Vanadium leaching method for high-chrome vanadium residues

A technology for high-chromium vanadium slag and vanadium slag is applied in the field of vanadium extraction from vanadium slag, which can solve the problems of low vanadium extraction rate, waste of resources, increase in production cost, etc., so as to avoid toxic and harmful substances, save resources and costs, and reduce leaching. rate effect

Inactive Publication Date: 2016-07-06
NORTHEASTERN UNIV
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Problems solved by technology

But this method mainly has two disadvantages: ① a large amount of Cl is produced during roasting 2 , SO 2 and other toxic and harmful gases, seriously polluting the environment; ②The tailings after vanadium extraction contain a large amount of sodium elements, which exceeds the requirements of blast furnace smelting, and it is difficult to return to the blast furnace for sintering for recycling. At the same time, it caused a serious waste of resources
The problems of this method are as follows: 1. the extraction rate of vanadium is low, generally below 80%, and the recovery rate for high-chromium vanadium slag is lower, often less than 70%; It will greatly increase the consumption of sulfuric acid and increase the production cost
[0005] The third method is the blank roasting-concentrated sulfuric acid acid leaching method. This method uses traditional muffle furnace or rotary kiln to directly heat, roast and oxidize the vanadium slag, and then uses concentrated sulfuric acid acid leaching to obtain a vanadium-containing solution. Vanadium slag is only for vanadium-containing iron water blasting vanadium vanadium slag, not suitable for high chromium vanadium slag
The trivalent vanadium in normal spinel is difficult to dissolve in acid, and can only be extracted after destroying the spinel phase and oxidizing the vanadium in it to tetravalent or pentavalent. The common roasting used in these three methods The method can only be aimed at this kind of vanadium spinel
For high chromium vanadium slag, chromium mainly exists in chromium spinel (FeCr 2 o 4 ), which is in solid solution with vanadium spinel, and chrome spinel is a kind of ore that is more difficult to oxidize and decompose than vanadium spinel, and the extraction method of ordinary vanadium slag is used, and the recovery rate of vanadium is extremely low

Method used

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  • Vanadium leaching method for high-chrome vanadium residues

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Effect test

Embodiment 1

[0043] Break 1Kg of high chromium vanadium slag into particles with a particle size of less than 150 mesh, take 300g of high chromium vanadium slag after crushing and sieving, place it under microwave conditions and air atmosphere for heating and roasting, control the microwave heating frequency to 2.45GHz, and the heating temperature to 900° C, heating time is 60min, obtains high chromium vanadium slag clinker; Then clinker is broken into particle size and is less than 200 mesh particles, gets high chromium vanadium slag clinker 100g after breaking, adds the sulfuric acid solution 2000ml of 3mol / L, at a temperature of Under the condition of 85°C, stirring and leaching for 120min, the stirring speed was 500r / min; after the mixture was filtered and separated, the vanadium-containing filtrate and vanadium extraction tailings were obtained respectively.

[0044] The vanadium extraction tailings are dried and then returned to the blast furnace for sintering.

[0045] The potassium...

Embodiment 2

[0047] Break 1Kg of high chromium vanadium slag into particles with a particle size of less than 150 mesh, take 300g of high chromium vanadium slag after crushing and screening, heat and roast in microwave conditions and air atmosphere, control the microwave heating frequency to 2.45GHz, and the heating temperature to 800° C, heating time is 90min, obtains high chromium vanadium slag clinker; Then clinker is broken into particle size and is less than 200 mesh particles, gets high chromium vanadium slag clinker 100g after breaking, adds the sulfuric acid solution 2000ml of 3mol / L, at temperature Under the condition of 85°C, stirring and leaching for 120min, the stirring speed was 500r / min; after the mixture was filtered and separated, the vanadium-containing filtrate and vanadium extraction tailings were obtained respectively.

[0048] The vanadium extraction tailings are dried and then returned to the blast furnace for sintering.

[0049] The potassium permanganate-ferrous sul...

Embodiment 3

[0051] Break 1Kg of high chromium vanadium slag into particles with a particle size of less than 150 mesh, take 300g of high chromium vanadium slag after crushing and screening, heat and roast in microwave conditions and air atmosphere, control the microwave heating frequency to 2.45GHz, and the heating temperature to 820° C, heating time is 80min, obtains high chromium vanadium slag clinker; Then clinker is broken into particle size and is less than 200 mesh particles, gets high chromium vanadium slag clinker 100g after breaking, adds the sulfuric acid solution 1000ml of 6mol / L, at a temperature of Under the condition of 95°C, stirring and leaching for 60 minutes, the stirring speed is 300r / min; after the mixture is filtered and separated, the vanadium-containing filtrate and vanadium extraction tailings are respectively obtained.

[0052] The vanadium extraction tailings are dried and then returned to the blast furnace for sintering.

[0053] The potassium permanganate-ferro...

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Abstract

The invention provides a vanadium leaching method for high-chrome vanadium residues. The vanadium leaching method includes the process steps that high-chrome vanadium residues are smashed into particles with the granularity smaller than 150 mesh; the particles are put in the microwave condition and the air atmosphere to be heated and baked to obtain high-chrome vanadium residue clinker, wherein the heating frequency of microwaves is controlled to be 2 GHz to 3 GHz, the heating temperature is controlled to be 700 DEG C to 1000 DEG C, and the heating time is controlled to be 10 min to 120 min; the high-chrome vanadium residue clinker is smashed into particles with the granularity smaller than 200 mesh; a dilute sulphuric acid solution with the concentration of 0.5 mol/L to 6 mol/L is added to the clink particles, the mixture is stirred and leached for 10 min to 180 min at the temperature of 70 DEG C to 100 DEG C; and vanadium-containing filtrate and vanadium tailings are obtained after the mixture is filtered and separated. The method is put forward for high-chrome vanadium residues without effective treatment methods on the current domestic market, various types of high-chrome vanadium residues with the chrome content reaching up to 8% to 14% can be effectively processed, and the final vanadium leaching rate reaches 86% or above.

Description

technical field [0001] The invention relates to a method for extracting vanadium from vanadium slag, in particular to a method for extracting vanadium from high-chromium vanadium slag. Background technique [0002] As an important valuable metal element, vanadium has been widely used in metallurgical industry and chemical industry. At present, the output of vanadium extracted from vanadium-titanium magnetite accounts for about 90% of the total output of vanadium in industrial production. At present, the method of extracting vanadium from vanadium-titanium magnetite in China is mainly pyrometallurgy. This method is to crush the vanadium-titanium magnetite and add a certain amount of additives, and then sinter it into sinter or pellets, and then mix it with coke Put vanadium into the molten iron from sinter or pellets together to form vanadium-containing molten iron, then put the vanadium-containing molten iron into the converter, add some oxidant and coolant into the convert...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C22B34/22C22B1/02C22B7/04
CPCC22B1/02C22B7/007C22B7/04C22B34/125Y02P10/20
Inventor 薛向欣张学飞姜涛杨合方得安
Owner NORTHEASTERN UNIV
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