CN106868238A - A kind of pelletizer system for molten slag granulation - Google Patents
A kind of pelletizer system for molten slag granulation Download PDFInfo
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- CN106868238A CN106868238A CN201710113948.1A CN201710113948A CN106868238A CN 106868238 A CN106868238 A CN 106868238A CN 201710113948 A CN201710113948 A CN 201710113948A CN 106868238 A CN106868238 A CN 106868238A
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- pelletizer
- airduct
- granulation
- base
- molten slag
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- C—CHEMISTRY; METALLURGY
- C21—METALLURGY OF IRON
- C21B—MANUFACTURE OF IRON OR STEEL
- C21B3/00—General features in the manufacture of pig-iron
- C21B3/04—Recovery of by-products, e.g. slag
- C21B3/06—Treatment of liquid slag
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- C—CHEMISTRY; METALLURGY
- C21—METALLURGY OF IRON
- C21B—MANUFACTURE OF IRON OR STEEL
- C21B3/00—General features in the manufacture of pig-iron
- C21B3/04—Recovery of by-products, e.g. slag
- C21B3/06—Treatment of liquid slag
- C21B3/08—Cooling slag
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- 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
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/50—Reuse, recycling or recovery technologies
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- Chemical & Material Sciences (AREA)
- Manufacturing & Machinery (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Furnace Details (AREA)
Abstract
The invention discloses a kind of pelletizer system for molten slag granulation, including pelletizer and pelletizer fixing device;Pelletizer is plate-like or cup-shaped, and pelletizer center sets deflection cone;Changing device fixing device includes pelletizer base;The center that there is an annular groove, pelletizer base pelletizer side is provided with a circular pelletizer mounting groove, and the side wall of mounting groove is provided with an annular groove, and pelletizer is fixed on pelletizer base by ring-shaped clip and two annular grooves cooperations;Pelletizer base is made up of left and right two parts, is fixed with anchor ear by pin;Pelletizer base bottom is hollow flange, and hollow flange is fixedly connected by pin with the flange of rotating shaft, and one section of air adiabatic layer is formed between pelletizer base and rotating shaft.The present invention is able to ensure that pelletizer safe and stable can run, and preferably realizes granulation effect.
Description
Technical field
The present invention relates to molten slag granulation technique field, more particularly to a kind of pelletizer system for molten slag granulation
System.
Background technology
China is currently global maximum steel producing country, iron and steel output the first in the world.Chinese pig iron yield reaches within 2015
To 6.91 hundred million tons, the 60% of Gross World Product is accounted for.Chinese pig iron yield is 5.86 hundred million tons within 10 months 2016, accounts for the world total
The 60% of yield.The blast furnace slag for containing huge heat can be produced during manUfaCtUre of pig iron, the tapping temperature of blast furnace slag is general
Between 1400~1550 DEG C, slag per ton contains (1260~1880) × 103The sensible heat of kJ, equivalent to 60kg standard coals.In China
Under existing ironmaking technology, 1 ton of pig iron by-product, 0.3 ton of blast furnace slag is often produced, carried out with current 5.86 hundred million tons of China's pig iron yield
Calculate, the blast furnace slag for producing more than 1.75 hundred million tons can be converted into, its sensible heat amount is equivalent to 10,500,000 tons of standard coals.
Dry pit cooling method and flush slag method are the most common Treating Methods for BF Slag of current China.Dry pit cooling method will
The molten slag of high temperature is directly discharged into dry pit air cooling, auxiliary water cooling.The method produces a large amount of vapor when lowering the temperature, while discharging
Substantial amounts of H2S and SO2Gas, corrosion building, destruction equipment and aggravating working environment are general that the method is only used in accident treatment.
The blast furnace slag of China 90% is all using the treatment of flush slag method.Flush slag method refer to using low temperature cooling water directly with the liquid of high temperature
State slag mixes so that molten slag temperature is reduced and form glass figure's slag granules rapidly.Flush slag method is according to different
Technological process can be divided into Yin Bafa, Tula method, bottom filter method, Lhasa method, Ming Tekefa.Although flush slag technique is continued to develop,
The core of its technology still carries out water spray water quenching to high-temperature liquid state slag, and then reaches cooling and the purpose being granulated, and then carries out
Grain slag is separated, and the water of flushing cinder is recycled after precipitating filtering.Although the glass figure slag that the method is produced can be applied
Recycling is carried out in cement industry, but processing procedure wastes great lot of water resources, produces SO2And H2The pernicious gases such as S,
The high-quality residual heat resources contained by high-temperature liquid state slag can not effectively be reclaimed.
During blast furnace slag dry method centrifugal granulation, liquid slag drops onto the disc surfaces by rotating at a high speed, in centrifugation
It is thrown out of in the presence of power and frictional force, droplet is formed in the presence of molten slag surface tension, these small drops
Forced-convection heat transfer is carried out with the heat transfer medium (generally air) in space, radiation heat transfer is carried out with surrounding environment, make small liquid
Drop temperature is reduced rapidly, and then is undergone phase transition, and forms solidification layer.As temperature is further reduced, drop is gradually transformed into solid
Little particle.For blast furnace slag centrifugal granulation system, granulation system is the core of whole system, and pelletizer is granulation system
Core component, while be also ensure granulation stability and granulation efficiency key.Current dry granulation technology is in liquid
Generally existing problems with during state blast furnace slag granulation:
1. good cooling is not carried out to pelletizer.During liquid blast furnace slag granulation, drive of the pelletizer in motor
Lower high speed rotation.Meanwhile, the blast furnace slag of molten state is constantly dropped onto on pelletizer.The temperature of liquid blast furnace is up to 1450
DEG C, under so severe working environment, if pelletizer does not carry out good cooling, so it is easy to pelletizer
Accident.
2. the replacing difficulty of pelletizer, replacement cost are big.The main component of the liquid blast furnace of high temperature be MgO, CaO,
SiO2, temperature is up to 1450 DEG C, extremely easy that corrosion abrasion is produced to pelletizer, and pelletizer needs periodic replacement.Existing granulation
Device structure pelletizer and base are the designs of integration, and replacing difficulty is high, cost is big.
3. flow perturbation is not applied when molten slag just leaves pelletizer.The disturbance for strengthening air-flow can make liquid
State slag is broken into droplet, enhancing molten slag and the heat convection of air as early as possible, molten slag is solidified as early as possible, strengthens grain
Change effect.Conventional molten slag granulation system does not consider that not applying air-flow when molten slag just leaves pelletizer disturbs
It is dynamic, miss the inning of enhancing granulation effect.
4. without can effectively block the heat transfer of pelletizer to rotating shaft.Pelletizer and temperature are 1450 DEG C of liquid
Slag directly contact, temperature is directly connected to more than 1400 DEG C between traditional molten slag granulation system pelletizer and rotating shaft,
Heat transfer without effectively blocking pelletizer is in rotating shaft.Under the high temperature conditions, the intensity of steel shafts declines, and can make granulation
The fluctuation of service of device, influence granulation effect.
The content of the invention
It is an object of the invention to provide a kind of pelletizer system for molten slag granulation, to ensure that pelletizer is obtained
Well cool down, be conveniently replaceable, while preventing the heat transfer of pelletizer to rotating shaft.Pelletizer and its fixation that the present invention is provided
Device can also increase air agitation, accelerate break up drops, enhancing heat exchange.The present invention can make the safe and stable operation of granulation system,
Preferably realize granulation effect.
To achieve these goals, the technical solution adopted by the present invention is:
A kind of pelletizer system for molten slag granulation, including pelletizer and pelletizer fixing device;Pelletizer is
Plate-like or cup-shaped, pelletizer center set deflection cone;Changing device fixing device includes pelletizer base;There is a ring pelletizer side
Connected in star, the center of pelletizer base is provided with a circular pelletizer mounting groove, and the side wall of mounting groove is provided with an annular groove, grain
Change device to be fixed on pelletizer base by ring-shaped clip and two annular grooves cooperations;Pelletizer base is by left and right two parts group
Into being fixed with anchor ear by pin;Pelletizer base bottom is hollow flange, and hollow flange is consolidated by pin with the flange of rotating shaft
Fixed connection, forms one section of air adiabatic layer between pelletizer base and rotating shaft.
Further, pelletizer base side wall is provided with the air vent of circular symmetric arrangement.
Further, pelletizer edge is provided with the auxiliary granulation air nozzle of circular symmetric arrangement.
Further, also including pelletizer cold wind control unit;Pelletizer cold wind control unit includes rotating shaft, motor and cold
Wind feeding unit;Rotating shaft is fixed with the motor of vertical setting;Rotating shaft is provided with the second temperature element for monitoring rotating shaft temperature;
Motor is sealed by seal closure, and seal closure air port is provided with seal closure, and rotating shaft periphery is cased with shaft sleeve, fixed on motor seal cover
There is airduct inner sleeve;Airduct inner sleeve is arranged at shaft sleeve periphery, and shaft sleeve is by the bearings with ventilating opening in airduct
Sleeve inner;The top of motor seal cover connects with airduct inner sleeve;The cooling air port of circular symmetric arrangement is provided with shaft sleeve;
Cold wind feeding unit is divided into axle cooling air channel and annular cooling air channel two-way, and cold blast main road is provided with master control valve, master control
The outlet of valve is divided into axle cooling wind branch road and annular cooling wind branch road two-way;Annular cooling wind branch road is provided with annular cooling wind branch
Road controls valve, axle cooling wind branch road to be provided with flowmeter;Axle cooling air channel is made up of airduct inner sleeve and shaft sleeve;Annular cooling
Air channel is made up of two different airduct inner sleeves of external diameter with the airduct outer sleeve for being arranged at airduct inner sleeve periphery, outside airduct
Sleeve bottom is provided with airduct outer sleeve air inlet, and blast cap is arranged at top;Axle cooling wind branch road connection seal closure sealed bottom cover air port;
Annular cooling wind branch road connection airduct outer sleeve bottom airduct outer sleeve air inlet.
Further, cooling air port is strip.
Further, some blast cap annulars are arranged at pelletizer lower, outer perimeter, for the slag to being flown out from pelletizer
Further cool down and strengthen granulation.
Further, the air outlet on airduct inner sleeve top is arranged at pelletizer bottom, the axle cooling wind of axle cooling air channel
Further cooled down by air vent countershaft, then from airduct inner sleeve top out, into pelletizer base side wall
The air vent for opening up is cooled down to pelletizer.
Further, also including feed unit;Feed unit includes the slag dropping tube being arranged at directly over pelletizer;Slag dropping tube
Including upper and lower two sections, upper end diameter is more than lower end diameter, and hypomere sets slide gate nozzle, and with accident guiding gutter;It is provided with slag dropping tube
The first temperature element for monitoring molten slag temperature in slag dropping tube.
Further, the airduct outer sleeve external welding wedge shape fixed block of annular cooling air channel, is engaged with sliding shoe, slides
Fixed by pin between block and fixed support, adjust the position of sliding shoe and then adjust pelletizer and the slag that falls by twisting pin
Spacing between pipe, realizes the regulation up and down of molten slag height of drop.
Relative to prior art, present invention evidence has following beneficial effect:
(1) the ring-shaped clip structure of pelletizer bottom is conducive to when pelletizer is damaged to its buffer time in the present invention,
Pelletizer is conveniently replaceable, while reducing the expense that general pelletizer changes whole granulating device because being damaged.Pelletizer base
It is made up of left and right two parts, is fixed by pin and anchor ear, facilitates the installation of the pelletizer with ring-shaped clip.
(2) pelletizer base side wall is provided with the air vent of circular symmetric arrangement in the present invention, and one is carried out to pelletizer base
Fixed cooling, increases the service life of pelletizer.
(3) pelletizer base bottom is hollow flange in the present invention, and hollow flange is connected with flange by pin, empty
The presence of heart flange, reduces pelletizer fixing device heat transfer from top to bottom to a certain extent.
(4) pelletizer edge upper part is provided with the auxiliary granulation air nozzle of circular symmetric arrangement in the present invention, and air is sprayed
Pelletizer edge is mapped to be granulated for assistant reinforcement.
Brief description of the drawings
The present invention is described in further details with reference to the accompanying drawings and detailed description.
Fig. 1 is to include pelletizer and pelletizer fixing device schematic diagram;
Fig. 2 is pelletizer cold wind control unit and feed unit schematic diagram.
1st, pelletizer;2nd, ring-shaped clip;3rd, pelletizer base;4th, ventilating opening;5th, pin;6th, anchor ear;7th, hollow flange;8、
Pin;9th, flange;10th, rotating shaft;11st, auxiliary granulation air nozzle.
Specific embodiment
Refer to shown in Fig. 1, a kind of pelletizer system for molten slag granulation of the present invention, including pelletizer 1 and grain
Change device fixing device.
Pelletizer 1 is plate-like or cup-shaped, the centrally disposed deflection cone of pelletizer 1;The top edge of pelletizer 1 is provided with circular symmetric
The auxiliary granulation air nozzle 11 of arrangement;The center that there is an annular groove, pelletizer base 3 side of pelletizer 1 is provided with a circle
Shape pelletizer mounting groove, the side wall of mounting groove is provided with an annular groove, and pelletizer 1 passes through ring-shaped clip 2 and two annular grooves
Cooperation is fixed on pelletizer base 3;The side wall of pelletizer base 3 is provided with the air vent 4 of circular symmetric arrangement;Pelletizer base 3
It is made up of left and right two parts, is fixed by pin 5, anchor ear 6;The bottom of pelletizer base 3 is hollow flange 7, and hollow flange 7 passes through
Pin 8 is fixedly connected with the flange 9 of rotating shaft 10.
Need to regularly replace this problem for pelletizer, in the present invention, pelletizer base 3 is by left and right two parts group
Into being fixed by pin 5, anchor ear 6.When pelletizer is damaged, pin 8 is pulled down, pelletizer 1 and pelletizer base 3 can be removed, torn open
Lower pin 5, anchor ear 6, can take left and right two parts of pelletizer base 3 apart, and pelletizer can be removed after removing ring-shaped clip 2
1.When pelletizer is cracking, due to the presence of pelletizer base and fixing device, the pelletizer of cracking will not be got rid of winged, together
When molten slag directly will not drop onto on transmission device and motor, before maintenance down ensure system safety.Meanwhile, only need
Changing pelletizer just can be to reduce the expense that general pelletizer changes whole granulating device because being damaged.
Need to cool down this problem for pelletizer base, in the present invention, the side wall of pelletizer base 3 is provided with circular symmetric
The air vent 4 of arrangement;Pelletizer base end face has certain gradient simultaneously, is easy to the wind sent by pelletizer base bottom to enter
Enter to air vent 4, pelletizer base 3 is cooled down, while being easy to the wind sent by pelletizer base to the side of pelletizer
Edge, to strengthen granulation.
For this problem of heat transfer between blocking pelletizer and rotating shaft, in the present invention, using the countershaft of hollow flange 7
10 and pelletizer base 3 be attached, hollow flange 7 makes to have between pelletizer base and rotating shaft 10 one section of air adiabatic layer, makes
The heat of pelletizer base is unlikely to be delivered in rotating shaft, it is ensured that pelletizer safe and stable can run, and preferably realizes granulation
Effect.
For how to accelerate blast furnace slag to solidify this problem, one auxiliary granulation is set on the top of pelletizer in the present invention
Air nozzle 11.One auxiliary granulation air nozzle 11 is set on the top of pelletizer and sprays the applying disturbance of one air-flow, strengthen gas
The disturbance of stream can make molten slag be broken into droplet, enhancing molten slag and the heat convection of air as early as possible, make molten slag
Solidify as early as possible, strengthen granulation effect.
Refer to shown in Fig. 2, further, in order to reduce the problem of pelletizer, present invention additionally comprises pelletizer cold wind control
Unit processed;
Pelletizer cold wind control unit, including rotating shaft 10, motor 101 and cold wind feeding unit.Rotating shaft 10 is fixedly connected vertical
The motor 101 that formula is set;Rotating shaft 10 is provided with the second temperature element 17 for monitoring rotating shaft temperature;Motor 101 and rotating shaft 10
Between be connected by shaft coupling 103;Motor 101 is sealed by seal closure 102, and air port 23, rotating shaft 10 are provided with seal closure 102
Periphery is cased with shaft sleeve 15, and airduct inner sleeve 107 is fixed with motor seal cover 102;Airduct inner sleeve 107 is arranged at shaft sleeve
15 peripheries, shaft sleeve 15 is by the bearings with ventilating opening inside airduct inner sleeve 107;The top of motor seal cover 102
Connected with airduct inner sleeve 107.The cooling air port 21 of circular symmetric arrangement is provided with shaft sleeve 15, cooling air port is strip.
Cold wind feeding unit is divided into axle cooling air channel and annular cooling air channel two-way, and cold blast main road is provided with master control valve
19, the outlet of master control valve is divided into axle cooling wind branch road and annular cooling wind branch road two-way;Annular cooling wind branch road is provided with control
Valve processed 18, axle cooling wind branch road is provided with flowmeter 22;Axle cooling air channel is made up of airduct inner sleeve 107 with shaft sleeve 15;Ring
Shape cooling air channel is made up of two different airduct sleeves (airduct inner sleeve 107 and airduct outer sleeve 108) of external diameter, outside airduct
The bottom of sleeve 108 is provided with air inlet 20, and blast cap 9 is arranged at top.The axle cooling wind branch road connection bottom tuyeres 23 of seal closure 102;Annular
The bottom air inlet mouthful 20 of cooling wind branch road connection airduct outer sleeve 108.
The external welding of the airduct outer sleeve 108 wedge shape fixed block 104 of annular cooling air channel, is engaged with sliding shoe 105, slides
Fixed by pin between block 105 and fixed support 106, adjust the position of sliding shoe and then adjust whole grain by twisting pin
The height that makeup is put, realizes the regulation up and down of molten slag height of drop, can control to fall into pelletizer to a certain extent
Slag temperature, so as to control to pass to the temperature of rotating shaft.The height that regulation slag falls simultaneously can also realize the regulation to particle diameter, reach
Preferably it is granulated effect.
Feed unit is additionally provided with pelletizer 1, comprising the slag dropping tube 111 being arranged at directly over pelletizer 1.Slag dropping tube 111
It is divided into upper and lower two sections, upper end diameter is more than lower end diameter, hypomere sets slide gate nozzle 112, and with accident guiding gutter 113.Liquid melts
Slag carries out centrifugal granulation by being fallen into the pelletizer 1 of rotation after upper and lower section of slag dropping tube.It is provided with for monitoring in slag dropping tube 111
First temperature element 110 of molten slag temperature in slag dropping tube 111.
Annular cooling wind enters from air inlet 20, and, blast cap 109 is arranged at pelletizer bottom from the blast cap 109 at top out
Periphery, the slag to being flown out from pelletizer 1 is further cooled down and strengthens granulation;Axle cools down wind of the wind from the bottom of seal closure 102
Mouth 23 enters, and certain cooling is carried out to motor, and the heat transfer for being prevented from being produced during motor operation causes rotating shaft to rotating shaft
The rising of temperature, improves the reliability of motor operation and the life-span of motor;Axle cooling wind in seal closure 102 is entered by air vent
Enter axle cooling air channel, the strip cooling air port 21 of circular symmetric arrangement is provided with shaft sleeve 15, can preferably cool down rotating shaft
10, prevent rotating shaft from overheating and be deformed, have influence on the granulation effect of driven pelletizer 1;The axle cooling wind of axle cooling air channel
Further cooled down by the air vent countershaft on top, then from the top of airduct inner sleeve 107 out, into pelletizer
The air vent 4 that the side wall of base 3 is opened up is cooled down to pelletizer 1.
Finally it should be noted that:Embodiment of above is only used to illustrate the present invention without limiting the present invention described technology
Scheme;Therefore, although this specification with reference to each above-mentioned implementation method to present invention has been detailed description, this
Field it is to be appreciated by one skilled in the art that still can be modified to the present invention or equivalent;And all do not depart from this
The technical scheme of the spirit and scope of invention and its improvement, it all should cover in scope of the presently claimed invention.
Claims (9)
1. a kind of pelletizer system for molten slag granulation, it is characterised in that fixed including pelletizer (1) and pelletizer and filled
Put;
Pelletizer (1) is plate-like or cup-shaped, and pelletizer center sets deflection cone;
Changing device fixing device includes pelletizer base (3);There are an annular groove, the center of pelletizer base (3) in pelletizer side
A circular pelletizer mounting groove is provided with, the side wall of mounting groove is provided with an annular groove, and pelletizer (1) is by ring-shaped clip (2)
Coordinate with two annular grooves and be fixed on pelletizer base (3);Pelletizer base is made up of left and right two parts, by pin with
Anchor ear is fixed;Pelletizer base bottom is hollow flange (7), and hollow flange (7) is fixed by pin with the flange of rotating shaft (10)
Connection, forms one section of air adiabatic layer between pelletizer base and rotating shaft (10).
2. it is according to claim 1 it is a kind of for molten slag granulation pelletizer system, it is characterised in that pelletizer bottom
Seat (3) side wall is provided with the air vent (4) of circular symmetric arrangement.
3. it is according to claim 1 it is a kind of for molten slag granulation pelletizer system, it is characterised in that pelletizer
(1) edge is provided with auxiliary granulation air nozzle (11) of circular symmetric arrangement.
4. it is according to claim 1 it is a kind of for molten slag granulation pelletizer system, it is characterised in that also including grain
Change device cold wind control unit;Pelletizer cold wind control unit includes rotating shaft, motor and cold wind feeding unit;Rotating shaft and vertical setting
Motor fix;Rotating shaft is provided with the second temperature element for monitoring rotating shaft temperature;Motor is sealed by seal closure, seal closure
On be provided with seal closure air port, rotating shaft periphery is cased with shaft sleeve, airduct inner sleeve is fixed with motor seal cover;Airduct inner sleeve sets
Shaft sleeve periphery is placed in, shaft sleeve is by the bearings with ventilating opening inside airduct inner sleeve;The top of motor seal cover
Connected with airduct inner sleeve;The cooling air port of circular symmetric arrangement is provided with shaft sleeve;Cold wind feeding unit is divided into axle cooling wind
Road and annular cooling air channel two-way, cold blast main road are provided with master control valve, and the outlet of master control valve is divided into axle cooling wind branch road
With annular cooling wind branch road two-way;Annular cooling wind branch road is provided with annular cooling wind branch road control valve, on axle cooling wind branch road
It is provided with flowmeter;Axle cooling air channel is made up of airduct inner sleeve and shaft sleeve;Annular cooling air channel is by the different wind of two external diameters
Pipe inner sleeve and the airduct outer sleeve composition for being arranged at airduct inner sleeve periphery, airduct outer sleeve is provided with airduct outer sleeve bottom
Blast cap is arranged at air inlet, top;Axle cooling wind branch road connection seal closure sealed bottom cover air port;Annular cooling wind branch road connection airduct
Outer sleeve bottom airduct outer sleeve air inlet.
5. it is according to claim 4 it is a kind of for molten slag granulation pelletizer system, it is characterised in that cooling air port
It is strip.
6. it is according to claim 4 it is a kind of for molten slag granulation pelletizer system, it is characterised in that some blast caps
Annular is arranged at pelletizer lower, outer perimeter, and granulation is further cooled down and strengthened for the slag to being flown out from pelletizer.
7. it is according to claim 4 it is a kind of for molten slag granulation pelletizer system, it is characterised in that airduct inner sleeve
The air outlet on cylinder top is arranged at pelletizer bottom, and the axle cooling wind of axle cooling air channel is carried out further by air vent countershaft
Cooling, then from airduct inner sleeve top out, the air vent opened up into pelletizer base side wall is cooled down to pelletizer.
8. it is according to claim 4 it is a kind of for molten slag granulation pelletizer system, it is characterised in that also including supply
Material unit;Feed unit includes the slag dropping tube being arranged at directly over pelletizer;Slag dropping tube includes upper and lower two sections, and upper end diameter is big
In lower end diameter, hypomere sets slide gate nozzle, and with accident guiding gutter;It is provided with slag dropping tube for monitoring molten slag in slag dropping tube
First temperature element of temperature.
9. it is according to claim 8 it is a kind of for molten slag granulation pelletizer system, it is characterised in that annular cooling
The airduct outer sleeve external welding wedge shape fixed block in air channel, is engaged with sliding shoe, and pin is passed through between sliding shoe and fixed support
It is fixed, adjust the position of sliding shoe and then adjust the spacing between pelletizer and slag dropping tube by twisting pin, realize that liquid melts
The regulation up and down of slag height of drop.
Priority Applications (2)
Application Number | Priority Date | Filing Date | Title |
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CN201710113948.1A CN106868238B (en) | 2017-02-28 | 2017-02-28 | One kind being used for the granulated granulator system of molten slag |
PCT/CN2017/080326 WO2018157450A1 (en) | 2017-02-28 | 2017-04-13 | Granulator system for granulating liquid-state slags |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
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CN201710113948.1A CN106868238B (en) | 2017-02-28 | 2017-02-28 | One kind being used for the granulated granulator system of molten slag |
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CN106868238A true CN106868238A (en) | 2017-06-20 |
CN106868238B CN106868238B (en) | 2019-04-12 |
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CN201710113948.1A Active CN106868238B (en) | 2017-02-28 | 2017-02-28 | One kind being used for the granulated granulator system of molten slag |
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Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN108130397A (en) * | 2017-12-22 | 2018-06-08 | 安徽工业大学 | A kind of two-fluid accelerator of slag and water |
CN108330236A (en) * | 2018-02-26 | 2018-07-27 | 西安交通大学 | Molten slag dry-type centrifugal is granulated slag particle quality and regulates and controls method |
CN108330234A (en) * | 2018-02-26 | 2018-07-27 | 西安交通大学 | A kind of dry-type centrifugal granulation and waste heat recovery experimental provision |
CN109865476A (en) * | 2019-04-22 | 2019-06-11 | 重庆大学 | The Multi-layer centrifugal granulator of efficient process big flow molten slag |
CN110238407A (en) * | 2019-06-21 | 2019-09-17 | 宁夏森源重工设备有限公司 | Novel iron alloy granulating device |
CN111074020A (en) * | 2019-12-04 | 2020-04-28 | 西安交通大学 | Integrated liquid slag caching and flow measurement and control device |
Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101893372A (en) * | 2010-07-22 | 2010-11-24 | 广东世创金属科技有限公司 | Furnace tank for pit furnace having structure for preventing/reducing leakage of heat in furnace |
CN203096087U (en) * | 2013-03-06 | 2013-07-31 | 圣火科技(河南)有限责任公司 | Liquid state slag granulating device |
CN105624347A (en) * | 2016-03-11 | 2016-06-01 | 西安交通大学 | Liquid high-temperature slag granulation and waste heat recovery device |
CN105624348A (en) * | 2016-03-11 | 2016-06-01 | 西安交通大学 | System for granulating high-temperature molten slag |
CN105624346A (en) * | 2016-03-11 | 2016-06-01 | 西安交通大学 | Slag buffering system with flow control function |
Family Cites Families (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20100242683A1 (en) * | 2009-03-26 | 2010-09-30 | Tetsuo Yamaki | Process for treating exhaust gas generated during water-granulation of slag and system for said treatment |
CN105755188B (en) * | 2016-03-11 | 2018-03-02 | 西安交通大学 | It is a kind of to be used to be granulated high-temperature liquid state slag and reclaim the mobile bed apparatus of high temperature sensible heat |
-
2017
- 2017-02-28 CN CN201710113948.1A patent/CN106868238B/en active Active
- 2017-04-13 WO PCT/CN2017/080326 patent/WO2018157450A1/en active Application Filing
Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101893372A (en) * | 2010-07-22 | 2010-11-24 | 广东世创金属科技有限公司 | Furnace tank for pit furnace having structure for preventing/reducing leakage of heat in furnace |
CN203096087U (en) * | 2013-03-06 | 2013-07-31 | 圣火科技(河南)有限责任公司 | Liquid state slag granulating device |
CN105624347A (en) * | 2016-03-11 | 2016-06-01 | 西安交通大学 | Liquid high-temperature slag granulation and waste heat recovery device |
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