adopts non-calcined oxygen pressure leaching technology, and then performs ion exchange on the leaching solution to obtain relatively pure vanadium-containing exchange liquid, NaOH desorption, vanadium precipitation , calcined to obtain V 2 o 5 , but the total vanadium yield is not high;
[0009] (4) Chinese patent 201410290331.3 "Method for extracting vanadium from converter vanadium slag" provides a vanadium extraction technology using non-roasting atmospheric pressure leaching-extraction-reextraction. After four-stage cross-flow extraction, the total vanadium yield of the three-stage process reaches More than 95%, but the leachate and extract of this process must be pretreated before the next step, and the valence control of vanadium is relatively strict, and the treatment is relatively complicated;
[0010] (5) Chinese patent 20060048733.8 "Method for oxidative conversion and leaching of vanadium from converter steelmaking slag under pressure field" discloses a method of oxygen pressure for steelmaking converter vanadium slag without roasting under pressure field oxidation atmosphere conditions Extraction of vanadium by leaching technology, using 50% to 98% concentrated sulfuric acid to destroy the hard vanadium iron spinel structure in the vanadium slag, avoiding the strong corrosive products produced by adding fluoride salt fluxing, is a low-pollution treatment method, but still has many deficiencies

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  • Method for comprehensively utilizing vanadium slag

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preparation example Construction

[0035] C, the preparation of vanadium-containing solution: the extract is carried out back extraction, and the lower clear liquid is the vanadium-containing solution; wherein, the stripping agent is the sulfuric acid of 50~300g / L, and stripping ratio (O / A)=(2 ~10): 1;

[0036]d. Preparation of electrolytic manganese: After adjusting the pH value of the raffinate obtained in step b to 4.0-6.0, add ammonium sulfate and trace selenium dioxide for electrolysis to obtain electrolytic manganese; wherein, the electrolytic current density is 100-300A / m -2 , electrolysis temperature 20~50℃; ammonium sulfate concentration 80~150g / L;

[0037] e, preparation of titanium dioxide: adding sulfuric acid to the leaching slag obtained in step a, carrying out secondary acid leaching, filtering to obtain a secondary leaching solution; heating the secondary leaching solution, adding Fe 3+ reduced to Fe 2+ , freeze to make ferrous sulfate crystallize, filter to obtain titanyl sulfate, hydrolyze...

Embodiment 1

[0050] Embodiment 1 Utilize the method of the present invention to reclaim vanadium, titanium, manganese in vanadium slag

[0051] (1) Oxygen pressure acid leaching:

[0052] Crush the vanadium slag, ball mill, take 100g of converter vanadium slag with a particle size of -0.075~+0.055mm (-200~+260 mesh), add it to a sulfuric acid solution with an initial acid concentration of 200g / L, and calculate the volume of sulfuric acid: the mass of converter vanadium slag The ratio (liquid-solid ratio) is 10:1, the acid leaching time is 90min, the stirring speed is 500rpm, the acid leaching temperature is 90°C, and oxygen is maintained during the acid leaching process, and the oxygen pressure is 0.5MPa. Liquid-solid separation is carried out after leaching, the leaching solution is the leaching solution containing vanadium acid, and the leaching residue is the leaching residue enriched in titanium. Under these conditions, the leaching rate of vanadium is 64.33%, and that of titanium is ...

Embodiment 2

[0060] Embodiment 2 Utilize the method of the present invention to recover vanadium, titanium, manganese in vanadium slag

[0061] (1) Oxygen pressure acid leaching:

[0062] Crush the vanadium slag, ball mill, take 100g of converter vanadium slag with a particle size of -0.075~+0.055mm (-200~+260 mesh), add it to a sulfuric acid solution with an initial acid concentration of 200g / L, and calculate the volume of sulfuric acid: the mass of converter vanadium slag The ratio (liquid-solid ratio) is 10:1, the acid leaching time is 90min, the stirring rate is 500rpm, the acid leaching temperature is 160°C, the oxygen flow is maintained during the acid leaching process, and the oxygen pressure is 0.5MPa. Liquid-solid separation is carried out after leaching, the leaching solution is the leaching solution containing vanadium acid, and the leaching residue is the leaching residue enriched in titanium. Under this condition, the leaching rate of vanadium was 98.37%, that of titanium was...

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Abstract

The invention relates to a method for comprehensively utilizing vanadium slag, belongs to the field of resource reclamation, and aims to solve the technical problem of providing the method for comprehensively utilizing the vanadium slag. The method comprises the following steps: a, acid leaching at oxygen pressure, namely at oxygen pressure, adding sulfuric acid into the vanadium slag, stirring and filtering to obtain leaching liquid and leaching slag; b, leaching liquid extraction, namely regulating the pH value of the leaching liquid, and extracting to obtain extraction liquid and raffinate; c, vanadium-containing solution preparation, namely carrying out back extracting on the extraction liquid to obtain subnatant which is the vanadium-containing solution; d, electrolytic manganese preparation, namely regulating the pH value of the raffinate, adding ammonium sulfate and selenium dioxide, and electrolyzing to obtain the electrolytic manganese; and e, titanium dioxide preparation, namely adding sulfuric acid into the leaching slag which is obtained in the step a to perform secondary acid leaching, heating, reducing, freezing, crystallizing, filtering, hydrolyzing, filtering, washing, evaporatively crystallizing and calcining to obtain the titanium dioxide. The method can be used for comprehensively reclaiming and recycling vanadium slag.

Description

technical field [0001] The invention relates to a comprehensive utilization method of vanadium slag, which belongs to the field of resource recovery. Background technique [0002] Vanadium is an element of important strategic value. It has the advantages of hard texture, high melting point, non-magnetism, and good toughness. At the same time, as an alloy additive, it has super grain refinement and precipitation strengthening effects, so it is widely used in steel Industry, aerospace industry, and medical, battery and other fields. As the most important industrial raw material for extracting vanadium at present, converter vanadium slag has relatively complex elemental composition, low content of valuable elements, and relatively stable chemical structure. Generally, the dense vanadium-iron tips in vanadium slag can only be destroyed by means of enhanced oxidation and roasting. The spar structure can effectively recover the vanadium in the vanadium slag. At present, in the v...

Claims

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Application Information

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IPC IPC(8): C22B7/00C22B34/22C25C1/10C22B34/12
CPCY02P10/20
Inventor 余彬孙朝晖鲜勇唐红建杜光超景涵王唐林
Owner PANZHIHUA IRON & STEEL RES INST OF PANGANG GROUP
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