CN106350626A - Solid particle multilayer distribution device - Google Patents
Solid particle multilayer distribution device Download PDFInfo
- Publication number
- CN106350626A CN106350626A CN201610789100.6A CN201610789100A CN106350626A CN 106350626 A CN106350626 A CN 106350626A CN 201610789100 A CN201610789100 A CN 201610789100A CN 106350626 A CN106350626 A CN 106350626A
- Authority
- CN
- China
- Prior art keywords
- flap
- granule
- upper spacer
- partition
- baffle
- 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.)
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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
The invention discloses a solid particle multilayer distribution device which comprises a rotating plate, a rotating shaft, a funnel, an upper partition, a lower partition, an upper baffle, a lower baffle, a shell, an upper outlet and a lower outlet, and is characterized in that the rotating plate intermittently swings around the rotating shaft to form an upper position and a lower position; the upper baffle is located at the front end of the upper partition, and a gap is reserved between the upper baffle and the upper partition; a 'V'-shaped region is formed by the upper baffle and the upper partition; the lower baffle is located at the front end of the lower partition, and a gap is reserved between the lower baffle and the lower partition; a 'V'-shaped region is formed by the lower baffle and the lower partition. Particles enter from the funnel, and fall onto the rotating plate first; the rotating plate is located at the upper position, and the particles slide to the upper partition and are stacked in the 'V'-shaped region formed by the upper baffle and the upper partition; then the particles can continuously pass through the gap between the upper baffle and the upper partition and fall to the upper outlet for discharging; when the rotating plate is located at the lower position, the working process is the same as the above-mentioned process. According to the solid particle multilayer distribution device, distribution of the particles is realized by use of the intermittently swinging rotating plate, and the distributed particles are continuous and uniform; the system is high in working efficiency.
Description
Technical field
The present invention relates to technical field of mechanical equipment is and in particular to a kind of solid particle multilamellar distributor.
Background technology
Steel and iron industry total energy consumption accounts for the 35% of whole process industry total energy consumption, and the temperature that ironmaking processes produce blast furnace slag exists
1450～1650 DEG C, the thermal content about 1.70～1.87gj/t of blast furnace slag, be equivalent to the heating of 0.058～0.06 ton of standard coal
Amount.Slag sensible heat total amount is huge and be important secondary energy sources, reclaim afterheat of slags to Energy-saving of Iron And Steel Industry reduce discharging, improve energy
Source utilization ratio has the economic implications of reality.At present, domestic smelter is mainly entered using water quenching technology for high temperature furnace slag
Row is processed.It is only the 10% of slag total amount of heat through what various Water Quenching techniques reclaimed, remaining heat arrives with moisture discharge
In air, cause the waste of heat and water resource.Additionally, blast furnace slag is also used as the raw material of industry using, there is certain warp
Ji value.The blast furnace slag that ironmaking processes produce needs the process through heat exchange and screening, and said process is usually by multiple
Multiple regions of equipment or an equipment are carried out simultaneously, how to realize the simple and effective distribution of blast furnace slag, thus improve setting
Standby overall work efficiency is an important technical problem.
Content of the invention
For solving above-mentioned problems of the prior art, it is an object of the invention to provide a kind of solid particle multilamellar is divided
It is equipped with and puts, granule continuously and uniformly can be distributed to multilayer insulating panel, so that further utilization is realized to the granule after distribution.
In order to achieve the above object, the technical solution adopted in the present invention is:
A kind of solid particle multilamellar distributor, including flap 1, rotating shaft 2, funnel 3, upper spacer 4, lower clapboard 5, overhead gage
6th, lower baffle plate 7, housing 8, upper outlet 9, lower outlet 10 it is characterised in that: described flap 1 around the shaft 2 intermittent swing formed upper,
Lower two positions, overhead gage 6 is located at the front end of upper spacer 4, and leaves gap and upper spacer 4 between, and the two constitutes " v " type area
Domain；Lower baffle plate 7 is located at the front end of lower clapboard 5, and leaves gap and lower clapboard 5 between, and the two constitutes " v " type region.Granule by
Funnel 3 enters, and falls first on flap 1, if flap 1 is in position, granule landing, to upper spacer 4, is piled up in overhead gage 6
" v " the type region constituting with upper spacer 4, subsequent granule will be sliding continually by the gap between overhead gage 6 and upper spacer 4
Drop down onto upper outlet 9 to discharge.Similarly, if granule is entered fashionable by funnel 3, flap 1 is in lower position, then granule landing is 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 granule will be continually by lower baffle plate 7 and lower clapboard
Gap between 5, landing is to lower outlet 10 discharge.
Described flap 1 is in and is 50 ° with horizontal plane angle during position, and flap 1 is in during lower position and horizontal plane angle
For 65 °.
Described overhead gage 6 is fixed on housing 8, and perpendicular to upper spacer 4, described lower baffle plate 7 is fixed on upper spacer 4, and hangs down
Directly in lower clapboard 5.
The length of described lower clapboard 5 is more than the length of upper spacer 4.
Compared to the prior art, the invention has the advantages that
A kind of solid particle multilamellar distributor that the present invention provides, it is possible to use the flap of intermittent oscillation, realizes granule
Distribution between different layers dividing plate, and the gap between baffle plate and dividing plate so that the granule of every Layer assignment gained continuously and uniformly
It is paved with place dividing plate.Granule needs the regular hour by the gap between baffle plate and dividing plate, during this period of time, intermittent oscillation
Flap again can be to the new granule of each Layer assignment, thus ensure that the continuous-feeding of granule on dividing plate.Present configuration is simple, energy consumption
Low, achieve the distribution of granule using the flap of intermittent oscillation, the granule of distribution gained is continuous, uniformly.Can after distributor
To connect the two-layer heating surface of slag granules heat exchanger, carry out feed with heat exchange so that the structure of heat exchanger is compacter simultaneously,
It is effectively improved the overall work efficiency of place system.
Brief description
Fig. 1 is a kind of front view of present invention solid particle multilamellar distributor.
Fig. 2 is a kind of right view of present invention solid particle multilamellar distributor.
Fig. 3 is a kind of top view of present invention solid particle multilamellar distributor.
Specific embodiment
With reference to the accompanying drawings and detailed description the present invention is described in further detail.
As Fig. 1, shown in Fig. 2 and Fig. 3, a kind of solid particle multilamellar distributor, including flap 1, rotating shaft 2, funnel 3, on
Dividing plate 4, lower clapboard 5, overhead gage 6, lower baffle plate 7, housing 8, upper outlet 9, lower outlet 10.Flap 12 intermittent swing shape around the shaft
Become upper and lower two positions, overhead gage 6 is located at the front end of upper spacer 4, and leaves gap and upper spacer 4 between, the two constitutes " v "
Type region；Lower baffle plate 7 is located at the front end of lower clapboard 5, and leaves gap and lower clapboard 5 between, and the two constitutes " v " type region.?
Grain is entered by funnel 3, falls first on flap 1, if flap 1 is in position, granule landing, to upper spacer 4, is piled up in
Baffle plate 6 and " v " the type region of upper spacer 4 composition, subsequent granule will be continually by the seam between overhead gage 6 and upper spacer 4
Gap, landing is discharged to upper outlet 9；Similarly, if granule is entered fashionable by funnel 3, flap 1 goes to lower position, then granule landing is extremely
Lower clapboard 5, is piled up in " v " the type region that lower baffle plate 7 and lower clapboard 5 are constituted, subsequent granule will continually by lower baffle plate 7 with
Gap between lower clapboard 5, landing is to lower outlet 10 discharge.When flap 1 be located at upper spacer 4 when, granule drop down onto overhead gage 6 with upper
Between dividing plate 4, form a certain amount of accumulation, then to the position of lower clapboard 5, granule drops down onto lower baffle plate 7 and lower clapboard for flap 1 action
Between 5, form a certain amount of accumulation, the intermittent flap 1 swinging returns to the position of upper spacer 4 again, continues distribution new
Granule.Distribute, to the granule of upper spacer 4 and lower clapboard 5, the regular hour is needed by respective gap, thus ensure that upper
At outlet 9 and lower outlet 10, the seriality of granule feed.Granule heat exchanger can be connected after upper outlet 9 and lower outlet 10
Two-layer heating surface, carries out feed with heat exchange so that the structure of heat exchanger is compacter simultaneously.Further, since the obstruction of baffle plate is made
With, granule is also more uniform in the distribution transversely of dividing plate and outlet, after this enters heat exchanger after making granule, can
More sufficiently uniformly carry out heat exchange.
As the preferred embodiment of the present invention, described flap 1 is in and is 50 ° with horizontal plane angle during position, flap 1
It is in and is 65 ° with horizontal plane angle during lower position, larger inclination angle can ensure that granule 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 rotating shaft 2.Flap stays in
During position, it is connected with upper spacer 4, the granule meeting landing now being entered by funnel 3 is to upper spacer 4；Flap 1 stays in lower position
When or during swinging, the granule that entered by funnel 3 can landing to lower clapboard 5.
As the preferred embodiment of the present invention, described overhead gage 6 is fixed on housing 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 described lower clapboard 5 is more than the length of upper spacer 4
Degree, thus lower clapboard 5, in the horizontal direction closer to rotating shaft 2, so can ensure that the landing when flap 1 is in diverse location
Granule can properly enter corresponding dividing plate.
Claims (4)
1. a kind of solid particle multilamellar distributor, including flap (1), rotating shaft (2), funnel (3), upper spacer (4), lower clapboard
(5), overhead gage (6), lower baffle plate (7), housing (8), upper outlet (9), lower outlet (10) it is characterised in that: described flap (1) around
The intermittent swing of rotating shaft (2) forms upper and lower two positions, and overhead gage (6) is located at the front end of upper spacer (4), and with upper spacer (4)
Between leave gap, the two constitute " v " type region；Lower baffle plate (7) is located at the front end of lower clapboard (5), and and lower clapboard (5) between
Leave gap, the two constitutes " v " type region.Granule is entered by funnel (3), falls first on flap (1), if flap (1) is in
Upper position, then granule landing is to upper spacer (4), is piled up in " v " the type region that overhead gage (6) and upper spacer (4) are constituted, subsequent
Grain will be continually by the gap between overhead gage (6) and upper spacer (4), and landing to upper outlet (9) is discharged；Similarly, if
Granule is entered fashionable by funnel (3), and flap (1) is in lower position, then granule landing is to lower clapboard (5), be piled up in lower baffle plate (7) and
" v " the type region that lower clapboard (5) is constituted, subsequent granule will be continually by the seam between lower baffle plate (7) and lower clapboard (5)
Gap, landing to lower outlet (10) is discharged.
2. a kind of solid particle multilamellar distributor according to claim 1 it is characterised in that: described flap (1) is in
It is 50 ° with horizontal plane angle during upper position, flap (1) is in and is 65 ° with horizontal plane angle during lower position.
3. a kind of solid particle multilamellar distributor according to claim 1 it is characterised in that: described overhead gage (6) is solid
It is scheduled on housing (8), and perpendicular to upper spacer (4), described lower baffle plate (7) is fixed on upper spacer (4), and perpendicular to lower clapboard (5).
4. a kind of solid particle multilamellar distributor according to claim 1 it is characterised in that: described 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 true CN106350626A (en) | 2017-01-25 |
| CN106350626B 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) |
Cited By (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 (6)
| 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 |
| CN104876034A (en) * | 2015-05-18 | 2015-09-02 | 杨祝红 | Pneumatic discharging mechanism |
| CN206014973U (en) * | 2016-08-31 | 2017-03-15 | 西安交通大学 | A kind of particle dispensing device for blast furnace cinder |
-
2016
- 2016-08-31 CN CN201610789100.6A patent/CN106350626B/en active Active
Patent Citations (6)
| 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 |
| CN104876034A (en) * | 2015-05-18 | 2015-09-02 | 杨祝红 | Pneumatic discharging mechanism |
| CN206014973U (en) * | 2016-08-31 | 2017-03-15 | 西安交通大学 | A kind of particle dispensing device for blast furnace cinder |
Cited By (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 |
Also Published As
| Publication number | Publication date |
|---|---|
| CN106350626B (en) | 2018-10-23 |
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