CN106288815B - A kind of vibration premixed type concentrate burner - Google Patents
A kind of vibration premixed type concentrate burner Download PDFInfo
- Publication number
- CN106288815B CN106288815B CN201610632799.5A CN201610632799A CN106288815B CN 106288815 B CN106288815 B CN 106288815B CN 201610632799 A CN201610632799 A CN 201610632799A CN 106288815 B CN106288815 B CN 106288815B
- Authority
- CN
- China
- Prior art keywords
- dispersion
- air hose
- material feeding
- feeding box
- vibration
- 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.)
- Active
Links
Classifications
-
- 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
- F27D3/00—Charging; Discharging; Manipulation of charge
- F27D3/18—Charging particulate material using a fluid carrier
-
- 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
- C22B15/0047—Smelting or converting flash smelting or converting
-
- 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
- F27D25/00—Devices or methods for removing incrustations, e.g. slag, metal deposits, dust; Devices or methods for preventing the adherence of slag
- F27D25/001—Devices or methods for removing incrustations, e.g. slag, metal deposits, dust; Devices or methods for preventing the adherence of slag comprising breaking tools, e.g. hammers, drills, scrapers
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F27—FURNACES; KILNS; OVENS; RETORTS
- F27M—INDEXING SCHEME RELATING TO ASPECTS OF THE CHARGES OR FURNACES, KILNS, OVENS OR RETORTS
- F27M2001/00—Composition, conformation or state of the charge
- F27M2001/01—Charges containing mainly non-ferrous metals
- F27M2001/015—Copper
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F27—FURNACES; KILNS; OVENS; RETORTS
- F27M—INDEXING SCHEME RELATING TO ASPECTS OF THE CHARGES OR FURNACES, KILNS, OVENS OR RETORTS
- F27M2003/00—Type of treatment of the charge
- F27M2003/13—Smelting
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Chemical & Material Sciences (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 present invention discloses a kind of vibration premixed type concentrate burner, the dispersion air hose of the oxygen supplying tube of arrangement, hollow annular is overlapped and is vertically arranged successively including tube core, and form the taper technique bellows of air compartment, the material feeding box of oblique under shed at the top of it is arranged on the outer wall of the dispersion air hose, and horizontal fixed plate is fixed at the top of the dispersion air hose of hollow annular, the end far from dispersion wind pipeline in fixed plate is fixed with by the way that dispersion air hose is driven to pump the pneumatic hammer vibrating device that falls dross of shaking;Material feeding box opening downside is equipped with the feed inlet premix air port of air port upward;Technique bellows entrance is equipped with the technique wind rotation direction device that gas is made tangentially to premix concentrate powder;It is additionally provided in dispersion air hose and leads to the independent premix supply air line of material feeding box bottom and pre-mixed air beam device, the inward turning air hose towards discharge port is additionally provided on the outside of material feeding box.The present invention is vibration premixed type concentrate burner, can effectively reduce dross phenomenon, the combustion efficiency for improving copper concentrate mineral aggregate.
Description
Technical field
The invention belongs to the technical field of smelting of copper, and in particular to a kind of vibration premixed type concentrate burner.
Background technology
It is that concentrate burner and the technique for blasting technique wind are set at the top of smelting furnace in the Flash Smelting Furnace smelting technology of copper
Bellows spray into copper concentrate mineral aggregate, oxygen and dispersion wind, in the bottom of concentrate burner, ore deposit by concentrate burner into smelting furnace
Material is mixed with technique wind and ignition forms clinker and matte, and mineral aggregate is sufficiently mixed with the realization of technique wind, this is mineral aggregate in essence
One of rapid, complete oxidation essential condition is carried out in the limited space in ore deposit nozzle lower part.
At present, the concentrate burner that copper mine enterprise uses is expanded by the center that Outokumpu company designs and produces mostly
Type concentrate burner is dissipated, as shown in Figure 1, being that mineral aggregate and technique wind are sprayed into stove in the same direction the characteristics of concentrate burner, mainly passes through gas phase
Achieve the purpose that mixing with the counterdiffusion of solid phase phase, infiltration, when carrying out low level material spray using this central diffused concentrate burner,
That is the entrance of mineral aggregate close to technique wind export when, mineral aggregate is easier to mix with technique wind, but in high-order material spray, also just say
The entrance of mineral aggregate is higher, when still having certain difference in height with the outlet of technique wind, mineral aggregate reaction time relative delay at this time, separately
Outside, when the input amount of mineral aggregate is less, enter stove mineral aggregate rapidly can be heated to reaction temperature by furnace high-temperature flue gas or radiant heat,
And in the range of about 1.5m is exported apart from concentrate burner begin to that violent combustion reaction occurs, and the input amount of mineral aggregate is more
When, in the finite spatial extent of reaction tower top feed mouth, it is difficult to ensure that mineral aggregate is enough sufficiently mixed with technique wind energy, Er Qie
Concentrate burner bottom easily generates bonding phenomenon;Simultaneously as the water cooled bottom plate of nozzle lower end, play certain heat-insulated and subtract
Few noclulation, but in actual motion, due to longtime running, certain dross phenomenon is still produced in water cooled bottom plate lower end, from
And the mass transfer of combustion reaction, rate of heat transfer are leveraged, the ferroso-ferric oxide content in clinker is not only caused to increase, dust rate
And SO3Production rate rises, and utilization ratio is also decreased obviously, and then influences the production capacity of melting product copper.
Therefore, how to ensure being sufficiently mixed for mineral aggregate and technique wind, improve the counterdiffusion of gas-solid phase, infiltration, solve in not shadow
Under conditions of ringing production, the problem of periodic cleaning nozzle lower part dross, the combustion efficiency of copper concentrate mineral aggregate is improved, this melts flash
It is extremely important for sweetening process.
Invention content
Against the above deficiency, the present invention provides one kind under conditions of production is not influenced, periodic cleaning nozzle lower junction
The problem of knurl, so as to effectively reduce the vibration premixed type concentrate spray of dross phenomenon, the combustion efficiency for improving copper concentrate mineral aggregate
Mouth.
To achieve the above object, present invention employs following technical schemes:
A kind of vibration premixed type concentrate burner including tube core overlaps and is vertically arranged successively the oxygen supplying tube, hollow of arrangement
Cricoid dispersion air hose and formed air compartment taper technique bellows, it is described dispersion air hose outer wall on be arranged at the top of it
The material feeding box of oblique under shed, and horizontal fixed plate is fixed at the top of the dispersion air hose of hollow annular, it is separate in fixed plate
The end of dispersion wind pipeline is fixed with by the way that dispersion air hose is driven to pump the pneumatic hammer vibrating device that falls dross of shaking.
The pneumatic hammer vibrating device include being installed in pneumatic hammer on the upside of fixed plate, be connected on the downside of fixed plate with pneumatic hammer it is strong
Power spring and guide rod;It is set on the upside of the brute spring on the guide rod, the lower end of brute spring is supported on charging
On case.
The lower semisection of the brute spring is sheathed in pilot sleeve, and locking nut is provided on the upside of pilot sleeve, is led
Be fixed on the top of material feeding box by the pedestal on the downside of it to sleeve, pilot sleeve between locking nut and pedestal
The positioning plate being fixedly connected with dispersion air hose is arranged on stack shell.
Further, it is 3 that the pneumatic hammer vibrating device is uniformly distributed in fixed plate.
Preferably, the neighbouring downside of the material feeding box opening is equipped with the feed inlet premix air port of air port upward.
Preferably, the technique bellows are equipped with the technique wind rotation direction that gas is made tangentially to premix concentrate powder in diameter maximum
Device.
Further, the technique wind rotation direction device be set as that inclined surface along taper technique bellows is parallel and the oblique work that sets
Ethics and practice import, to form the whirlwind that can tangentially premix concentrate powder.
Preferably, it is described to disperse to be additionally provided with the independent premix supply air line for leading to material feeding box bottom in air hose and around this
Pre-mixed air beam device in pipeline side;The pre-mixed air beam device is equipped with the tangential swing angle that 30 ° are tilted towards lateral direction.
The beneficial effects of the present invention are:
1), the present invention is provided with pneumatic hammer vibrating device, pneumatic hammer vibrating device include being installed in pneumatic hammer on the upside of fixed plate,
The brute spring and guide rod being connected on the downside of fixed plate with pneumatic hammer;Wherein, the brute spring is set on the guide rod;By
In the prolonged difference smelted or concentrate amount is how many, a certain amount of dross phenomenon can be caused in nozzle bottom end, when pneumatic hammer is hammered into shape
When hitting, fixed plate compresses brute spring so as to which dispersion air hose be driven to do guiding movement up and down along guide rod therewith, makes dispersion wind
Pipe generates transient vibration, and caking product can shake and fall;Therefore the present invention can clear up dross operation automatically in process of production, greatly
Ground improves production efficiency, while can greatly reduce equipment maintenance cost.
2), the neighbouring downside of material feeding box opening of the present invention is equipped with the feed inlet premix air port of air port upward, when by drying
Powdery concentrate when entering material feeding box, be put into upwards by air port feed inlet pre-mixed air can bulk concentrate powder feed when
Disperse as possible, the unlikely situation for causing charging uneven ensure that the reliability service of the present invention.
3) it is, of the invention when concentrate powder falls to the pre-mixed air beam that the independent gas premixed in supply air line is made tangentially to blow out
During device, further disperseed using 30 ° of tangential swing angle of pre-mixed air beam device, improve the effect of gas-solid mixing.
4), the present invention passes through technique wind rotation direction when concentrate powder down and when passing through taper technique bellows and disperseing around
The whirlwind of device blowout, tangentially premixes concentrate powder, can improve premix residence time of the concentrate powder in reversed nozzle, further carry
High premixing effect improves production efficiency.
5), in conclusion the present invention is a kind of vibration premixed type concentrate burner, by disperseing air hose, independent premix gas supply
Pipeline and pre-mixed air beam device, feed inlet premix air port are entered the wind obliquely, multiple its cloth of premix of technique wind rotation direction device progress is equal
It is even, inner space can be made full use of so that concentrate and oxygen can be mixed more fully, and be had by pneumatic hammer vibrating device
Effect completes automatic clear knurl operation, improves the service life of concentrate burner, and improve the product quality of Copper making, reduces
Environmental pollution.
Description of the drawings
The structure diagram that it is the concentrate burner of flash smelting furnace in the prior art that Fig. 1, which is,.
Fig. 2 is the structure sectional view of the present invention.
Fig. 3 is the amplification assumption diagram of pneumatic hammer vibrating device of the present invention (wherein brute spring only depicts the first part).
Fig. 4 is the partial enlarged view of Fig. 2.
Fig. 5 is the vertical view schematic diagram of Fig. 2.
Fig. 6 is technique wind rotation direction device graphics
The meaning of label symbol is as follows in figure:
10- oxygen supplying tubes 11- dispersions air hose 110- independently premixes supply air line
111- pre-mixed air beam device 112- lamellated plate 113- water cooled bottom plate 12- material feeding box
120- feed inlets premix air port 13- water-cooling system 14- technique bellows
140- technique wind rotation direction devices
20- fixed plate 21- pneumatic hammer vibrating device 210- pneumatic hammer 211- brute springs
212- guide rod 213- pilot sleeve 214- positioning plate 215- locking nuts
Specific embodiment
Below in conjunction with the attached drawing in the embodiment of the present invention, the technical solution in the present invention is clearly and completely retouched
It states.Based on the embodiments of the present invention, those of ordinary skill in the art are obtained without making creative work
Every other embodiment, shall fall within the protection scope of the present invention.
As shown in Fig. 2, for a kind of vibration premixed type concentrate burner, overlapped including tube core and be vertically arranged arrangement successively
The taper technique bellows 14 of oxygen supplying tube 10, the dispersion air hose 11 of hollow annular and formation air compartment, the dispersion air hose 11 is side
To air inlet, the material feeding box 12 of oblique under shed at the top of it, and point of hollow annular are arranged on the outer wall of dispersion air hose 11
11 top of relieve heat pipe is fixed with horizontal fixed plate 20, and one end far from dispersion wind pipeline in fixed plate 20, which is fixed with, passes through band
Dynamic dispersion air hose 11 pumps and removes the pneumatic hammer vibrating device 21 of dross.
Specifically, with reference to shown in Fig. 3, the pneumatic hammer vibrating device 21 include being installed in the pneumatic hammer 210 of 20 upside of fixed plate,
The brute spring 211 and guide rod 212 being connected in 20 downside of fixed plate with pneumatic hammer 210;Wherein, the guide rod 212 is inserted in
In brute spring 211;The downside movable supporting of brute spring 211 is at the top of material feeding box 12.It is fixed when pneumatic hammer 210 hammers
Plate 20 drives guide rod 212 to compress brute spring 211 therewith, is transported up and down so as to dispersion air hose 11 be driven to do by fixed plate 20
It is dynamic.
It is furthermore preferred that the lower semisection of above-mentioned brute spring 211 is also arranged with pilot sleeve 213, the upside of pilot sleeve 213
Locking nut 215 is provided with, pilot sleeve 213 is fixed on by the pedestal on the downside of it on top of material feeding box 12, pilot sleeve
The positioning plate 214 being fixedly connected with dispersion air hose 11 is arranged on 213;This structure design causes locking nut 215, pilot sleeve
213 are fixed together with material feeding box 12, and when pneumatic hammer vibrating device 21 works, pneumatic hammer 210 drives fixed plate 20 to compress downwards
Brute spring 211, brute spring 211 do guiding movement in the direction that pilot sleeve 213 limits, and ensure that fixed plate 20, dispersion
Air hose 11, positioning plate 214 and brute spring 211 4 do the reciprocating motion above and below stablizing with pneumatic hammer 210, are not sent out because shaking
Raw horizontal direction displacement.The setting of the locking nut 215 can adjust the stroke of positioning plate 214.
And it as shown in figure 5, it is 3 that pneumatic hammer vibrating device 21 is uniformly distributed on ring-type fixing plate 20, is spaced
120 ° of central angle;So that the more smoothly vibration of pneumatic hammer 210, and avoid dispersion air hose 11 and rotated in vibration.
As a kind of further preferred embodiment, the neighbouring downside that the material feeding box 12 is open is equipped with the charging of air port upward
Mouth premix air port 120.
As a kind of further preferred embodiment, the technique bellows 14 are equipped in diameter maximum makes gas tangentially pre-
The technique wind rotation direction device 140 of mixed concentrate powder.
Specifically, the technique wind rotation direction device 140 is as shown in fig. 6, it is set as along the inclined surface of taper technique bellows 14
The parallel and oblique technique wind inlet that sets, to form the whirlwind that can tangentially premix concentrate powder.
As a kind of further preferred embodiment, as shown in Figure 2,4, it is additionally provided in the dispersion air hose 11 and leads to material feeding box
The independent of bottom premixes supply air line 110 and around the pre-mixed air beam device 111 in pipeline side;The pre-mixed air beam device
111 equipped with the tangential swing angle β for rolling oblique 30 ° outwardly.
Following detailed description is made to the pre-compounding process of the present invention below in conjunction with the accompanying drawings.
S1, first, when dried powdery concentrate is directly entered material feeding box 12, the powder for being placed in nozzle interior cannot be equal
Point, it is entered the wind at air port 120 by being premixed from the upward feed inlet in air port so that disperse as possible during bulk concentrate powder feed;
S2, then, when concentrate powder falls to the pre-mixed air that the independent gas premixed in supply air line 110 is made tangentially to blow out
During beam device 111, the tangential swing angle using 30 degree on pre-mixed air beam device 111 further disperses;
Also, when disperseing gas in air hose 11 and flowing to one end close to air outlet, across ventilative lamellated plate 112,
It is even to be contacted with concentrate powder, improve gas-solid mixing effect;
When concentrate powder down and when passing through taper technique bellows 14 and disperseing around, pass through technique wind rotation direction device 140
The whirlwind of blowout, tangentially premixes concentrate powder, can improve premix residence time of the concentrate powder in nozzle, further improve premix
Effect improves production efficiency;
S3, due to smelting for a long time, concentrate amount it is how much different, in nozzle bottom end can cause a certain amount of caking phenomenon,
It can be hammered by pneumatic hammer 210, so as to which fixed plate 20 compresses brute spring 212 so as to drive dispersion wind along guide rod 212 therewith
Pipe 11 does guiding movement up and down, and dispersion air hose 11 is made to generate transient vibration, caking product are shaken and are fallen.
Claims (4)
1. a kind of vibration premixed type concentrate burner overlaps including tube core and is vertically arranged the oxygen supplying tube (10) of arrangement, sky successively
The cricoid dispersion air hose (11) of the heart and the taper technique bellows (14) for forming air compartment, it is characterised in that:The dispersion air hose
(11) material feeding box (12) of oblique under shed at the top of it is arranged on outer wall, and at the top of the dispersion air hose (11) of hollow annular
Horizontal fixed plate (20) is fixed with, the end far from dispersion wind pipeline in fixed plate (20) is fixed with disperses wind by drive
Pipe (11) pumps and shakes and fall the pneumatic hammer vibrating device (21) of dross;
The pneumatic hammer vibrating device (21) including being installed in pneumatic hammer (210) on the upside of fixed plate (20), on the downside of fixed plate (20)
The brute spring (211) and guide rod (212) being connected with pneumatic hammer (210);It is set on the upside of the brute spring (211) described
On guide rod (212), the lower end of brute spring (211) is supported on material feeding box (12).
2. a kind of vibration premixed type concentrate burner according to claim 1, it is characterised in that:The brute spring (211)
Lower semisection be sheathed in pilot sleeve (213), locking nut (215), pilot sleeve are provided on the upside of pilot sleeve (213)
(213) it is fixed on by the pedestal on the downside of it on top of material feeding box (12), pilot sleeve (213) is located at locking nut
(215) positioning plate (214) being fixedly connected with dispersion air hose (11) is arranged on the stack shell between pedestal.
3. a kind of vibration premixed type concentrate burner according to claim 2, it is characterised in that:The pneumatic hammer vibrating device
(21) uniformly distributed in fixed plate (20) is 3.
4. a kind of vibration premixed type concentrate burner according to claim 1, it is characterised in that:Material feeding box (12) opening
Neighbouring downside be equipped with air port upward feed inlet premix air port (120).
Priority Applications (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201610632799.5A CN106288815B (en) | 2016-08-04 | 2016-08-04 | A kind of vibration premixed type concentrate burner |
CN201810262167.3A CN108680029B (en) | 2016-08-04 | 2016-08-04 | A kind of improved vibration premixed type concentrate burner |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201610632799.5A CN106288815B (en) | 2016-08-04 | 2016-08-04 | A kind of vibration premixed type concentrate burner |
Related Child Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201810262167.3A Division CN108680029B (en) | 2016-08-04 | 2016-08-04 | A kind of improved vibration premixed type concentrate burner |
Publications (2)
Publication Number | Publication Date |
---|---|
CN106288815A CN106288815A (en) | 2017-01-04 |
CN106288815B true CN106288815B (en) | 2018-06-29 |
Family
ID=57664686
Family Applications (2)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201810262167.3A Active CN108680029B (en) | 2016-08-04 | 2016-08-04 | A kind of improved vibration premixed type concentrate burner |
CN201610632799.5A Active CN106288815B (en) | 2016-08-04 | 2016-08-04 | A kind of vibration premixed type concentrate burner |
Family Applications Before (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201810262167.3A Active CN108680029B (en) | 2016-08-04 | 2016-08-04 | A kind of improved vibration premixed type concentrate burner |
Country Status (1)
Country | Link |
---|---|
CN (2) | CN108680029B (en) |
Families Citing this family (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN108489277B (en) * | 2018-03-26 | 2019-08-30 | 合肥通用机械研究院有限公司 | A kind of adjustable premixed type concentrate burner of charging |
CN110777265B (en) * | 2019-12-02 | 2024-02-20 | 江西铜业股份有限公司 | Concentrate nozzle of cyclone diffusion type flash furnace |
CN110804702A (en) * | 2019-12-02 | 2020-02-18 | 江西铜业股份有限公司 | Concentrate nozzle for flash smelting |
CN112710159A (en) * | 2020-12-10 | 2021-04-27 | 广西金川有色金属有限公司 | Pure oxygen smelting device of flash furnace and using method thereof |
CN116951987B (en) * | 2023-09-18 | 2024-01-05 | 张家港广大特材股份有限公司 | Air impact type powder dispersing device, method and reaction melting furnace applied to furnace mouth feeding pipe |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1353771A (en) * | 1999-05-31 | 2002-06-12 | 奥托库姆普联合股份公司 | Equipment for even feed of pulverous materials to concentrate burner of suspension smelting furnace |
CN104263966A (en) * | 2009-10-19 | 2015-01-07 | 奥图泰有限公司 | Method Of Using A Suspension Smelting Furnace, A Suspension Smelting Furnace, And A Concentrate Burner |
CN204434699U (en) * | 2015-01-20 | 2015-07-01 | 铜陵有色金属集团股份有限公司金冠铜业分公司 | The concentrate burner of flash smelting furnace |
Family Cites Families (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP2705317B1 (en) * | 2011-05-06 | 2017-12-27 | Hatch Ltd | Burner and feed apparatus for flash smelter |
CN104388695B (en) * | 2014-11-26 | 2018-03-13 | 铜陵有色金属集团股份有限公司金冠铜业分公司 | Concentrate burner |
CN104567431B (en) * | 2014-12-04 | 2017-03-15 | 金川集团股份有限公司 | Cyclone type concentrate burner |
CN104561587B (en) * | 2015-01-20 | 2017-01-18 | 铜陵有色金属集团股份有限公司金冠铜业分公司 | Concentrate jet nozzle of smelting furnace |
-
2016
- 2016-08-04 CN CN201810262167.3A patent/CN108680029B/en active Active
- 2016-08-04 CN CN201610632799.5A patent/CN106288815B/en active Active
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1353771A (en) * | 1999-05-31 | 2002-06-12 | 奥托库姆普联合股份公司 | Equipment for even feed of pulverous materials to concentrate burner of suspension smelting furnace |
CN104263966A (en) * | 2009-10-19 | 2015-01-07 | 奥图泰有限公司 | Method Of Using A Suspension Smelting Furnace, A Suspension Smelting Furnace, And A Concentrate Burner |
CN204434699U (en) * | 2015-01-20 | 2015-07-01 | 铜陵有色金属集团股份有限公司金冠铜业分公司 | The concentrate burner of flash smelting furnace |
Non-Patent Citations (1)
Title |
---|
新型精矿喷嘴在贵溪冶炼厂二期闪速炉的应用;姚绍芸;《有色冶金设计与研究》;20001230;第21卷(第4期);第2.2"中央扩散型精矿喷嘴",图3,第12-16页, * |
Also Published As
Publication number | Publication date |
---|---|
CN108680029B (en) | 2019-08-02 |
CN108680029A (en) | 2018-10-19 |
CN106288815A (en) | 2017-01-04 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN106288815B (en) | A kind of vibration premixed type concentrate burner | |
CN103759546B (en) | Calcium carbide furnace purification ash back-to-furnace combustion system | |
CN201988675U (en) | Full-countercurrent heat exchange two-stage waste sand casting roasting furnace | |
CN102199680B (en) | Cyclical low-carbon metallurgical method with tail gas conversion by plasma | |
CN102410715B (en) | Parallel-flow heating vertical static dryer | |
CN202465830U (en) | Residual heat reclaiming system for pellets and sintered ores | |
CN202836180U (en) | Ring-shaped sleeve kiln | |
CN106282467A (en) | A kind of iron mine fine coal base produces direct-reduction facilities and method | |
CN203284438U (en) | Magnetizing roasting reducing atmosphere preparation device and iron mine flash magnetizing roasting system | |
CN106969639A (en) | A kind of chamber type sintering ore deposit waste-heat recovery device | |
CN101962696B (en) | Method for blowing furnace washing agent by using air inlet of blast furnace | |
CN103697467B (en) | Method for coal slime combustion of circulating fluidized bed boiler | |
CN103205584B (en) | Production device and production method of manganese monoxide mineral powder | |
CN102506421B (en) | Circulating fluid bed (CFB) boiler coal supply system for blending combustion of middling coal | |
CN111412753A (en) | Vertical cooling device with steady flow rectification characteristic and cooling method thereof | |
CN209131421U (en) | A kind of kiln integral structure and the process system using the kiln integral structure | |
CN108168292B (en) | Multifunctional environment-friendly BSK sintering technology shaft kiln and use method thereof | |
CN213656724U (en) | Coal powder direct-fired heat supply pipeline anti-sedimentation structure | |
CN203364615U (en) | Material scattering device | |
CN205980817U (en) | System is used multipurposely to vertical cooling of sintering and pelletizing and sintering waste heat | |
CN201488507U (en) | Energy-saving hot air drying system used in ceramics factory | |
CN203771999U (en) | Smelting reverberatory furnace | |
CN201106023Y (en) | Environment-friendly type calcining vertical kiln | |
CN110628463A (en) | Mixed air distribution system of gas producer and working method | |
CN210826072U (en) | Mixed air distribution system of gas producer |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C06 | Publication | ||
PB01 | Publication | ||
C10 | Entry into substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
GR01 | Patent grant | ||
GR01 | Patent grant | ||
CP01 | Change in the name or title of a patent holder | ||
CP01 | Change in the name or title of a patent holder |
Address after: 230031 No. 888 Changjiang West Road, Shushan District, Hefei, Anhui. Patentee after: Hefei General Machinery Research Institute Co., Ltd. Address before: 230031 No. 888 Changjiang West Road, Shushan District, Hefei, Anhui. Patentee before: Hefei Universal Machinery Inst. |