CN106350626B - A kind of solid particle multilayer distributor - Google Patents
A kind of solid particle multilayer distributor Download PDFInfo
- Publication number
- CN106350626B CN106350626B CN201610789100.6A CN201610789100A CN106350626B CN 106350626 B CN106350626 B CN 106350626B CN 201610789100 A CN201610789100 A CN 201610789100A CN 106350626 B CN106350626 B CN 106350626B
- Authority
- CN
- China
- Prior art keywords
- particle
- flap
- upper spacer
- overhead gage
- baffle plate
- 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
-
- 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
-
- 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
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Manufacturing & Machinery (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Feeding, Discharge, Calcimining, Fusing, And Gas-Generation Devices (AREA)
- Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
Abstract
A kind of solid particle multilayer distributor, including flap, shaft, funnel, upper spacer, lower clapboard, overhead gage, lower baffle plate, shell, upper outlet, lower outlet, it is characterised in that:Intermittent swing forms upper and lower two positions to the flap around the shaft, and overhead gage is located at the front end of upper spacer, and there are gaps, the two to constitute " V " type region between upper spacer;Lower baffle plate is located at the front end of lower clapboard, and there are gaps, the two to constitute " V " type region between lower clapboard.Particle is entered by funnel, is first fallen on flap, and flap is in upper position; then particle slides to upper spacer; it is piled up in " V " the type region that overhead gage and upper spacer are constituted, subsequent particle will slide to upper outlet and be discharged continually by the gap between overhead gage and upper spacer;Work when flap is in lower position is same as described above.The present invention realizes the distribution of particle using the flap of intermittent oscillation, and the particle for distributing gained is continuous, uniform, and work efficiency is high for system.
Description
Technical field
The present invention relates to machinery equipment field, and in particular to a kind of solid particle multilayer distributor.
Background technology
Steel and iron industry total energy consumption accounts for about the 35% of whole process industry total energy consumption, and the temperature that ironmaking processes generate blast furnace slag exists
1450~1650 DEG C, thermal content about 1.70~1.87GJ/t of blast furnace slag is equivalent to the fever of 0.058~0.06 ton of standard coal
Amount.Clinker sensible heat total amount is huge and is important secondary energy sources, and recycling afterheat of slags improves energy to Energy-saving of Iron And Steel Industry emission reduction
Source utilization ratio has the economic implications of reality.Currently, domestic smelter high temperature furnace slag is mainly used water quenching technology into
Row processing.What it is by the recycling of various Water Quenching techniques is only the 10% of clinker total amount of heat, and excess heat is arrived with moisture discharge
In air, the waste of heat and water resource is caused.In addition, blast furnace slag is also used as raw material of industry use, there is certain warp
Ji utility value.It is usually by multiple that the blast furnace slag that ironmaking processes generate, which needs the process by heat exchange and screening, the above process,
What the multiple regions of equipment or an equipment were carried out at the same time, how to realize that blast furnace slag simply and effectively distributes, is set to improve
Standby whole working efficiency is an important technical problem.
Invention content
To solve above-mentioned problems of the prior art, the purpose of the present invention is to provide a kind of solid particle multilayers point
With device, particle can continuously and uniformly be distributed to multilayer insulating panel, to realize further utilize to the particle after distribution.
In order to achieve the above object, the technical solution adopted in the present invention is:
A kind of solid particle multilayer distributor, including flap 1, shaft 2, funnel 3, upper spacer 4, lower clapboard 5, overhead gage
6, lower baffle plate 7, shell 8, upper outlet 9, lower outlet 10, it is characterised in that:In the 2 intermittent swing formation around the shaft of the flap 1,
Lower two positions, overhead gage 6 is located at the front end of upper spacer 4, and there are gaps, the two to constitute " V " type area between upper spacer 4
Domain;Lower baffle plate 7 is located at the front end of lower clapboard 5, and there are gaps, the two to constitute " V " type region between lower clapboard 5.Particle by
Funnel 3 enters, and falls first on flap 1, if flap 1 is in upper position, particle slides to upper spacer 4, is piled up in overhead gage 6
" V " the type region constituted with upper spacer 4, subsequent particle will be sliding continually by the gap between overhead gage 6 and upper spacer 4
Drop down onto the discharge of upper outlet 9.Similarly, if particle by funnel 3 into fashionable, flap 1 is in lower position, then particle slides to lower clapboard
5, it is piled up in " V " the type region that lower baffle plate 7 and lower clapboard 5 are constituted, subsequent particle will be continually by lower baffle plate 7 and lower clapboard
Gap between 5 slides to 10 discharge of lower outlet.
Angle with horizontal plane is 50 ° when the flap 1 is in upper position, angle with horizontal plane when flap 1 is in lower position
It is 65 °.
The overhead gage 6 is fixed on shell 8, and perpendicular to upper spacer 4, the lower baffle plate 7 is fixed on upper spacer 4, and hangs down
Directly in lower clapboard 5.
The length of the lower clapboard 5 is more than the length of upper spacer 4.
Compared to the prior art, the present invention has the following advantages:
A kind of solid particle multilayer distributor provided by the invention can utilize the flap of intermittent oscillation, realize particle
In the distribution of different layers partition room, and the gap of baffle and partition room can make the particle obtained by every Layer assignment continuously and uniformly
Partition board where being paved with.Particle needs the regular hour by the gap of baffle and partition room, during this period of time, intermittent oscillation
The particle that flap can give each Layer assignment new again, to ensure that the continuous-feeding of particle on partition board.The configuration of the present invention is simple, energy consumption
It is low, the distribution of particle is realized using the flap of intermittent oscillation, the particle for distributing gained is continuous, uniform.It can behind distributor
To connect two layers of heating surface of slag granules heat exchanger, it being carried out at the same time feed and heat exchange so that the structure of heat exchanger is compacter,
The working efficiency of system entirety where being effectively improved.
Description of the drawings
Fig. 1 is a kind of front view of solid particle multilayer distributor of the present invention.
Fig. 2 is a kind of right view of solid particle multilayer distributor of the present invention.
Fig. 3 is a kind of vertical view of solid particle multilayer distributor of the present invention.
Specific implementation mode
Invention is further described in detail with reference to the accompanying drawings and detailed description.
As shown in Fig. 1, Fig. 2 and Fig. 3, a kind of solid particle multilayer distributor, including flap 1, shaft 2, funnel 3, on
Partition board 4, lower clapboard 5, overhead gage 6, lower baffle plate 7, shell 8, upper outlet 9, lower outlet 10.2 intermittences swing shape to flap 1 around the shaft
At upper and lower two positions, overhead gage 6 is located at the front end of upper spacer 4, and there are gaps, the two to constitute " V " between upper spacer 4
Type region;Lower baffle plate 7 is located at the front end of lower clapboard 5, and there are gaps, the two to constitute " V " type region between lower clapboard 5.
Grain is entered by funnel 3, is fallen first on flap 1, if flap 1 is in upper position, particle slides to upper spacer 4, is piled up in
" V " the type region that baffle 6 and upper spacer 4 are constituted, subsequent particle will be continually by the seam between overhead gage 6 and upper spacer 4
Gap slides to upper outlet 9 and is discharged;Similarly, if particle by funnel 3 into fashionable, flap 1 goes to lower position, then particle slide to
Lower clapboard 5, is piled up in " V " the type region that lower baffle plate 7 and lower clapboard 5 are constituted, subsequent particle will continually by lower baffle plate 7 with
Gap between lower clapboard 5 slides to 10 discharge of lower outlet.When flap 1 is located at upper spacer 4, particle drop down onto overhead gage 6 with it is upper
Between partition board 4, a certain amount of accumulation is formed, then the action of flap 1 to the position of lower clapboard 5, particle drop down onto lower baffle plate 7 and lower clapboard
Between 5, a certain amount of accumulation is formed, the flap 1 that intermittence is swung returns to the position of upper spacer 4 again, continues to distribute newly
Particle.Distribution needs the regular hour to the particle of upper spacer 4 and lower clapboard 5 by respective gap, to ensure that upper
At outlet 9 and lower outlet 10, the continuity of particle feed.Particle heat exchanger can be connected after upper outlet 9 and lower outlet 10
Two layers of heating surface is carried out at the same time feed and heat exchange so that the structure of heat exchanger is compacter.Further, since the obstruction of baffle is made
With distribution of the particle in the transverse direction of partition board and outlet is also more uniform, can after this makes particle enter heat exchanger later
More sufficiently uniformly exchange heat.
As the preferred embodiment of the present invention, angle with horizontal plane is 50 ° when the flap 1 is in upper position, flap 1
Angle with horizontal plane is 65 ° when in lower position, and larger inclination angle can ensure that particle passes through seam under gravity
Gap falls.As shown in Figure 1, lower clapboard 5 is longer than upper spacer 4, and in the horizontal direction closer to shaft 2.Flap stays in
When position, it is connected with upper spacer 4, the particle entered at this time by funnel 3 can slide to upper spacer 4;Flap 1 stays in lower position
When or during swing, the particle entered by funnel 3 can slide to lower clapboard 5.
As the preferred embodiment of the present invention, the overhead gage 6 is fixed on shell 8, and perpendicular to upper spacer 4, described
Lower baffle plate 7 is fixed on upper spacer 4, and perpendicular to lower clapboard 5.
As the preferred embodiment of the present invention, as shown in Figure 1, the length of the lower clapboard 5 is more than the length of upper spacer 4
Degree, thus lower clapboard 5 is in the horizontal direction closer to shaft 2 can ensure to slide when flap 1 is in different location in this way
Particle can properly enter corresponding partition board.
Claims (3)
1. a kind of solid particle multilayer distributor, including flap (1), shaft (2), funnel (3), upper spacer (4), lower clapboard
(5), overhead gage (6), lower baffle plate (7), shell (8), upper outlet (9), lower outlet (10), it is characterised in that:The flap (1) around
Intermittent swing of shaft (2) forms upper and lower two positions, and the overhead gage (6) is fixed on shell (8), and perpendicular to upper spacer
(4), overhead gage (6) is located at the front end of upper spacer (4), and there are gaps, the two to constitute " V " type region between upper spacer (4);
The lower baffle plate (7) is fixed on upper spacer (4), and perpendicular to lower clapboard (5), and lower baffle plate (7) is located at the front end of lower clapboard (5),
And there are gap between lower clapboard (5), the two constitutes " V " type region, and particle is entered by funnel (3), fallen first in flap (1)
On, if flap (1) is in upper position, particle slides to upper spacer (4), is piled up in what overhead gage (6) and upper spacer (4) were constituted
" V " type region, subsequent particle will slide continually by the gap between overhead gage (6) and upper spacer (4) to upper outlet
(9) it is discharged;Similarly, if particle by funnel (3) into fashionable, flap (1) is in lower position, then particle slides to lower clapboard (5),
It is piled up in " V " the type region that lower baffle plate (7) and lower clapboard (5) are constituted, subsequent particle will be continually by lower baffle plate (7) under
Gap between partition board (5) slides to lower outlet (10) and is discharged.
2. a kind of solid particle multilayer distributor according to claim 1, it is characterised in that:The flap (1) is in
Angle with horizontal plane is 50 ° when upper position, and angle with horizontal plane is 65 ° when flap (1) is in lower position.
3. a kind of solid particle multilayer distributor according to claim 1, it is characterised in that:The lower clapboard (5)
Length is more than the length of upper spacer (4).
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201610789100.6A CN106350626B (en) | 2016-08-31 | 2016-08-31 | A kind of solid particle multilayer distributor |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201610789100.6A CN106350626B (en) | 2016-08-31 | 2016-08-31 | A kind of solid particle multilayer distributor |
Publications (2)
Publication Number | Publication Date |
---|---|
CN106350626A CN106350626A (en) | 2017-01-25 |
CN106350626B true CN106350626B (en) | 2018-10-23 |
Family
ID=57856877
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201610789100.6A Active CN106350626B (en) | 2016-08-31 | 2016-08-31 | A kind of solid particle multilayer distributor |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN106350626B (en) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN112066716A (en) * | 2020-09-15 | 2020-12-11 | 江苏省晶石磁性材料与器件工程技术研究有限公司 | Sintering device and sintering method for ferrite powder |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN206014973U (en) * | 2016-08-31 | 2017-03-15 | 西安交通大学 | A kind of particle dispensing device for blast furnace cinder |
Family Cites Families (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN201458333U (en) * | 2009-07-23 | 2010-05-12 | 宝山钢铁股份有限公司 | Unloading device |
CN202321611U (en) * | 2011-11-26 | 2012-07-11 | 重庆华浩冶炼有限公司 | Material shunt control device |
CN202529557U (en) * | 2012-03-26 | 2012-11-14 | 攀钢集团西昌钢钒有限公司 | Adjustable material flow three-way distributor |
CN202762643U (en) * | 2012-08-07 | 2013-03-06 | 郑州真金耐火材料有限责任公司 | Material distributing device for feed port of vibrating sieve |
CN104876034B (en) * | 2015-05-18 | 2017-04-05 | 南京泽众环保科技有限公司 | Pneumatic cutting agency |
-
2016
- 2016-08-31 CN CN201610789100.6A patent/CN106350626B/en active Active
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN206014973U (en) * | 2016-08-31 | 2017-03-15 | 西安交通大学 | A kind of particle dispensing device for blast furnace cinder |
Also Published As
Publication number | Publication date |
---|---|
CN106350626A (en) | 2017-01-25 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN108396136B (en) | A kind of sintered compound preparation method for material and its distributing method and device | |
CN103993115B (en) | Dry integrated with reduction flash ironmaking equipment and iron smelting method | |
CN207180369U (en) | A kind of sintering circular-cooler distribution device | |
CN103868364A (en) | Furnace type cooling device | |
CN106350626B (en) | A kind of solid particle multilayer distributor | |
CN105112583B (en) | A kind of method for allocating State of Blast Furnace past raising coal combustion rate in injection coal into | |
CN106191345A (en) | A kind of converter melts red slag heat recovering device and exhaust heat recovering method | |
CN104131120B (en) | Improve the Burden distribution method of blast furnace of agglomerate utilising efficiency | |
CN205119745U (en) | Blast furnace lump ore complete set drying device | |
CN206014973U (en) | A kind of particle dispensing device for blast furnace cinder | |
CN207850029U (en) | A kind of pretreatment system of laterite | |
CN106403660B (en) | A kind of particle heat exchanger multilayer distribution and screened simultaneously | |
CN101799240A (en) | Method for using waste heat flue gas from rotary hearth furnace | |
CN205957726U (en) | A distributing device that is used for metallurgical pelletizing ring cold quick -witted | |
CN206014975U (en) | A kind of novel blast-furnace slag heat transmission equipment | |
CN206014974U (en) | A kind of adjustable distributor of slag particles flow | |
CN115164567B (en) | Block ore pretreatment system and method based on angle adjustment of distribution plate | |
CN214276357U (en) | High-temperature combined heat exchange type drying device | |
CN114370757B (en) | Storage bin lump ore pretreatment system and lump ore pretreatment method | |
CN204385257U (en) | The drying of flash metallurgy and prereduction system | |
CN209974847U (en) | Distributing device for vertical cooling device of sinter | |
CN107816898B (en) | Slag heat exchange device and high-temperature waste heat recovery device comprising same | |
CN108571885B (en) | Tangential wind distribution device around sinter shaft furnace cooling | |
CN207918932U (en) | Lead cadmia residual neat recovering system | |
CN106399605B (en) | A kind of adjustable solid particle distributor of ratio |
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 |