CN109279606A - Promote the method that TiC grows up in slag - Google Patents

Promote the method that TiC grows up in slag Download PDF

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Publication number
CN109279606A
CN109279606A CN201811284895.0A CN201811284895A CN109279606A CN 109279606 A CN109279606 A CN 109279606A CN 201811284895 A CN201811284895 A CN 201811284895A CN 109279606 A CN109279606 A CN 109279606A
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Prior art keywords
slag
tic
titanium
promote
titanium carbide
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CN201811284895.0A
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王东生
张溅波
赵青娥
黄家旭
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Pangang Group Panzhihua Iron and Steel Research Institute Co Ltd
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Pangang Group Panzhihua Iron and Steel Research Institute Co Ltd
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    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B32/00Carbon; Compounds thereof
    • C01B32/90Carbides
    • C01B32/914Carbides of single elements
    • C01B32/921Titanium carbide
    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22BPRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B7/00Working up raw materials other than ores, e.g. scrap, to produce non-ferrous metals and compounds thereof; Methods of a general interest or applied to the winning of more than two metals
    • C22B7/001Dry processes
    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22BPRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B7/00Working up raw materials other than ores, e.g. scrap, to produce non-ferrous metals and compounds thereof; Methods of a general interest or applied to the winning of more than two metals
    • C22B7/04Working-up slag
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01PINDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
    • C01P2004/00Particle morphology
    • C01P2004/60Particles characterised by their size
    • C01P2004/61Micrometer sized, i.e. from 1-100 micrometer
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01PINDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
    • C01P2006/00Physical properties of inorganic compounds
    • C01P2006/80Compositional purity
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P10/00Technologies related to metal processing
    • Y02P10/20Recycling

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Organic Chemistry (AREA)
  • Geology (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Manufacturing & Machinery (AREA)
  • General Life Sciences & Earth Sciences (AREA)
  • Materials Engineering (AREA)
  • Mechanical Engineering (AREA)
  • Metallurgy (AREA)
  • Environmental & Geological Engineering (AREA)
  • Inorganic Chemistry (AREA)
  • Manufacture And Refinement Of Metals (AREA)

Abstract

The present invention relates to the method that TiC grows up in slag is promoted, belong to titanium field of smelting.Present invention solves the technical problem that being that TiC partial size prepared by Ti-containing slag carbon thermal reduction is smaller, cause the difficulty of subsequent purification enrichment TiC big.The present invention discloses the method for promoting that TiC grows up in titanium slag smelting, during titaniferous materials carbon thermal reduction prepares titanium carbide clinker, the electric stove dust ash generated in smelting process is added in electric furnace, is smelted together with titaniferous materials, reducing agent, titanium carbide clinker is prepared.More high-grade carbonization titanium products can be obtained up to 7~30 μm, through wet magnetic separation in the titanium carbide granule that the present invention is prepared, and the dedusting ash that the present invention can generate smelting process is effectively recycled, and alleviate environmental pressure.

Description

Promote the method that TiC grows up in slag
Technical field
The invention belongs to titanium field of smelting, and in particular to promote the method that TiC grows up in slag.
Background technique
Panxi Diqu titanium resource is abundant, and a large amount of Ti-containing slags, such as high-titanium blast furnace slag are generated during development and utilization In contain TiO220%~26%, TiO is contained in titanium slag electric furnace dedusting ash220%~35% etc..It is domestic many for clinker containing titanium-type Research institution had once carried out a variety of researchs for mentioning titanium technology path, for example produce silicotitanium, production cinder microcrystalline glass etc., but Processing capacity is limited, cannot fundamentally solve the problem of complex utilization of Ti-containing slag.Currently, " high temperature cabonization-is low for Ti-containing slag TiCl is produced in warm chlorination4" process route be most industrialization prospect technology path, technique be divided into high temperature cabonization, low temperature boiling Three steps of utilization for rising chlorination and chloride residue have many advantages, such as that process is short, treating capacity is big, titanium resource comprehensive utilization ratio is high.
In Ti-containing slag, " high temperature cabonization-low temperature chlorination produces TiCl4" technique in, high temperature cabonization mainly will be in clinker Titanium dioxide is changed into titanium carbide, obtains titanium carbide clinker, is further used for low temperature chlorination and prepares titanium tetrachloride.By in raw material TiO2The influence of content, the TiC grade in titanium carbide clinker obtained is lower, leads to chlorination efficiency during subsequent low temperature chlorination Low, chlorine consumes big, chlorination higher cost, therefore needs further to sort or be enriched in titanium carbide slag before low temperature chlorination technique TiC.However, since the TiC particle size in titanium carbide clinker is smaller, usually 0.2 μm~10 μm, and Dispersed precipitate exists In slag, when the TiC in titanium carbide clinker is sorted or is enriched with, the difficulty using techniques such as magnetic separation, acidleach is larger.
Various dedusting ash, including sintering dust separation ash, blast furnace dedusting ash, converter dust-removing ash, electric furnace can be generated in steel production Dedusting ash etc..If the dedusting ash generated in titanium slag smelting process contains 25%~40% ilmenite concentrate, can with after pelletizing back into Furnace is smelted.Patent document CN104310535A discloses the resource utilization method of a kind of blast furnace dedusting ash and coking dedusting ash, Blast furnace process dedusting ash and coking dedusting ash are granulated and are sintered, the degradation for organic matter in coking wastewater.Patent document CN107385222A discloses a kind of utilization method of carbon containing dedusting ash of rotary kiln, carbon containing dedusting ash is covered in pelletizing surface or Person and the balling process for being directly used in lateritic nickel ore.Dedusting ash is different according to its source technique, and ingredient is also corresponding different, partially removes For dust since valuable element content is low, utilization is at high cost, is mostly handled using heap abandoning.
Summary of the invention
Present invention solves the technical problem that being that TiC partial size prepared by Ti-containing slag carbon thermal reduction is smaller, lead to subsequent purification The difficulty for being enriched with TiC is big.
Technical proposal that the invention solves the above-mentioned problems is to provide the method for promoting that TiC grows up in slag, in titaniferous materials During preparing titanium carbide clinker by carbon thermal reduction, the electric stove dust ash generated in smelting process is added in electric furnace, with Titaniferous materials, reducing agent are smelted together, and cooling of slagging tap after smelting obtains titanium carbide clinker.
Wherein, in titaniferous materials content of titanium dioxide between 15%~45%.
It wherein, include fixed carbon 10~45%, K in dedusting ash2O 5~18%, Na2O 5~15%.
Wherein, reducing agent is carbonaceous reducing agent, selects coke powder, lean coal, at least one of anthracite, usage amount by C with TiO21.3~1.4 times of determinations of chemical reaction metering ratio.
Wherein, reducing agent control adds in 50~75min, and the control of present invention temperature is added 1550 DEG C~1600 ℃。
Wherein, it is 1620 DEG C~1670 DEG C that bath temperature is promoted after reducing agent adds, 25~50min of duration.
Wherein, it is slagged tap cooling after smelting by slag pan.
Wherein, single slag pan volume > 8t, single > 10h slag pan cooling time.
Beneficial effects of the present invention:
The present invention by titanium slag smelting process be added smelting process generate dedusting ash, through carbon thermal reduction, slag tap it is cold But the titanium carbide granule being prepared is up to 7~30 μm;The titanium carbide that the present invention is prepared is available higher through wet magnetic separation The carbonization titanium products of grade can reduce chlorine consumption and level of residue for producing titanium tetrachloride, improve chlorination efficiency, final to realize The efficient utilization of titanium carbide slag, improves the comprehensive utilization ratio of titanium resource;The present invention can carry out the dedusting ash that smelting process generates It is effective to recycle, alleviate environmental pressure.
Specific embodiment
Electric furnace smelting titaniferous materials prepare the electric stove dust ash of generation 1%~3% during titanium carbide slag, pass through detection point Analysis discovery, the main component of electric stove dust ash include dust pelletizing system take out damage reducing agent, reducing agent burn ash content and CaO、MgO、Al2O3Ingredients are waited, the constituent contents such as C, Na and K are higher in dedusting ash.
The present invention provides the method for promoting that TiC grows up in titanium slag smelting, passes through carbon thermal reduction in titaniferous materials and prepares carbonization During titanium clinker, the electric stove dust ash generated in smelting process is added in electric furnace, the smelting together with titaniferous materials, reducing agent Refining, cooling of slagging tap after smelting obtain titanium carbide clinker.
The dedusting ash that smelting process generates is using the upper common processing collection process of metallurgy, and specially ash-laden gas is through cooling Enter dust collecting system afterwards, dedusting ash enters in ash cellar, and flue gas direct emission up to standard is collected.
Wherein, in titaniferous materials content of titanium dioxide between 15%~45%.Titaniferous materials can be according to different works What skill obtained contains TiO2Industrial slags, the titaniferous materials that the present invention uses can be what smelting vanadium-titanium magnetite by blast furnace obtained Electric furnace melting slag that blast furnace slag, direct-reduction vanadium titano-magnetite obtain, the dedusting ash of smelting titanium slag with electric stove, in low-grade ilmenite One or more.
It wherein, include fixed carbon 10~45%, K in dedusting ash2O 5~18%, Na2O 5~15%.
Wherein, reducing agent is carbonaceous reducing agent, selects at least one of coke powder, lean coal, anthracite, usage amount is according to C With TiO21.2~1.3 times of determinations of chemical reaction metering ratio.
Wherein, electric stove dust ash can titaniferous materials addition after heating initial stage be added, can also material formed molten bath after, It is added together with reducing agent.
Wherein, add the reducing agent stage of reaction, control reaction temperature is 1550 DEG C~1600 DEG C, reducing agent control 50~ It is added in 75min.
Wherein, promotion bath temperature is 1620 DEG C~1670 DEG C after adding reducing agent, 25~50min of duration.
The generation phase of TiC crystal grain occurs mainly in the reducing agent stage of reaction, then promotes bath temperature, may advantageously facilitate TiC crystal grain is grown up.
Wherein, smelting the titanium carbide slag for completing to obtain needs Slow cooling in slag pan, so that titanium carbide granule is further grown Big enrichment, cooling velocity are indirectly controlled by slag pan volume, preferably, single slag pan volume > 8t, single slag pan are cooling Time > 10h.
The following further explains the present invention by way of examples.
Embodiment 1
Electric furnace smelting high-titanium blast furnace slag prepares titanium carbide slag, TiO in high-titanium blast furnace slag2Content 22.5%, additional amount For 25.3t, using metallurgical coke as reducing agent, carbon content 81.3% is fixed in coke powder, is 4100kg, electric stove dust with dosage Grey usage amount 600kg contains fixed carbon 22.3%, K in dedusting ash2O 16.5%, Na2O 13.6% and other Al, Si, Ca, Mg Oxide, be added after being mixed with reducing agent.Add the reducing agent stage of reaction, reaction temperature is 1550 DEG C~1600 DEG C, time control System adds in 50min, and promotion bath temperature is 1620 DEG C~1670 DEG C after adding reducing agent, duration 30min.Carbonization is anti- After should reaching home, open slag notch, titanium carbide slag flowed into Slow cooling in slag pan, by the titanium carbide slag after cooling 12h into Row is broken, and the granularity for measuring TiC particle in titanium carbide slag is 7~20 μm, and carbonization Ti content 36.5% is obtained after wet magnetic separation Titanium carbide slag product.
Embodiment 2
Electric furnace smelting Ti-containing slag prepares titanium carbide slag, Ti-containing slag TiO2Content 31.2%, additional amount 22.7t, is adopted It uses metallurgical coke as reducing agent, fixes carbon content 81.3% in coke powder, be 6000kg, electric stove dust ash usage amount with dosage 600kg contains fixed carbon 30.7%, K in dedusting ash2O 11.6%, Na2The oxidation of O 10.7% and other Al, Si, Ca, Mg Object, electric stove dust ash are added after mixing with reducing agent.Adding the reducing agent stage of reaction, reaction temperature is 1550 DEG C~1600 DEG C, when Between control and added in 60min, adding and promoting bath temperature after reducing agent is 1620 DEG C~1670 DEG C, duration 40min.Carbon After change reaction is reached home, slag notch is opened, titanium carbide slag is flowed into Slow cooling in slag pan, by the titanium carbide after cooling 12h Slag is crushed, and the granularity for measuring TiC particle in titanium carbide slag is 9~24 μm, and carbonization Ti content is obtained after wet magnetic separation 52.7% titanium carbide slag product.
Embodiment 3
Electric furnace smelting Ti-containing slag prepares titanium carbide slag, Ti-containing slag TiO2Content 41.8%, additional amount 20.4t, is adopted It uses metallurgical coke as reducing agent, fixes carbon content 81.3% in coke powder, be 6200kg, electric stove dust ash usage amount with dosage 600kg contains fixed carbon 40.3%, K in dedusting ash2O 10.7%, Na2The oxide of O 8.4% and other Al, Si, Ca, Mg, It is added after being mixed with reducing agent.Add the reducing agent stage of reaction, reaction temperature is 1550 DEG C~1600 DEG C, and the time controls in 75min It inside adds, promotion bath temperature is 1620 DEG C~1670 DEG C after adding reducing agent, duration 50min.Carburizing reagent reaches eventually After point, slag notch is opened, titanium carbide slag is flowed into Slow cooling in slag pan, the titanium carbide slag after cooling 12h is crushed, is surveyed The granularity for obtaining TiC particle in titanium carbide slag is 12~28 μm, and the titanium carbide slag of carbonization Ti content 66.4% is obtained after wet magnetic separation Product.

Claims (7)

1. promoting the method that TiC grows up in slag, it is characterised in that: prepare titanium carbide clinker by carbon thermal reduction in titaniferous materials During, the dedusting ash generated in smelting process is added in electric furnace, is smelted together with titaniferous materials, reducing agent, knot is smelted Cooling of slagging tap after beam obtains titanium carbide clinker.
2. according to claim 1 promote the method that TiC grows up in slag, it is characterised in that: two in the titaniferous materials Titanium oxide content is between 15%~45%.
3. according to claim 1 or 2 promote the method grown up of TiC in slag, it is characterised in that: in the dedusting ash with Mass percent meter includes fixed carbon 10~45%, K2O 5~18%, Na2O 5~15%.
4. described in any item according to claim 1~3 promote the method that TiC grows up in slag, it is characterised in that: the reduction Agent is carbonaceous reducing agent, selects at least one of coke powder, lean coal, anthracite, and usage amount presses C and TiO2Chemical reaction metering ratio 1.3~1.4 times of determinations.
5. according to any one of claims 1 to 4 promote the method that TiC grows up in slag, it is characterised in that: the reduction Agent control adds in 50~75min, and the control of present invention temperature is added at 1550 DEG C~1600 DEG C.
6. described in any item according to claim 1~5 promote the method that TiC grows up in slag, it is characterised in that: the reduction Agent promotes bath temperature after adding be 1620 DEG C~1670 DEG C, 25~50min of duration.
7. described in any item according to claim 1~6 promote the method that TiC grows up in slag, it is characterised in that: smelting terminates It is slagged tap cooling by slag pan afterwards, single slag pan volume > 8t, single > 10h slag pan cooling time.
CN201811284895.0A 2018-10-31 2018-10-31 Promote the method that TiC grows up in slag Pending CN109279606A (en)

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Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110156019A (en) * 2019-06-21 2019-08-23 攀钢集团攀枝花钢铁研究院有限公司 It is used to prepare the electric arc furnaces and titanium carbide slag preparation method of titanium carbide slag
CN111573718A (en) * 2020-05-25 2020-08-25 攀钢集团攀枝花钢铁研究院有限公司 Treatment method of titanium extraction tailings
CN111650329A (en) * 2020-06-17 2020-09-11 攀钢集团攀枝花钢铁研究院有限公司 Method for judging Ti-containing blast furnace slag high-temperature carbonization smelting end point
CN111646499A (en) * 2020-06-29 2020-09-11 攀钢集团钒钛资源股份有限公司 Titanium extraction tailing washing treatment method
CN113462901A (en) * 2021-07-06 2021-10-01 攀钢集团攀枝花钢钒有限公司 Method for smelting titanium-containing slag

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20150064094A1 (en) * 2013-08-27 2015-03-05 Nano Tech Co., Ltd. Method of preparing titanium carbide powder
CN105256152A (en) * 2015-10-28 2016-01-20 攀钢集团攀枝花钢铁研究院有限公司 Method for quick reduction smelting of titaniferous furnace slag
CN105950804A (en) * 2016-07-18 2016-09-21 攀钢集团攀枝花钢铁研究院有限公司 Blast furnace slag reduction method
CN106517202A (en) * 2016-10-21 2017-03-22 攀钢集团攀枝花钢铁研究院有限公司 Preparation method of titanium carbide slag
CN107324336A (en) * 2017-09-01 2017-11-07 攀钢集团研究院有限公司 A kind of method that acid-dissolved titanium slag prepares titanium carbide
CN108677022A (en) * 2018-06-19 2018-10-19 苏州大学 A kind of method that sintering dust separation ash prepares removing harmful element during cementite

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20150064094A1 (en) * 2013-08-27 2015-03-05 Nano Tech Co., Ltd. Method of preparing titanium carbide powder
CN105256152A (en) * 2015-10-28 2016-01-20 攀钢集团攀枝花钢铁研究院有限公司 Method for quick reduction smelting of titaniferous furnace slag
CN105950804A (en) * 2016-07-18 2016-09-21 攀钢集团攀枝花钢铁研究院有限公司 Blast furnace slag reduction method
CN106517202A (en) * 2016-10-21 2017-03-22 攀钢集团攀枝花钢铁研究院有限公司 Preparation method of titanium carbide slag
CN107324336A (en) * 2017-09-01 2017-11-07 攀钢集团研究院有限公司 A kind of method that acid-dissolved titanium slag prepares titanium carbide
CN108677022A (en) * 2018-06-19 2018-10-19 苏州大学 A kind of method that sintering dust separation ash prepares removing harmful element during cementite

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110156019A (en) * 2019-06-21 2019-08-23 攀钢集团攀枝花钢铁研究院有限公司 It is used to prepare the electric arc furnaces and titanium carbide slag preparation method of titanium carbide slag
CN111573718A (en) * 2020-05-25 2020-08-25 攀钢集团攀枝花钢铁研究院有限公司 Treatment method of titanium extraction tailings
CN111573718B (en) * 2020-05-25 2022-07-26 攀钢集团攀枝花钢铁研究院有限公司 Treatment method of titanium extraction tailings
CN111650329A (en) * 2020-06-17 2020-09-11 攀钢集团攀枝花钢铁研究院有限公司 Method for judging Ti-containing blast furnace slag high-temperature carbonization smelting end point
CN111646499A (en) * 2020-06-29 2020-09-11 攀钢集团钒钛资源股份有限公司 Titanium extraction tailing washing treatment method
CN113462901A (en) * 2021-07-06 2021-10-01 攀钢集团攀枝花钢钒有限公司 Method for smelting titanium-containing slag

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Application publication date: 20190129