CN207811837U - A kind of single system continuous copper smelting apparatus - Google Patents
A kind of single system continuous copper smelting apparatus Download PDFInfo
- Publication number
- CN207811837U CN207811837U CN201820274633.5U CN201820274633U CN207811837U CN 207811837 U CN207811837 U CN 207811837U CN 201820274633 U CN201820274633 U CN 201820274633U CN 207811837 U CN207811837 U CN 207811837U
- Authority
- CN
- China
- Prior art keywords
- smelting
- discharge port
- blowing
- copper
- blowing area
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P10/00—Technologies related to metal processing
- Y02P10/20—Recycling
Landscapes
- Manufacture And Refinement Of Metals (AREA)
Abstract
The utility model discloses a kind of single system continuous copper smelting apparatus, including smelting zone, blowing area, siphon passage, blister copper discharge port, smelting slag discharge port and blowing slag discharge port, the smelting zone is connect with blowing area by siphon passage, the blister copper discharge port, blowing slag discharge port are connect with blowing area, and the smelting slag discharge port is connect with smelting zone.Side-blown smelting technology is combined by the utility model with continous way converting process, provides a kind of single system continuous copper smelting apparatus, which can repeatedly aoxidize copper concentrate in single system, is segmented deslagging, is directly obtained high quality blister copper.
Description
Technical field
The utility model is related to non-ferrous metal metallurgy technical fields, and in particular to a kind of single system continuous copper smelting apparatus.
Background technology
Copper making technology just develops progressively towards the direction of cleaning, efficient, short route and serialization, domestic and international Copper making enterprise
The Copper making technique that production capacity is big, investment is low with operating cost, operation is continuous, environmental-friendly is actively sought or developed to industry.China exists
During large and medium-sized Copper making is newly-built or transformation project, the selection and exploitation of smelting technology and converting process are paid much attention to, introducing, disappearing
While changing advanced technology, melting technique and continuous converting technology of the exploitation with independent intellectual property right are put forth effort on, in work
Skill is developed and equipment manufacturing, operational management etc. gradually reduce and world-class gap.
Existing Copper making thermal process additionally includes flash smelting+flash based on single stove melting matte+bessemerize
Blowing, the techniques such as Mitsubishi method melting+blowing, removal of impurities and desulfurization journey of the main still control copper concentrate in different stoves
Degree, the shortcomings that these techniques are that the raw material-matte bessemerized is transported by metallurgical traveling crane, should in the process there are inorganization flue gas,
Its air supply process is periodically, to prevent the content of sulfur dioxide in flue gas from keeping stable, influence flue gas acid preparing process simultaneously
Stable operation, fire door and petticoat pipe seal are bad, largely suck air, increase equipment investment and operating cost;Flash blows
It needs the matte of melting being first granulated, re-melting increases operating cost;The blister copper sulfur-bearing of Mitsubishi process blowing is high, influences
Anode furnace production efficiency.
Existing converting furnace preferably completes blowing task, but existing low vacancy pollution, periodic job, high operation at
Sheet, low blister copper quality, the problems such as flow is longer, and make that copper furnace structure is unreasonable, and it is still necessary to Optimal improvements.
Utility model content
For the low vacancy pollution of existing converter, relieving haperacidity cycling service fluctuation, flash blowing operating cost height, Mitsubishi's blowing
Side-blown smelting technology is combined by the problems such as blister copper quality is low, the utility model with continous way converting process, provides a kind of list
System continuous copper smelting apparatus, the device can repeatedly aoxidize copper concentrate in single system, are segmented deslagging, directly obtain high quality
Blister copper.
To realize that purpose of utility model, the utility model use following technical scheme:
A kind of single system continuous copper smelting apparatus, including smelting zone, blowing area, siphon passage, blister copper discharge port, melting
Slag discharge port and blowing slag discharge port, the smelting zone are connect with blowing area by siphon passage, and the product after one section of oxidation is logical
It crosses siphon passage and is directly entered blowing area, do not need metallurgical traveling crane transhipment, solve the problems, such as the low vacancy pollution in transport process, institute
State blister copper discharge port, blowing slag discharge port is connect with blowing area, the smelting slag discharge port is connect with smelting zone.
Preferably, there are liquid level differences with inside blowing area for the smelting zone, and the liquid level of the smelting zone is higher than blowing area
Liquid level, the melting white metal that smelting zone generates voluntarily flow to blowing area, therefore the building base of smelting zone and blowing area because of liquid level difference
Plinth may be at identical horizontal plane, it is not necessary to have normal throw, reduce production cost.
Preferably, further include top-blown spray gun and the side-blown eye of wind, the top-blown spray gun is perpendicularly inserted into from top in blowing area,
For the side-blown eye of wind horizontal arrangement in blowing area both sides, impurity desulfurization is more thorough.
Preferably, the top-blown spray gun and the side-blown eye of wind are multiple, and air-supply is uniform.
The course of work:By copper-contained material(Including copper concentrate, containing copper fumes, return slag etc.)Make one section of oxidation removal in smelting zone
Most iron and other impurity, obtain high-grade white metal(Cupric 70%-75%), white metal enters blowing by siphon passage
Area makees two sections of oxidations, and by top-blown spray gun and the side-blown eye of wind, into blowing area, melt is blown air feed, based on top blast, it is side-blown supplemented by,
Almost all sulphur and remaining impurity are removed, the blister copper for meeting subsequent production is obtained.
The utility model has the beneficial effects that:
1, smelting zone and blowing area are combined together by the utility model by siphon passage, become an entirety, are utilized
Production capacity big feature in smelting zone provides enough white metal melts, and blowing area persistently blows, and continual can produce high quality
Blister copper, do not need additional transhipment and intermediary advanced treating, be allowed to continuously make copper in single device, it is steady to reach total system
Surely the purpose run, improves work efficiency, and effectively reduces production cost;
2, the blowing area of the utility model during the reaction, oxidation oxygen demand, Ke Yichi is controlled by white metal amount
Continuous oxygen supply, is not present periodic job process, reduces the fluctuation of acid making system, keep production run more stable;
3, the utility model fusion process all carries out in the present apparatus, and situation of leaking out existing for previous converter obtains effectively
Improve, while white metal is also not required to specially treated, it is directly hot to enter blowing area, improve production efficiency;
4, all smoke evacuation points of the utility model are fixed smoke evacuation, and exhaust smoke level is limited, can all pass through live ring collection
Facility collects post-processing, and handled exhaust gas volumn is only the 10%-15% of converter ring collection tolerance, and exhaust gas volumn is stablized, and is conducive to pollutant
Removing is handled;
5, the utility model is due to being equipped with siphon passage, avoids the problem of outdoor chute flue gas loss, institute's loss it is micro-
Amount flue gas, which can be collected all, send subsequent processing, and scene environmental protection situation is excellent;
6, the utility model solves the problems, such as that previous copper metallurgy operating cost is high, such as:Converter high warm air caused by leaking out
The operating cost of machine, acid making system, to solve the ring collecting system operating cost of converter low vacancy pollution special configuration, flash blowing institute
The white metal granulation of need, melting cost, Mitsubishi process blowing is caused by blister copper sulfur-bearing height needed for the reduction of anode furnace production efficiency
Operating cost etc., significantly reduces operating cost.
Description of the drawings
Fig. 1 is the structural schematic diagram of the utility model;
In figure:1, smelting zone;2, blow area;3, siphon passage;4, blister copper discharge port;5, smelting slag discharge port;6、
Blow slag discharge port;7, top-blown spray gun;8, the side-blown eye of wind.
Specific implementation mode
The utility model is further described by specific implementation mode below in conjunction with the accompanying drawings.
As shown in Figure 1, a kind of single system continuous copper smelting apparatus, including smelting zone 1, blowing area 2, siphon passage 3, blister copper production
Product discharge port 4, smelting slag discharge port 5 and blowing slag discharge port 6, the smelting zone 1 are connect with blowing area 2 by siphon passage 3,
Product after one section of oxidation is directly entered blowing area 2 by siphon passage 3, does not need metallurgical traveling crane transhipment, solves and transported
Low vacancy pollution problem in journey, the blister copper discharge port 4, blowing slag discharge port 6 are connect with blowing area 2, the melting
Slag discharge port 5 is connect with smelting zone 1, and there are liquid level difference, the liquid level height of the smelting zone 1 with inside blowing area 2 for the smelting zone 1
Liquid level in blowing area 2, the melting white metal that smelting zone 1 generates voluntarily flow to blowing area 2, therefore 1 He of smelting zone because of liquid level difference
The building foundation in blowing area 2 may be at identical horizontal plane, it is not necessary to have normal throw, reduce production cost.
Specifically, further including top-blown spray gun 7 and the side-blown eye of wind 8, the top-blown spray gun 7 is perpendicularly inserted into blowing area from top
In 2,8 horizontal arrangement of the side-blown eye of wind is in blowing 2 both sides of area, and impurity desulfurization is more thorough, the top-blown spray gun 7 and cross air blasting
Eye 8 is multiple, and air-supply is uniform.
The course of work:By copper-contained material(Including copper concentrate, containing copper fumes, return slag etc.)Make one section of oxidation removal in smelting zone
Most iron and other impurity, obtain high-grade white metal(Cupric 70%-75%), white metal enters blowing by siphon passage
Area makees two sections of oxidations, and by top-blown spray gun and the side-blown eye of wind, into blowing area, melt is blown air feed, based on top blast, it is side-blown supplemented by,
Almost all sulphur and remaining impurity are removed, the blister copper for meeting subsequent production is obtained.
The foregoing is merely the structure features of specific embodiment of the utility model, but the utility model to be not limited to
This, the utility model can be used on similar product, and any those skilled in the art is in the field of the utility model, institute
The changes or modifications of work all cover among the scope of the claims of the utility model.
Claims (4)
1. a kind of single system continuous copper smelting apparatus, it is characterised in that:It is put including smelting zone, blowing area, siphon passage, blister copper
Outlet, smelting slag discharge port and blowing slag discharge port, the smelting zone are connect with blowing area by siphon passage, the blister copper production
Product discharge port, blowing slag discharge port are connect with blowing area, and the smelting slag discharge port is connect with smelting zone.
2. single system continuous copper smelting apparatus as described in claim 1, it is characterised in that:It is deposited inside the smelting zone and blowing area
In liquid level difference, the liquid level of the smelting zone is higher than the liquid level in blowing area.
3. single system continuous copper smelting apparatus as described in claim 1, it is characterised in that:Further include top-blown spray gun and cross air blasting
Eye, the top-blown spray gun are perpendicularly inserted into from top in blowing area, and the side-blown eye of wind horizontal arrangement is in blowing area both sides.
4. single system continuous copper smelting apparatus as claimed in claim 3, it is characterised in that:The top-blown spray gun and the side-blown eye of wind are equal
It is multiple.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201820274633.5U CN207811837U (en) | 2018-02-27 | 2018-02-27 | A kind of single system continuous copper smelting apparatus |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201820274633.5U CN207811837U (en) | 2018-02-27 | 2018-02-27 | A kind of single system continuous copper smelting apparatus |
Publications (1)
Publication Number | Publication Date |
---|---|
CN207811837U true CN207811837U (en) | 2018-09-04 |
Family
ID=63321430
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201820274633.5U Expired - Fee Related CN207811837U (en) | 2018-02-27 | 2018-02-27 | A kind of single system continuous copper smelting apparatus |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN207811837U (en) |
-
2018
- 2018-02-27 CN CN201820274633.5U patent/CN207811837U/en not_active Expired - Fee Related
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN101165196B (en) | Technique for continuously smelting copper by employing oxygen bottom converter and device thereof | |
CN101705367B (en) | Copper nickel smelting process with oxygen-enriched side-blowing bath smelting method | |
CN101086038B (en) | Direct lead smelting method in molten pool and its device | |
FI75602C (en) | FOERFARANDE OCH ANORDNING FOER KONTINUERLIG KONVERTERING AV KOPPAR- OCH ICKE-JAERNMETALLSTENAR. | |
CN106048254A (en) | Continuous smelting device and method of nickel-containing material | |
CN107287442A (en) | Continuous copper smelting device and copper smelting method | |
CN101328545A (en) | Process of oxygen bottom blowing continuous copper smelting | |
CN103451446A (en) | Smelting side-blowing reduction lead-zinc smelting device | |
CN104988332A (en) | One-step copper smelting process and device | |
CN106399713A (en) | Oxygen enrichment bottom blowing copper smelting process | |
CN101899580B (en) | Zinc concentrate smelting equipment | |
CN103643051A (en) | Process and device for treating copper-lead smelting mixed slag through bottom-blowing bath smelting technology | |
CN101328544A (en) | Bottom blowing converting furnace for bottom blowing continuous copper smelting | |
CN108220610A (en) | A kind of processing method of the dedusting ash containing heavy metal | |
CN110257637A (en) | A kind of solid waste of heavy metal high-efficient treatment method and treatment furnace | |
CN110205483A (en) | A kind of reduction roasting handles the system and technique of low-grade tin raw material | |
CN203498450U (en) | Side-blown reducing lead-zinc smelting equipment | |
CN113481380A (en) | Full-thermal-state continuous bottom blowing copper smelting method and equipment | |
CN207811837U (en) | A kind of single system continuous copper smelting apparatus | |
CN105506299A (en) | Low-grade secondary lead smelting slag fuming furnace treatment system and method | |
CN210560649U (en) | Heavy metal solid waste high-efficiency treatment furnace | |
CN205382195U (en) | Low -grade reviver smelting slag fuming furnace processing system | |
CN201793692U (en) | Zinc concentrate smelting device | |
CN101886183B (en) | Lead smelting device and lead smelting method employing same | |
US4451291A (en) | Method and apparatus for converting matte, particularly high-grade matte |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
GR01 | Patent grant | ||
GR01 | Patent grant | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20180904 Termination date: 20190227 |
|
CF01 | Termination of patent right due to non-payment of annual fee |