CN107858530A - A kind of antimony sulfide ore oxygen-enriched smelting method - Google Patents

A kind of antimony sulfide ore oxygen-enriched smelting method Download PDF

Info

Publication number
CN107858530A
CN107858530A CN201711242100.5A CN201711242100A CN107858530A CN 107858530 A CN107858530 A CN 107858530A CN 201711242100 A CN201711242100 A CN 201711242100A CN 107858530 A CN107858530 A CN 107858530A
Authority
CN
China
Prior art keywords
oxygen
enriched
sulfide ore
passed
antimony sulfide
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
CN201711242100.5A
Other languages
Chinese (zh)
Inventor
韦建初
韦竣严
兰岱龙
何正军
陆宏卫
曹应科
卢忠讲
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Guangxi Sheng Fu Antimony Industry Polytron Technologies Inc
Original Assignee
Guangxi Sheng Fu Antimony Industry Polytron Technologies Inc
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Guangxi Sheng Fu Antimony Industry Polytron Technologies Inc filed Critical Guangxi Sheng Fu Antimony Industry Polytron Technologies Inc
Priority to CN201711242100.5A priority Critical patent/CN107858530A/en
Publication of CN107858530A publication Critical patent/CN107858530A/en
Pending legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22BPRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B30/00Obtaining antimony, arsenic or bismuth
    • C22B30/02Obtaining antimony
    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22BPRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B5/00General methods of reducing to metals
    • C22B5/02Dry methods smelting of sulfides or formation of mattes
    • C22B5/10Dry methods smelting of sulfides or formation of mattes by solid carbonaceous reducing agents

Abstract

The invention discloses a kind of antimony sulfide ore oxygen-enriched smelting method, comprise the steps of:(1) it is 100 in mass ratio by the antimony sulfide ore after crushing, lime stone and quartz sand:20‑25:18 20 are mixed evenly, and obtain compound;(2) spherolite is made in compound, and is sent into oxygen-rich oxide stove and carries out oxidizing semlting, oxygen-enriched air is preheated to >=200 DEG C, and be passed through in oxygen-rich oxide stove, smelting temperature is 1000 DEG C 1200 DEG C, the 40min of melting 30, obtains melted gangue;(3) melted gangue is entered into oxygen-enriched reduction furnace by material trough, coal powder is put into oxygen-enriched reduction furnace, and be passed through and be preheated to >=200 DEG C of oxygen-enriched air, smelting temperature is 1250 DEG C 1350 DEG C, the 60min of melting 50, obtains reduced blast furnace;(4) reduced blast furnace is entered in fuming furnace by material trough, reclaims antimony.The oxygen-enriched air smelting technological process of the present invention simplifies, and by oxygen-enriched strengthening smelting, production efficiency greatly improves, and labor intensity is low, while power and Fuel Consumption are few.

Description

A kind of antimony sulfide ore oxygen-enriched smelting method
Technical field
The invention belongs to non-ferrous metal metallurgy technical field, more particularly to a kind of antimony sulfide ore oxygen-enriched smelting method.
Background technology
At present, in antimony sulfide ore oxidation furnace fusion process, substantial amounts of oxygen need to be provided and aoxidized with coke or metal Reaction, existing offering oxygen way is directly to be blasted air in stove with air blower.Due to oxygen concentration relatively low (only 21% in air Left and right), the useless composition such as nitrogen is high (up to 79%), smelting process is strengthened, and has taken away substantial amounts of heat energy, So that the technique is low (about 20t/m2.d) compared with other non-ferrous metal metallurgy technique unit capacities, energy consumption, high (the burnt rate of material consumption More than 30%, iron ore rate more than 50%), SO in waste gas2Concentration is low (0.8%-1.5%), is unfavorable for recovery comprehensive utilization, from And improve production cost.For antimony metal as a kind of small metal, production scale of enterprise is smaller, in smelting equipment technology relative to What the metals such as copper, lead, zinc fell behind at last, that environmental pollution serious, high energy consumption, metal recovery rate are low etc. be present.
The content of the invention
It is an object of the invention to:For above-mentioned problem, there is provided a kind of degree of oxidation is high, reduces pollution, simultaneously Improve the rate of recovery, the antimony sulfide ore oxygen-enriched smelting method that technique is simple, energy consumption is low.
In order to realize foregoing invention purpose, the technical solution adopted by the present invention is as follows:
A kind of antimony sulfide ore oxygen-enriched smelting method, is comprised the steps of:
(1) it is 100 in mass ratio by the antimony sulfide ore after crushing, lime stone and quartz sand:20-25:18-20 is mixed Uniformly, compound is obtained;
(2) spherolite is made in compound, spherolite then is sent into oxygen-rich oxide stove carries out oxidizing semlting, and oxygen-enriched air is pre- Heat is passed through in oxygen-rich oxide stove to >=200 DEG C, and smelting temperature is 1000 DEG C -1200 DEG C, after melting 30-40min, is stopped logical Enter oxygen-enriched air, be incubated 20-25min, obtain melted gangue;
(3) melted gangue is entered into oxygen-enriched reduction furnace by material trough, by melted gangue:Coal powder=10:0.5-1 matter Amount ratio, coal powder is put into oxygen-enriched reduction furnace, and be passed through and be preheated to >=200 DEG C of oxygen-enriched air, smelting temperature 1250 DEG C -1350 DEG C, after melting 50-60min, stopping is passed through oxygen-enriched air, is incubated 30-35min, obtains reduced blast furnace;
(5) reduced blast furnace is entered in fuming furnace by material trough, reclaims antimony;The cigarette ash of reduction melting process is by granulation Reduction melting process is returned afterwards.
It is preferred that the particle diameter of the spherolite is 15-20mm, water content 8-10%.
It is preferred that the lime stone ﹥ containing CaO 70%, quartz sand contain SiO2﹥ 80%.
It is preferred that the oxygenous volumetric concentration of oxygen-enriched air being passed through in oxygen-rich oxide stove is 50-85%, it is described oxygen-enriched Air using bottom blowing or it is side-blown by the way of be blown into oxygen-rich oxide stove.
It is preferred that the oxygenous volumetric concentration of oxygen-enriched air being passed through in oxygen-enriched reduction furnace is 50-85%, it is described oxygen-enriched Air using bottom blowing or it is side-blown by the way of be blown into oxygen-enriched reduction furnace.
It is preferred that the pressure in the oxygen-rich oxide stove is 0.1-0.3MPa, the pressure in the oxygen-enriched reduction furnace is 0.2-0.4MPa。
It is preferred that the average grain diameter of the coal powder is 0.5-4mm.
In summary, by adopting the above-described technical solution, the beneficial effects of the invention are as follows:
(1) antimony sulfide ore oxygen-enriched smelting method of the present invention is by improving in oxygen-enriched air the volumetric concentration of oxygen and to oxygen-enriched Air is preheated, so that the fusing of antimong-containing material, the volatilization oxidation reaction uniform velocity of antimony are accelerated, reactant in the unit interval Increase, and directly enter stove after concentrate and the granulation of auxiliary material dispensing, without sintering back powder operation;Therefore equipment disposal ability improves, so as to Cause various energy consumptions, the reduction of material consumption.
(2) present invention uses oxygen-rich oxide stove and oxygen-enriched reduction furnace simultaneously, and oxygen-enriched air is used into bottom blowing or side-blown Mode, oxidation and reduction all more can be fully carried out, improve metal recovery rate;By the way that melted gangue is directly entered by material trough Oxygen-enriched reduction furnace, the change of melt transporting mode, realize and seethe stirring, realize material non-clotted slag.
(3) oxygen-enriched air smelting technological process of the invention simplifies, and is not required to back powder and sintering circuit, oxidation furnace, reduction furnace pass through Oxygen-enriched strengthening smelting, so as to which production efficiency greatly improves, labor intensity is low, while power and Fuel Consumption are few.
Embodiment
For the objects, technical solutions and advantages of the present invention are more clearly understood, preferred embodiment is enumerated below, to this hair Bright further description.However, it is necessary to illustrate, many details listed in specification are used for the purpose of making reader to this The one or more aspects of invention have a thorough explanation, can also realize the present invention's even without these specific details These aspects.
Embodiment 1
A kind of antimony sulfide ore oxygen-enriched smelting method, is comprised the steps of:
(1) it is 100 in mass ratio by the antimony sulfide ore after crushing, lime stone and quartz sand:20:18 are mixed evenly, Obtain compound;Lime stone contains 75% CaO, and quartz sand contains 85% SiO2
(2) compound is made spherolite, the particle diameter of spherolite is 15mm, water content 8%;Then spherolite is sent into oxygen-enriched oxygen Change stove and carry out oxidizing semlting, oxygen-enriched air is preheated to 300 DEG C, and be passed through in oxygen-rich oxide stove, smelting temperature is 1000 DEG C, is melted After refining 40min, stopping is passed through oxygen-enriched air, is incubated 20min, obtains melted gangue;The oxygenous volumetric concentration of oxygen-enriched air is 70%, the oxygen-enriched air is blown into oxygen-rich oxide stove by the way of bottom blowing;
(3) melted gangue is entered into oxygen-enriched reduction furnace by material trough, by melted gangue:Coal powder=10:0.5 quality Ratio, into oxygen-enriched reduction furnace putting into average grain diameter is 2mm coal powder, and is passed through and is preheated to 300 DEG C of oxygen-enriched air, melting Temperature is 1300 DEG C, and after melting 50min, stopping is passed through oxygen-enriched air, is incubated 30min, obtains reduced blast furnace;Oxygen-enriched air is oxygen-containing Air volume concentration is 70%, and the oxygen-enriched air is blown into oxygen-enriched reduction furnace by the way of bottom blowing;
(4) reduced blast furnace is entered in fuming furnace by material trough, reclaims antimony;The cigarette ash of reduction melting process is by granulation Reduction melting process is returned afterwards.
The present embodiment actual production effectively feeds intake operating rate > 95%, and the antimony metal rate of recovery is up to 91%.
Embodiment 2
A kind of antimony sulfide ore oxygen-enriched smelting method, is comprised the steps of:
(1) it is 100 in mass ratio by the antimony sulfide ore after crushing, lime stone and quartz sand:25:20 are mixed evenly, Obtain compound;Lime stone contains 80% CaO, and quartz sand contains 90% SiO2
(2) compound is made spherolite, the particle diameter of spherolite is 15mm, water content 8%;Then spherolite is sent into oxygen-enriched oxygen Change stove and carry out oxidizing semlting, oxygen-enriched air is preheated to 500 DEG C, and be passed through in oxygen-rich oxide stove, smelting temperature is 1200 DEG C, is melted After refining 30min, stopping is passed through oxygen-enriched air, is incubated 25min, obtains melted gangue;The oxygenous volumetric concentration of oxygen-enriched air is 50%, the oxygen-enriched air is blown into oxygen-rich oxide stove by the way of bottom blowing;
(3) melted gangue is entered into oxygen-enriched reduction furnace by material trough, by melted gangue:Coal powder=10:1 mass ratio Example, coal powder of the average grain diameter for 4mm is put into oxygen-enriched reduction furnace, and be passed through and be preheated to 500 DEG C of oxygen-enriched air, melting temperature Spend for 1250 DEG C, after melting 60min, stopping is passed through oxygen-enriched air, is incubated 35min, obtains reduced blast furnace;Oxygen-enriched air is oxygenous Volumetric concentration is 50%, and the oxygen-enriched air is blown into oxygen-enriched reduction furnace by the way of bottom blowing;
(4) reduced blast furnace is entered in fuming furnace by material trough, reclaims antimony;The cigarette ash of reduction melting process is by granulation Reduction melting process is returned afterwards.
The present embodiment actual production effectively feeds intake operating rate > 95%, and the antimony metal rate of recovery is up to 90%.
Embodiment 3
A kind of antimony sulfide ore oxygen-enriched smelting method, is comprised the steps of:
(1) it is 100 in mass ratio by the antimony sulfide ore after crushing, lime stone and quartz sand:25:20 are mixed evenly, Obtain compound;Lime stone contains 85% CaO, and quartz sand contains 90% SiO2
(2) compound is made spherolite, the particle diameter of spherolite is 20mm, water content 10%;Then spherolite is sent into oxygen-enriched Oxidation furnace carries out oxidizing semlting, and oxygen-enriched air is preheated into 700 DEG C, and is passed through in oxygen-rich oxide stove, and smelting temperature is 1000 DEG C, After melting 40min, stopping is passed through oxygen-enriched air, is incubated 20min, obtains melted gangue;The oxygenous volumetric concentration of oxygen-enriched air is 85%, the oxygen-enriched air is blown into oxygen-rich oxide stove by the way of side-blown;
(3) melted gangue is entered into oxygen-enriched reduction furnace by material trough, by melted gangue:Coal powder=10:1 mass ratio Example, coal powder of the average grain diameter for 4mm is put into oxygen-enriched reduction furnace, and be passed through and be preheated to 700 DEG C of oxygen-enriched air, melting temperature Spend for 1350 DEG C, after melting 50min, stopping is passed through oxygen-enriched air, is incubated 30min, obtains reduced blast furnace;Oxygen-enriched air is oxygenous Volumetric concentration is 85%, and the oxygen-enriched air is blown into oxygen-enriched reduction furnace by the way of side-blown;
(4) reduced blast furnace is entered in fuming furnace by material trough, reclaims antimony;The cigarette ash of reduction melting process is by granulation Reduction melting process is returned afterwards.
The present embodiment actual production effectively feeds intake operating rate > 95%, and the antimony metal rate of recovery is up to 89.0%.
Embodiment 4
A kind of antimony sulfide ore oxygen-enriched smelting method, is comprised the steps of:
(1) it is 100 in mass ratio by the antimony sulfide ore after crushing, lime stone and quartz sand:20:18 are mixed evenly, Obtain compound;Lime stone contains 75% CaO, and quartz sand contains 85% SiO2
(2) compound is made spherolite, the particle diameter of spherolite is 20mm, water content 10%;Then spherolite is sent into oxygen-enriched Oxidation furnace carries out oxidizing semlting, and oxygen-enriched air is preheated into 200 DEG C, and is passed through in oxygen-rich oxide stove, and smelting temperature is 1000 DEG C, After melting 40min, stopping is passed through oxygen-enriched air, is incubated 20min, obtains melted gangue;The oxygenous volumetric concentration of oxygen-enriched air is 85%, the oxygen-enriched air is blown into oxygen-rich oxide stove by the way of side-blown;
(3) melted gangue is entered into oxygen-enriched reduction furnace by material trough, by melted gangue:Coal powder=10:1 mass ratio Example, coal powder of the average grain diameter for 4mm is put into oxygen-enriched reduction furnace, and be passed through and be preheated to 200 DEG C of oxygen-enriched air, melting temperature Spend for 1350 DEG C, after melting 50min, stopping is passed through oxygen-enriched air, is incubated 30min, obtains reduced blast furnace;Oxygen-enriched air is oxygenous Volumetric concentration is 85%, and the oxygen-enriched air is blown into oxygen-enriched reduction furnace by the way of side-blown;
(4) reduced blast furnace is entered in fuming furnace by material trough, reclaims antimony;The cigarette ash of reduction melting process is by granulation Reduction melting process is returned afterwards.
The present embodiment actual production effectively feeds intake operating rate > 95%, and the antimony metal rate of recovery is up to 90%.
Described above is only the preferred embodiment of the present invention, it is noted that for the ordinary skill people of the art For member, under the premise without departing from the principles of the invention, some improvements and modifications can also be made, these improvements and modifications also should It is considered as protection scope of the present invention.

Claims (7)

  1. A kind of 1. antimony sulfide ore oxygen-enriched smelting method, it is characterised in that:Comprise the steps of:
    (1) it is 100 in mass ratio by the antimony sulfide ore after crushing, lime stone and quartz sand:20-25:18-20 mixes equal It is even, obtain compound;
    (2) spherolite is made in compound, spherolite then is sent into oxygen-rich oxide stove carries out oxidizing semlting, and oxygen-enriched air is preheated to >=200 DEG C, and be passed through in oxygen-rich oxide stove, smelting temperature is 1000 DEG C -1200 DEG C, and after melting 30-40min, stopping is passed through richness Oxygen air, 20-25min is incubated, obtains melted gangue;
    (3) melted gangue is entered into oxygen-enriched reduction furnace by material trough, by melted gangue:Coal powder=10:0.5-1 mass ratio Example, puts into coal powder, and be passed through and be preheated to >=200 DEG C of oxygen-enriched air into oxygen-enriched reduction furnace, smelting temperature for 1250 DEG C- 1350 DEG C, after melting 50-60min, stopping is passed through oxygen-enriched air, is incubated 30-35min, obtains reduced blast furnace;
    (4) reduced blast furnace is entered in fuming furnace by material trough, reclaims antimony;The cigarette ash of reduction melting process returns after granulation Return former fusion process.
  2. 2. antimony sulfide ore oxygen-enriched smelting method according to claim 1, it is characterised in that:The particle diameter of the spherolite is 15- 20mm, water content 8-10%.
  3. 3. antimony sulfide ore oxygen-enriched smelting method according to claim 1, it is characterised in that:The lime stone ﹥ containing CaO 70%, quartz sand contains SiO2﹥ 80%.
  4. 4. antimony sulfide ore oxygen-enriched smelting method according to claim 1, it is characterised in that:It is described to be passed through in oxygen-rich oxide stove The oxygenous volumetric concentration of oxygen-enriched air be 50-85%, the oxygen-enriched air using bottom blowing or it is side-blown by the way of be blown into oxygen-enriched oxygen Change in stove.
  5. 5. antimony sulfide ore oxygen-enriched smelting method according to claim 1, it is characterised in that:It is described to be passed through in oxygen-enriched reduction furnace The oxygenous volumetric concentration of oxygen-enriched air be 50-85%, the oxygen-enriched air using bottom blowing or it is side-blown by the way of be blown into it is oxygen-enriched also In former stove.
  6. 6. antimony sulfide ore oxygen-enriched smelting method according to claim 4, it is characterised in that:Pressure in the oxygen-rich oxide stove Strong is 0.1-0.3MPa, and the pressure in the oxygen-enriched reduction furnace is 0.2-0.4MPa.
  7. 7. antimony sulfide ore oxygen-enriched smelting method according to claim 5, it is characterised in that:The average grain diameter of the coal powder For 0.5-4mm.
CN201711242100.5A 2017-11-30 2017-11-30 A kind of antimony sulfide ore oxygen-enriched smelting method Pending CN107858530A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201711242100.5A CN107858530A (en) 2017-11-30 2017-11-30 A kind of antimony sulfide ore oxygen-enriched smelting method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201711242100.5A CN107858530A (en) 2017-11-30 2017-11-30 A kind of antimony sulfide ore oxygen-enriched smelting method

Publications (1)

Publication Number Publication Date
CN107858530A true CN107858530A (en) 2018-03-30

Family

ID=61704374

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201711242100.5A Pending CN107858530A (en) 2017-11-30 2017-11-30 A kind of antimony sulfide ore oxygen-enriched smelting method

Country Status (1)

Country Link
CN (1) CN107858530A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108359814A (en) * 2018-04-08 2018-08-03 邝江华 A method of vulcanization Sb-Au ore oxygen enriched molten bath melting
CN112176202A (en) * 2020-10-28 2021-01-05 广西华远金属化工有限公司 Antimony smelting method adopting oxygen-enriched side-blown column smelting
CN113046571A (en) * 2021-03-08 2021-06-29 易门铜业有限公司 Smelting system and method for reducing generation of magnetic iron in copper ore smelting process

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101423252A (en) * 2008-11-17 2009-05-06 河南豫光金铅股份有限公司 Oxygen-enriched production process of diantimony trioxide
CN102433448A (en) * 2011-12-28 2012-05-02 北京矿冶研究总院 Smelting method of antimony-zinc-lead-containing concentrate
CN103173636A (en) * 2013-03-06 2013-06-26 中南大学 Antimony sulfide concentrate oxygen-enriched melting tank melting method
CN103173637A (en) * 2013-03-06 2013-06-26 中南大学 Antimony sulfide concentrate oxygen-enriched melting tank melting method and side-blown furnace
CN106521189A (en) * 2016-10-21 2017-03-22 河池市生富冶炼有限责任公司 Oxygen-enriched molten pool antimony refining production process
CN106916966A (en) * 2017-02-21 2017-07-04 广西生富锑业科技股份有限公司 The oxygen-rich oxide method of smelting and its device of a kind of antimong-containing material

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101423252A (en) * 2008-11-17 2009-05-06 河南豫光金铅股份有限公司 Oxygen-enriched production process of diantimony trioxide
CN102433448A (en) * 2011-12-28 2012-05-02 北京矿冶研究总院 Smelting method of antimony-zinc-lead-containing concentrate
CN103173636A (en) * 2013-03-06 2013-06-26 中南大学 Antimony sulfide concentrate oxygen-enriched melting tank melting method
CN103173637A (en) * 2013-03-06 2013-06-26 中南大学 Antimony sulfide concentrate oxygen-enriched melting tank melting method and side-blown furnace
CN106521189A (en) * 2016-10-21 2017-03-22 河池市生富冶炼有限责任公司 Oxygen-enriched molten pool antimony refining production process
CN106916966A (en) * 2017-02-21 2017-07-04 广西生富锑业科技股份有限公司 The oxygen-rich oxide method of smelting and its device of a kind of antimong-containing material

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108359814A (en) * 2018-04-08 2018-08-03 邝江华 A method of vulcanization Sb-Au ore oxygen enriched molten bath melting
CN108359814B (en) * 2018-04-08 2020-07-17 邝江华 Antimony sulfide gold ore oxygen-enriched molten pool smelting method
CN112176202A (en) * 2020-10-28 2021-01-05 广西华远金属化工有限公司 Antimony smelting method adopting oxygen-enriched side-blown column smelting
CN113046571A (en) * 2021-03-08 2021-06-29 易门铜业有限公司 Smelting system and method for reducing generation of magnetic iron in copper ore smelting process

Similar Documents

Publication Publication Date Title
US11091816B2 (en) Method for ironmaking by smelting reduction in stir-generated vortex
CN103421955B (en) Zinc leaching slag treatment method
CN101665871B (en) Method for producing titanium carbide slag
CN106048109A (en) Method for mixed slag smelting reduction recycling and thermal refining
WO2019071788A1 (en) Manufacturing method using copper and iron containing mixing slag
CN106916966B (en) A kind of the oxygen-rich oxide method of smelting and its device of antimong-containing material
CN101705366B (en) Direct lead smelting method for processing zinc smelting slag by matching
WO2019071794A1 (en) Method for recovering valuable components from mixed slag containing copper and iron
CN101509081A (en) Process for direct reduction of liquid high-lead skim with reduction furnace
CN107858530A (en) A kind of antimony sulfide ore oxygen-enriched smelting method
CN108278901A (en) A kind of industrial furnace and production technology for smelting slag composition adjustment
CN104232925B (en) The method of the complicated Treating Low-grade Copper Ores producing white matte by mixed smelting of multi-source
CN106755655A (en) A kind of recovery method for mixing the reduction of slag metallurgy melting
WO2018228073A1 (en) Anode copper production method and device
CN107557597B (en) A kind of method that antimony is smelted
CN102102152A (en) Method for smelting lead by reducing lead-rich slags
CN101280351A (en) Production method of vanadium slag
CN109385521B (en) Production process for lead-antimony mixed ore oxygen-enriched molten pool low-temperature oxidation smelting
CN101280368B (en) Stibium blast furnace treatment method using oxygenized air
CN1325672C (en) Lead smelting method and apparatus implementing the same
CN104232911A (en) Method for producing white matte by mixed smelting of copper refining slags-pyrite-bornite tailings
CN107190138A (en) A kind of method and device that manganese-silicon is prepared using poor ferrous manganese ore
CN111394588A (en) Method and device for directly producing iron-vanadium-chromium alloy by treating vanadium extraction tailings
CN1035848A (en) Vanadium chromium leaches tailings ironmaking comprehensive utilization process
CN1110330A (en) Method for smelting iron alloy containing manganese and silicon in midfrequency electric furnace

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
RJ01 Rejection of invention patent application after publication

Application publication date: 20180330

RJ01 Rejection of invention patent application after publication