CN110564906A - Method for separating and enriching vanadium from iron ore concentrate and producing pure iron - Google Patents
Method for separating and enriching vanadium from iron ore concentrate and producing pure iron Download PDFInfo
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- C—CHEMISTRY; METALLURGY
- C21—METALLURGY OF IRON
- C21B—MANUFACTURE OF IRON OR STEEL
- C21B13/00—Making spongy iron or liquid steel, by direct processes
- C21B13/006—Starting from ores containing non ferrous metallic oxides
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- C—CHEMISTRY; METALLURGY
- C21—METALLURGY OF IRON
- C21B—MANUFACTURE OF IRON OR STEEL
- C21B13/00—Making spongy iron or liquid steel, by direct processes
- C21B13/02—Making spongy iron or liquid steel, by direct processes in shaft furnaces
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- C—CHEMISTRY; METALLURGY
- C21—METALLURGY OF IRON
- C21B—MANUFACTURE OF IRON OR STEEL
- C21B13/00—Making spongy iron or liquid steel, by direct processes
- C21B13/12—Making spongy iron or liquid steel, by direct processes in electric furnaces
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- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
- C22B1/00—Preliminary treatment of ores or scrap
- C22B1/14—Agglomerating; Briquetting; Binding; Granulating
- C22B1/24—Binding; Briquetting ; Granulating
- C22B1/2406—Binding; Briquetting ; Granulating pelletizing
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- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
- C22B1/00—Preliminary treatment of ores or scrap
- C22B1/14—Agglomerating; Briquetting; Binding; Granulating
- C22B1/24—Binding; Briquetting ; Granulating
- C22B1/242—Binding; Briquetting ; Granulating with binders
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- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
- C22B34/00—Obtaining refractory metals
- C22B34/20—Obtaining niobium, tantalum or vanadium
- C22B34/22—Obtaining vanadium
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
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Abstract
The invention discloses a method for separating and enriching vanadium from iron ore concentrate and producing pure iron, which comprises the following steps: and drying the vanadium titano-magnetite briquettes to obtain vanadium titano-magnetite pellets, directly reducing the vanadium titano-magnetite pellets by using a coal-based shaft furnace to obtain metalized pellets, and carrying out melt separation and enrichment on the metalized pellets in an electric arc furnace. The recovery rate of vanadium can reach more than 93 percent, and the grade of vanadium slag is about 6 to 8 percent. Meanwhile, the molten steel obtained by melting and separating has high purity, the iron content reaches more than 99.7 percent, and the molten steel has low contents of phosphorus, sulfur, silicon, manganese and titanium, so that the electromagnetic pure iron and the military pure iron can be produced by simple refining.
Description
The technical field is as follows:
The invention belongs to the technical field of nonferrous metallurgy, and particularly relates to a method for separating and enriching vanadium from iron ore concentrate and producing pure iron.
Background art:
The steel material is a basic industrial product in China, the yield is high, the product types are multiple, and the price difference of different products is huge. The raw materials for producing industrial pure iron are usually common fine iron powder and vanadium titano-magnetite.
at present, most domestic enterprises for producing industrial pure iron adopt traditional common iron concentrate powder as a raw material, and produce the industrial pure iron by adopting a long flow of ' sintering (or pellet ore) ' -blast furnace ironmaking-steelmaking refining-continuous casting-hot rolling ', but the industrial pure iron has extremely strict requirements on the content of slag inclusions, high refining requirements and higher cost. Another commonly used method for producing industrial pure iron is electrolysis of iron melt, but the cost of iron electrolysis is high.
Aiming at the discovered vanadium titano-magnetite mineral products in the southern Shaanxi region, the distribution is concentrated, the storage capacity is large, and through analysis, the vanadium titano-magnetite in the southern Shaanxi region has high Fe grade and more V (V) compared with vanadium titano-magnetite such as Panzhihua ore, Chengde ore, Hongdansuanyin ore in Sichuan and the like2O50.90-1.05 percent), less Ti and the like, and the improvement of the utilization rate of V and the acquisition of high value-added products of Fe are important directions for the comprehensive utilization of the ore resources.
the traditional process flow for realizing the utilization of the iron and vanadium resources of the vanadium-titanium magnetite mainly comprises two major types of direct reduction-submerged arc furnace melting and deep reduction processes of a blast furnace-converter process, a tunnel kiln, a rotary hearth furnace, a rotary kiln and the like.
In the process flow of smelting vanadium titano-magnetite by blast furnace-converter process, vanadium titano-magnetite and common ore are put into blast furnace together to be smelted to obtain vanadium-containing molten iron and blast furnace slag (TiO)222 percent), wherein the vanadium-containing molten iron is put into a vanadium extraction converter for vanadium extraction, and blast furnace slag is stockpiled. Deep processing of vanadium slag of vanadium extraction converter product to produce V2O5And the semisteel is put into a steelmaking converter to produce molten steel. The process realizes the utilization of Fe and V resources. The problems of high operation difficulty of the blast furnace, serious environmental pollution of the iron pre-process, low vanadium recovery rate and the like exist; typical applications are as follows: domestic climbing steel, Chengde steel, Wei steel, German steel, etc.
The direct reduction-submerged arc furnace melting and separating deep reduction process flow can realize the comprehensive recycling of iron and vanadium in the vanadium-titanium magnetite. The process flow has the characteristics that: the recycling of iron and vanadium resources can be realized, and the vanadium-containing molten iron can be cast and sold; the method has the defects that the melting and separating of molten iron components of the submerged arc furnace is complex, the market capacity of the obtained vanadium-containing molten iron is limited, and in addition, the vanadium resource value is not reflected. Typical applications are as follows: climbing 10 ten thousand tons of pilot line, python, New Zealand, south Africa, etc.
From the aspect of utilization of vanadium resources, no matter the vanadium extraction process for treating the vanadium-titanium magnetite is a process of 'blast furnace + converter process' or a process of 'direct reduction + submerged arc furnace melting and separating deep reduction process', vanadium is firstly reduced and enters molten iron, and then is oxidized to extract vanadium, so that the recovery rate of vanadium is relatively low; from the utilization angle of iron resources, most of molten iron produced by the traditional process produces products with lower added values due to complex components.
The invention content is as follows:
The invention overcomes the defects of different process flows and provides a method for separating and enriching vanadium and producing pure iron from iron ore concentrate, pure iron and vanadium-enriched slag can be directly produced and obtained by the method, the process flow is short, and the recovery rate of vanadium and iron is high.
The technical scheme of the invention is as follows:
The technical scheme of the invention comprises the steps of drying the vanadium titano-magnetite pellet, directly reducing the vanadium titano-magnetite pellet in a coal-based shaft furnace and enriching the melting component in an electric arc furnace, and is characterized in that the vanadium titano-magnetite pellet dried by the pellet is selectively reduced in the coal-based shaft furnace to obtain a metallized pellet, and then the metallized pellet is subjected to melting component enrichment in the electric arc furnace.
The iron ore concentrate refers to vanadium-titanium magnetite and common iron ore concentrate, and the vanadium-titanium magnetite is taken as an example, and the technical scheme of the common iron concentrate is similar.
The technical scheme of the invention comprises the steps of drying the vanadium titano-magnetite pressed pellets, directly reducing the pressed pellets in a coal-based shaft furnace and enriching the melt in an electric arc furnace, and is characterized in that the iron ore concentrate pellets after the pressed pellets are dried are subjected to selective reduction in the coal-based shaft furnace to obtain metallized pellets, and then the metallized pellets are subjected to melt separation in the electric arc furnace.
The vanadium titano-magnetite press-ball drying refers to: the vanadium titano-magnetite is used as a raw material, the binder and the raw material are mixed, the mixture is uniformly mixed and pressed into balls, and the balls are dried by using the waste heat of the high-temperature flue gas of the coal-based shaft furnace.
The selective reduction of the coal-based shaft furnace is as follows: the dried pellets are naturally mixed with a reducing agent and a desulfurizing agent according to the proportion (about 1:0.4:0.02) to form charging materials, the charging materials are added into a reduction chamber of a coal-based shaft furnace according to the process requirement, the charging materials are reduced for 8 to 9 hours at the temperature of 1100 to 1250 ℃, and products are discharged through inert gas protective cooling; magnetically separating the furnace charge discharged from the shaft furnace to obtain metallized pellets and a reducing agent; after the reducing agent is classified, large particles are used as the reducing agent for recycling, iron is reduced to the maximum extent in the reduction process, and vanadium is still in the form of oxide without being reduced.
The melting separation iron and vanadium separation of the electric arc furnace is as follows: the metallized pellet produced by direct reduction in the shaft furnace is operated by an electric arc furnace melting and separating smelting process, so that vanadium is effectively kept in a slag phase in an oxide form, and the purpose of enriching vanadium slag is achieved. Meanwhile, the molten steel obtained by melting the sponge iron has high purity, the iron content reaches more than 99.7 percent, and the molten steel has low contents of phosphorus, sulfur, silicon, manganese and titanium, so that the method can be used for producing industrial pure iron or military pure iron.
The electric furnace slag refers to vanadium-rich slag (when the raw material is vanadium-titanium magnetite) and common electric furnace slag (when the raw material is common iron fine powder).
The invention innovatively proposes the short-flow process of 'selective reduction of a coal-based shaft furnace and melting separation of an electric arc furnace' to produce, vanadium directly enters slag in the melting separation process, the process that the vanadium is reduced to enter molten iron and is oxidized again to enter the slag is avoided, the recovery rate of the vanadium is greatly improved, and meanwhile, high-purity industrial pure iron is produced in the process.
According to the carbon content of the metallized pellets produced by direct reduction of the coal-based shaft furnace, the metallized pellets can be divided into low-carbon vanadium-titanium metallized pellets and high-carbon vanadium-titanium metallized pellets. Aiming at pellets with different carbon contents in the smelting process of the electric arc furnace, different smelting process operations can be adopted, and the method specifically comprises the following steps: measures such as large-flow oxygen supply, iron ore addition, soda ash addition and the like are matched with a reasonable power supply system, so that the purpose of vanadium slag enrichment is realized.
normally producing to obtain low-carbon pellets: smelting metallized pellet in arc furnace, smelting in arc furnace directly, adding vanadium into molten steel with vanadium content below 0.06%, and smelting in low carbon pellet slag2O5The content is 5.88 to 6.08 percent, the high-carbon pellet vanadium completely enters molten steel, and V in slag2O5The content is very low.
Production is unstable, high carbon pellets appear: the metallized pellet is smelted by an electric arc furnace, the electric arc furnace is directly smelted and separated, and different smelting process operations can be adopted, and the method specifically comprises the following steps: temperature control, large-flow oxygen supply, iron ore addition, soda ash addition and the like, and reasonable power supply system matching, thereby realizing the purpose of vanadium slag enrichment.
the influence of different oxygen supply flow rates on vanadium: when oxygen is supplied at a small flow, the vanadium content in the steel is slowly reduced; after the oxygen supply flow is increased, the oxidation effect is obviously improved, and the vanadium content in the steel is rapidly reduced. V in slag under large-flow oxygen supply2O5the content is 3.61-5.16%. V in slag under small flow oxygen supply2O5The content is 2.70-2.90%. The vanadium content of the molten steel is reduced rapidly under the condition of large-flow oxygen supply, and the vanadium extraction and slag feeding efficiency is better.
The addition of soda ash affects vanadium: during the vanadium extraction process, the addition of the soda ash can promote the oxidation of vanadium into slag. Under the conditions that the carbon content of the pellets is high, the temperature of a carbon-oxygen reaction molten pool generated by oxygen blowing is high, and vanadium extraction is not facilitated, the aim of extracting vanadium under high carbon content can be realized by considering adding soda ash, and after soda ash is added to the slag surface, the vanadium content in steel is rapidly reduced, which shows that soda ash is beneficial to vanadium extraction.
The influence of adding iron ore on vanadium: in the process of smelting metallized pellets in an electric arc furnace, oxygen can be supplied by adding iron ore in addition to blowing oxygen into a molten pool. The iron ore can not only supply oxygen to the molten pool, but also adjust the temperature of the molten pool, and is beneficial to extracting vanadium and feeding slag. The iron ore is added into the furnace burden, so that the vanadium content in steel during melting can be obviously reduced, the pressure of blowing oxygen to extract vanadium after melting is reduced, and the process goal of extracting vanadium and adding slag is facilitated.
When the raw material is common fine iron powder, the pure iron and the electric furnace slag are obtained by adopting the process.
The invention innovatively provides that a short-flow process of 'selective reduction of a coal-based shaft furnace and melting separation of an electric arc furnace' is adopted to enrich pure iron and vanadium, vanadium is kept in a slag phase in the reduction process, vanadium directly enters slag in an oxide form in the melting separation process, the recovery rate of vanadium elements is greatly improved, the recovery rate of vanadium in the traditional vanadium-containing molten iron vanadium extraction process is only 46%, the recovery rate of vanadium in the invention can reach more than 93%, and the grade of vanadium slag is about 6-8%. Meanwhile, the molten steel obtained by melting and separating has high purity, the iron content reaches more than 99.7 percent, and the molten steel has low contents of phosphorus, sulfur, silicon, manganese and titanium, so that the magnetic pure iron and the military pure iron can be produced by simple refining, and the production cost is low.
The metallized pellet produced by direct reduction of the coal-based shaft furnace has good conductivity, the arc striking in the electric arc furnace is smooth, the process route for melting and separating the vanadium-titanium metallized pellet by the electric arc furnace is feasible, and the recycling of vanadium is realized.
According to the carbon content of the metallized pellets produced by direct reduction of the coal-based shaft furnace, the metallized pellets can be divided into low-carbon vanadium-titanium metallized pellets and high-carbon vanadium-titanium metallized pellets. Aiming at pellets with different carbon contents in the smelting process of the electric arc furnace, different smelting process operations can be adopted, and the method specifically comprises the following steps: measures such as large-flow oxygen supply, iron ore addition, soda ash addition and the like are matched with a reasonable power supply system, so that the purpose of vanadium slag enrichment is realized.
Normally producing to obtain low-carbon pellets: smelting metallized pellet in arc furnace, smelting in arc furnace directly, adding vanadium into molten steel with vanadium content of 0.067%, and smelting in low carbon pellet slag with V content2O5The content is 5.88 to 6.08 percent, the high-carbon pellet vanadium completely enters molten steel, and V in slag2O5The content is very low. Production is unstable, high carbon pellets appear: the metallized pellet is smelted by an electric arc furnace, the electric arc furnace is directly smelted and separated, and different smelting process operations can be adopted, and the method specifically comprises the following steps: measures such as large-flow oxygen supply, iron ore addition, soda ash addition and the like are matched with a reasonable power supply system, so that the purpose of vanadium slag enrichment is realized.
The influence of different oxygen supply flow rates on vanadium: when oxygen is supplied at a small flow, the vanadium content in the steel is slowly reduced; after the oxygen supply flow is increased, the oxidation effect is obviously improved, and the vanadium content in the steel is rapidly reduced. V in slag under large-flow oxygen supply2O5The content is 3.61-5.16%. V in slag under small flow oxygen supply2O5The content is 2.70-2.90%. The vanadium content of the molten steel is reduced rapidly under the condition of large-flow oxygen supply, and the vanadium extraction and slag feeding efficiency is better.
The addition of soda ash affects vanadium: during the vanadium extraction process, the addition of the soda ash can promote the oxidation of vanadium into slag. Under the conditions that the carbon content of the pellets is high, the temperature of a carbon-oxygen reaction molten pool generated by oxygen blowing is high, and vanadium extraction is not facilitated, the aim of extracting vanadium under high carbon content can be realized by considering adding soda ash, and after soda ash is added to the slag surface, the vanadium content in steel is rapidly reduced, which shows that soda ash is beneficial to vanadium extraction.
The influence of adding iron ore on vanadium: in the process of smelting metallized pellets in an electric arc furnace, oxygen can be supplied by adding iron ore in addition to blowing oxygen into a molten pool. The iron ore can not only supply oxygen to the molten pool, but also adjust the temperature of the molten pool, and is beneficial to extracting vanadium and feeding slag. The iron ore is added into the furnace burden, so that the vanadium content in steel during melting can be obviously reduced, the pressure of blowing oxygen to extract vanadium after melting is reduced, and the process goal of extracting vanadium and adding slag is facilitated.
Description of the drawings:
FIG. 1 is a process flow diagram of the present invention.
The specific implementation mode is as follows:
The invention is further illustrated by the following examples:
1. Combining the process flow chart of the invention, vanadium-titanium magnetite concentrate (component: TFe 64.38% FeO 29.67% Fe) is processed according to weight percentage2O3 59.08％TiO2 2.98％V2O50.95 percent) and a binder are mixed according to a certain proportion (about 1:0.05) and are mixed uniformly, after the mixture is pressed into balls and dried by the waste heat of flue gas, a reducing agent, a desulfurizing agent and dry balls are mixed according to a certain proportion and are fed into a coal-based shaft furnace, the reducing temperature is kept at 1100-1250 ℃, the reducing time is controlled to be about 8-9h, the average metallization rate of the product is 93.59 percent, and the enrichment of vanadium slag and the high recovery rate of vanadium can be realized by direct melt separation or melt separation under a small amount of metallurgical operation; the recovery rate of vanadium can reach 93.29 percent, and the grade of vanadium slag is 6.4 percent. In addition, the molten steel has the components of 99.75 percent, less than 0.001 percent of silicon, less than 0.001 percent of manganese and 0.004 percent of phosphorus.
2. Combining the process flow chart of the invention, vanadium-titanium magnetite concentrate (component: TFe 61.88% FeO 25.04% Fe) is processed according to weight percentage2O3 60.65％TiO2 3.33％V2O50.91%) and binder, according to a certain proportion (about 1:0.05), blending and uniformly mixing, pressing into balls, drying by using the waste heat of flue gas, then proportionally mixing reducing agent, desulfurizing agent and dry balls, feeding into a coal-based shaft furnace, keeping the reduction temperature at 1100-1250 ℃, controlling the reduction time to be about 8-9h, controlling the average metallization rate of the product to be 92.89%, and carrying out less metallizationThe enrichment of vanadium slag and the high recovery rate of vanadium are realized by melting under the metallurgical operation; the recovery rate of vanadium is 93.08%, and the grade of vanadium slag is 6.0%. In addition, the molten steel has the components of 99.71 percent, less than 0.001 percent of silicon, less than 0.001 percent of manganese and 0.004 percent of phosphorus.
3. Vanadium titano-magnetite metallized pellet produced by selective reduction of electric arc furnace melting coal-based shaft furnace (according to weight percentage, MD 95.9%, FeO 4.49%, V)2O51.20 percent and 0.67 percent of C), the carbon content of the pellets is lower, the pellets have good slag fluidity in an electric arc furnace and good slag-iron separation effect under the condition of no metallurgical operation in the melting and separating process of the electric arc furnace, and finally the vanadium content in steel is lower than 0.07 percent, the vanadium slag grade is 7.28 percent and the recovery rate of vanadium is more than 93 percent. The iron grade in the molten steel is 99.72%, the silicon content is less than 0.001%, the manganese content is less than 0.001%, the phosphorus content is 0.004%, and the recovery rate of iron is 95.79%.
4. vanadium titano-magnetite metallized pellet produced by selective reduction of electric arc furnace melting separation coal-based shaft furnace (according to weight percentage, MD 95.8%, FeO 4.48%, V)2O51.18 percent and C1.61 percent), the carbon content of the pellets is higher, oxygen is supplied to the oxygen lance in a large flow and accumulated mode for 1 hour, 200Kg of iron ore and metallized pellets are mixed and fed into the furnace, and after the process operation of adding 120Kg of soda ash into a furnace door, the slag fluidity is good, the slag-iron separation effect is good, finally, the vanadium content in steel is lower than 0.09 percent, the vanadium slag grade is 6.16 percent, and the recovery rate of vanadium is more than 93 percent. The iron grade in the molten steel is 99.70 percent, the phosphorus is 0.004 percent, the sulfur is 0.03 percent, and the recovery rate of iron is 96 percent.
5. Combining the process flow chart of the invention, iron ore concentrate (composition: TFe 63.18% FeO 23.40% CaO0.59% MgO 0.51% Al) is mixed according to weight percentage2O31.76 percent) and a binder, are mixed according to a certain proportion (about 1:0.05), are pressed into balls, are dried by the waste heat of flue gas, are mixed with a reducing agent, a desulfurizing agent and dry balls according to a certain proportion and are fed into a coal-based shaft furnace, the reducing temperature is kept between 1100 and 1250 ℃, the reducing time is controlled to be about 7 to 8 hours, and the average metallization rate of the product is more than 96 percent. The vanadium titano-magnetite metallized pellet produced by selective reduction of the coal-based shaft furnace is melted and separated by the electric arc furnace, and the slag fluidity in the electric arc furnace is good and the slag-iron separation effect is good under the condition of no metallurgical operation, so that the vanadium titano-magnetite metallized pellet can be finally produced by the selective reduction of the coal-based shaft furnaceThe iron grade in the molten steel is 99.8 percent, the phosphorus content is below 0.004 percent, and the recovery rate of iron is 97 percent.
The invention innovatively proposes a short-flow process of 'selective reduction of a coal-based shaft furnace and melting separation of an electric arc furnace' to produce, vanadium directly enters slag in the melting separation process, the vanadium is prevented from being reduced and entering molten iron to be oxidized again and entering the slag, and the recovery rate of the vanadium is greatly improved.
The metallized pellet produced by direct reduction of the coal-based shaft furnace has good conductivity, the arc striking in the electric arc furnace is smooth, the process route of melting and separating the vanadium-titanium metallized pellet by the electric arc furnace is feasible, and the melting and separating oxygen blowing process can realize vanadium extraction and slag entering and vanadium recycling.
Claims (6)
1. A method for separating and enriching vanadium and producing pure iron from iron ore concentrate is characterized by comprising the following steps: the method adopts a short flow process of coal-based shaft furnace selective reduction and electric arc furnace melting separation to produce pure iron and enriched vanadium, so that the vanadium is kept in a slag phase in the selective reduction process of the coal-based shaft furnace, and the vanadium directly enters slag in an oxide form in the melting separation process of the electric arc furnace.
2. The method as claimed in claim 2, wherein the vanadium titano-magnetite pellet is obtained after drying the pressed pellet, the vanadium titano-magnetite pellet is directly reduced by a coal-based shaft furnace to obtain a metallized pellet, and the metallized pellet is subjected to melt separation and enrichment in an electric arc furnace.
3. The method of claim 2, wherein the vanadium titano-magnetite pellet drying is: the vanadium-titanium magnetite powder is used as a raw material, the binder and the raw material are mixed, uniformly mixed and pressed into balls, and the balls are dried by using the waste heat of the high-temperature flue gas of the coal-based shaft furnace.
4. The method of claim 2, wherein the selective reduction of the coal-based shaft furnace is: naturally mixing the dried pellets, a reducing agent and a desulfurizing agent according to the proportion of 1:0.4:0.02 to form furnace charge, adding the furnace charge into a reduction chamber of a coal-based shaft furnace, reducing for 8 to 9 hours at the temperature of 1050 to 1250 ℃, and discharging the product through inert gas protective cooling; and magnetically separating the furnace charge discharged from the coal-based shaft furnace to obtain metallized pellets and a reducing agent.
5. The method of claim 4, wherein the reductant is selectively classified such that large particles are recycled as reductant and iron is reduced to a maximum extent during reduction while vanadium is not reduced and remains in the form of oxides.
6. The method of claim 2, wherein the melting and enriching in the electric arc furnace is performed by: the metallized pellet produced by direct reduction of the coal-based shaft furnace is smelted by melting in an electric arc furnace, and vanadium continuously enters a slag phase in an oxide form, so that the purpose of enriching vanadium slag is realized.
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Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
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| CN111961803A (en) * | 2020-09-08 | 2020-11-20 | 中冶赛迪工程技术股份有限公司 | Production process and method of industrial pure iron |
| CN112024121A (en) * | 2020-08-31 | 2020-12-04 | 重庆优钛实业有限公司 | Vanadium titano-magnetite separation and extraction method |
| CN113981214A (en) * | 2021-11-16 | 2022-01-28 | 新疆葱岭钒钛有限公司 | Smelting method for preparing pellet vanadium titano-magnetite by internal carbon distribution |
| CN114480881A (en) * | 2022-01-18 | 2022-05-13 | 龙佰集团股份有限公司 | Method for extracting valuable elements in iron ore concentrate by wet-fire combined process |
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| CN114480881A (en) * | 2022-01-18 | 2022-05-13 | 龙佰集团股份有限公司 | Method for extracting valuable elements in iron ore concentrate by wet-fire combined process |
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