CN110284009A - A kind of Copper Matte Converting method and apparatus - Google Patents
A kind of Copper Matte Converting method and apparatus Download PDFInfo
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- CN110284009A CN110284009A CN201910568198.6A CN201910568198A CN110284009A CN 110284009 A CN110284009 A CN 110284009A CN 201910568198 A CN201910568198 A CN 201910568198A CN 110284009 A CN110284009 A CN 110284009A
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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
- C22B15/00—Obtaining copper
- C22B15/0026—Pyrometallurgy
- C22B15/0028—Smelting or converting
- C22B15/003—Bath smelting or converting
- C22B15/0041—Bath smelting or converting in converters
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Abstract
The invention discloses a kind of Copper Matte Converting method and apparatus, the Copper Matte Converting method includes: feed step, by the copper matte regulus of smelting furnace generation, is added at one time in converter by the feed inlet being arranged on converter headwall, closes the feed inlet;Blowing step blows to the copper matte regulus in converter, and required cold copper is added in converter by anode scrap charger from fire door in the converting process, and blow grate copper to terminal.Copper matte regulus required in converting process is disposably continuously emitted into converter by Copper Matte Converting method of the present invention from the feed inlet being arranged on converter headwall, to solve the problems, such as that the prior art has that grate is frequent and low vacancy pollution is serious.
Description
Technical field
The present invention relates to copper pyrometallurgy field more particularly to a kind of Copper Matte Converting method and apparatus.
Background technique
Global Copper making is quickly grown, and the scarcity of raw material makes smelting enterprise that must not be not suitable for the variation of raw material, main body
Now high miscellaneous raw material proportion is higher and higher in the feed;Meanwhile being full of to the processing capacity of high miscellaneous raw material as cupper smelting
The criterion of benefit.Copper concentrate material composition is increasingly sophisticated and blister copper impurity element is higher and higher, be mainly reflected in Pb, As, Sb,
The content of Bi, Ni increase;Copper pyrometallurgy end product quality is influenced by more serious, cause anode copper quality fluctuation compared with
Greatly, the stabilization of Cathode Copper Quality is influenced.Anode copper mass directly affects the economic skill of items of Cathode Copper Quality and electrowinning process
Art index;Meanwhile a large amount of unqualified anode copper need to melt down processing, and pyro-refining process back mixing processing cost is caused to increase, and
Cause the back mixing loss of the metals such as copper, gold, silver.
The converting process of copper matte regulus is intermittent cycle operation, and whole process can be divided into two ranks of slag-formation period and copper making period
Section.In the first stage of blowing, with the oxygen blasted in air or oxygen-enriched air strong oxidation reaction occurs for the FeS in copper matte regulus,
The FeS in copper matte regulus is oxidized to FeO and SO at this time2.FeO can be with the SiO in flux after adding flux2It reacts and carries out slag making,
Gradually rise copper content in sulfonium.Since copper matte regulus is different from the mutual solubility very little and density of clinker, so stopping in blowing
Melt can be divided into two layers when wind, and upper layer clinker is periodically discharged.The first stage of Copper Matte Converting characterized by a large amount of clinkers of output,
Therefore also known as slag-formation period.In the second stage of blowing, the oxygen and Cu in air are blasted2Strong oxidation reaction occurs for S, generates
Cu2O and SO2, Cu2O again with unoxidized Cu2S reaction generates Ni metal and SO2.The second stage of Copper Matte Converting be added without flux,
Not slag making, characterized by output blister copper, therefore also known as copper making period.
The side-blown converting process of currently used P-S converter (Pierce-Smith converter), can better adapt to raw material
Variation, product quality reach control and require, and with compared with bottom blowing converting furnace, multiple gun top blast converting furnace, side-blown converting furnace has operation
Simply, the advantages such as cold material processing is more, removing impurities ability is strong.But due to the operation mode of its discontinuity operation, a period needs sublevel
Section feeding leads to its frequent grate;Meanwhile the space requirement to consider crane charging, petticoat pipe design cannot achieve effectively close
Envelope;Because P-S is bessemerized, grate is frequent and petticoat pipe leakproofness difference causes low vacancy pollution more serious, is unable to satisfy environmental protection production and wants
It asks.
Therefore, the existing technology needs to be improved and developed.
Summary of the invention
In view of above-mentioned deficiencies of the prior art, the purpose of the present invention is to provide a kind of Copper Matte Converting method and apparatus, purports
It is frequent there are grate and low vacancy pollution is serious asks using the operation mode of discontinuity operation in solving existing converting process
Topic.
A kind of Copper Matte Converting method, wherein include:
Feed step, the copper matte regulus for generating smelting furnace, are added at one time in converter by the feed inlet being arranged on converter headwall,
Close the feed inlet;
Blowing step blows to the copper matte regulus in converter, and required cold copper passes through anode scrap charger from furnace in the converting process
Mouth is added in converter, and blow grate copper to terminal.
The Copper Matte Converting method, wherein the copper matte regulus flows into the feed inlet from the smelting furnace through chute.
The Copper Matte Converting method, wherein in the feed step, the inlet amount of the copper matte regulus is 180-190t.
The Copper Matte Converting method, wherein in the feed step, loading frequency is 4h/ furnace.
The Copper Matte Converting method, wherein in the feed step, the copper content of the copper matte regulus (copper in copper matte regulus
Mass percent) be 70%-72%.
The Copper Matte Converting method, wherein in the blowing step, volume of air supply 18000-30000Nm3/h。
The Copper Matte Converting method, wherein in the blowing step, the inlet amount of the cold copper is 90-110t.
The Copper Matte Converting method, wherein in the blowing step, the time of the blowing is 200-220min.
The Copper Matte Converting method, wherein include:
When the first converter carries out the feed step, the second converter carries out the blowing step;
When second converter carries out the blowing step, first converter carries out the feed step.
A kind of Copper Matte Converting equipment, wherein include:
Revolving furnace body, the feed inlet being arranged on the revolving furnace body headwall, configuration the feed inlet hermatic door;
The revolving furnace body is P-S converter;
The Copper Matte Converting equipment is for implementing Copper Matte Converting method as described above.
The utility model has the advantages that
1, Copper Matte Converting method of the present invention required copper matte regulus in converting process is disposably continuously emitted into converter, is realized
Single heat continuous converting of converter, avoids the grate in converting process from operating;
2, Copper Matte Converting method of the present invention is not necessarily to feed by crane, is advantageously implemented converter environmental protection collection cigarette system airtightness
Optimization design, so that it is guaranteed that flue gas is further effectively collected;
3, Copper Matte Converting method of the present invention, which remains, original has that P-S converter cold burden rate is high, removing impurities is high-efficient, adaptability
By force, the characteristics of flexible operation.
Detailed description of the invention
Fig. 1 is the schematic perspective view of Copper Matte Converting equipment of the present invention.
Specific embodiment
The present invention provides a kind of Copper Matte Converting method and apparatus, to make the purpose of the present invention, technical solution and effect more
Clear, clear, the present invention is described in more detail below.It should be appreciated that specific embodiment described herein is only used to
It explains the present invention, is not intended to limit the present invention.
In the prior art since the process of bessemerizing is intermittent periodic job, two in the exhaust gas volumn and flue gas of output
Sulfur oxide concentration all fluctuates in very large range, brings a great deal of trouble to acid manufacturing processes.In addition, due to the charging of converting process
It is operated with slagging, so that flue gas is spilt into workshop, be degrading productive labor environment.For existing for existing P-S converter blowing process
Because frequent grate and charging operation caused by low vacancy pollution problem, the purpose of the present invention is to provide a kind of novel Copper Matte Converting sides
Method and equipment, on the basis of pyrometallurgical smelting process provides high-grade matte (copper matte regulus), it is intended to retain original P-S and bessemerize work
The advantage of skill, at the same solve the problems, such as in prior art because frequent grate and charging operation caused by low vacancy pollution.
The present invention provides a kind of Copper Matte Converting method, wherein includes:
Feed step, the copper matte regulus for generating smelting furnace, are added at one time in converter by the feed inlet being arranged on converter headwall,
Close the feed inlet;
Blowing step blows to the copper matte regulus in converter, and required cold copper passes through anode scrap charger from furnace in the converting process
Mouth is added in converter, and blow grate copper to terminal.
Compared with prior art method, Copper Matte Converting method of the present invention passes through the feed inlet being arranged on converter headwall
Disposable continuous feed, the problem for avoiding intermittent periodic job from causing grate frequent;Simultaneously as the present invention is without adopting
It is fed with crane, and then can realize that petticoat pipe seals optimization design.Therefore, Copper Matte Converting method of the present invention can solve because frequently
The problem of low vacancy pollution caused by grate and leakproofness difference, be a kind of converting process technology of high-efficiency environment friendly.
Specifically, the Copper Matte Converting method the following steps are included:
A, the matte (copper matte regulus) of the cupric of Copper making smelting furnace output by successively closed chute and is set to the charging of converter headwall
Mouth is emitted into converter, and realizes the disposable required copper matte regulus amount of completion blowing, closure of feed mouth hermatic door;
B, blowing operation is carried out, required copper-contained material, flux pass through anode scrap charger respectively in converting process and system is added in flux
System is added in converter in converting process by fire door;
C, blister copper terminal is judged automatically by endpoint system, blowing is to terminal inclined the blister copper of output in converter by fire door
Down in blister copper packet, the progress anode furnace pyro-refining of pyro-refining region is transported to by transporting copper trolley.
Copper Matte Converting method of the present invention is the method for bessemerizing, specifically based on the side-blown converting process of P-S converter
A kind of improvement technique.Copper Matte Converting refers to pyrometallurgic copper process of the melting copper matte regulus through oxidative slagging removing sulphur and iron output blister copper.
The Copper Matte Converting process overwhelming majority is carried out in horizontal rotary furnace (PS converter).Fire door, furnace body one are equipped in the middle part of converter body
The horizontally arranged exhaust outlet of lateral edge, to blast compressed air or oxygen-enriched air.The side-blown converting process of P-S converter be pass through by
Air or oxygen-enriched air blast converter, the melt in rabble furnace, and carry out physical-chemical reaction therewith, the final life for obtaining blister copper
Production. art.
Wherein, anode scrap charger mainly by rack, hydraulic system, apparatus for shaping, chain and flight conveyer, throw furnace apparatus, lift
Pushing in device, chute of tumbling, head device, tail-pulley device and detector composition.Specifically the cold copper is inclined by chain scraper conveyor
It is transported to converter feed opening obliquely, after fire door lifts, is pushed anode scrap pile in investment furnace by hydraulic push rod.Anode scrap charger exists
Continuously anode scrap is added in furnace at any time under conditions of not blowing-out, improves converter producing efficiency, it is excessive to reduce converter gas, improves
Site environment, while being of great benefit to flue gas concentration and relieving haperacidity is improved.
System is added in flux, should ensure that supply in time, feed is uniform, easy to operate, accurate measurement.The system is by roasting
Quartzy storehouse is added in flux by charging belt, then is added in furnace through weighing belt, quartzy feeder pipe from converter mouth.During normal production,
Opening, stopping for weighing belt is controlled by computer, and control can also be started switch by scene.
Preferably, the copper matte regulus flows into the feed inlet from smelting furnace through chute.That is, in smelting furnace and converter
Between be provided with chute, for by smelting furnace copper matte regulus be sent into converter in, can be realized continuous feed, avoid passing through crane from
The operation of fire door charging.
In the step A, it is preferable that the copper matte regulus is a kind of high-grade copper matte regulus, the high-grade copper generated by smelting furnace
Sulfonium, copper matte regulus cupric 70-72% help to obtain the blister copper of high-quality, reduce rework rate, reduce production cost.
In the step A, it is preferable that the inlet amount of the copper matte regulus is 180-190t.The present invention can disposably be added
180-190t copper matte regulus, it is not necessary that copper matte regulus is added into furnace in batches in converting process.
In the step B, volume of air supply is controlled by computer control system and is agreed with inlet amount, stove angle perfection.
Specifically, during melting down, stove fascinates from 65 ° to 0 °, and the depth that the eye of wind immerses melt gradually increases, and volume of air supply gradually increases
Add, controls volume of air supply from 18000 Nm3/ h increases to 30000Nm3/ h can effectively reduce the melt splash in converting process.Separately
Outside, at the feed inlet headwall part eye of wind block, i.e., be inserted into drill steel in the eye of wind, block the eye of wind, make compress wind without
Method blasts, and control feed inlet headwall side spray is splashed.
In the step B, single cold Copper treatment amount of furnace is 90-110t, and cold copper is sent into furnace by anode scrap charger,
Charging process not grate.The cold copper of the present invention and flux are added during the blowing of side-blown converting furnace by charging (feeding) equipment.Specifically, cold
Copper is added portionwise in converter by anode scrap charger from fire door, and the cold copper is added portionwise from fire door by anode scrap charger and is turned
Not grate when in furnace.The treating capacity of the cold copper of list furnace of the present invention is big, improves production efficiency.
In the step C, the exhaust gas volumn generated in converting process is about 64000 Nm3/ h, flue gas concentration are about
9.81%, blowing flue gas is effectively collected by closed exhaust fume collecting hood, until reaching blowing end point, grate copper.
Preferably, in the converting process, volume of air supply 18000-30000Nm3/ h, oxygen-supplying amount are 800 ~ 1500 Nm3/ h,
Guarantee converter fully reacting, improves the product quality of blister copper.
The Copper Matte Converting method, wherein in the converting process, cold copper is added by anode scrap charger from fire door in batches
Enter in converter, and the cold copper not grate when being added portionwise in converter by anode scrap charger from fire door.
Preferably, the Copper Matte Converting method, wherein include:
When the first converter carries out feed step, the second converter carries out blowing step;
When the second converter carries out blowing step, the first converter carries out feed step.
In preferred Copper Matte Converting method, the present invention has two side-blown converting furnaces (P-S converter) and alternately produces.Specifically
Ground, smelting furnace quantity-produced method, smelting furnace press certain discharge quantity continuous production, generate copper matte regulus, and two side-blown converting furnaces are
First converter and the second converter, first converter are being blown in feed operation (carrying out the feed step), second converter
Refining operation (carrying out the blowing step), second converter after blowing operation, second converter in feed operation,
First converter is operated in blowing, is guaranteed that copper matte regulus can continuously flow into side-blown converting furnace, is realized smelting furnace continuous production.
More specifically, loading frequency is 4h/ furnace in the step A.It that is to say, the time once fed is 4 hours;The blowing
Time be 200-220min.The time of loading frequency of the present invention and blowing can satisfy two side-blown converting furnaces alternately into
Row feed step and blowing step, and then realize smelting furnace continuous production, improve production efficiency.
The material that the present invention is added in converting furnace has copper matte regulus, cold copper, contains a certain amount of Pb, As, Bi etc. in above-mentioned material
Impurity element, in converting process, impurity element Pb, As, Bi are obtained miscellaneous by removing with agent reaction slag making, voloxidation
The lower blister copper of matter content, ratio of removing amount of impurity and the content for the impurity being added in substance is exactly that impurity is de- during this
Except rate.Copper Matte Converting method impurity removal percentage of the present invention: Pb removal efficiency is de- up to 20% or more, Bi up to 55% or more, As removal efficiency
Except rate is up to 40% or more.
Referring to Figure 1, the present invention provides a kind of Copper Matte Converting equipment, wherein includes:
Revolving furnace body 1, the feed inlet 2 being arranged on 1 headwall of revolving furnace body, the feed inlet 2 are configured with hermatic door;
The revolving furnace body 1 is P-S converter;
The Copper Matte Converting equipment is for implementing Copper Matte Converting method as described above.
Preferably, the charging of 600mm × 600mm is set centered on the above 706mm in center on 1 headwall of revolving furnace body
Mouth 2.The feed inlet 2 is rectangular feed inlet, and the upper half area of headwall is arranged in the feed inlet 2, reduces copper matte regulus at feed inlet 2
Splash.
Preferably, the feed inlet 2 is connect by chute 3 with smelting furnace.Can be realized by the chute 3 will be in smelting furnace
Copper matte regulus is continuously delivered to inside the converter, and crane is avoided to feed.
Preferably, the feed inlet 2 is additionally provided with smoke collecting device.The smoke collecting device is used to collect the cigarette at feed inlet
Gas is further reduced the pollution to air.
Copper Matte Converting equipment of the present invention can realize Copper Matte Converting method as described above, that is, realize copper matte regulus and pass through setting
Feed inlet 2 on 1 headwall of revolving furnace body is fed, and so as to avoid the problem that grate is frequent, is conducive to improve copper products
Quality, effectively reduce the high problem of rework rate.
Specifically, the revolving furnace body 1 is made of furnace foundation and the big main part of furnace body two.
(1) furnace foundation
The furnace foundation is cast by reinforced concrete, and there is the fixed carrying roller chassis of fang bolt in furnace foundation upper surface, on carrying roller chassis
There is the quality of two pairs of carrying roller support stoves in every side above, and makes stove rotate on it.
(2) furnace body
The furnace body is made of furnace shell, fire door, backplate, backing ring, gear wheel, the eye of wind and furnace lining etc..
1. furnace shell
The main body of the revolving furnace body is furnace shell, and furnace shell is welded into cylinder by 40-50mm boiler plate, and cylinder both ends are end cap,
Also it is made of the steel plate of same specification.
Respectively there is a great circle at furnace shell both ends, is supported on carrying roller, and support roller is fixed on stove pedestal by chassis.
2. fire door
A sweptback fire door is opened in the center of furnace shell, fire door is rectangle or circle, and fire door area can account for molten bath maximum
The 15-25% of horizontal plane, preferably 20% or so.
3. backplate
The backplate is welded to the protection board around fire door, its purpose is to protect the furnace shell near fire door, can also protect
The air-intake devices such as air loop duct are protected, make them from the erosion of splash melt.Fire door backplate should have enough length, width and thickness
Degree.
4. rolling ring
The rolling ring is supported by support roller, is played the role of rotating furnace body and is transmitted, carries furnace body quality.The rolling ring of converter has square
Shape, box-shaped, I-shape cross section, copper converter use I-shape cross section.
5. gear wheel
One gear wheel is housed on the furnace shell of converter side, is the driven wheel of converter rotation, when driver motor rotation by subtracting
Fast machine drives pinion gear, and pinion gear drives gear wheel that converter can be made to do 360 ° of positive and negative direction rotations.
6. the eye of wind
The eye of wind is specifically located at below the rear side of converter shell, and according to needing to be provided with 30-60 circular hole, air hose passes through circular hole
And be mounted on bellows by spiral marking connection, after the air hose part protruded into converter builds refractory brick, that is, formed.
7. furnace lining
The refractory materials such as magnesia, chromium is magnesia specifically can be used in the refractory material that the furnace lining is served as a contrast in furnace shell.
Technical solution of the present invention is illustrated below by specific embodiment.
Embodiment 1
The Copper Matte Converting equipment
Original P-S converter is transformed into novel Copper Matte Converting equipment, is in the P-S revolving furnace body headwall above 706mm in center
The feed inlet 2 of center (at the just upper 706mm in the round headwall center of circle) setting 600mm × 600mm, and configured in the feed inlet 2
Hermatic door and smoke collecting device.
It is provided with chute 3 between the feed inlet 2 and smelting furnace, for the copper matte regulus in smelting furnace to be sent into converter,
Wherein the chute can be folded flexible close to one end of feed inlet 2, after the completion of charging, by chute from feed inlet 2
It withdraws from, convenient for closing feed inlet 2.
Copper Matte Converting method described in the present embodiment comprising following steps:
S1, the high-grade matte 72% for generating smelting furnace, are flowed into furnace, inlet amount is by feed chute 3 and feed inlet 2
180t realizes disposable continuous feed, feed time 4h;
S2, air quantity-grate angle linkage control is opened, and it is 18000 ~ 30000Nm that volume of air supply, which is arranged,3/ h, oxygen-supplying amount be 800 ~
1500 Nm3/ h carries out blowing operation;
S3, in converting process, according to furnace temperature and the working of a furnace, system is added in batches by cold copper in the cold copper of 90 ~ 110t(such as 100t)
In secondary addition furnace, converting process not grate;
S4, in converting process, blowing flue gas effectively collected by closed exhaust fume collecting hood, until reaching blowing end point, grate
Copper, duration of blast 200min.
Through detecting, Pb removal efficiency is up to 59.6%, As removal efficiency up to 33.2% or more, Bi removal efficiency up to 43.1%.
Embodiment 2
The Copper Matte Converting equipment
The present embodiment include two be set side by side novel Copper Matte Converting equipment is transformed into as described in the embodiment of the present invention 1, i.e.,
One converter and the second converter.
It is provided with and slips between first converter and the smelting furnace and second converter and the smelting furnace
Slot 3 that is to say that same smelting furnace is connect with the first converter and the second converter respectively by two chutes 3.
Copper Matte Converting method described in the present embodiment, comprising the following steps:
First stage, the first converter: the first converter starts to feed, and the high-grade matte (72%) that smelting furnace is generated passes through charging
Chute 3 flows into the first converter, and inlet amount 180t realizes disposable continuous feed, feed time 4h;
Second converter: the second converter charging finishes, and opens the control of air quantity-grate angle linkage, and be arranged volume of air supply be 18000 ~
30000Nm3/ h, oxygen-supplying amount are 800 ~ 1500 Nm3/ h carries out blowing operation;It, will according to furnace temperature and the working of a furnace in converting process
The cold copper of 90t is added system by cold copper and is added in furnace in batches, converting process not grate;In converting process, the flue gas that blows passes through
Closed exhaust fume collecting hood is effectively collected, until reaching blowing end point, grate copper, duration of blast 220min.
Second stage, the first converter: the first converter charging finishes, and opens air quantity-grate angle linkage control, and confession is arranged
Air quantity is 18000 ~ 30000Nm3/ h, oxygen-supplying amount are 800 ~ 1500 Nm3/ h carries out blowing operation;In converting process, according to furnace
The cold copper of 90t is added system by cold copper and is added in furnace in batches by the mild working of a furnace, converting process not grate;In converting process, blow
Refining flue gas is effectively collected by closed exhaust fume collecting hood, until reaching blowing end point, grate copper, duration of blast 220min;
Second converter: the second converter starts to feed, and the high-grade matte (72%) that smelting furnace is generated is flowed by feed chute 3
In first converter, inlet amount 180t realizes disposable continuous feed, feed time 4h.
Flue gas of the present invention using headwall continuous feed and in fill process effectively collected, converting process not grate
Side-blown converting process technology, can not only retain that original converter adaptability to raw material is strong, and cold burden treating capacity is big, high-efficient excellent of removing impurities
Point, and solve the problems, such as that the flue gas during original converter grate escapes, realize high-efficiency environment friendly production, and scrap build letter
Single, clearly, it can be achieved that quickly up to standard up to producing, the raw material mix trend complicated to reply future has more outstanding for process flow
Advantage has a extensive future.
It should be understood that the application of the present invention is not limited to the above for those of ordinary skills can
With improvement or transformation based on the above description, all these modifications and variations all should belong to the guarantor of appended claims of the present invention
Protect range.
Claims (10)
1. a kind of Copper Matte Converting method characterized by comprising
Feed step, the copper matte regulus for generating smelting furnace, are added at one time in converter by the feed inlet being arranged on converter headwall,
Close the feed inlet;
Blowing step blows to the copper matte regulus in converter, and required cold copper passes through anode scrap charger from furnace in the converting process
Mouth is added in converter, and blow grate copper to terminal.
2. Copper Matte Converting method according to claim 1, which is characterized in that the copper matte regulus is from the smelting furnace through chute stream
Enter in the feed inlet.
3. Copper Matte Converting method according to claim 1, which is characterized in that in the feed step, the copper matte regulus into
Doses is 180-190t.
4. Copper Matte Converting method according to claim 1, which is characterized in that in the feed step, loading frequency 4h/
Furnace.
5. Copper Matte Converting method according to claim 1, which is characterized in that in the feed step, the copper matte regulus contains
Amount of copper is 70%-72%.
6. Copper Matte Converting method according to claim 1, which is characterized in that in the blowing step, volume of air supply is
18000-30000Nm3/h。
7. Copper Matte Converting method according to claim 1, which is characterized in that in the blowing step, the cold copper into
Doses is 90-110t.
8. Copper Matte Converting method according to claim 1, which is characterized in that in the blowing step, the blowing when
Between be 200-220min.
9. Copper Matte Converting method according to claim 1 characterized by comprising
When the first converter carries out the feed step, the second converter carries out the blowing step;
When second converter carries out the blowing step, first converter carries out the feed step.
10. a kind of Copper Matte Converting equipment characterized by comprising
Revolving furnace body, the feed inlet being arranged on the revolving furnace body headwall, configuration the feed inlet hermatic door;
The revolving furnace body is P-S converter;
The Copper Matte Converting equipment is for implementing Copper Matte Converting method as described in claim 1.
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Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101328545A (en) * | 2006-10-19 | 2008-12-24 | 中国恩菲工程技术有限公司 | Process of oxygen bottom blowing continuous copper smelting |
JP2011174175A (en) * | 2010-01-26 | 2011-09-08 | Furukawa Electric Co Ltd:The | Method and apparatus for removing coating layer |
CN105986128A (en) * | 2016-07-05 | 2016-10-05 | 中国恩菲工程技术有限公司 | Thermal state copper and sulfur blowing device |
JP2017500442A (en) * | 2013-11-28 | 2017-01-05 | 金隆銅業有限公司 | Method and device for intelligent determination and endpoint prediction of PS copper converter blowing process |
CN205974630U (en) * | 2016-08-17 | 2017-02-22 | 沈阳有色冶金设计研究院 | Copper smelting device |
-
2019
- 2019-06-27 CN CN201910568198.6A patent/CN110284009B/en active Active
Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101328545A (en) * | 2006-10-19 | 2008-12-24 | 中国恩菲工程技术有限公司 | Process of oxygen bottom blowing continuous copper smelting |
JP2011174175A (en) * | 2010-01-26 | 2011-09-08 | Furukawa Electric Co Ltd:The | Method and apparatus for removing coating layer |
JP2017500442A (en) * | 2013-11-28 | 2017-01-05 | 金隆銅業有限公司 | Method and device for intelligent determination and endpoint prediction of PS copper converter blowing process |
CN105986128A (en) * | 2016-07-05 | 2016-10-05 | 中国恩菲工程技术有限公司 | Thermal state copper and sulfur blowing device |
CN205974630U (en) * | 2016-08-17 | 2017-02-22 | 沈阳有色冶金设计研究院 | Copper smelting device |
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