CN205288649U - A crushing apparatus for sludge drying - Google Patents

A crushing apparatus for sludge drying Download PDF

Info

Publication number
CN205288649U
CN205288649U CN201620015619.4U CN201620015619U CN205288649U CN 205288649 U CN205288649 U CN 205288649U CN 201620015619 U CN201620015619 U CN 201620015619U CN 205288649 U CN205288649 U CN 205288649U
Authority
CN
China
Prior art keywords
fluid bed
discharging opening
sludge drying
crushing bin
air
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
Application number
CN201620015619.4U
Other languages
Chinese (zh)
Inventor
肖扬
梁峙
梁骁
杨瑞卿
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Xuzhou University of Technology
Original Assignee
Xuzhou University of Technology
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Xuzhou University of Technology filed Critical Xuzhou University of Technology
Priority to CN201620015619.4U priority Critical patent/CN205288649U/en
Application granted granted Critical
Publication of CN205288649U publication Critical patent/CN205288649U/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Landscapes

  • Drying Of Solid Materials (AREA)

Abstract

The utility model provides a sieve mesh net gets into saves the storehouse that a crushing apparatus for sludge drying, material get into from the feed inlet and once smash the storehouse, and the material after smashing is equipped with from once smashing the storehouse bottom. The storage is equipped with a discharge gate control panel in the storehouse, can control the material export, the ordinary crushing ordinary discharge gate discharge of directly following, to the strict material of farine particle diameter, get into fluidized bed rubbing crusher from once smashing the discharge gate. Be equipped with gas pipeline in the fluidized bed, air compressor passes through during gas pipeline carries the fluidized bed with high -pressure gas, repulverizes kibbling material once, and the farine after smashing gets into cyclone from pipeline, and cyclone press particle diameter separation farine, final finished product from separator lower extreme product outlet discharge.

Description

A kind of disintegrating apparatus for sludge drying
Technical field
The utility model belongs to materiel machining field, is specifically related to a kind of disintegrating apparatus for sludge drying.
Background technology
Pulverizer is most widely used general production equipment in workers and peasants' animal husbandry, according to pulverizer being divided into boulder crusher, pulverizer, micronizer by the size of comminuting matter. Pulverizer is commonly used in life, but exists that energy consumption is large, comminuting matter granularity is inhomogeneous and the problem such as output is not high.
Summary of the invention
In order to solve the problems of the technologies described above, the utility model provides a kind of disintegrating apparatus for sludge drying, comprises charging aperture 1, a crushing bin 2, discharging bin 3, fluid bed 4, gas pipeline 5, meal discharging opening 6, conveyance conduit 7, cyclone separator 8, product outlet 9, air-introduced machine pipeline 10, air-introduced machine 11, air compressor 12, storage silo 13, housing 14, controller 15, superposed charging aperture 1, its underpart is provided with crushing bin 2 one time, the bottom of a crushing bin 2 is provided with storage silo 13, one side of storage silo 13 is provided with discharging bin 3, storage silo 13 opposite sides are provided with fluid bed 4, fluid bed 4 bottoms are provided with gas pipeline 5, meal discharging opening 6, air compressor 12, fluid bed 4 tops are provided with conveyance conduit 7, conveyance conduit 7 successively with cyclone separator 8, air-introduced machine pipeline 10, air-introduced machine 11 connects, cyclone separator 8 bottoms are provided with product outlet 9, controller 15 is positioned at air-introduced machine 11 1 sides, controller 15 is connected by wire with air-introduced machine 11, controller 15 is connected by wire with air compressor 12.
Further, one time crushing bin 2 is cylindrical structure, and its diameter is 50cm~150cm, and one time crushing bin 2 comprises acoustical panel 2-1, oppositely blade 2-2, Disintegrating knife 2-3, sieve aperture net 2-4; The internal axis of a crushing bin 2 is provided with Disintegrating knife 2-3, and Disintegrating knife 2-3 arranged in dislocation is in rotating shaft, and the quantity of Disintegrating knife 2-3 is 5~20, and Disintegrating knife 2-3 is with central shaft symmetric mode layout, and Disintegrating knife 2-3 also has certain inclination angle; The inwall of a crushing bin 2 is provided with reverse blade 2-2, and oppositely the quantity of blade 2-2 is 5~20, and oppositely blade 2-2 is with central shaft symmetric configuration; One time crushing bin 2 bottoms are provided with sieve aperture net 2-4, and sieve aperture net 2-4 is communicated with the storage silo 13 that is positioned at bottom.
Further, storage silo 13 comprises: blanking channel 13-1, discharging opening control panel 13-2; Described discharging opening control panel 13-2 is positioned at blanking channel 13-1 bottom, and discharging opening control panel 13-2 is incline structure, and discharging opening control panel 13-2 can realize blanking channel 13-1 and close or open.
Further, fluid bed 4 comprises: fluid bed housing 4-1, fluid bed internal layer 4-2; Fluid bed housing 4-1 is cylindrical structure, and its diameter is 50cm~150cm, and fluid bed housing 4-1 is provided with certain angle of inclination along cylinder axis direction, and its inclination angle is 5 °~10 °, and fluid bed internal layer 4-2 and conveyance conduit 7 connect.
Further, conveyance conduit 7 comprises: supervisor 7-1, arm 7-2; Supervisor 7-1 one end is communicated with cyclone separator 8, and the supervisor 7-1 other end is communicated with arm 7-2; 2~8 of the quantity of described arm 7-2, the arm 7-2 other end is communicated with fluid bed internal layer 4-2.
Further, gas pipeline 5 comprises: main pipeline 5-1, nozzle 5-2; Main pipeline 5-1 is a horizontal tube, and main pipeline 5-1 one end is communicated with air compressor 12, and the main pipeline 5-1 other end is communicated with nozzle 5-2,2~8 of the quantity of nozzle 5-2, and nozzle 5-2 is communicated with fluid bed internal layer 4-2 through fluid bed housing 4-1.
Further, discharging bin 3 comprises common discharging opening 3-1, once pulverizes discharging opening 3-2; Blanking channel 13-1 mono-side lower part is provided with common discharging opening 3-1, and blanking channel 13-1 opposite side bottom is provided with once pulverizes discharging opening 3-2, and three connects mutually, and three's passage is subject to the control of discharging opening control panel 13-2.
The disclosed a kind of disintegrating apparatus for sludge drying of the utility model, its advantage is.
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 to be provided with reverse blade 2-2, fully improve crushing effect; Crushing bin 2 outsides are provided with acoustical panel 2-1, can reduce noise pollution; Crushing bin 2 bottoms are provided with sieve aperture net 2-4, require regulation and control screen number according to powder particle diameter, can control flexibly powder footpath.
2. in storage silo 13, be provided with a discharging opening control panel 13-2, can regulate and control material outlet, conveniently need selecting paths according to pulverizing.
3. fluid bed 4 has certain angle of inclination, and material can be advanced into certainly does not need transmission equipment in fluid bed 4.
4. this equipment is provided with cyclone separator 8, the comminuting matter epigranular of separated and collected, and automaticity is high.
5. this equipment is provided with acoustical panel, can reduce noise.
Brief description of the drawings
Fig. 1 is a kind of disintegrating apparatus outside drawing for sludge drying described in the utility model.
Fig. 2 is crushing bin structure chart described in the utility model.
Fig. 3 is storage silo structure chart described in the utility model.
Fig. 4 is fluidized-bed structure figure described in the utility model.
In above Fig. 1~Fig. 4, charging aperture 1, a crushing bin 2, acoustical panel 2-1, oppositely blade 2-2, Disintegrating knife 2-3, sieve aperture net 2-4, discharging bin 3, common discharging opening 3-1, once pulverize discharging opening 3-2, fluid bed 4, fluid bed housing 4-1, fluid bed internal layer 4-2, gas pipeline 5, main pipeline 5-1, nozzle 5-2, meal discharging opening 6, conveyance conduit 7, supervisor 7-1, arm 7-2, cyclone separator 8, product outlet 9, air-introduced machine pipeline 10, air-introduced machine 11, air compressor 12, storage silo 13, blanking channel 13-1, discharging opening control panel 13-2, housing 14, controller 15.
Detailed description of the invention
A kind of disintegrating apparatus for sludge drying the utility model being provided below in conjunction with accompanying drawing is further described.
As shown in Figure 1, be a kind of disintegrating apparatus outside drawing for sludge drying described in the utility model. In figure, find out, material enters crushing bin 2 one time from charging aperture 1, and the sieve aperture net 2-4 that the material after pulverizing is provided with from crushing bin 2 bottom enters storage silo 13, is provided with a discharging opening control panel 13-2 in storage silo 13, can regulate and control material outlet. According to pulverizing requirement, Ordinary pulverization is directly discharged from common discharging opening 3-1, and the powder particle diameter of Ordinary pulverization can be by changing sieve aperture net 2-4 regulation and control; Require strict fine powder for powder particle diameter, enter fluid bed 4 from once pulverizing discharging opening 3-2. Fluid bed 4 is provided with gas pipeline 5, air compressor 12 is conveyed into gases at high pressure in fluid bed 4 by gas pipeline 5, the material of once pulverizing is pulverized again, fine powder after pulverizing enters cyclone separator 8 from conveyance conduit 7, meal continues to pulverize in fluid bed 4, also can discharge by the meal discharging opening 6 of fluid bed 4 bottoms. 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, makes fine powder can 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 crushing bin 2 structure charts that the utility model provides. In figure, find out, the Disintegrating knife 2-3 arranged in dislocation in a crushing bin 2, on the turning cylinder being connected with motor, and has certain inclination angle; The inwall of crushing bin 2 is provided with reverse blade 2-2, has improved crushing effect; Crushing bin 2 outsides are provided with noise reduction layer 2-1, can reduce noise; Crushing bin 2 bottoms are provided with sieve aperture net 2-4, require regulation and control screen number according to powder particle diameter, can control flexibly powder footpath.
As shown in Figure 3, be storage silo 13 structure charts that the utility model provides. In figure, find out, in storage silo 13, be provided with a discharging opening control panel 13-2, can regulate and control material outlet, conveniently need to select to pulverize path according to pulverizing.
As shown in Figure 4, be fluid bed 4 structure charts that the utility model provides. In figure, find out, fluid bed 4 is made up of housing 4-1 and internal layer 4-2, and internal layer 4-2 has certain angle of inclination, once pulverizes discharging opening 3-2 in internal layer 4-2, and 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 main pipeline 5-1 produces compressor 12 is transported in fluid bed internal layer 4-2, spurt in fluid bed 4 by nozzle 5-2, the material that utilizes storeroom mutually to collide once pulverizing is pulverized again, fine powder after pulverizing is washed by transmission mouth 7 and is entered cyclone separator 8, meal 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 (7)

1. for a disintegrating apparatus for sludge drying, comprise charging aperture (1), a crushing bin (2), discharging bin (3), fluid bed (4), gas pipeline (5), meal discharging opening (6), conveyance conduit (7), cyclone separator (8), product outlet (9), air-introduced machine pipeline (10), air-introduced machine (11), air compressor (12), storage silo (13), housing (14), controller (15), it is characterized in that, superposed charging aperture (1), its underpart is provided with a crushing bin (2), the bottom of a crushing bin (2) is provided with storage silo (13), one side of storage silo (13) is provided with discharging bin (3), storage silo (13) opposite side is provided with fluid bed (4), fluid bed (4) bottom is provided with gas pipeline (5), meal discharging opening (6), air compressor (12), fluid bed (4) top is provided with conveyance conduit (7), conveyance conduit (7) successively with cyclone separator (8), air-introduced machine pipeline (10), air-introduced machine (11) connects, cyclone separator (8) bottom is provided with product outlet (9), controller (15) is positioned at air-introduced machine (11) one sides, controller (15) is connected by wire with air-introduced machine (11), controller (15) is connected by wire with air compressor (12).
2. a kind of disintegrating apparatus for sludge drying according to claim 1, it is characterized in that, a crushing bin (2) is cylindrical structure, its diameter is 50cm~150cm, a crushing bin (2) comprises acoustical panel (2-1), oppositely blade (2-2), Disintegrating knife (2-3), sieve aperture net (2-4); The internal axis of a crushing bin (2) is provided with Disintegrating knife (2-3), Disintegrating knife (2-3) arranged in dislocation is in rotating shaft, the quantity of Disintegrating knife (2-3) is 5~20, and Disintegrating knife (2-3) is with central shaft symmetric mode layout, and Disintegrating knife (2-3) also has certain inclination angle; The inwall of a crushing bin (2) is provided with reverse blade (2-2), and oppositely the quantity of blade (2-2) is 5~20, and oppositely blade (2-2) is with central shaft symmetric configuration; A crushing bin (2) bottom is provided with sieve aperture net (2-4), and sieve aperture net (2-4) is communicated with the storage silo (13) that is positioned at bottom.
3. a kind of disintegrating apparatus for sludge drying according to claim 1, is characterized in that, storage silo (13) comprising: blanking channel (13-1), discharging opening control panel (13-2); Described discharging opening control panel (13-2) is positioned at blanking channel (13-1) bottom, and discharging opening control panel (13-2) is incline structure, and discharging opening control panel (13-2) can be realized blanking channel (13-1) and close or open.
4. a kind of disintegrating apparatus for sludge drying according to claim 1, is characterized in that, fluid bed (4) comprising: fluid bed housing (4-1), fluid bed internal layer (4-2); Fluid bed housing (4-1) is cylindrical structure, and its diameter is 50cm~150cm, and fluid bed housing (4-1) is provided with certain angle of inclination along cylinder axis direction, and its inclination angle is 5 °~10 °, and fluid bed internal layer (4-2) connects with conveyance conduit (7).
5. a kind of disintegrating apparatus for sludge drying according to claim 1, is characterized in that, conveyance conduit (7) comprising: supervisor (7-1), arm (7-2); Supervisor (7-1) one end is communicated with cyclone separator (8), and supervisor's (7-1) other end is communicated with arm (7-2); 2~8 of the quantity of described arm (7-2), arm (7-2) other end is communicated with fluid bed internal layer (4-2).
6. a kind of disintegrating apparatus for sludge drying according to claim 1, is characterized in that, gas pipeline (5) comprising: main pipeline (5-1), nozzle (5-2); Main pipeline (5-1) is a horizontal tube, main pipeline (5-1) one end is communicated with air compressor (12), main pipeline (5-1) other end is communicated with nozzle (5-2), 2~8 of the quantity of nozzle (5-2), nozzle (5-2) is communicated with fluid bed internal layer (4-2) through fluid bed housing (4-1).
7. a kind of disintegrating apparatus for sludge drying according to claim 1, is characterized in that, discharging bin (3) comprises common discharging opening (3-1), once pulverizes discharging opening (3-2); Blanking channel (13-1) side lower part is provided with common discharging opening (3-1), and blanking channel (13-1) opposite side bottom is provided with once pulverizes discharging opening (3-2), and three connects mutually, and three's passage is subject to the control of discharging opening control panel (13-2).
CN201620015619.4U 2016-01-10 2016-01-10 A crushing apparatus for sludge drying Expired - Fee Related CN205288649U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201620015619.4U CN205288649U (en) 2016-01-10 2016-01-10 A crushing apparatus for sludge drying

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201620015619.4U CN205288649U (en) 2016-01-10 2016-01-10 A crushing apparatus for sludge drying

Publications (1)

Publication Number Publication Date
CN205288649U true CN205288649U (en) 2016-06-08

Family

ID=56485398

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201620015619.4U Expired - Fee Related CN205288649U (en) 2016-01-10 2016-01-10 A crushing apparatus for sludge drying

Country Status (1)

Country Link
CN (1) CN205288649U (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110624932A (en) * 2019-09-11 2019-12-31 上海海顾新材料科技有限公司 River, lake and reservoir bottom mud building material treatment system and treatment method
CN112499931A (en) * 2020-12-09 2021-03-16 王鹏程 Environment-friendly efficient centrifugal water treatment sludge drying device
WO2024077715A1 (en) * 2022-10-09 2024-04-18 青岛理工大学 Ultrafine grinding system for rhizome traditional chinese medicine

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110624932A (en) * 2019-09-11 2019-12-31 上海海顾新材料科技有限公司 River, lake and reservoir bottom mud building material treatment system and treatment method
CN112499931A (en) * 2020-12-09 2021-03-16 王鹏程 Environment-friendly efficient centrifugal water treatment sludge drying device
WO2024077715A1 (en) * 2022-10-09 2024-04-18 青岛理工大学 Ultrafine grinding system for rhizome traditional chinese medicine

Similar Documents

Publication Publication Date Title
CN103263955B (en) Production equipment for extracting cotton protein from cottonseed meal
CN203803615U (en) Horizontal multistage pulverizer
CN203355840U (en) Production line for manufacturing sand through ball-milling
CN205288649U (en) A crushing apparatus for sludge drying
CN108325715B (en) Classified air-assisted cooling system for crushing materials for feed production
CN204996527U (en) Disc type fluid energy mill
CN202447180U (en) Material smashing device
CN104923330A (en) Whole wheat flour processing device and process
CN204866067U (en) Fluid unit of adjustable crushing particle diameter
CN205868518U (en) Broken grading plant of large granule
JPH01194950A (en) Manufacture of granule and its apparatus
CN204866068U (en) Adjustable rubbing crusher equipment
CN105772197B (en) A kind of ultra tiny roller mill equipment production flow
CN202823560U (en) Complete production line for crushing nano-calcium
CN203281380U (en) Production device used for extracting cotton proteins from cottonseed meal
CN203833244U (en) Separator of pneumatic ash conveying system
CN206716076U (en) Glutinous rice flour bulky grain ultramicro grinding circulation and stress device
CN206996802U (en) A kind of mechanical classification mill prevents from accumulating continuous feeding device
CN213914268U (en) Inner and outer compound grading flour mill
CN206104080U (en) A automatic micronization grading system for fodder preparation
CN206043338U (en) A kind of corn deep processing device
WO2015042003A1 (en) System for shredding and grinding biomass
CN204769034U (en) Food rubbing crusher with self grading function
CN103706452B (en) A kind of nanometer calcium pulverizes complete production line
CN209205474U (en) A kind of pulverizer with the dedicated storehouse of corn

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: 20160608

Termination date: 20170110