CN204866067U - Fluid unit of adjustable crushing particle diameter - Google Patents
Fluid unit of adjustable crushing particle diameter Download PDFInfo
- Publication number
- CN204866067U CN204866067U CN201520462522.3U CN201520462522U CN204866067U CN 204866067 U CN204866067 U CN 204866067U CN 201520462522 U CN201520462522 U CN 201520462522U CN 204866067 U CN204866067 U CN 204866067U
- Authority
- CN
- China
- Prior art keywords
- particle diameter
- discharging opening
- crushing bin
- fluid bed
- powder particle
- 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.)
- Expired - Fee Related
Links
- 239000002245 particles Substances 0.000 title claims abstract description 30
- 239000000843 powders Substances 0.000 claims abstract description 32
- 239000007789 gases Substances 0.000 claims abstract description 11
- 239000003570 air Substances 0.000 claims abstract description 6
- 239000000047 products Substances 0.000 claims abstract description 4
- 238000007599 discharging Methods 0.000 claims description 30
- 238000010298 pulverizing process Methods 0.000 claims description 14
- 241001438449 Silo Species 0.000 claims description 13
- 235000012054 meals Nutrition 0.000 claims description 8
- 239000000463 materials Substances 0.000 abstract description 14
- 238000005243 fluidization Methods 0.000 abstract 1
- 238000000034 methods Methods 0.000 abstract 1
- 238000000926 separation method Methods 0.000 abstract 1
- 239000010410 layers Substances 0.000 description 6
- 230000000694 effects Effects 0.000 description 3
- 230000001105 regulatory Effects 0.000 description 3
- 230000005540 biological transmission Effects 0.000 description 2
- 239000007795 chemical reaction products Substances 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 238000005516 engineering processes Methods 0.000 description 1
- 238000003754 machining Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
Abstract
The utility model discloses a fluid unit of adjustable crushing particle diameter, including the feed inlet, once smash storehouse, storage storehouse, fluidized bed. Wherein save the inside discharge gate control panel that is equipped with in storehouse, steerable material ejection of compact operation, to the strict material of particle diameter, the utility model designs a carry out the advanced treatment process from once smashing the reentrant fluidized bed of discharge gate, gas pipeline who wherein is equipped with and air compressor intercommunication import the fluidization bed with high -pressure gas, carry out the repulverize to the material, and the farine after smashing gets into cyclone to press the particle diameter separation, final finished product is discharged from the separator lower extreme. This equipment main advantages: (1 )Can be based on and smash particle diameter regulation and control mesh size, control the powder diameter in a flexible way, (2 )The discharge gate is equipped with the control panel, and is convenient according to smashing needs selection route, (3 ) cyclone can separate the crushing material of collecting different particle diameters, and degree of automation is high, (4 )This equipment is equipped with the acoustical panel can noise abatement.
Description
Technical field
The utility model relates to a kind of fluid unit of controllable both thick and thin, belongs to materiel machining field.
Background technology
Powder particle diameter is adjustable, and fluid bed is most widely used general production equipment in workers and peasants' animal husbandry, pulverizer can be divided into boulder crusher, pulverizer, micronizer according to by the size of comminuting matter.Pulverizer is commonly used in life, but also exists that energy consumption is comparatively large, comminuting matter granularity is uneven and the problem such as output is not high.
Summary of the invention
Technical problem to be solved in the utility model is to provide a kind of pulverizing evenly, the adjustable fluid bed of powder particle diameter of auto-control both thick and thin type.
A fluid unit for adjustable powder particle diameter, the charging aperture 1 being positioned at top with on the left of it a crushing bin 2 be communicated with, described crushing bin 2 inside is provided with sieve aperture net 2-4; The bottom of a crushing bin 2 is provided with storage silo 13, is provided with discharging opening control panel 13-2 in storage silo 13, is provided with common discharging opening 3-1 on the right side of the bottom of described discharging opening control panel 13-2, and the lower left side of discharging opening control panel 13-2 is provided with once pulverizes discharging opening 3-2; Described left side of once pulverizing discharging opening 3-2 is provided with fluid bed 4, and the bottom of described fluid bed 4 is provided with gas pipeline 5, and described gas pipeline 5 is communicated with air compressor 12; The top of described fluid bed 4 is provided with conveyance conduit 7, and conveyance conduit 7 is communicated with the cyclone separator 8 on the left of it; The bottom of described fluid bed 4 is provided with meal discharging opening 6; Described cyclone separator 8 is communicated with the air-introduced machine pipeline 10 on the left of it, and air-introduced machine pipeline 10 is communicated with the air-introduced machine 11 on the left of it; The bottom of described cyclone separator 8 is provided with product outlet 9.
Further, the inside of a crushing bin 2 is provided with Disintegrating knife 2-3, described Disintegrating knife 2-3 arranged in dislocation; The inwall of a described crushing bin 2 is provided with reverse blade 2-2; The outside of a crushing bin 2 is provided with acoustical panel 2-1, sieve aperture net 2-4.
Further, discharging opening control panel 13-2 is provided with in storage silo 13.
Further, described cyclone separator 8 is connected by conveyance conduit 7 with fluid bed 4.
Further, this apparatus casing 14 is provided with acoustical panel 2-1.
beneficial effect
1, the Disintegrating knife 2-3 arranged in dislocation in a crushing bin 2, and have certain inclination angle, the inwall of crushing bin 2 is provided with reverse blade 2-2, substantially increases crushing effect; Crushing bin 2 outside is provided with acoustical panel 2-1, can reduce noise pollution; Crushing bin 2 bottom is provided with sieve aperture net 2-4, requires regulation and control screen number, can control powder footpath flexibly according to powder particle diameter.
2, be provided with a discharging opening control panel 13-2 in storage silo 13, can material outlet be regulated and controled, conveniently need selecting paths according to pulverizing.
3, fluid bed 4 has certain angle of inclination, and material can be advanced in fluid bed 4 does not certainly need transmission equipment.
4, this equipment is provided with cyclone separator 8, and the comminuting matter epigranular of separated and collected, automaticity is high.
5, this equipment is provided with acoustical panel, can reduce noise.
Accompanying drawing explanation
Fig. 1 is the fluid unit outside drawing of a kind of adjustable powder particle diameter described in the utility model.
Fig. 2 is the crushing bin structure chart of the fluid unit of a kind of adjustable powder particle diameter described in the utility model.
Fig. 3 is the storage silo structure chart of the fluid unit of a kind of adjustable powder particle diameter described in the utility model
Fig. 4 is the fluid unit structure chart of a kind of adjustable powder particle diameter described in the utility model.
Fig. 5 is the fluid unit outside drawing of a kind of adjustable powder particle diameter described in the utility model.
Fig. 6 is the fluid unit side elevation structure chart of a kind of adjustable powder particle diameter described in the utility model.
Fig. 7 is the axle construction figure such as the fluid unit of a kind of adjustable powder particle diameter described in the utility model.
Fig. 8 is the positive facade structure chart of fluid unit of a kind of adjustable powder particle diameter described in the utility model.
In above figure, 1 is charging aperture, 2 is a crushing bin, 2-1 is acoustical panel, 2-2 is reverse blade, 2-3 is Disintegrating knife, 2-4 is sieve aperture net, 3 is discharging opening, 3-1 is common discharging opening, 3-2 is for once to pulverize discharging opening, 4 is fluid bed, 4-1 is fluid bed housing, 4-2 is fluid bed internal layer, 5 is gas pipeline, 5-1 is main pipeline, 5-2 is nozzle, 6 is meal discharging opening, 7 is conveyance conduit, 7-1 is supervisor, 7-2 is arm, 8 is cyclone separator, 9 is product outlet, 10 is air-introduced machine pipeline, 11 is air-introduced machine, 12 is air compressor, 13 is storage silo, 13-1 is housing, 13-2 is discharging opening control panel, 14 is housing.
Detailed description of the invention
Be further described below in conjunction with the fluid unit of accompanying drawing to a kind of adjustable powder particle diameter that the utility model provides.
As shown in Figure 1, for the fluid unit outside drawing of a kind of adjustable powder particle diameter that the utility model provides, material enters a crushing bin 2 from charging aperture 1, the sieve aperture net 2-4 that material after pulverizing is provided with bottom a crushing bin 2 enters storage silo 13, be provided with a discharging opening control panel 13-2 in storage silo 13, can material outlet be regulated and controled.According to pulverizing requirement, Ordinary pulverization is directly discharged from common discharging opening 3-1, and the powder particle diameter of Ordinary pulverization can by changing sieve aperture net 2-4 regulation and control; Strict fine powder is required for powder particle diameter, then enters fluid bed 4 from once pulverizing discharging opening 3-2.Fluid bed 4 is provided with gas pipeline 5, gases at high pressure are conveyed in fluid bed 4 by gas pipeline 5 by air compressor 12, the material once pulverized is pulverized again, fine powder after pulverizing enters cyclone separator 8 from conveyance conduit 7, meal then continues to pulverize in fluid bed 4, also can be discharged by the meal discharging opening 6 bottom fluid bed 4.Material after fluid bed 4 is pulverized enters cyclone separator 8, and cyclone separator 8 is connected by air-introduced machine pipeline 10 with air-introduced machine 11, enables fine powder enter cyclone separator 8.Cyclone separator 8 is pressed particle diameter and is separated fine powder, and final finished is discharged from separator lower end product outlet 9.
As shown in Figure 2, be the crushing bin structure chart that the utility model provides, one time crushing bin 2 is provided with Disintegrating knife 2-3, and Disintegrating knife 2-3 has certain inclination angle; The inwall of crushing bin 2 is provided with reverse blade 2-2, improves crushing effect; Crushing bin 2 outside is provided with noise reduction layer 2-1, can reduce noise; Crushing bin 2 bottom is provided with sieve aperture net 2-4, requires regulation and control screen number, can control powder footpath flexibly according to powder particle diameter.
As shown in Figure 3, be the storage silo structure chart that the utility model provides, be provided with a discharging opening control panel 13-2 in storage silo 13, can material outlet be regulated and controled, convenient according to pulverizing needs selection pulverizing path.
As shown in Figure 4, be the fluidized-bed structure figure that the utility model provides, fluid bed 4 is made up of housing 4-1 and internal layer 4-2, internal layer 4-2 has certain angle of inclination, once pulverize discharging opening 3-2 in internal layer 4-2, material can certainly be advanced in fluid bed 4 after discharging opening 3-2 discharges, and does not need transfer equipment; Fluid bed 4 is provided with gas pipeline 5, the pressure-air that compressor 12 produces is transported in fluid bed internal layer 4-2 by main pipeline 5-1, spurt in fluid bed 4 by nozzle 5-2, the material utilizing storeroom mutually to collide once pulverizing is pulverized again, fine powder after pulverizing is washed and is entered cyclone separator 8 by transmission mouth 7, meal then continues to pulverize in fluid bed 4, and meal also can be discharged from the meal discharging opening 6 of bottom.Fine powder after fluid bed 4 is pulverized enters cyclone separator 8 separated and collected.
Claims (5)
1. a fluid unit for adjustable powder particle diameter, is characterized in that, the charging aperture (1) being positioned at top with on the left of it a crushing bin (2) be communicated with, described crushing bin (2) inside is provided with sieve aperture net (2-4); The bottom of a crushing bin (2) is provided with storage silo (13), discharging opening control panel (13-2) is provided with in storage silo (13), be provided with common discharging opening (3-1) on the right side of the bottom of described discharging opening control panel (13-2), the lower left side of discharging opening control panel (13-2) is provided with once pulverizes discharging opening (3-2); Described left side of once pulverizing discharging opening (3-2) is provided with fluid bed (4), and the bottom of described fluid bed (4) is provided with gas pipeline (5), and described gas pipeline (5) is communicated with air compressor (12); The top of described fluid bed (4) is provided with conveyance conduit (7), and conveyance conduit (7) is communicated with the cyclone separator (8) on the left of it; The bottom of described fluid bed (4) is provided with meal discharging opening (6); Described cyclone separator (8) is communicated with the air-introduced machine pipeline (10) on the left of it, and air-introduced machine pipeline (10) is communicated with the air-introduced machine (11) on the left of it; The bottom of described cyclone separator (8) is provided with product outlet (9).
2. the fluid unit of a kind of adjustable powder particle diameter according to claim 1, is characterized in that, the inside of a crushing bin (2) is provided with Disintegrating knife (2-3), described Disintegrating knife (2-3) arranged in dislocation; The inwall of a described crushing bin (2) is provided with reverse blade (2-2); The outside of a crushing bin (2) is provided with acoustical panel (2-1), sieve aperture net (2-4).
3. the fluid unit of a kind of adjustable powder particle diameter according to claim 1, is characterized in that, is provided with discharging opening control panel (13-2) in storage silo (13).
4. the fluid unit of a kind of adjustable powder particle diameter according to claim 1, is characterized in that, described cyclone separator (8) is connected by conveyance conduit (7) with fluid bed (4).
5. the fluid unit of a kind of adjustable powder particle diameter according to claim 1, is characterized in that, this apparatus casing (14) is provided with acoustical panel (2-1).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520462522.3U CN204866067U (en) | 2015-07-01 | 2015-07-01 | Fluid unit of adjustable crushing particle diameter |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520462522.3U CN204866067U (en) | 2015-07-01 | 2015-07-01 | Fluid unit of adjustable crushing particle diameter |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204866067U true CN204866067U (en) | 2015-12-16 |
Family
ID=54810501
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520462522.3U Expired - Fee Related CN204866067U (en) | 2015-07-01 | 2015-07-01 | Fluid unit of adjustable crushing particle diameter |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204866067U (en) |
-
2015
- 2015-07-01 CN CN201520462522.3U patent/CN204866067U/en not_active Expired - Fee Related
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20151216 Termination date: 20160701 |