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Method of receiving of vanadium-bearing alloys and ligatures

IPC classes for russian patent Method of receiving of vanadium-bearing alloys and ligatures (RU 2368689):
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Method of regeneration of metallic chromium from slags containing chromium oxide Method of regeneration of metallic chromium from slags containing chromium oxide / 2247161
Proposed method is used for converter processes such as AOD, MRP, AOD-L, MRP-L, CLU, ASM, Conars-Stainless steel, or vacuum processes such as VOD, SS-VOD, RH and RH with use of oxygen lance. Slag formed at the end of blowing and treatment in converter or vacuum plant is drained and removed in unreduced state; this slag is fed to electric furnace which is loaded with standard charge consisting of metal scrap and residual dust; then carbon is additionally fed and silicon if necessary; during melting, chromium oxide contained is slag is reduced by means of carbon and silicon.

FIELD: metallurgy.

SUBSTANCE: in method in the capacity of charge it is used vanadium-bearing wastes and lime, herewith in oxidising area it is implemented separation of metal from vanadium-bearing melted slag with periodic or continuous discharge of it from furnace. It is implemented reduction of vanadium oxides from melted slag in reducing zone by introduction into melt of silicon-bearing alloy with acceptable content of aluminium 2-15%, taken in amount for 2-50% more than stoichiometrically necessary for reduction vanadium oxides.

EFFECT: invention provides increasing of vanadium concentration in alloy, reducing of power inputs, improving of ecological situation.

2 ex, 2 tbl

 

The invention relates to the field of ferrous and nonferrous metallurgy, specifically to obtain vanadium alloys and alloys of slag, sludge, dust and other compounds of vanadium.

Because of the low content of vanadium ores in the technology of their processing is a complex process consisting of a combination of a number of metallurgical and chemical processing.

A known method of producing ferrovanadium, consisting of batch preparation, which comprises the oxides of vanadium, lime, ferrosilicon and recycled slag, melting, recovery, refining, production of finished products of melt from the furnace and casting molds (RISS M.A. Production of ferroalloys. - M.: metallurgy, 1975, s-292).

The feature of the known method of producing ferrovanadium is that fusion consists of two periods: the recovery and refining. In the first period carry out the recovery of vanadium from vanadium oxides in conditions of significant excess reductant - ferrosilicon and high basicity slag. The result is an alloy containing vanadium 25-30%, silicon - 21-23%, carbon is 0.3 - 0.5% and slag containing vanadium less than 0.35%, the slag produced is cooled and sent to the dump. In the second period, the alloy is enriched with vanadium by refining it from silicon oxides of vanadium, which is loaded into the furnace the place of lime. Upon reaching the concentration of silicon in ferrovanadium within 9-12% slag produced and sent to the dump, and liquid ferrovanadium upload a new batch containing a mixture of oxides of vanadium and lime, and continue to Refine the metal to silicon in it to 1.5-2%. The resulting alloy contains 40-45% vanadium 1,2-1,4% manganese, 0.08% phosphorus and refining slag containing vanadium 6-12%. His return to the oven for the next melting during the first period. One base ton of ferrovanadium (40% vanadium) expended: 710 kg V2O5(100%), 425 kg of ferrosilicon, 75 kg aluminum 1350 kg lime, 300 kg of iron trimmings and about 1500-1800 kW·h of electricity.

The disadvantages of this method is:

- high power consumption;

- the difficulty of obtaining a stable composition of the alloy;

low kiln productivity due to the need for recovery and refining processes in one unit.

It is known that in recent years, production of ferrovanadium directly use the Converter slag, bypassing the stage of chemical secretions from him pure vanadium oxide.

Vanadium slag is shlakometallicheskih conglomerate with a ratio of metal and slag phases, respectively 30-80% and 20-70%.

The composition of the slag phase: 17-24% V2O5; 2,5-3,0 the r 2About3; 17-20% SiO2; 7-11% IGOs; 8-12% Al2About3; 6-9% TiO2; 0.5 to 2% Cao; 5-8% MgO; 35-49% Fetotal.

The composition of the metal phase: 3%; 0,02-0,06% V; traces of other elements, the base - Fe.

A known method of producing Ferroalloy, including the filling mixture, melting vanadium-containing mixture with a reducing agent in an electric furnace and the release of the melt in the ladle. To reduce harmful impurities in the alloy before filling the mixture in a furnace heated to 1200-1700°C enter the sulfates of alkali and alkaline earth metals, then they are covered by the coke at a certain weight ratio (Author's certificate of USSR No. 589273, CL SS 33/04, priority from 1.09.1976, publ. 18.01.78).

The disadvantages of the method are:

- low productivity furnace Assembly;

- high power consumption;

- significant loss of vanadium from the slag;

- environmental degradation.

A known method of producing ferrovanadium, consisting of the preparation of vanadium-containing melt in an electric furnace, release it into the bucket at a temperature of 1400-1550 With and submission to the bucket of lime, iron and liquid ferrosilicon (Author's certificate of USSR No. 258348, CL SS 38/12, declared 16.07.76, publ. 25.12.77).

The disadvantages of the method are:

- the need to have another electric furnace to obtain a molten ferrosilicon;

- unstable thermal balance of the melt;

- Tr is bullying; appropriate regulation of the composition of the vanadium in the bucket.

The closest in technical essence and the achieved effect is a method of processing raw materials containing non-ferrous metals and iron (RF Patent No. 2194781, priority dated 28.11.2000, publ. 20.12.2002, Bulletin No. 35). He adopted us as a prototype.

The method involves feeding in the oxidation zone two-zone furnace slag on the melt mixture consisting of a source of ore, fluxes, carbonaceous material and oxygen-containing blast, melting the mixture to a melt which enters into the recovery area, which serves additionally carbonaceous material in an oxygen-containing blast, and the quantity of carbonaceous material and oxygen-containing blast in the oxidation zone give just enough to the carbon of coal burned, and its amount in the reducing zone support to fully translate the oxides of vanadium in the metallic phase and to compensate for heat loss. In this respect, the specific consumption of carbonaceous material per ton of recoverable metal in the oxidizing and reducing zones maintained within the range of 0.3 to 2.5, and the ratio of specific consumption of oxygen in these areas in the range from 0.7 to 3.0.

The disadvantages of this method are:

- the impossibility of its use for raw materials, which contains large quantities of meth is lofaso, for example, Converter slag;

- poor performance of the unit;

- high concentration of iron (oxide and metal) in the melt.

The aim of the present invention are:

- increasing the concentration of vanadium in the alloy when receiving it from vanadium slag;

- reducing energy consumption;

- improved performance;

- the improvement of the environment.

This goal is achieved by the fact that:

in the oxidation zone of the furnace otpravlyautsa metallocene present in the vanadium slag and separated from the slag melt;

metal periodically or continuously produced from the oxidation zone;

as the reducing agent used silicon-containing material, which may include: aluminum in the amount of 2-15% and an impurity is magnesium, calcium and other metals, thermodynamic strength of which is higher than that of silicon dioxide;

- silicon alloy is taken in quantity at 2-50% more than the stoichiometric required for the recovery of vanadium oxides

The basis of the proposed method are the following processes:

in the oxidation zone:+2O2=2SD2+Q; V2O3+O2=V2O5;

in the reducing zone: 2/4V2O5+Si=4/5V+SiO2.

In the presence of calcium oxide latter reaction takes the form: 2/5V2O 5+Si+2CaO=4/5V+2CaO*SiO2.

As the carbonaceous material is coal, oxygen-containing blast - air enriched with oxygen and a reducing agent - ferrosilicon with silicon content not less than 65%.

The amount of siliceous material is taken to ensure full recovery of vanadium oxides from the melt and some of its final content in ferrovanadium (upon Customer request). When its content in the mixture is less than 2% reduced vanadium recovery, and the introduction of it in the range of 2 to 50% is achieved not only the full recovery of the oxides of vanadium, but also getting kremnievoi ligatures, a higher concentration of silicon-containing material (>50%) not economically justified.

Introduction the composition of the charge certain amount of aluminum provides improved kinetic and thermodynamic conditions for the restoration of oxides and receiving slag with lower viscosity.

Below are examples of carrying out the invention does not exclude other in the scope of the claims.

Example 1.

The charge, consisting of 1000 kg Converter slag and 400 kg of lime, thoroughly mixed, and the portions were loaded into a preheated 1350°C oven (oxidation zone). Further heating of the mixture produced by burning coal in a stream of air enriched with oxygen. On on the stijene temperature in the oxidation zone of 1650°C, without interrupting the loading of the charge, opened pulmonary hole and released the metal deposited on the furnace hearth furnace. After gunning the accumulated melt started to cross in the recovery area, where continuously at a certain speed download ferrosilicon brand FS (170 kg) and lime (400 kg). The oven has worked for 3 hours. Proflavine 1000 kg of Converter slag, 170 kg of ferrosilicon and 800 kg of lime. The obtained iron 155 kg (oxidation zone) and ferrovanadium 320-350 (recovery zone). Table 1 presents the results of chemical analysis of samples of the metal recovery zone, taken during the experiments.

Table 1
no experience The composition of the mixture of the oxidizing zone, kg The composition of the charge recovery zone, kg The composition of the metal recovery zone, wt.% Note
slag lime FS lime vanadium manganese chrome silicon
1 100 40 15 30 23,5 10,7 2,0 0,5 In experiment 1 contents FS in the mixture is less than 2% of stoichiometry
2 100 50 17 30 24,1 9,9 1,9 2,0
3 100 50 17 30 24,0 9,6 1,9 1,9
4 100 50 20 30 24,4 9,0 1,7 3,5
5 100 60 22 30 24,0 8,3 1,4 5,6
6 100 60 24 30 23,6 7,7 1,2 8,3
7 100 70 26 30 22,6 7,1 0,9 9,8

Ferrovanadium obtained by known techniques using the same slag, had composition, %: vanadium - 18-18,6, manganese - 5-6,4, silicon is 7.5 and 8.6, chrome - 2,9, titanium - 0,14-0,65, aluminum - 0.3 to 0.5.

The composition of the metal released from the oxidation zone, %: vanadium - 0,02, carbon - 2,73, manganese - 0,34, chrome - 0,13, iron - rest.

Experiments showed that the proposed technology allows to increase the concentration of vanadium in ferrovanadium by 5-7%, and the extraction of vanadium in the alloy was 85-89%.

Example 2.

Experiments were performed by the same method; the charge was partially replaced ferrosilicon aluminum; in some experiments in order to obtain margaretanndavis ligatures in charge of the injected waste ø the AK manganese metal composition, %: IGOs and 22.6; Cao - 42,1; SiO2 - 33,6; MgO - 4,4; Al2About3is 2.2.

The results of the experiments are presented in table 2.

13
Table 2
no experience The composition of the mixture of the oxidizing zone, kg The composition of the charge recovery zone, kg The composition of the metal recovery zone, wt.% Note
slag lime FS 75 lime Al MP slag vanadium manganese chrome silicon
8 100 50 16 30 3 - 24,6 9,8 1,8 1,8
9 100 50 14 30 5 25,1 9,8 1,8 1,4
10 100 50 5 30 18 to 25.3 9,3 1,7 0,9
11 100 50 17 30 - 20 20,2 15,2 1,1 0,9
12 100 50 17 30 - 30 18,6 20,4 0,9 1,0
100 50 20 30 - 30 18,4 25,7 0,6 1,2
14 100 50 20 30 - 40 15,3 32,4 0,4 1,4

The composition of the metal oxidation zone has not changed. The analysis of the conducted experiments showed that the introduction of the slag dump, in particular slag manganese metal, allows you to get magnetventile ligatures specified composition with almost complete recovery of manganese and vanadium.

The present invention can be implemented at the metallurgical enterprises, which produces the Converter vanadium-containing slags, there is waste in the form of dust from furnaces and converters, for example the Nizhniy Tagil metallurgical plant.

The proposed technology of redistribution of vanadium-containing slag is characterized by missing the eating of poisonous substances in the exhaust gases, a high level of mechanization and automation is performed by means of highly efficient equipment and instrumentation.

The invention can be used for processing other metal-containing wastes, in particular, from the production of Nickel, chromium, manganese added to the basic mixture of oxidizing and/or reducing the period of melting.

The economic effect from implementation of the invention consists of energy savings, increase furnace productivity and simplifying the technology and reduce costs for environmentally harmful emissions.

The method of obtaining vanadium alloys and alloys, including the preparation of the charge, a continuous feed her in the oxidation zone of the furnace, melting the mixture of carbonaceous material in oxygen-containing blast, taken in the ratio that ensures complete combustion of the carbon in the oxidation zone, obtaining shlakometallicheskih melt, the restoration of its oxides in the reducing zone, characterized in that as the charge is used vanadium waste and lime, while in the oxidation zone carry out the separation of metal from vanadium bearing slag melt with periodic or continuous release it from the oven, carry out the recovery of oxides of vanadium from the slag melt in vosstanovit the tion zone by introducing into the silicon melt alloy with a valid aluminium content of 2-15%, taken in quantity at 2-50% more than the stoichiometric required for the recovery of vanadium oxides.

 

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