CN105907988A - Device for lead and zinc ore smelting - Google Patents
Device for lead and zinc ore smelting Download PDFInfo
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- CN105907988A CN105907988A CN201610439929.3A CN201610439929A CN105907988A CN 105907988 A CN105907988 A CN 105907988A CN 201610439929 A CN201610439929 A CN 201610439929A CN 105907988 A CN105907988 A CN 105907988A
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- zinc
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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
- C22B19/00—Obtaining zinc or zinc oxide
- C22B19/04—Obtaining zinc by distilling
- C22B19/16—Distilling vessels
- C22B19/18—Condensers, Receiving vessels
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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
- C22B13/00—Obtaining lead
- C22B13/02—Obtaining lead by dry processes
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F27—FURNACES; KILNS; OVENS; RETORTS
- F27D—DETAILS OR ACCESSORIES OF FURNACES, KILNS, OVENS, OR RETORTS, IN SO FAR AS THEY ARE OF KINDS OCCURRING IN MORE THAN ONE KIND OF FURNACE
- F27D17/00—Arrangements for using waste heat; Arrangements for using, or disposing of, waste gases
- F27D17/004—Systems for reclaiming waste heat
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F27—FURNACES; KILNS; OVENS; RETORTS
- F27D—DETAILS OR ACCESSORIES OF FURNACES, KILNS, OVENS, OR RETORTS, IN SO FAR AS THEY ARE OF KINDS OCCURRING IN MORE THAN ONE KIND OF FURNACE
- F27D17/00—Arrangements for using waste heat; Arrangements for using, or disposing of, waste gases
- F27D17/008—Arrangements for using waste heat; Arrangements for using, or disposing of, waste gases cleaning gases
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F27—FURNACES; KILNS; OVENS; RETORTS
- F27D—DETAILS OR ACCESSORIES OF FURNACES, KILNS, OVENS, OR RETORTS, IN SO FAR AS THEY ARE OF KINDS OCCURRING IN MORE THAN ONE KIND OF FURNACE
- F27D17/00—Arrangements for using waste heat; Arrangements for using, or disposing of, waste gases
- F27D17/004—Systems for reclaiming waste heat
- F27D2017/006—Systems for reclaiming waste heat using a boiler
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- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Chemical & Material Sciences (AREA)
- Environmental & Geological Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Manufacturing & Machinery (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Manufacture And Refinement Of Metals (AREA)
Abstract
The invention discloses a device for lead and zinc ore smelting. The device for lead and zinc ore smelting comprises an oxidization smelting furnace, a power frequency electric heating reduction furnace and a zinc rain condenser; the oxidization smelting furnace is provided with a lead and zinc ore inlet, a fluxing agent inlet, a smelting flue gas outlet and a melt outlet, and melt contains zinc oxide and lead oxide; the power frequency electric heating reduction furnace is provided with a melt inlet, a reduction agent inlet, a liquid lead outlet, a furnace slag outlet and a zinc-containing flue gas outlet, and the melt inlet is connected with the melt outlet; and the zinc rain condenser is provided with a zinc-containing flue gas inlet, a liquid zinc outlet and a coal gas outlet, and the zinc-containing flue gas inlet is connected with the zinc-containing flue gas outlet. By means of the device, after being subjected to oxidization melting, the lead and zinc ore can be directly supplied to the power frequency electric heating reduction furnace in a high-temperature melt state, in the furnace body, the zinc oxide is reduced into metal zinc steam by high-temperature carbon, and liquid metal zinc is further obtained through condensation. The lead oxide entering the furnace body is reduced into liquid metal lead by high-temperature carbon, and the liquid metal lead and liquid metal lead slag composed of iron oxide, silicon oxide, calcium oxide, aluminum oxide, magnesium oxide and other oxides jointly descend into a settling chamber on the lower portion of a vertical shaft type power frequency electric heating furnace.
Description
Technical field
The present invention relates to field of metallurgy.Concrete, the present invention relates to the equipment smelted for Pb-Zn deposits.
Background technology
It mostly is mineral intergrowth based on led-zinc-silver deposit, is generally individually sorted at present as lead concentrate and zinc concentrate after exploitation, send lead respectively
Smeltery and zinc abstraction factory separately process.Owing to sorting is difficult to thoroughly, the most miscellaneous in lead concentrate have a number of zinc, zinc concentrate
In miscellaneous have a number of lead.Smelt Hou Qian factory output Zn dust Xu Song zinc factory and office reason, zinc factory output lead smelting gas Xu Song lead factory and office
Reason.
Thus, current Pb-Zn deposits is smelted means and is still had much room for improvement.
Summary of the invention
It is contemplated that solve one of above-mentioned technical problem the most to a certain extent or provide at a kind of useful business choosing
Select.To this end, it is an object of the present invention to propose a kind of means having and can effectively Pb-Zn deposits being smelted.
The present invention is following discovery based on inventor and completes:
During by using main frequency furnace that the melt of zinc oxide and lead oxide is carried out reduction treatment, reduzate zinc can become gaseous state,
Reduzate lead then can maintain liquid.
In one aspect of the invention, the present invention proposes a kind of equipment smelted for Pb-Zn deposits, according to the enforcement of the present invention
Example, this equipment includes: oxidizing semlting stove, and described oxidizing semlting stove has Pb-Zn deposits entrance, flux entrance, melting flue gas to go out
Mouth and melt outlet, described melt contains zinc oxide and lead oxide；Power frequency electric thermal reduction furnace, described power frequency electric thermal reduction stove
Having the outlet of melt inlet, reducing agent entrance, liquid lead, slag outlet and the exhanst gas outlet on zinc, described melt inlet is with described
Melt outlet is connected；And zinc rain condenser, described zinc rain condenser has containing zinc smoke inlet, liquid Zn outlet and coal gas
Outlet, described is connected with the described exhanst gas outlet containing zinc containing zinc smoke inlet.
Utilize this equipment, it is possible to effectively Pb-Zn deposits is smelted, as it was previously stated, utilize this technique, it is not necessary to lead zinc
Ore deposit sorts, and directly by after oxidized for Pb-Zn deposits fusing, supplies to power frequency electric thermal reduction furnace under high-temperature fusant state,
In this body of heater, zinc oxide can be reduced to metallic zinc steam by pyrocarbon, obtains liquid metal zinc by condensation further.Enter
Enter the lead oxide in body of heater, be reduced to liquid metal lead by pyrocarbon, with the oxide such as iron, silicon, calcium, aluminium, magnesium composition
Liquid lead skim drops to straight well formula power frequency electrothermal furnace bottom expansion chamber together.Slag lead separation is carried out at expansion chamber.By under expansion chamber
Portion's discharge port releases metallic lead.According to embodiments of the invention, slag can be released by expansion chamber top discharge port.Slag water
Sell outside after quenching.
It addition, the equipment smelted for Pb-Zn deposits according to the above embodiment of the present invention can also have following additional technology spy
Levy:
In some embodiments of the invention, described reducing agent porch is provided with double-charging bell feeder.Thus, it is possible to it is notable
Raising equipment sealing property.
In some embodiments of the invention, waste heat boiler, the smoke inlet of described waste heat boiler and described melting flue gas are also included
Outlet is connected.Thus, it is possible to make system waste heat be fully utilized.
In some embodiments of the invention, the smoke of deduster, the import of described deduster and described waste heat boiler is also included
Mouth is connected.
In some embodiments of the invention, described deduster is electric cleaner.
In some embodiments of the invention, described power frequency electric thermal reduction furnace includes vertical reduction section and Horizontal sedimentation section, and
It is provided with coil on the outer wall of described vertical reduction section and described Horizontal sedimentation section.Thus, it is possible to effectively maintain furnace temperature.
In some embodiments of the invention, by siphon port, by described melt input to described power frequency electric thermal reduction furnace.
Thus, it is possible to improve equipment sealing property further.
In some embodiments of the invention, described reducing agent is coke.
In some embodiments of the invention, described reducing agent farther includes magnetic conductor.
In some embodiments of the invention, described magnetic conductor is graphite.
In some embodiments of the invention, described graphite is the 10～50% of described reducing agent quality.
In some embodiments of the invention, the temperature of described melt is at least 900 degrees Celsius.
In some embodiments of the invention, liquid lead is discharged by siphon port.Seal thus, it is possible to improve equipment further
Performance.
The additional aspect of the present invention and advantage will part be given in the following description, and part will become bright from the following description
Aobvious, or recognized by the practice of the present invention.
Accompanying drawing explanation
Above-mentioned and/or the additional aspect of the present invention and advantage will be apparent from from combining the accompanying drawings below description to embodiment
With easy to understand, wherein:
Fig. 1 shows the cross section structure schematic diagram of the equipment smelted for Pb-Zn deposits of one embodiment of the invention；
Fig. 2 shows the part-structure top view in the equipment that Pb-Zn deposits is smelted of further embodiment of the present invention；
Fig. 3 shows the structural representation of the equipment smelted for Pb-Zn deposits of another embodiment of the present invention；
Fig. 4 shows the structural representation of the equipment smelted for Pb-Zn deposits of another embodiment of the present invention；
Fig. 5 shows the stream of the equipment enforcement Pb-Zn deposits smelting process smelted for Pb-Zn deposits utilizing one embodiment of the invention
Journey schematic diagram.
Detailed description of the invention
Embodiments of the invention are described below in detail, and the example of described embodiment is shown in the drawings, the most identical
Or similar label represents same or similar element or has the element of same or like function.Retouch below with reference to accompanying drawing
The embodiment stated is exemplary, it is intended to is used for explaining the present invention, and is not considered as limiting the invention.
In describing the invention, it is to be understood that term " " center ", " longitudinally ", " laterally ", " length ", " width ",
" thickness ", " on ", D score, "front", "rear", "left", "right", " vertically ", " level ", " top ", " end ", " interior ", " outward ",
Orientation or the position relationship of the instruction such as " clockwise ", " counterclockwise ", " axially ", " radially ", " circumferential " are based on shown in the drawings
Orientation or position relationship, be for only for ease of describe the present invention and simplify describe rather than instruction or hint indication device or
Element must have specific orientation, with specific azimuth configuration and operation, be therefore not considered as limiting the invention.
Additionally, term " first ", " second " are only used for describing purpose, and it is not intended that instruction or hint relative importance or
Person implies the quantity indicating indicated technical characteristic.Thus, define " first ", the feature of " second " can express or
Implicitly include at least one this feature.In describing the invention, " multiple " are meant that at least two, such as two,
Three etc., unless otherwise expressly limited specifically.
In the present invention, unless otherwise clearly defined and limited, term " install ", " being connected ", " connection ", the art such as " fixing "
Language should be interpreted broadly, and connects for example, it may be fixing, it is also possible to be to removably connect, or integral；Can be machinery
Connect, it is also possible to be electrical connection；Can be to be joined directly together, it is also possible to be indirectly connected to by intermediary, can be two units
Connection within part or the interaction relationship of two elements, unless otherwise clear and definite restriction.Ordinary skill for this area
For personnel, above-mentioned term concrete meaning in the present invention can be understood as the case may be.
In the present invention, unless otherwise clearly defined and limited, fisrt feature second feature " on " or D score can be
One directly contacts with second feature, or the first and second features are by intermediary mediate contact.And, fisrt feature is
Two features " on ", " top " and " above " but fisrt feature directly over second feature or oblique upper, or be merely representative of first
Characteristic level height is higher than second feature.Fisrt feature second feature " under ", " lower section " and " below " can be fisrt feature
Immediately below second feature or obliquely downward, or it is merely representative of fisrt feature level height less than second feature.
Embodiments of the invention are described below in detail, and the embodiment described below with reference to accompanying drawing is exemplary, it is intended to use
In explaining the present invention, and it is not considered as limiting the invention.
All bibliography mentioned in this article are all incorporated herein by.
Unless there are indicating on the contrary, all technology used herein and scientific terminology all have and art ordinary skill of the present invention
The identical implication that personnel are generally understood.Unless there are indicating on the contrary, technology that is used herein or that mention is that this area is general
Standard technique known to logical technical staff.Material, method and example are only used as to illustrate, rather than are any limitation as.
The present invention is following discovery based on inventor and completes:
During by using main frequency furnace that the melt of zinc oxide and lead oxide is carried out reduction treatment, reduzate zinc can become gaseous state,
Reduzate lead then can keep liquid.
In one aspect of the invention, the present invention proposes a kind of equipment smelted for Pb-Zn deposits, according to the enforcement of the present invention
Example, with reference to Fig. 1, this equipment includes: oxidizing semlting stove 100, power frequency electric thermal reduction furnace 200 and zinc rain condenser 300.
According to embodiments of the invention, oxidizing semlting stove 100 has Pb-Zn deposits entrance 101, flux entrance 102, melting flue gas
Outlet 103 and melt outlet 104, and be suitable to the mixture obtained by being mixed with flux by Pb-Zn deposits and carry out oxidizing semlting, from
And the melt containing zinc oxide and lead oxide can be obtained.Concrete, Pb-Zn deposits can be lead zinc composite sulfuration ore deposit, and
Suitable slag former can be added during oxidizing semlting.It should be noted that those skilled in the art can be according to actual need
The condition of the flux used and oxidizing semlting is selected, and Pb-Zn deposits entrance 101 and flux entrance 102 can
Think same entrance or independent two entrances
According to one embodiment of present invention, the temperature containing zinc oxide and the melt of lead oxide is at least 900 degrees Celsius.By
This, can improve the Environmental Protection Level that in subsequent process, Pb-Zn deposits is smelted further.
According to embodiments of the invention, power frequency electric thermal reduction furnace 200 has melt inlet 201, reducing agent entrance 202, liquid
Lead outlet 203, slag outlet 204 and containing zinc exhanst gas outlet 205, melt inlet 201 is connected with melt outlet 104, and fits
In utilizing reducing agent, the melt containing zinc oxide and lead oxide obtained by above-mentioned is reduced in power frequency electric thermal reduction furnace
Process and slag settlement treatment, it is hereby achieved that containing zinc flue gas, liquid lead and slag.
According to one embodiment of present invention, siphon port can be passed through, oxidizing semlting operation is obtained containing zinc oxide and oxygen
The melt changing lead supplies to power frequency electric thermal reduction furnace.Inventor finds by using siphon port to feed, can be effectively close
Feed under the conditions of envelope, such that it is able to improve the efficiency that Pb-Zn deposits is smelted further.
According to still a further embodiment, with reference to Fig. 1 and Fig. 2, power frequency electric thermal reduction furnace 200 can include the most also
It is provided with coil 23 in former section 21 and Horizontal sedimentation section 22, and the outer wall of vertical reduction section 21 and Horizontal sedimentation section 22.
Concrete, as it is shown in figure 1, vertically the lower end passage of reduction section 21 is connected with the Upper passage of Horizontal sedimentation section 22, and
And the lower end passage of vertical reduction section 21 tilts upward, such that it is able to avoid the reducing agent adding reduction section to enter into settling section.
Thus, by arranging coil on the outer wall of vertical reduction section 21 and Horizontal sedimentation section 22, coil is used to produce alternating magnetic field
Maintain reduction section and the furnace temperature of settling section, such that it is able to improve the efficiency that Pb-Zn deposits is smelted further.Concrete according to the present invention
Embodiment, can use the induction coil of 200～400 kilowatts.
According to still another embodiment of the invention, reducing agent can be coke.Smelt thus, it is possible to improve Pb-Zn deposits further
Efficiency.
According to still another embodiment of the invention, reducing agent may further include magnetic conductor.Thus, produce at external coil
Under raw action of alternating magnetic field, magnetic conductor can temperature stabilization in holding furnace effectively, such that it is able to improve Pb-Zn deposits further
The efficiency smelted.
According to still another embodiment of the invention, magnetic conductor can be graphite.Inventor find graphite can magnetic conduction effectively,
And subsequent reactions will not be introduced impurity, such that it is able to improve the efficiency that Pb-Zn deposits is smelted further.Concrete, coke and
Graphite block mixture is added directly in the reduction section in power frequency electric thermal reduction furnace, and coke is used as reducing agent, and graphite block is as leading
Magnetic exothermic material (during actual production, the carbon in graphite has certain reproducibility equally), reduction section furnace shell is outer equipped with single-core line circle,
During indirect current coil produce change magnetic field, graphite block affected by this variation magnetic field start heating and circumference coke with
Melt, maintains reaction zone thermal balance, makes the temperature of whole direct-reduction section meet the requirement of smelting charge of lead and zinc direct-reduction.
According to one embodiment of present invention, graphite can be the 10～50% of reducing agent quality.Thus, it is possible to improve further
The efficiency that Pb-Zn deposits is smelted.Inventor finds, if the ratio of graphite is too small, then not enough so that the temperature in reduction space is steady
Fixed, if the ratio of graphite is excessive, then can affect the efficiency of reduction treatment.
According to still another embodiment of the invention, liquid lead is discharged by siphon port.Thus, it is possible to improve Pb-Zn deposits further
The efficiency smelted.
According to still another embodiment of the invention, it is provided with double-charging bell feeder 24 at reducing agent entrance 202.Concrete, logical
Cross Special crane and will fill the charging bell of incandescent coke and graphite block, accurately fall to sitting to double-charging bell feeder, then put down and add
Material bell bottom valve, incandescent coke and graphite fall in the bucket of double-charging bell feeder top, then hang away charging bell, then puts down extra quality
The top bottom valve of clock feeder, coke and graphite fall in the bottom bucket of double-charging bell feeder, now promote top bottom valve, close
Closing gas passage, then open the bottom bottom valve of double-charging bell feeder, incandescent coke and graphite block are by reducing agent entrance the most at last
Add in power frequency electric thermal reduction furnace in reduction reaction district, and with this cycle operation, be continuously replenished Jiao of continuous consumption in reaction zone
Charcoal and graphite block.
In this step, concrete, in the melt containing zinc oxide and lead oxide falls into the reduction section of power frequency electric thermal reduction furnace,
Run into red-hot coke, reduction reaction can be occurred immediately to generate melted metallic lead, slag and contain zinc fume and an oxidation
The flue gas of carbon/carbon dioxide.Melted metallic lead and slag flow downward, logical from the upper end of settling section through reduction section hypomere passage
Road (being inclined upwardly, in order to avoid coke and graphite block fall into precipitating phase) flows into precipitating phase.It is also provided with coil outside precipitating phase furnace shell,
Melted metallic lead can generate heat maintenance furnace temperature under the effect of variation magnetic field, thus keeps certain mobility.Finally, melted
Metallic lead bottom precipitating phase siphon lead tap release, a small amount of slag after running up to a certain degree, slag pass through top slagging
Mouth is released.
According to embodiments of the invention, zinc rain condenser 300 has containing zinc smoke inlet 301, liquid Zn outlet 302 and coal
Gas outlet 303, is connected with containing zinc exhanst gas outlet 205 containing zinc smoke inlet 301, and is suitable to obtain in power frequency electric thermal reduction furnace
To the flue gas containing zinc condense, in order to obtain liquid Zn and coal gas.According to one embodiment of present invention, it is possible to use zinc
The condensation to carrying out Pb-Zn deposits smelting containing zinc flue gas of the rain condenser.Thus, employing zinc rain can be by containing the gold carried in zinc flue gas
Belong to zinc to condense out, and the carbon monoxide wherein carried is or/and carbon dioxide continues to exist in a gaseous form, and wash further
It is recycled with coal gas form after purification.Concrete, that zinc rain condenser is trapped by zinc rain liquid Zn rain lead, uses pump
Delivering to zinc liquid cooling bath, after refrigerated separation lead, part zinc liquid is cast into product coarse zinc ingot metal, and part zinc liquid returns zinc rain condenser
It is cycled to used in trapping zinc fume.
Thus, the equipment smelted for Pb-Zn deposits according to embodiments of the present invention, it is possible to effectively Pb-Zn deposits is smelted,
As it was previously stated, utilize this technique, it is not necessary to Pb-Zn deposits is sorted, directly by after oxidized for Pb-Zn deposits fusing, at high temperature
Supplying under melt state to power frequency electric thermal reduction furnace, in this body of heater, zinc oxide can be reduced to metallic zinc steam by pyrocarbon,
Liquid metal zinc is obtained further by condensation.Enter the lead oxide in body of heater, be reduced to liquid metal lead by pyrocarbon, with
The liquid lead skim of the oxide compositions such as iron, silicon, calcium, aluminium, magnesium drops to straight well formula power frequency electrothermal furnace bottom expansion chamber together.
Slag lead separation is carried out at expansion chamber.Metallic lead is released by expansion chamber lower tap hole.According to embodiments of the invention, Ke Yiyou
Expansion chamber top discharge port releases slag.Sell outside after furnace slag granulating.
With reference to Fig. 3, the equipment for Pb-Zn deposits smelting according to embodiments of the present invention farther includes: waste heat boiler 400.
According to embodiments of the invention, the smoke inlet of waste heat boiler 400 is connected with melting exhanst gas outlet 103.Thus, it is possible to
System waste heat is fully utilized.
With reference to Fig. 4, the equipment for Pb-Zn deposits smelting according to embodiments of the present invention farther includes: deduster 500.
According to embodiments of the invention, the import of deduster 500 is connected with the outlet flue of waste heat boiler 400.According to the present invention
An embodiment, deduster can be electric cleaner.Thus, it is possible to improve efficiency of dust collection further.
According to embodiments of the invention, the equipment for Pb-Zn deposits smelting according to embodiments of the present invention can at least have following
At least one advantage:
According to embodiments of the invention, simplify the mineral processing circuit of lead and zinc mineral resources, improve recovery rate of valuable metals,
Reduce beneficiation cost.
According to embodiments of the invention, lead zinc synchronous smelting together, eliminate association unit between the lead factory of original technique and zinc factory
The intermediate material that element produces is had bad luck the most back and forth, transports without intermediate material, reduces main Metal Production cost.
According to embodiments of the invention, use main frequency furnace electrothermal reduction lead zinc, it is to avoid original technique uses air-supply or send oxygen,
Fuel burning heat supply is relied on just to maintain reduction process thermal balance.Fuel burning dimension temperature, exhaust gas volumn is big, and it is more that flue gas takes away waste heat, because of
This energy consumption is higher.The lead oxide that needs in the high-temperature fusant that electrothermal reduction only adds to be reduced, zinc oxide, di-iron trioxide
The oxygen brought into Deng material just consumes reducing agent carbon or hydrogen.Reducing agent consumption is theoretical value, and the exhaust gas volumn of generation is also theoretical value,
Energy consumption is minimum in all technique.
According to embodiments of the invention, the zinc of more than 85% is produced by wet method smelting process the most in the world, and its leached mud is
Danger waste dump is one the difficult problem of environmental protection, and its harmless treatment, existing process energy consumption is the highest.This technique can economical and effective
Solution zinc leaching residue pollute environment a difficult problem.
According to the expansion examination authorizing invention CN200610066648.4 " a kind of lead smelting process and for realizing the device of this lead smelting process "
Testing parameter, use vertical shaft type electrothermal reduction, lead, zinc metal recovery rate are the highest.Accompanying element beyond lead zinc, as Au,
Ag, Cu, Ni, Bi, Sn, the overwhelming majority is reduced in entrance lead bullion, and the volatile matters such as Cd, Ga, In, Il, Ge are equal
Be condensed entrance crude zinc.Along with lead bullion and crude zinc refining process, these associated metals can be reclaimed the most one by one, it is achieved the most comprehensive
Close and utilize.As for As, Hg accompanying element contained in lead and zinc industry, big absolutely portion during first step oxidizing semlting
Divide entrance flue gas to be removed, do not inquire in the range of this patent.
Using ore deposit thermal resistance stove heat supply in prior art, have multiple electrode-inserting holes, electrode-inserting holes is difficult to positive confinement, many
Rare flue gas leaks and affects environment.This patent uses main frequency furnace heat supply, does not has electrode-inserting holes, body of heater all to seal, nothing
Flue gas leaks, and has optimal environmental benefit.Employing ore-smelting electric furnace reduces, internal by air or nitrogen to ore-smelting electric furnace
Pulverized coal injection can make zinc fume concentration reduce as reducing agent, air or nitrogen, and slag is containing Zn >=3%, and uses main frequency furnace
Reduction liquid smelting charge of lead and zinc, zinc fume concentration is high, and slag can reach theoretical value≤0.22% containing zinc, so using ore deposit thermoelectricity
Stove carries out reducing and smelting smelting charge of lead and zinc to be needed to be followed by fuming furnace and is further processed slag, uses main frequency furnace then without again
Slag is carried out advanced treating.
Understand for convenience, below with reference to the Fig. 5 equipment enforcement lead zinc smelted for Pb-Zn deposits to using the embodiment of the present invention
Mining and metallurgy smelting method is described in detail.According to embodiments of the invention, the method includes:
S100: Pb-Zn deposits is mixed with flux, and obtained mixture is carried out oxidizing semlting
In this step Pb-Zn deposits is mixed with flux, and obtained mixture is carried out oxidizing semlting, in order to obtain and contain
Zinc oxide and the melt of lead oxide.Concrete, herein Pb-Zn deposits can refer to include lead content > 40wt% high-grade raw ore,
Or general lead zine ores lead and zinc total amount after ore dressing > lead and zinc concentrate of 50wt%, and can add during oxidizing semlting
Suitable slag former.It should be noted that those skilled in the art can be according to actual needs to the flux used and oxygen
The condition changing melting selects.
According to one embodiment of present invention, the temperature containing zinc oxide and the melt of lead oxide is at least 900 degrees Celsius.By
This, can improve the efficiency that in subsequent process, Pb-Zn deposits is smelted further.
S200: utilize reducing agent, carries out reduction treatment to the melt containing zinc oxide and lead oxide in power frequency electric thermal reduction furnace
With slag settlement treatment
In this step, utilize reducing agent, to the above-mentioned obtained melt containing zinc oxide and lead oxide at power frequency electric heating also
Former stove carries out reduction treatment and slag settlement treatment, in order to obtain containing zinc flue gas, liquid lead and slag.
According to one embodiment of present invention, siphon port can be passed through, oxidizing semlting operation is obtained containing zinc oxide and oxygen
The melt changing lead supplies to power frequency electric thermal reduction furnace.Inventor finds by using siphon port to feed, can be effectively close
Feed under the conditions of envelope, such that it is able to improve the Environmental Protection Level that Pb-Zn deposits is smelted further.
According to still a further embodiment, power frequency electric thermal reduction furnace can have multiple coil, and multiple coil is arranged
On the outer wall of power frequency electric thermal reduction furnace.Thus, by using coil to produce alternating magnetic field maintenance furnace temperature, such that it is able to enter one
Step improves the efficiency that Pb-Zn deposits is smelted.According to a particular embodiment of the invention, the induction coil of 200～400 kilowatts can be used.
According to still another embodiment of the invention, reducing agent can be coke.Smelt thus, it is possible to improve Pb-Zn deposits further
Efficiency.
According to still another embodiment of the invention, reducing agent may further include magnetic conductor.Thus, produce at external coil
Under raw action of alternating magnetic field, magnetic conductor can keep stablizing of in-furnace temperature effectively, such that it is able to improve lead zinc further
The efficiency of mining and metallurgy refining.
According to still another embodiment of the invention, magnetic conductor can be graphite.Inventor find graphite can magnetic conduction effectively,
And subsequent reactions will not be introduced impurity, such that it is able to improve the efficiency that Pb-Zn deposits is smelted further.
According to one embodiment of present invention, graphite can be the 10～50% of reducing agent quality.Thus, it is possible to improve further
The efficiency that Pb-Zn deposits is smelted.Inventor finds, if the ratio of graphite is too small, then not enough so that the temperature in reduction space is steady
Fixed, if the ratio of graphite is excessive, then can affect the efficiency of reduction treatment.
According to still another embodiment of the invention, liquid lead is discharged by siphon port.Thus, it is possible to improve Pb-Zn deposits further
The efficiency smelted.
S300: zinc flue gas will be contained and condense
In this step, the flue gas containing zinc obtained in power frequency electric thermal reduction furnace is condensed, in order to obtain liquid Zn and coal gas.
According to one embodiment of present invention, it is possible to use the condensation to carrying out Pb-Zn deposits smelting containing zinc flue gas of the zinc rain condenser.Thus,
Use zinc rain will condense out containing the metallic zinc carried in zinc flue gas, and the carbon monoxide wherein carried is or/and carbon dioxide
Continue to exist in a gaseous form, and be recycled with coal gas form after further washing, purifying.
Thus, the equipment enforcement Pb-Zn deposits smelting process smelted for Pb-Zn deposits of the embodiment of the present invention is utilized, it is not necessary to lead
Zinc ore sorts, and directly by after oxidized for Pb-Zn deposits fusing, supplies to power frequency electric thermal reduction furnace under high-temperature fusant state,
In this body of heater, zinc oxide can be reduced to metallic zinc steam by pyrocarbon, obtains liquid metal zinc by condensation further.
Enter the lead oxide in body of heater, be reduced to liquid metal lead by pyrocarbon, with the oxide composition such as iron, silicon, calcium, aluminium, magnesium
Liquid lead skim drop to straight well formula power frequency electrothermal furnace bottom expansion chamber together.Slag lead separation is carried out at expansion chamber.By expansion chamber
Lower tap hole releases metallic lead.According to embodiments of the invention, slag, slag can be released by expansion chamber top discharge port
Sell outside after shrend.
In the description of this specification, reference term " embodiment ", " some embodiments ", " example ", " concrete example ",
Or specific features, structure, material or the feature bag that the description of " some examples " etc. means to combine this embodiment or example describes
It is contained at least one embodiment or the example of the present invention.In this manual, to the schematic representation of above-mentioned term not necessarily
Refer to identical embodiment or example.And, the specific features of description, structure, material or feature can be any
One or more embodiments or example combine in an appropriate manner.
Although above it has been shown and described that embodiments of the invention, it is to be understood that above-described embodiment is exemplary,
Being not considered as limiting the invention, those of ordinary skill in the art is without departing from the principle of the present invention and the situation of objective
Under above-described embodiment can be changed within the scope of the invention, revise, replace and modification.
Claims (13)
1. the equipment smelted for Pb-Zn deposits, it is characterised in that including:
Oxidizing semlting stove, described oxidizing semlting stove has Pb-Zn deposits entrance, flux entrance, melting exhanst gas outlet and melt outlet,
Described melt contains zinc oxide and lead oxide；
Power frequency electric thermal reduction furnace, described power frequency electric thermal reduction furnace has melt inlet, reducing agent entrance, liquid lead outlet, stove
Slag outlet and the exhanst gas outlet on zinc, described melt inlet is connected with described melt outlet；And
Zinc rain condenser, described zinc rain condenser has containing zinc smoke inlet, liquid Zn outlet and gas exit, described containing zinc
Smoke inlet is connected with the described exhanst gas outlet containing zinc.
Equipment the most according to claim 1, it is characterised in that described reducing agent porch is provided with double-charging bell feeder.
Equipment the most according to claim 1 and 2, it is characterised in that also include waste heat boiler, described waste heat boiler
Smoke inlet is connected with described melting exhanst gas outlet.
Equipment the most according to claim 3, it is characterised in that also include deduster, the import of described deduster and institute
The outlet flue stating waste heat boiler is connected.
Equipment the most according to claim 4, it is characterised in that described deduster is electric cleaner.
Equipment the most according to claim 1, it is characterised in that described power frequency electric thermal reduction furnace include vertical reduction section and
It is provided with coil in Horizontal sedimentation section, and the outer wall of described vertical reduction section and described Horizontal sedimentation section.
Equipment the most according to claim 6, it is characterised in that by siphon port, by the input of described melt to described work
Frequently in electric reduction furnace.
Equipment the most according to claim 1, it is characterised in that described reducing agent is coke.
Equipment the most according to claim 8, it is characterised in that described reducing agent farther includes magnetic conductor.
Equipment the most according to claim 9, it is characterised in that described magnetic conductor is graphite.
11. equipment according to claim 10, it is characterised in that described graphite is the 10～50% of described reducing agent quality.
12. equipment according to claim 1, it is characterised in that the temperature of described melt is at least 900 degrees Celsius.
13. equipment according to claim 1, it is characterised in that discharge liquid lead by siphon port.
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| CN201610439929.3A CN105907988B (en) | 2016-06-17 | 2016-06-17 | The equipment smelted for Pb-Zn deposits |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112048625A (en) * | 2020-07-16 | 2020-12-08 | 云南驰宏锌锗股份有限公司 | Lead-zinc oxide ore recycling harmless treatment system and method |
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| CN105907988B (en) | 2019-05-07 |
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