CN201901695U - Continuous lead smelting device - Google Patents
Continuous lead smelting device Download PDFInfo
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- CN201901695U CN201901695U CN2010206321018U CN201020632101U CN201901695U CN 201901695 U CN201901695 U CN 201901695U CN 2010206321018 U CN2010206321018 U CN 2010206321018U CN 201020632101 U CN201020632101 U CN 201020632101U CN 201901695 U CN201901695 U CN 201901695U
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Abstract
The utility model discloses a continuous lead smelting device, comprising a reacting furnace, a side-blowing gun at an oxidation zone, and a side-blowing gun at a reduction zone, wherein the reacting furnace is internally provided with a partition wall so as to be divided into the oxidation zone and the reduction zone; the lower part of a furnace cavity forms melting tanks; the bottom of the partition wall is provided with a communicating channel for communicating the oxidation zone and the reduction zone; the top wall of the oxidation zone is respectively provided with an oxidation zone feeding port and an oxidation zone smoke discharging port; the top wall of the reduction zone is provided with a reducing agent adding port and a reducing agent smoke discharging port; the furnace wall of the furnace cavity is provided with a siphon lead discharging port and a slag discharging port; the side-blowing gun at the oxidation zone side is connected with the oxidation zone side wall of the reacting furnace so as to side-blow oxygen into the melting tank in the oxidation zone; and the side-blowing gun at the reduction zone is connected with the reduction zone side wall of the reacting furnace so as to side-blow fuel and the oxygen to the melting tank in the reduction zone. According to the continuous lead smelting device disclosed by the utility model, oxidation and reduction are realized in the single reacting furnace, the content of lead in the slag is low, the stability and sealing performances are good, the environmental protection is high, heat content of the slag is fully utilized, so that the energy consumption is reduced.
Description
Technical field
The utility model relates to the plumbous device of a kind of refining, especially relates to a kind of continual lead smelting device.
Background technology
In this year, for improving environment, the refining splicer skill that has been used for suitability for industrialized production both at home and abroad mainly contains QSL method, SKS method, Kivcet method, top blast submergence molten pool melting technology (being mainly Ausmelt method, ISA method and kaldo process).The many lead smelting process of Ka Er are because the stove life-span is short, and operating rate is low, and cost is high all multifactor, therefore is difficult to apply.The SKS method, ISA-blast furnace reduction lead smelting process is the method for carrying out oxidation-reduction smelting in two independent stoves respectively, the Ausmelt method is that the sublevel district carries out redox method in the separate unit stove, and QSL method and Kivcet method are that redox processes is realized in the subregion in the separate unit stove.But Ausmelt method sublevel district's oxidation reduction process dust rate height and flue gas acid preparing and ionic liquid absorb the gas distributing system complexity.The Kivcet method needs strict material preparation process, and flux needs grinding system, and the moisture need of raw material are dried to below 0.5%, and coke also needs dry, the complexity of getting the raw materials ready, energy consumption height, lead-in-dreg instability, cost of investment height.The SKS method, ISA-blast furnace reduction lead smelting process, blast furnace needs the metallurgical coke of consume expensive, and energy consumption is higher, and flow process is longer, the high deficiency of dust rate.
The QSL method realizes redox processes in a reaction vessel, thereby uses wider.But QSL method dust rate is up to 25-30%, and owing to adopt bottom blowing, the lead bullion part that has restored is by oxidation and reduction repeatedly, and leaded being difficult in the finishing slag controlled, and the finishing slag index is undesirable, energy consumption is high, in addition, owing to need rotating, reaction vessel changes rifle, the cost height.
The utility model content
The utility model is intended to solve at least one of technical problem that exists in the prior art.
For this reason, a purpose of the present utility model be to propose that a kind of energy consumption is low, environmental protection, plumbous direct yield height, the simple and low continual lead smelting device of cost.
The utility model proposes a kind of continual lead smelting device, comprise: Reaktionsofen, be provided with partition wall in the described Reaktionsofen and be divided into oxidation zone and reduction zone with furnace chamber with described Reaktionsofen, the bottom of described furnace chamber constitutes the molten bath, the bottom of described partition wall is provided with the communication passage that is communicated with described oxidation zone and reduction zone, be respectively equipped with oxidation zone charging opening and oxidation zone smoke outlet on the roof of described oxidation zone, the roof of described reduction zone is provided with reductive agent and adds inlet and reduction zone smoke outlet, and the furnace wall of described furnace chamber is provided with siphon lead tap and slag notch; Oxidation zone side-blown spray gun, described oxidation zone side-blown spray gun link to each other with the oxidation zone sidewall of described Reaktionsofen so that oxygen side-blowing is arrived in the molten bath of described oxidation zone; With the reduction zone side-blown spray gun, described reduction zone side-blown spray gun links to each other with the reduction zone sidewall of described Reaktionsofen so that fuel and oxygen side-blowing are arrived in the molten bath of described reduction zone.
According to continual lead smelting device of the present utility model, in single Reaktionsofen, can realize oxidation and reduction, and owing to take side-blown, therefore fuel that blows side and oxygen are without the lead bullion that has restored in the reduction zone, therefore oxidation lead bullion repeatedly not, lead tolerance reduces and stable in the slag.And oxidation zone and reduction zone separate, and only the communication passage by the partition wall bottom is communicated with, and communication passage is immersed in the melt when operation, so the upper isolation of oxidation zone and reduction zone, and the flue gas of oxidation zone and reduction zone can not mix, and can distinguish individual curing.Owing to realized continual lead smelting in the Reaktionsofen of single sealing, so good seal performance, feature of environmental protection height has made full use of the heat content of slag, has reduced energy consumption.
Can have following additional technical feature according to continual lead smelting device of the present utility model.
Described oxidation zone sidewall is provided with the oxidation zone gun slot, and described reduction zone sidewall is provided with the reduction zone gun slot, and wherein said oxidation zone side-blown spray gun links to each other with described oxidation zone gun slot and described reduction zone side-blown spray gun links to each other with described reduction zone gun slot.
Described siphon lead tap is arranged on the sidewall of described Reaktionsofen and contiguous described partition wall, and described slag notch is arranged on the reduction zone end wall of described Reaktionsofen.
On the diapire of described furnace chamber, be provided with the settling region in the position of contiguous described siphon lead tap.
The diapire of described furnace chamber is recessed arc.
The top of the reduction zone sidewall of described Reaktionsofen is provided with overfiren air port.
Contiguous slag lining is provided with the furnace wall refrigerating unit in the sidewall of described Reaktionsofen.
Further comprise the oxidation zone burner nozzle on the oxidation zone end wall that is respectively formed at described Reaktionsofen and be formed on reduction zone burner nozzle on the reduction zone end wall of described Reaktionsofen according to the continual lead smelting device of the utility model embodiment.
Be provided with the partition wall refrigerating unit in the described partition wall.
Continual lead smelting device according to the utility model embodiment further comprises oxidation zone waste heat boiler and dust precipitator, and described oxidation zone waste heat boiler links to each other with described oxidation zone smoke outlet and described dust precipitator links to each other with described oxidation zone waste heat boiler.
Continual lead smelting device according to the utility model embodiment further comprises reduction zone waste heat boiler, water cooler and bagroom, described reduction zone waste heat boiler links to each other with described reduction zone smoke outlet, and described water cooler links to each other with described reduction zone waste heat boiler and described bagroom links to each other with described water cooler.
Additional aspect of the present utility model and advantage part in the following description provide, and part will become obviously from the following description, or recognize by practice of the present utility model.
Description of drawings
Above-mentioned and/or additional aspect of the present utility model and advantage are from obviously and easily understanding becoming the description of embodiment in conjunction with following accompanying drawing, wherein:
Fig. 1 is the sectional view according to the continual lead smelting device of the utility model embodiment;
Fig. 2 is the vertical view according to the continual lead smelting device of the utility model embodiment;
Fig. 3 is the sectional view along the line A-A among Fig. 2;
Fig. 4 is the schema according to the continual lead smelting technology of the utility model embodiment continual lead smelting device; With
Fig. 5 is the schema according to the continual lead smelting technology of the continual lead smelting device of another embodiment of the utility model.
Embodiment
Describe embodiment of the present utility model below in detail, the example of described embodiment is shown in the drawings, and wherein identical from start to finish or similar label is represented identical or similar elements or the element with identical or similar functions.Below by the embodiment that is described with reference to the drawings is exemplary, only is used to explain the utility model, and can not be interpreted as restriction of the present utility model.
In description of the present utility model, term " vertically ", " laterally ", " on ", close the orientation of indications such as D score, " preceding ", " back ", " left side ", " right side ", " vertically ", " level ", " top ", " end " or position is based on orientation shown in the drawings or position relation, it only is the utility model rather than require the utility model therefore can not be interpreted as for convenience of description with specific orientation structure and operation to restriction of the present utility model.
In description of the present utility model, term " links to each other ", " connection " should do broad understanding, for example, can be mechanical connection or electrical connection, also can be the connection of two element internals, can be directly to link to each other, and also can link to each other by intermediary, for the ordinary skill in the art, can understand the concrete implication of above-mentioned term as the case may be.
Below with reference to the continual lead smelting device of Fig. 1-3 description according to the utility model embodiment.
As Figure 1-3, the continual lead smelting device according to the utility model embodiment comprises Reaktionsofen 1, oxidation zone side-blown spray gun 2 and reduction zone side-blown spray gun 3.
Be provided with partition wall 4 in the Reaktionsofen 1, partition wall 4 is divided into oxidation zone Y and reduction zone H with the furnace chamber of Reaktionsofen 1, and the bottom of partition wall 4 is provided with the communication passage 41 that is communicated with oxidation zone Y and reduction zone H.The bottom of the furnace chamber of Reaktionsofen 1 constitutes the molten bath, and in the molten bath, L1 is the liquid level of slag, and L2 is the liquid level of lead bullion.In a concrete example of the present utility model, Reaktionsofen 1 can be the fixedly horizontal reacting container of long ellipse shape.Therefore, the Reaktionsofen 1 according to the utility model embodiment also can be called fixedly horizontal chamber oven.The diapire of the furnace chamber of reflection stove 1 can be recessed arc, as shown in Figure 3.
Be respectively equipped with oxidation zone charging opening 11 and oxidation zone smoke outlet 12 on the roof of oxidation zone Y.The roof of reduction zone H is provided with reductive agent and adds inlet 13 and reduction zone smoke outlet 14.The furnace wall of the furnace chamber of Reaktionsofen 1 is provided with siphon lead tap 18 and slag notch 20.
Oxidation zone side-blown spray gun 2 links to each other with the oxidation zone sidewall of Reaktionsofen 1 in the molten bath with oxidation zone Y that industrial oxygen (or oxygen-rich air) is blown side, thereby lead-containing material is carried out melting.Reduction zone side-blown spray gun 3 link to each other with the reduction zone sidewall of Reaktionsofen 1 with fuel and oxygen side-blowing in the molten bath of reduction zone H.
As shown in Figure 1, more specifically, oxidation zone side-blown spray gun 2 is injected to oxidation with industrial oxygen and goes under the liquid level L1 of slag on the liquid level L2 of lead bullion in the molten bath of Y, in other words, oxidation zone side-blown spray gun 2 is injected to industrial oxygen in the rich lead skim in the oxidation zone Y, reduction zone side-blown spray gun 3 is injected to fuel and oxygen in the slag in the H of reduction zone, thereby in the H of reduction zone, the not lead bullion that restored of oxidation repeatedly of fuel in the molten bath of reduction zone H and oxygen is gone in reduction zone side-blown spray gun 3 side-blown.
Continual lead smelting device according to the utility model embodiment, also can be called continuous side-blown and refine plumbous device, lead-containing material (for example lead ore concentrate) and flux join in the oxidation zone Y from oxidation zone charging opening 11, and the industrial oxygen that sprays into by oxidation zone side-blown spray gun 2 carries out melting to lead ore concentrate and obtains lead bullion and rich lead skim.Rich lead skim in the oxidation zone Y flows in the H of reduction zone from the communication passage 41 (being the bottom surface of partition wall 4 and the passage between the furnace chamber bottom surface) of partition wall 4 bottoms.From reductive agent add inlet 13 in the H of reduction zone, add reductive agent for example beans the lead the rich lead skim is reduced, and spray into fuel and oxygen to keep the temperature of reduction zone H by the slag inboard of reduction zone side-blown spray gun 3 in the H of reduction zone.It will be appreciated that by the control straying quatity, the part of fuel that reduction zone side-blown spray gun 3 sprays into also can be made reductive agent and reduce rich lead skim simultaneously with the beans of adding.
Continual lead smelting device according to the utility model embodiment, in single Reaktionsofen 1, can realize oxidation and reduction, and owing to take side-blown, therefore fuel that H blows side in the reduction zone and oxygen are without the lead bullion that has restored, therefore oxidation lead bullion repeatedly not, lead tolerance reduces and stable in the slag.And oxidation zone Y and reduction zone H separate, and only the communication passage 41 by partition wall 4 bottoms is communicated with, communication passage 41 is immersed in the melt when operation, so the upper isolation of oxidation zone Y and reduction zone H, the flue gas of oxidation zone and reduction zone can not mix, and can distinguish individual curing.Owing to realized continual lead smelting in the Reaktionsofen of single sealing, so good seal performance, feature of environmental protection height has made full use of the heat content of slag, has reduced energy consumption.
The lead bullion that produces in lead bullion that produces in the H of reduction zone and the oxidation zone Y is discharged by siphon lead tap 18, and the slag (slag after promptly being reduced in the H of reduction zone) that produces in the H of reduction zone is regularly discharged from slag notch 20.
The flue gas that produces in the oxidation zone Y contains a large amount of sulfurous gas, discharges from oxidation zone smoke outlet 12, through waste heat recovery and dedusting, in order to relieving haperacidity.The flue gas that produces in the H of reduction zone is discharged from reduction zone smoke outlet 14, through waste heat recovery and dedusting discharging.The flue dust that reclaims the flue gas in oxidation zone Y and reduction zone H turns back in the oxidation zone Y.
Thus, continual lead smelting device according to the utility model embodiment, continual lead smelting and regular deslagging have been realized, and oxidation zone Y only is communicated with by communication passage 41 with reduction zone H, and communication passage 41 is owing to be immersed in the melt, therefore the flue gas that produces in the oxidation zone Y can not mix with the interior flue gas that produces of reduction zone H, helps the high density S0 in the oxidation zone Y
2The continuous relieving haperacidity of flue gas and maintenance oxidation zone Y and reduction zone H melting system separately.And owing to adopt side-blown spray gun, therefore the side-blown of oxidation zone Y and reduction zone H can not influence the lead bullion that has produced, therefore control and the reduction easily of the lead tolerance in the slag, for example lead tolerance can stably be reduced to 2-3%, and in the existing QSL lead smelting process, lead tolerance is more than 5% and unstable in the slag.
In specific embodiments more of the present utility model, the oxidation zone sidewall is provided with the oxidation zone gun slot, the reduction zone sidewall is provided with the reduction zone gun slot, and oxidation zone side-blown spray gun 2 links to each other with the oxidation zone gun slot and reduction zone side-blown spray gun 3 links to each other with described reduction zone gun slot.Here, it can be that oxidation zone side-blown spray gun 2 is inserted in the oxidation zone gun slot that oxidation zone side-blown spray gun 2 links to each other with the oxidation zone gun slot, and it can be that reduction zone side-blown spray gun 3 is inserted in the gun slot of described reduction zone that reduction zone side-blown spray gun 3 links to each other with described reduction zone gun slot.
Shown in Fig. 2 and 3, siphon lead tap 18 is arranged on the sidewall of Reaktionsofen 1 and contiguous partition wall 4, and slag notch 20 is arranged on the reduction zone end wall (the left end wall of reflection stove 1 among Fig. 1).
In embodiment more of the present utility model, the position of contiguous siphon lead tap 18 is provided with settling region 19 on the diapire of furnace chamber.Thus, the lead bullion that oxidation zone Y and reduction zone H produce accumulates in the settling region 19, discharges continuously from siphon lead tap 18 then, has reduced the lead tolerance in the slag.
In embodiment more of the present utility model, the top of the reduction zone sidewall of Reaktionsofen 1 is provided with overfiren air port 15.The flue gas that reduction zone H produces is discharged by reduction zone smoke outlet 14 behind the superfluous combustiblematerialss such as C0 in by the secondary air combustion product gases that infeeds by overfiren air port 15 on H top, reduction zone, has improved environmental-protecting performance and safety performance.
In embodiment more of the present utility model, the position of contiguous slag line L1 is provided with the furnace wall refrigerating unit in the furnace wall of Reaktionsofen 1, and for example watercooling jacket 5, thus Reaktionsofen 1 cooled off, and prolonged the life-span of Reaktionsofen 1.
May further include the oxidation zone burner nozzle 17 on the oxidation zone end wall (the right-hand member wall among Fig. 1) that is respectively formed at Reaktionsofen 1 and be formed on reduction zone burner nozzle 16 on the reduction zone end wall (the left end wall among Fig. 1) of Reaktionsofen 1 according to the continual lead smelting device of the utility model embodiment.Can be respectively in oxidation zone Y and reduction zone H, spray into fuel by oxidation zone burner and reduction zone burner when the blow-on by oxidation zone burner nozzle 17 and reduction zone burner nozzle 16, for example heavy oil.
In embodiment more of the present utility model, be provided with the partition wall refrigerating unit in the partition wall 4, can cool off partition wall 4 thus.
Continual lead smelting device according to the utility model embodiment may further include oxidation zone waste heat boiler and dust precipitator, described oxidation zone waste heat boiler links to each other with oxidation zone smoke outlet 12 and described dust precipitator links to each other with described oxidation zone waste heat boiler, thus the oxidation zone flue gas of discharging from oxidation zone smoke outlet 12 is carried out waste heat recovery and dedusting, send to relieving haperacidity then.The waste heat that reclaims can generate electricity or for resident living usefulness, flue dust can return oxidation zone Y.
Continual lead smelting device according to the utility model embodiment may further include reduction zone waste heat boiler, water cooler and bagroom, described reduction zone waste heat boiler links to each other with reduction zone smoke outlet 14, and for example surface cooler links to each other with described reduction zone waste heat boiler described water cooler and described bagroom links to each other with described water cooler.The reduction zone waste heat boiler reclaims the waste heat of reduction zone flue gas, and then through the supercooler cooling, then through discharging after the bagroom dedusting, the flue dust of recovery can return oxidation zone Y.
The continual lead smelting technology that utilization is carried out according to the continual lead smelting device of the utility model embodiment is described below.
As shown in Figure 4, in conjunction with Fig. 1-3, may further comprise the steps according to the continual lead smelting technology of the utility model embodiment:
Lead-containing material and flux are joined in the oxidation zone Y of Reaktionsofen 1;
(be slag line L2 below and lead bullion line L1 top) sprays into oxygen and obtains lead bullion and rich lead skim lead-containing material is carried out melting in the molten bath of oxidation zone Y from the side of the oxidation zone Y of Reaktionsofen 1;
Reductive agent and flux are joined in the reduction zone H of Reaktionsofen 1;
In the molten bath of reduction zone H, spray into oxygen and fuel from the side of the reduction zone H of Reaktionsofen 1 to reduce and obtain lead bullion and slag to flow to rich lead skim in the H molten bath, reduction zone by communication passage 41;
Discharge lead bullion from siphon lead tap 18; With
Regularly discharge slag from slag notch 20.
As shown in Figure 5, may further include from the side, reduction zone of Reaktionsofen 1 according to the continual lead smelting technology of another embodiment of the utility model and send into the combustiblecomponentss such as carbon monoxide of secondary air with the oxidation surplus that reduction process produces in the H of reduction zone to the top in the molten bath of reduction zone H; Discharge the oxidation zone flue gas that produces in the oxidation zone Y from the top of oxidation zone Y; Reclaim the waste heat of oxidation zone flue gas; Oxidation zone flue gas behind the recovery waste heat is carried out dedusting; With the oxidation zone flue gas acid preparing that utilizes after the dedusting; Discharge the reduction zone flue gas that produces in the H of reduction zone from the top of reduction zone H; Reclaim the waste heat of reduction zone flue gas; Reduction zone flue gas behind the cooling recovery waste heat; Carry out discharging after the dedusting with cooled reduction zone flue gas.
In an embodiment of the present utility model, oxidation zone flue gas ash removal and reduction zone flue gas ash removal are obtained flue dust turn back in the oxidation zone Y.
In an example of the present utility model, reductive agent can be beans, does not need more expensive metallurgical coke relatively thus, has further reduced cost.Lead-containing material can be lead ore concentrate, and can arrange in pairs or groups and handle other lead-containing materials.Fuel is fine coal, Sweet natural gas, coal gas or kerosene.
Continual lead smelting device according to the utility model embodiment is continuously the plumbous device of side-blown refining, compared with prior art has outstanding technical superiority.
In separate unit side-blown Reaktionsofen, realize that the subregion carries out oxidation, retailoring continuously according to the continual lead smelting device of the utility model embodiment, therefore belong to molten pool melting technology, to going into stove granularity, moisture less demanding, the system that gets the raw materials ready is simple, and technical process is short, airborne dust point and dispersion point are few, and system is airtight, help environmental protection, two smelting zones are that oxidation zone Y and reduction zone H all adopt industrial oxygen, reduction zone H fuel consumption is low, reduces controlledly, and exhaust gas volumn is few, dust rate is low, and energy consumption is low.
More specifically, be continuous side-blowing bath smelting technique according to the continual lead smelting device of the utility model embodiment, directly refining is plumbous to be used for concentrate of lead sulfide ore (and the treating part lead-containing material of can arranging in pairs or groups).In separate unit side-blown Reaktionsofen, finish oxidation, the retailoring process, lead ore concentrate and lead-containing material, flux, return dirt etc. after batching is granulated, the oxidation zone Y that adds the side-blown smelting furnace continuously, send into industrial oxygen by oxidation zone side-blown spray gun 2, finish melting, oxidation, desulfuration operations, the sulfur dioxide flue gas of output high density is discharged by oxidation zone smoke outlet 12, after waste heat recovery and dedusting, send the relieving haperacidity of sour factory, the tail gas qualified discharge, the lead bullion of oxidation zone Y output is discharged by siphon lead tap 18, rich lead skim enters reduction zone H, reduction zone side-blown spray gun 3 sprays into fuel (for example, fine coal in the H of reduction zone, Sweet natural gas, coal gas or fuel oil) and industrial oxygen, the temperature of reducing and keeping reduction zone H improved, the required reductive agent beans of process adds inlet 13 by reductive agent and adds, and drops to 2-3% and stable to guarantee the lead-in-dreg after the reduction.The flue gas that reduction zone H produces in by the secondary air combustion product gases behind the superfluous combustiblematerialss such as CO, is discharged qualified discharge after waste heat recovery, cooling dedusting on H top, reduction zone by reduction zone smoke outlet 14.Slag in the H of reduction zone regularly discharges (for example, every 1.5-2h discharging once), and slag can send the valuable metals such as zinc in the fuming furnace recovery slag.
Technical superiority according to the continual lead smelting device of the utility model embodiment is:
1, energy consumption is low: realizing the fusion process from the lead ore concentrate to the lead bullion in separate unit side-blown Reaktionsofen 1 the inside, the fuel that does not need to replenish other at oxidation zone Y, make full use of reaction heat, made full use of the heat content of slag at reduction zone H, consume less fuel, use beans as reductive agent, do not need more expensive metallurgical coke relatively, reclaim the waste heat in oxidation zone and the reduction zone flue gas simultaneously.
2, environmental protection is good: the lead ore concentrate fusion process carries out in the airtight melting of separate unit blows side Reaktionsofen 1, has avoided flue gas to escape, the SO in the oxidation zone Y
2Flue gas through waste heat recovery and electricity gather dust send relieving haperacidity after, exhaust emissions has reached environmental requirement.Lead ore concentrate or other leady raw materials cooperate the back of granulating directly into stove, and the material preparation process is simple, and the lead fume dirt of output all seals conveying and returns batching in the production process, has effectively prevented the disperse of lead dust; The flue gas of reduction zone H output after waste heat recovery and gathering dust, the tail gas qualified discharge.The lead bullion of oxidation zone Y and reduction zone H output is discharged from siphon lead tap 18, and the slag of output is regularly discharged from slag notch 20, can establish the ventilating chamber at siphon lead tap 18 and slag notch 20 simultaneously, prevents the diffusion of plumbous steam.Can the plumbous flue gas during smelting of very thorough solution, the problem of lead dust pollution.
3, rate of recovery height: in the Reaktionsofen 1 that blows side continuously, owing to utilized the heat content of slag fully, to consume less fuel at reduction zone H and carry out concurrent heating, use beans as reductive agent, effectively reduce exhaust gas volumn and dust rate, reduced the lead content in the slag, improved the plumbous direct yield and the rate of recovery.
4. the lead smelting process that blows side continuously is in all lead smelting processs, comprises the material preparation system, the technology that flow process is the shortest, and process unit is simple, reduced investment.
In the description of this specification sheets, concrete feature, structure, material or characteristics that the description of reference term " embodiment ", " some embodiment ", " example ", " concrete example " or " some examples " etc. means in conjunction with this embodiment or example description are contained at least one embodiment of the present utility model or the example.In this manual, the schematic statement to above-mentioned term not necessarily refers to identical embodiment or example.And concrete feature, structure, material or the characteristics of description can be with the suitable manner combination in any one or more embodiment or example.
Although illustrated and described embodiment of the present utility model, those having ordinary skill in the art will appreciate that: can carry out multiple variation, modification, replacement and modification to these embodiment under the situation that does not break away from principle of the present utility model and aim, scope of the present utility model is limited by claim and equivalent thereof.
Claims (11)
1. a continual lead smelting device is characterized in that, comprising:
Reaktionsofen, be provided with partition wall in the described Reaktionsofen and be divided into oxidation zone and reduction zone with furnace chamber with described Reaktionsofen, the bottom of described furnace chamber constitutes the molten bath, the bottom of described partition wall is provided with the communication passage that is communicated with described oxidation zone and reduction zone, be respectively equipped with oxidation zone charging opening and oxidation zone smoke outlet on the roof of described oxidation zone, the roof of described reduction zone is provided with reductive agent and adds inlet and reduction zone smoke outlet, and the furnace wall of described furnace chamber is provided with siphon lead tap and slag notch;
Oxidation zone side-blown spray gun, described oxidation zone side-blown spray gun link to each other with the oxidation zone sidewall of described Reaktionsofen so that oxygen side-blowing is arrived in the molten bath of described oxidation zone; With
Reduction zone side-blown spray gun, described reduction zone side-blown spray gun link to each other with the reduction zone sidewall of described Reaktionsofen so that fuel and oxygen side-blowing are arrived in the molten bath of described reduction zone.
2. continual lead smelting device according to claim 1, it is characterized in that, described oxidation zone sidewall is provided with the oxidation zone gun slot, described reduction zone sidewall is provided with the reduction zone gun slot, and wherein said oxidation zone side-blown spray gun links to each other with described oxidation zone gun slot and described reduction zone side-blown spray gun links to each other with described reduction zone gun slot.
3. continual lead smelting device according to claim 1 is characterized in that, described siphon lead tap is arranged on the sidewall of described Reaktionsofen and contiguous described partition wall, and described slag notch is arranged on the reduction zone end wall of described Reaktionsofen.
4. continual lead smelting device according to claim 1 is characterized in that, is provided with the settling region in the position of contiguous described siphon lead tap on the diapire of described furnace chamber.
5. continual lead smelting device according to claim 1 is characterized in that, the diapire of described furnace chamber is recessed arc.
6. continual lead smelting device according to claim 1 is characterized in that, the top of the reduction zone sidewall of described Reaktionsofen is provided with overfiren air port.
7. continual lead smelting device according to claim 1 is characterized in that, contiguous slag lining is provided with the furnace wall refrigerating unit in the sidewall of described Reaktionsofen.
8. continual lead smelting device according to claim 1 is characterized in that, further comprises the oxidation zone burner nozzle on the oxidation zone end wall that is respectively formed at described Reaktionsofen and is formed on reduction zone burner nozzle on the reduction zone end wall of described Reaktionsofen.
9. continual lead smelting device according to claim 1 is characterized in that, is provided with the partition wall refrigerating unit in the described partition wall.
10. continual lead smelting device according to claim 1, it is characterized in that, further comprise oxidation zone waste heat boiler and dust precipitator, described oxidation zone waste heat boiler links to each other with described oxidation zone smoke outlet and described dust precipitator links to each other with described oxidation zone waste heat boiler.
11. continual lead smelting device according to claim 1, it is characterized in that, further comprise reduction zone waste heat boiler, water cooler and bagroom, described reduction zone waste heat boiler links to each other with described reduction zone smoke outlet, and described water cooler links to each other with described reduction zone waste heat boiler and described bagroom links to each other with described water cooler.
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| CN2010206321018U CN201901695U (en) | 2010-11-21 | 2010-11-21 | Continuous lead smelting device |
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| CN2010206321018U CN201901695U (en) | 2010-11-21 | 2010-11-21 | Continuous lead smelting device |
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Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102011014A (en) * | 2010-11-21 | 2011-04-13 | 中国恩菲工程技术有限公司 | Continuous lead-smelting device and continuous lead-smelting process |
| CN103146929A (en) * | 2013-03-29 | 2013-06-12 | 郴州市金贵银业股份有限公司 | Efficient enrichment and recycling technique of valuable metals in lead smelting slags |
| CN103937991A (en) * | 2014-04-08 | 2014-07-23 | 云南锡业股份有限公司 | Fractional collecting process of lead-smelting soot of top blowing furnace |
| CN105907987A (en) * | 2016-04-26 | 2016-08-31 | 中国瑞林工程技术有限公司 | Smelting furnace and copper matte preparation method using same |
| CN106744758A (en) * | 2016-11-11 | 2017-05-31 | 长沙有色冶金设计研究院有限公司 | A kind of method that decomposing phosphate rock stone produces phosphoric acid |
| WO2017197985A1 (en) * | 2016-05-16 | 2017-11-23 | 中国恩菲工程技术有限公司 | Side-submerged combustion smelting apparatus for spraying oxygen-enriched air and pulverized coal |
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2010
- 2010-11-21 CN CN2010206321018U patent/CN201901695U/en not_active Expired - Lifetime
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| Publication number | Priority date | Publication date | Assignee | Title |
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| CN102011014A (en) * | 2010-11-21 | 2011-04-13 | 中国恩菲工程技术有限公司 | Continuous lead-smelting device and continuous lead-smelting process |
| WO2012065327A1 (en) * | 2010-11-21 | 2012-05-24 | 中国恩菲工程技术有限公司 | Continuous lead smelting device and continuous lead smelting method |
| CN102011014B (en) * | 2010-11-21 | 2012-11-14 | 中国恩菲工程技术有限公司 | Continuous lead-smelting device and continuous lead-smelting process |
| CN103146929A (en) * | 2013-03-29 | 2013-06-12 | 郴州市金贵银业股份有限公司 | Efficient enrichment and recycling technique of valuable metals in lead smelting slags |
| CN103937991A (en) * | 2014-04-08 | 2014-07-23 | 云南锡业股份有限公司 | Fractional collecting process of lead-smelting soot of top blowing furnace |
| CN105907987A (en) * | 2016-04-26 | 2016-08-31 | 中国瑞林工程技术有限公司 | Smelting furnace and copper matte preparation method using same |
| WO2017197985A1 (en) * | 2016-05-16 | 2017-11-23 | 中国恩菲工程技术有限公司 | Side-submerged combustion smelting apparatus for spraying oxygen-enriched air and pulverized coal |
| RU2710084C1 (en) * | 2016-05-16 | 2019-12-24 | Чайна Энфи Инжиниринг Корпорейшн | Melting unit with side submersible combustion of pulverized coal and oxygen enriched air |
| AU2017266791B2 (en) * | 2016-05-16 | 2020-07-23 | China Enfi Engineering Corporation | Side-submerged combustion smelting apparatus for spraying oxygen-enriched air and pulverized coal |
| CN106744758A (en) * | 2016-11-11 | 2017-05-31 | 长沙有色冶金设计研究院有限公司 | A kind of method that decomposing phosphate rock stone produces phosphoric acid |
| CN106744758B (en) * | 2016-11-11 | 2019-02-12 | 长沙有色冶金设计研究院有限公司 | A kind of method of decomposing phosphate rock stone production phosphoric acid |
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