CN108680029A - A kind of improved vibration premixed type concentrate burner - Google Patents

A kind of improved vibration premixed type concentrate burner Download PDF

Info

Publication number
CN108680029A
CN108680029A CN201810262167.3A CN201810262167A CN108680029A CN 108680029 A CN108680029 A CN 108680029A CN 201810262167 A CN201810262167 A CN 201810262167A CN 108680029 A CN108680029 A CN 108680029A
Authority
CN
China
Prior art keywords
air hose
dispersion
air
material feeding
feeding box
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.)
Granted
Application number
CN201810262167.3A
Other languages
Chinese (zh)
Other versions
CN108680029B (en
Inventor
吴玉月
徐鹏
张劲松
王守全
臧轲轲
唐辰
徐武
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Hefei General Machinery Research Institute Co Ltd
Original Assignee
Hefei General Machinery Research Institute Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Hefei General Machinery Research Institute Co Ltd filed Critical Hefei General Machinery Research Institute Co Ltd
Priority to CN201810262167.3A priority Critical patent/CN108680029B/en
Publication of CN108680029A publication Critical patent/CN108680029A/en
Application granted granted Critical
Publication of CN108680029B publication Critical patent/CN108680029B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F27FURNACES; KILNS; OVENS; RETORTS
    • F27DDETAILS OR ACCESSORIES OF FURNACES, KILNS, OVENS, OR RETORTS, IN SO FAR AS THEY ARE OF KINDS OCCURRING IN MORE THAN ONE KIND OF FURNACE
    • F27D3/00Charging; Discharging; Manipulation of charge
    • F27D3/18Charging particulate material using a fluid carrier
    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22BPRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B15/00Obtaining copper
    • C22B15/0026Pyrometallurgy
    • C22B15/0028Smelting or converting
    • C22B15/0047Smelting or converting flash smelting or converting
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F27FURNACES; KILNS; OVENS; RETORTS
    • F27DDETAILS OR ACCESSORIES OF FURNACES, KILNS, OVENS, OR RETORTS, IN SO FAR AS THEY ARE OF KINDS OCCURRING IN MORE THAN ONE KIND OF FURNACE
    • F27D25/00Devices or methods for removing incrustations, e.g. slag, metal deposits, dust; Devices or methods for preventing the adherence of slag
    • F27D25/001Devices 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
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F27FURNACES; KILNS; OVENS; RETORTS
    • F27MINDEXING SCHEME RELATING TO ASPECTS OF THE CHARGES OR FURNACES, KILNS, OVENS OR RETORTS
    • F27M2001/00Composition, conformation or state of the charge
    • F27M2001/01Charges containing mainly non-ferrous metals
    • F27M2001/015Copper
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F27FURNACES; KILNS; OVENS; RETORTS
    • F27MINDEXING SCHEME RELATING TO ASPECTS OF THE CHARGES OR FURNACES, KILNS, OVENS OR RETORTS
    • F27M2003/00Type of treatment of the charge
    • F27M2003/13Smelting

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Manufacturing & Machinery (AREA)
  • Materials Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Manufacture And Refinement Of Metals (AREA)

Abstract

This divisional application discloses a kind of improved vibration premixed type concentrate burner, the dispersion air hose of the oxygen supplying tube of arrangement, hollow annular is overlapped and is vertically arranged including tube core, and form the taper technique bellows of air compartment, disperse the material feeding box that oblique under shed at the top of it is arranged on the outer wall of air hose, and it is fixed with horizontal fixed plate at the top of the dispersion air hose of hollow annular, it is fixed in the end far from dispersion wind pipeline in fixed plate and falls the pneumatic hammer vibrating device of dross by driving to disperse to shake by air hose pumps;It feeds and is equipped with the feed inlet premix air port of air port upward on the downside of box opening;Technique bellows entrance is equipped with the technique wind rotation direction device for making gas tangentially premix concentrate powder;It is additionally provided with the independent premix supply air line and pre-mixed air beam device for leading to material feeding box bottom in dispersion air hose, 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, the combustion efficiency that can effectively reduce dross phenomenon, improve copper concentrate mineral aggregate.

Description

A kind of improved vibration premixed type concentrate burner
The application is application number 201610632799.5, on 08 04th, 2016 applying date, " a kind of vibration is pre- for denomination of invention The divisional application of mixed type concentrate burner ".
Technical field
The invention belongs to the technical field of smelting of copper, and in particular to a kind of improved 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, mine 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 Rapid, complete oxidation one of essential condition is carried out in the limited space in mine nozzle lower part.
Currently, the concentrate burner that copper mine enterprise uses is expanded by the center that Outokumpu company designs and produces mostly It dissipates type concentrate burner and mainly passes through gas phase as shown in Figure 1, being that mineral aggregate and technique wind spray into stove in the same direction the characteristics of concentrate burner 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 when the entrance of mineral aggregate is exported close to technique wind, mineral aggregate is easier to mix with technique wind, but in high-order material spray, also just says 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 exporting about 1.5m 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 easy tos produce bonding phenomenon;Simultaneously as the water cooled bottom plate of nozzle lower end, plays 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, not only cause the ferroso-ferric oxide content in clinker 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 is molten to flash It is extremely important for sweetening process.
Invention content
Against the above deficiency, the present invention provides one kind under conditions of not influencing production, is sufficiently mixed mineral aggregate and technique The problem of wind, periodic cleaning nozzle lower part dross, so as to the burning effect for effectively reducing dross phenomenon, improving copper concentrate mineral aggregate The vibration premixed type concentrate burner of fruit.
To achieve the above object, present invention employs following technical schemes:
A kind of improved vibration premixed type concentrate burner, including tube core overlap and are vertically arranged the oxygen supply of arrangement successively The dispersion air hose of pipe, hollow annular, and the taper technique bellows of air compartment are formed, it is arranged on the outer wall of the dispersion air hose The material feeding box of its oblique under shed in top, and it is fixed with horizontal fixed plate at the top of the dispersion air hose of hollow annular, in fixed plate The upper end far from dispersion wind pipeline is fixed with to disperse to shake by air hose pumps by drive and falls the pneumatic hammer of dross and shake Dynamic device;The pneumatic hammer vibrating device include be installed in pneumatic hammer on the upside of fixed plate, be connected with pneumatic hammer on the downside of fixed plate it is strong Power spring and guide rod are set on the guide rod on the upside of the brute spring, and the lower end of brute spring is supported on charging On case;The technique bellows are equipped with the technique wind rotation direction device for making gas tangentially premix concentrate powder in diameter maximum.
Preferably, the lower semisection of the brute spring is sheathed in pilot sleeve, and locking is provided on the upside of pilot sleeve Nut, pilot sleeve are fixed on by the pedestal on the downside of it on the top of material feeding box, and pilot sleeve is located at locking nut and bottom The positioning plate being fixedly connected with dispersion air hose is arranged on stack shell between seat.
Further, it is 3 that the pneumatic hammer vibrating device is uniformly distributed in fixed plate.
Preferably, the neighbouring downside of the charging box opening is equipped with the feed inlet of air port upward and premixes air port.
Preferably, the technique wind rotation direction device is set as oblique technique that is parallel along the inclined surface of taper technique bellows and setting Wind inlet, to form the whirlwind that can tangentially premix concentrate powder.
Preferably, it is additionally provided with the independent premix supply air line for leading to material feeding box bottom in the dispersion air hose and surrounds and is somebody's turn to do Pre-mixed air beam device in pipeline side;The pre-mixed air beam device is equipped with the tangential swing angle for tilting 30 ° 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 be installed in pneumatic hammer on the upside of fixed plate, The brute spring and guide rod being connected with pneumatic hammer on the downside of fixed plate;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 to drive dispersion air hose 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 present invention charging box opening is equipped with the feed inlet of air port upward and premixes air port, when by drying Powdery concentrate when entering material feeding box, when bulk concentrate powder feed can be made by being put into feed inlet pre-mixed air upwards by air port Disperse as possible, the unlikely situation for causing charging uneven ensure that the reliability service of the present invention.
3), of the invention when concentrate powder falls to the pre-mixed air beam for making the independent gas premixed in supply air line tangentially blow out When device, is 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 disperseing around by taper technique bellows The whirlwind of device blowout, tangentially premixes concentrate powder, premix residence time of the concentrate powder in reversed nozzle can be improved, 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 tumor operation, improves the service life of concentrate burner, and improve the product quality of Copper making, reduces Environmental pollution.
Description of the drawings
Fig. 1 is the structural schematic diagram for being the concentrate burner of flash smelting furnace in the prior art.
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 implementation mode
Following will be combined with the drawings in the embodiments of the present invention, is clearly and completely retouched to the technical solution in the present invention It states.Based on the embodiments of the present invention, obtained by those of ordinary skill in the art without making creative efforts Every other embodiment, shall fall within the protection scope of the present invention.
As shown in Fig. 2, for a kind of improved vibration premixed type concentrate burner, including tube core is overlapped and is vertically arranged successively The oxygen supplying tube 10 of arrangement, the dispersion air hose 11 of hollow annular, and form the taper technique bellows 14 of air compartment, the dispersion air hose 11 be side air admission, and the material feeding box 12 of oblique under shed at the top of it, and cavity ring are arranged on the outer wall of dispersion air hose 11 11 top of dispersion air hose of shape is fixed with horizontal fixed plate 20, and one end far from dispersion wind pipeline in fixed plate 20 is fixed with Disperse the pneumatic hammer vibrating device 21 that dross is removed by air hose 11 pumps by drive.
Specifically, in conjunction with shown in Fig. 3, the pneumatic hammer vibrating device 21 include the pneumatic hammer 210 for being installed in 20 upside of fixed plate, The brute spring 211 and guide rod 212 being connected with pneumatic hammer 210 in 20 downside of fixed plate;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, to drive dispersion air hose 11 to do fortune up and down 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 It is provided with locking nut 215, 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 makes 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.
Heretofore described technique bellows 14 are equipped with the technique wind for making gas tangentially premix concentrate powder in diameter maximum Rotation direction device 140.
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 when bulk concentrate powder feed;
S2, then, when concentrate powder falls to the pre-mixed air for making the independent gas premixed in supply air line 110 tangentially blow out When 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, ventilative lamellated plate 112 is passed through, It is even to be contacted with concentrate powder, improve gas-solid mixing effect;
When concentrate powder down and when disperseing around by taper technique bellows 14, pass through technique wind rotation direction device 140 The whirlwind of blowout, tangentially premixes concentrate powder, and premix residence time of the concentrate powder in nozzle can be improved, further increase 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, to which fixed plate 20 compresses brute spring 212 to drive dispersion wind along guide rod 212 therewith Pipe 11 does guiding movement up and down, so that dispersion air hose 11 is generated transient vibration, caking product are shaken and are fallen.

Claims (6)

1. a kind of improved vibration premixed type concentrate burner, including tube core overlap and are vertically arranged the oxygen supplying tube of arrangement successively (10), the dispersion air hose (11) of hollow annular, and form the taper technique bellows (14) of air compartment, it is characterised in that:Described point The material feeding box (12) of oblique under shed at the top of it, and the dispersion air hose of hollow annular are arranged on the outer wall of relieve heat pipe (11) (11) top is fixed with horizontal fixed plate (20), and the end far from dispersion wind pipeline in fixed plate (20), which is fixed with, passes through band Dynamic dispersion air hose (11) pumps and shakes and fall the pneumatic hammer vibrating device (21) of dross;The pneumatic hammer vibrating device (21) Including the pneumatic hammer (210) being installed on the upside of fixed plate (20), the brute spring being connected with pneumatic hammer (210) on the downside of fixed plate (20) (211) and guide rod (212) it, is set on the guide rod (212) on the upside of the brute spring (211), brute spring (211) lower end is supported on material feeding box (12);The technique bellows (14) are equipped in diameter maximum keeps gas tangentially pre- The technique wind rotation direction device (140) of mixed concentrate powder.
2. the improved vibration premixed type concentrate burner of one kind according to claim 1, it is characterised in that:The brute spring (211) lower semisection is sheathed in pilot sleeve (213), and locking nut (215) is provided on the upside of pilot sleeve (213), is led It is fixed on the top of material feeding box (12) by the pedestal on the downside of it to sleeve (213), pilot sleeve (213) is located at locking screw It is arranged with the positioning plate (214) being fixedly connected with dispersion air hose (11) on the stack shell of female (215) between pedestal.
3. the improved vibration premixed type concentrate burner of one kind according to claim 2, it is characterised in that:The pneumatic hammer vibration It is 3 that device (21) is uniformly distributed in fixed plate (20).
4. the improved vibration premixed type concentrate burner of one kind according to claim 1, it is characterised in that:The material feeding box (12) the neighbouring downside being open is equipped with feed inlet premix air port (120) of air port upward.
5. the improved vibration premixed type concentrate burner of one kind according to claim 1, it is characterised in that:The technique wind rotation It is set as oblique technique wind inlet that is parallel along the inclined surface of taper technique bellows (14) and setting to device (140), it can edge with formation The whirlwind of tangential premix concentrate powder.
6. the improved vibration premixed type concentrate burner of one kind according to claim 1, it is characterised in that:The dispersion air hose (11) the independent premix supply air line (110) for leading to material feeding box (12) bottom is additionally provided in and around this in the pre- of pipeline side Mixed wind beam device (111);The pre-mixed air beam device (111) is equipped with the tangential swing angle (β) for rolling oblique 30 ° outwardly.
CN201810262167.3A 2016-08-04 2016-08-04 A kind of improved vibration premixed type concentrate burner Active CN108680029B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201810262167.3A CN108680029B (en) 2016-08-04 2016-08-04 A kind of improved vibration premixed type concentrate burner

Applications Claiming Priority (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

Related Parent Applications (1)

Application Number Title Priority Date Filing Date
CN201610632799.5A Division CN106288815B (en) 2016-08-04 2016-08-04 A kind of vibration premixed type concentrate burner

Publications (2)

Publication Number Publication Date
CN108680029A true CN108680029A (en) 2018-10-19
CN108680029B CN108680029B (en) 2019-08-02

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 After (1)

Application Number Title Priority Date Filing Date
CN201610632799.5A Active CN106288815B (en) 2016-08-04 2016-08-04 A kind of vibration premixed type concentrate burner

Country Status (1)

Country Link
CN (2) CN108680029B (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
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
CN116951987A (en) * 2023-09-18 2023-10-27 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

Families Citing this family (3)

* Cited by examiner, † Cited by third party
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
CN110804702B (en) * 2019-12-02 2024-09-27 江西铜业股份有限公司 Concentrate burner for flash smelting

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104388695A (en) * 2014-11-26 2015-03-04 铜陵有色金属集团股份有限公司金冠铜业分公司 Jet nozzle of concentrate
CN104567431A (en) * 2014-12-04 2015-04-29 金川集团股份有限公司 Cyclone concentrate spray nozzle
CN104561587A (en) * 2015-01-20 2015-04-29 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
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 (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FI105828B (en) * 1999-05-31 2000-10-13 Outokumpu Oy Device for equalizing the feeding-in of pulverulent material in an enrichment burner in the ore concentrate burner of a suspension smelting furnace
FI121852B (en) * 2009-10-19 2011-05-13 Outotec Oyj Process for feeding fuel gas into the reaction shaft in a suspension melting furnace and burner
ES2662572T3 (en) * 2011-05-06 2018-04-09 Hatch Ltd Burner and feeding apparatus for fast melting furnace

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104388695A (en) * 2014-11-26 2015-03-04 铜陵有色金属集团股份有限公司金冠铜业分公司 Jet nozzle of concentrate
CN104567431A (en) * 2014-12-04 2015-04-29 金川集团股份有限公司 Cyclone concentrate spray nozzle
CN104561587A (en) * 2015-01-20 2015-04-29 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
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)

* Cited by examiner, † Cited by third party
Title
姚绍芸: "新型精矿喷嘴在贵溪冶炼厂二期闪速炉的应用", 《有色冶金设计与研究》 *

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
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
CN116951987A (en) * 2023-09-18 2023-10-27 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
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

Also Published As

Publication number Publication date
CN106288815B (en) 2018-06-29
CN106288815A (en) 2017-01-04
CN108680029B (en) 2019-08-02

Similar Documents

Publication Publication Date Title
CN108680029B (en) A kind of improved vibration premixed type concentrate burner
CN201988675U (en) Full-countercurrent heat exchange two-stage waste sand casting roasting furnace
CN201245560Y (en) Cocurrent heat storing type dual-chamber limekiln capable of realizing two-stage calcination
CN102410715B (en) Parallel-flow heating vertical static dryer
CN102042757A (en) Method of using a suspension smelting furnace, a suspension smelting furnace, and a concentrate burner
CN102777894A (en) Reverse powder injection combustor
CN201242342Y (en) Shaft kiln
CN202836180U (en) Ring-shaped sleeve kiln
CN106276901A (en) A kind of oxygen full-boiled process produces carbide and the method and system of CO gas
CN1166198A (en) Metal fusion furnace and metal fusing method
CN207002588U (en) A kind of active powder lime two level suspension calcining device
CN102660673A (en) Process and device for roasting reinforced high-sulfur pyrite ore concentrate in fluidized bed roaster
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
CN105112683A (en) Suspension smelting method and suspension smelting nozzle
CN212504611U (en) Straight cylinder type light-burned magnesium oxide suspension roasting device
CA3016821C (en) System having a furnace and method for operating such a system
CN111777343A (en) Efficient and environment-friendly tower type mixed combustion light-burning magnesium shaft kiln and production process thereof
CN101962696A (en) Method for blowing furnace washing agent by using air inlet of blast furnace
CN105318681B (en) Drier or pyrolysis apparatus
CN102506421A (en) Circulating fluid bed (CFB) boiler coal supply system for blending combustion of middling coal
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
CN210826072U (en) Mixed air distribution system of gas producer
CN210163146U (en) Limestone powder instantaneous sintering device and system thereof

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
GR01 Patent grant
GR01 Patent grant