CN106350626B - A kind of solid particle multilayer distributor - Google Patents

A kind of solid particle multilayer distributor Download PDF

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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
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CN
China
Prior art keywords
particle
flap
upper spacer
overhead gage
baffle plate
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CN201610789100.6A
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Chinese (zh)
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CN106350626A (en
Inventor
吴东垠
孔伟佳
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Xian Jiaotong University
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Xian Jiaotong University
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Priority to CN201610789100.6A priority Critical patent/CN106350626B/en
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    • CCHEMISTRY; METALLURGY
    • C21METALLURGY OF IRON
    • C21BMANUFACTURE OF IRON OR STEEL
    • C21B3/00General features in the manufacture of pig-iron
    • C21B3/04Recovery of by-products, e.g. slag
    • C21B3/06Treatment of liquid slag
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W30/00Technologies for solid waste management
    • Y02W30/50Reuse, recycling or recovery technologies

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  • 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

A kind of solid particle multilayer distributor
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).
CN201610789100.6A 2016-08-31 2016-08-31 A kind of solid particle multilayer distributor Active CN106350626B (en)

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CN106350626A CN106350626A (en) 2017-01-25
CN106350626B true CN106350626B (en) 2018-10-23

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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)

* Cited by examiner, † Cited by third party
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

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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

Patent Citations (1)

* Cited by examiner, † Cited by third party
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

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