CN211660203U - Material sphericization production system - Google Patents

Material sphericization production system Download PDF

Info

Publication number
CN211660203U
CN211660203U CN201921788011.5U CN201921788011U CN211660203U CN 211660203 U CN211660203 U CN 211660203U CN 201921788011 U CN201921788011 U CN 201921788011U CN 211660203 U CN211660203 U CN 211660203U
Authority
CN
China
Prior art keywords
collecting
dust
shaping
collecting tower
tower
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
Application number
CN201921788011.5U
Other languages
Chinese (zh)
Inventor
王京旭
信永睦
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.)
Suzhou Xi Ran Industrial Equipment Co ltd
Original Assignee
Suzhou Xi Ran Industrial Equipment Co ltd
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 Suzhou Xi Ran Industrial Equipment Co ltd filed Critical Suzhou Xi Ran Industrial Equipment Co ltd
Priority to CN201921788011.5U priority Critical patent/CN211660203U/en
Application granted granted Critical
Publication of CN211660203U publication Critical patent/CN211660203U/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Landscapes

  • Combined Means For Separation Of Solids (AREA)

Abstract

The utility model relates to a material sphericization production system, which comprises a sphericization shaping machine, a first collecting tower, a second collecting tower, a fan and a main air outlet; the top of the first collecting tower is provided with a cyclone separator, and the bottom of the first collecting tower is provided with a coarse powder collecting port; the upper part in the second collecting tower is provided with a bag-type dust collector, and the bottom is provided with a fine powder collecting port. The system realizes continuous operation of material sphericization shaping, different particle size classification, collection and dust removal, and has high production efficiency; meanwhile, the air flow discharged from the air outlet contains less dust, has little influence on the environment, has the advantage of environmental protection, and is simple in system structure, low in cost and suitable for large-scale popularization. Meanwhile, the system is provided with the spiral dust collector with the dust collecting disc and the cyclone hole, so that the dust-containing air flow can generate cyclone and accelerate, and the dust in the air flow can be favorably thrown out and absorbed, thereby being favorable for separating particulate matters from the air flow and improving the air flow purification effect and efficiency.

Description

Material sphericization production system
Technical Field
The utility model relates to a material grinding plastic field especially relates to a material sphericization production system.
Background
In industrial production, materials are ground and shaped to form spheres with large specific surface area, and the produced materials with different particle sizes are classified and used differently. The conventional equipment at present can not continuously shape, classify and collect materials; in addition, a large amount of dust is often generated in the production process, and adverse effects are caused to the environment; consequently it is to provide a material sphericization production system that can carry out plastic, classification and collection to the material in succession and just influence little to the environment the utility model aims to solve the problem.
Disclosure of Invention
The utility model overcomes prior art's is not enough, provides one kind can carry out plastic, categorised and collection and to the material sphericization production system that the environmental impact is little in succession.
In order to achieve the above purpose, the utility model adopts the technical scheme that: the utility model provides a sphericization of material production system which characterized in that: comprises a sphericizing shaper, a first collecting tower, a second collecting tower, a fan and a main air outlet;
the spheroidizing shaping machine is used for crushing and shaping the fed materials and conveying the shaped powder materials to a first collecting tower;
the top of the first collecting tower is provided with a cyclone separator, and the bottom of the first collecting tower is provided with a coarse powder collecting port; wherein, the cyclone separator separates the coarse powder and the fine powder in the powder; collecting coarse powder through a coarse powder collecting port, and conveying fine powder to a second collecting tower;
the upper part of the second collecting tower is provided with a bag-type dust collector, and the bottom of the second collecting tower is provided with a fine powder collecting port; wherein, the fine powder is collected through a fine powder collecting port, the dust is removed by a bag-type dust remover, and the outlet of the bag-type dust remover is communicated with a main air outlet through a fan.
As a preferable scheme, the spheroidizing shaping machine comprises a machine shell, a shaping wheel and a grading rotary cylinder, wherein the shaping wheel and the grading rotary cylinder are arranged in the machine shell; the periphery of the shaping wheel is provided with a plurality of shaping knives, and the shaping wheel drives the shaping knives to rotate by taking the center of the shaping wheel as an axis under the driving of a driving device; the grading rotary drum is of a hollow cylindrical structure, and the side wall of the grading rotary drum is at least partially formed by a filter screen; the grading rotary drum can rotate around the axis of the grading rotary drum under the driving of a driving device; a material inlet, a powder outlet and a granular material outlet are formed in the side wall of the shell; the material inlet and the powder outlet are positioned above the shaping wheel, and the granular material outlet is positioned below the shaping wheel; the grading rotary drum is arranged above the shaping wheel, a hollow inner cavity of the grading rotary drum is communicated with the powder outlet, and materials with small particle sizes can enter the hollow inner cavity through a filter screen on the side wall of the grading rotary drum and then leave from the powder outlet.
More preferably, the shaping wheel is circular.
As a preferable scheme, the second collecting tower also comprises a spiral dust collector arranged between the air inlet of the second collecting tower and the bag-type dust collector; the spiral dust collector comprises a dust collecting disc with a through hole in the center and a spiral flow hole; the cyclone hole is communicated with the through hole of the dust collecting disc; the dust collecting disc is provided with a spiral baffle; one end of the spiral baffle extends to the through hole, and the other end of the spiral baffle extends to the edge of the dust collecting disc; and threads are arranged in the rotational flow holes.
As a more preferable scheme, a ring-shaped baffle plate which is vertically upward is arranged on the circumference of the through hole.
As a preferred scheme, a silencer is arranged on the main air outlet.
As a preferred scheme, pneumatic butterfly valves are arranged at the coarse powder collecting opening and the fine powder collecting opening.
As a preferable scheme, the sphericizing shaper, the first collecting tower, the second collecting tower, the fan and the main air outlet are sequentially communicated through a connecting pipeline, and a flow meter is arranged on the connecting pipeline.
Preferably, the lower part of the second collecting tower is provided with an inward contraction structure and an air hammer.
The beneficial technical effects of the utility model mainly lie in: the material sphericization production system can continuously shape, classify and collect materials and has small influence on the environment.
(1) The system realizes continuous operation of material sphericization shaping, different particle size classification, collection and dust removal, and has high production efficiency; meanwhile, the air flow discharged from the air outlet contains less dust, has little influence on the environment and has the advantage of environmental protection; in addition, the system is simple in structure, low in cost and suitable for large-scale popularization.
(2) The system is provided with the spiral dust collector with the dust collecting disc and the cyclone hole, so that the dust-containing air flow can generate cyclone and accelerate, and the dust in the air flow can be favorably thrown out and absorbed, thereby being favorable for separating particulate matters from the air flow and improving the effect and the efficiency of air flow purification.
Drawings
The present invention will be further explained with reference to the drawings and examples.
Fig. 1 is a schematic structural diagram of a preferred embodiment of the present invention.
Fig. 2 is an external view of the spherical shaper of the present invention.
Fig. 3 is a schematic structural diagram of the spheroidizing shaper of the present invention.
Fig. 4 is a schematic structural view of the spiral dust collector of the present invention.
Fig. 5 is a schematic top view of the dust collecting tray of the present invention.
Detailed Description
The invention will now be described in further detail with reference to the accompanying drawings, which are simplified schematic drawings and illustrate, by way of illustration only, the basic structure of the invention, and which therefore show only the constituents relevant to the invention. It should be noted that the terms "left," "right," "upper" and "lower" used in the following description refer to directions in the drawings, and the terms "inner" and "outer" refer to directions toward and away from, respectively, the geometric center of a particular component.
As shown in fig. 1-5, a material spheroidization production system comprises a spheroidization shaper 1, a first collecting tower 2, a second collecting tower 3, a fan 4 and a main air outlet 5 which are sequentially communicated through a connecting pipeline 6 according to a feeding sequence.
The sphericizing shaper 1 comprises a machine shell 11, a circular shaping wheel 12 and a grading rotary drum 14 which are arranged in the machine shell 11, wherein a plurality of shaping knives 13 are arranged at equal intervals on the peripheral edge of the shaping wheel 12, and the shaping knives 13 are of a block-shaped structure with sharp edges; the shaping wheel 12 drives the shaping knife 13 to rotate by taking the center of the shaping wheel 12 as an axis under the driving of a motor, and the shaping knife 13 collides with the material through high-speed rotation, so that large materials are crushed, irregular edges of the material are removed, and spherical materials are formed; the grading rotary drum 14 is a hollow cylindrical structure, the side wall of the grading rotary drum is formed by a filter screen, and the grading rotary drum 14 can rotate around the axis of the grading rotary drum under the drive of a motor; a material inlet 15, a powder outlet 16 and a granular material outlet 17 are formed in the side wall of the shell 11; the material inlet 15 and the powder outlet 16 are positioned above the shaping wheel 12, and the granular material outlet 17 is positioned below the shaping wheel 12; the grading drum 14 is arranged on the shaping wheel 12 and is shielded at the powder outlet 16; one end of the powder outlet 16 is communicated with the hollow inner cavity of the grading rotary drum 14, and the other end is communicated with the connecting pipeline 6 communicated with the first collecting tower 2.
The first collecting tower 2 is a cylindrical structure with a wide upper part and a narrow lower part, the top of the first collecting tower is provided with a cyclone separator 21, and the bottom of the first collecting tower is provided with a coarse powder collecting port 22; the air inlet 23 of the first collecting tower is arranged below the cyclone separator 21, and the air outlet 24 of the first collecting tower is arranged on the side of the cyclone separator 21.
The second collecting tower 3 is sequentially provided with a fine powder collecting port 31, a second collecting tower air inlet 32, a spiral dust collector 33, a bag-type dust collector 34 and a second collecting tower air outlet 35 from bottom to top; the lower part of the second collecting tower is arranged in an inward-contracting structure and is provided with an air hammer 36 which is beneficial to sliding off the fine powder collecting port 31.
The spiral dust collector 33 includes a dust collecting plate 331 having a through hole 331a centrally provided therein and a spiral flow hole 332; the cyclone hole 332 communicates with the dust collection tray through hole 331 a; the dust collecting plate 331 is provided with a spiral baffle 331b, and the spiral baffle 331b is vertically arranged; one end of the spiral baffle 331b extends toward the through hole 331a, and the other end extends toward the edge of the dust collection tray 331; threads are provided in swirl holes 332; in addition, a vertically upward ring-shaped baffle 331c is provided on the circumference of the through hole 331 a.
The main air outlet 5 is provided with a silencer 51 to reduce noise generated during operation.
Pneumatic butterfly valves 7 are arranged at the coarse powder collecting port 22 and the fine powder collecting port 31; a flow meter 8 is arranged on the connecting line 6 to monitor the entire process. In addition, the system is also provided with an electric control cabinet 9 for controlling the whole crushing and spheroidizing process; the second collecting tower 3 is higher in height, so an operating platform 10 is arranged, and the second collecting tower 3 is convenient to monitor, maintain and repair.
The operation principle of the system is as follows:
(1) the material enters from a material inlet 15 of the sphericizing shaper 1; shaping the material by the rotation of the shaping knife 13; at the moment, the fan 4 operates, and air is drawn from the powder outlet 16 to the inside of the shell 11 through the connecting pipeline 6; the material with small particle size enters the hollow inner cavity of the grading rotary drum 14 from the filter screen thereof under the action of the air draft, further moves to the powder outlet 16 and is pumped out of the sphericizing shaper 1; while the particles with large size and unable to pass through the filter screen remain in the housing 11 or are continuously shaped into small-size particles or are collected from a particle material outlet 17 below the shaping wheel 12; by adjusting the rotation speed of the classifying drum 14 and the grade of the filter screen, the size of dust particles passing through the classifying drum 14 can be controlled, thereby realizing classification.
(2) The materials enter the first collecting tower 2 along with the airflow through the connecting pipeline 6, and under the action of the cyclone separator 21, coarse powder with larger particle size falls down and is discharged from the coarse powder collecting opening 22; the gas stream with entrained fines continues on.
(3) The airflow with the fine powder enters a second collection tower 3; the fine powder falls due to the sedimentation and is discharged from the fine powder collection port 31; the dust/dirt laden air flow rises through the swirl holes 332 and forms a swirl due to the action of the threads; after entering the dust collecting tray 331, the dust is separated from the air flow and falls onto the dust collecting tray 331 due to the centrifugal action and the blocking of the spiral baffle 331b, and the arrangement of the annular baffle 331c prevents the dust from sliding downwards and falling into the fine powder collecting port 31; meanwhile, because the swirl holes 332 are relatively narrow, the dust-containing airflow not only forms a swirl, but also rises into the dust collecting disc 331 at an accelerated speed, and the pressure of the gas is reduced according to the Bernoulli principle, so that peripheral gas can be attracted, mutual adsorption of dust in the airflow is facilitated, and the dust can be separated from the airflow more easily; then the air flow enters a bag-type dust remover 34 to further remove dust, so that the environmental protection requirement is met; the rear airflow passes through the connecting pipeline 6 and finally flows out of the main air outlet 5.
In light of the foregoing, it is to be understood that various changes and modifications may be made by those skilled in the art without departing from the spirit and scope of the invention. The technical scope of the present invention is not limited to the content of the specification, and must be determined according to the scope of the claims.

Claims (9)

1. The utility model provides a material sphericization production system which characterized in that: comprises a sphericizing shaper, a first collecting tower, a second collecting tower, a fan and a main air outlet;
the spheroidizing shaping machine is used for crushing and shaping the fed materials and conveying the shaped powder materials to a first collecting tower;
the top of the first collecting tower is provided with a cyclone separator, and the bottom of the first collecting tower is provided with a coarse powder collecting port; wherein, the cyclone separator separates the coarse powder and the fine powder in the powder; collecting coarse powder through a coarse powder collecting port, and conveying fine powder to a second collecting tower;
the upper part of the second collecting tower is provided with a bag-type dust collector, and the bottom of the second collecting tower is provided with a fine powder collecting port; wherein, the fine powder is collected through a fine powder collecting port, the dust is removed by a bag-type dust remover, and the outlet of the bag-type dust remover is communicated with a main air outlet through a fan.
2. The material spheroidization production system according to claim 1, wherein: the spheroidization shaping machine comprises a shell, a shaping wheel and a grading rotary drum, wherein the shaping wheel and the grading rotary drum are arranged in the shell; the periphery of the shaping wheel is provided with a plurality of shaping knives, and the shaping wheel drives the shaping knives to rotate by taking the center of the shaping wheel as an axis under the driving of a driving device; the grading rotary drum is of a hollow cylindrical structure, and the side wall of the grading rotary drum is at least partially formed by a filter screen; the grading rotary drum can rotate around the axis of the grading rotary drum under the driving of a driving device; a material inlet, a powder outlet and a granular material outlet are formed in the side wall of the shell; the material inlet and the powder outlet are positioned above the shaping wheel, and the granular material outlet is positioned below the shaping wheel; the grading rotary drum is arranged above the shaping wheel, a hollow inner cavity of the grading rotary drum is communicated with the powder outlet, and materials with small particle sizes can enter the hollow inner cavity through a filter screen on the side wall of the grading rotary drum and then leave from the powder outlet.
3. The material spheroidization production system according to claim 2, wherein: the shaping wheel is circular.
4. The material spheroidization production system according to claim 1, wherein: the second collecting tower also comprises a spiral dust collector arranged between the air inlet of the second collecting tower and the bag-type dust collector; the spiral dust collector comprises a dust collecting disc with a through hole in the center and a spiral flow hole; the cyclone hole is communicated with the through hole of the dust collecting disc; the dust collecting disc is provided with a spiral baffle; one end of the spiral baffle extends to the through hole, and the other end of the spiral baffle extends to the edge of the dust collecting disc; and threads are arranged in the rotational flow holes.
5. The material spheroidization production system according to claim 4, wherein: and a vertically upward annular baffle is arranged on the circumference of the through hole.
6. The material spheroidization production system according to claim 1, wherein: and a silencer is arranged on the main air outlet.
7. The material spheroidization production system according to claim 1, wherein: pneumatic butterfly valves are arranged at the coarse powder collecting opening and the fine powder collecting opening.
8. The material spheroidization production system according to claim 1, wherein: the spherical shaping machine, the first collecting tower, the second collecting tower, the fan and the main air outlet are sequentially communicated through a connecting pipeline, and a flow meter is arranged on the connecting pipeline.
9. The material spheroidization production system according to claim 1, wherein: the lower part of the second collecting tower is provided with an inward-contracting structure and an air hammer.
CN201921788011.5U 2019-10-23 2019-10-23 Material sphericization production system Active CN211660203U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201921788011.5U CN211660203U (en) 2019-10-23 2019-10-23 Material sphericization production system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201921788011.5U CN211660203U (en) 2019-10-23 2019-10-23 Material sphericization production system

Publications (1)

Publication Number Publication Date
CN211660203U true CN211660203U (en) 2020-10-13

Family

ID=72731528

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201921788011.5U Active CN211660203U (en) 2019-10-23 2019-10-23 Material sphericization production system

Country Status (1)

Country Link
CN (1) CN211660203U (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112973887A (en) * 2021-02-08 2021-06-18 陈红丽 Ceramic tile powder preparation facilities

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112973887A (en) * 2021-02-08 2021-06-18 陈红丽 Ceramic tile powder preparation facilities
CN112973887B (en) * 2021-02-08 2022-09-09 临沂坤宇建陶有限公司 Ceramic tile powder preparation facilities

Similar Documents

Publication Publication Date Title
CN111467884A (en) Front dust removal and collection system of cloth bag type air dust collector
CN104984910A (en) High-dispersibility vortex powder selecting machine
CN101954317A (en) Radial spray regular cyclone separator
CN211660203U (en) Material sphericization production system
CN210752975U (en) Resin binder negative pressure grinding system for abrasive disc and brake pad
CN204892373U (en) High dispersivity vortex selection powder machine
CN202078978U (en) Cyclone separator
CN203526178U (en) Plastic and dust frequency conversion separating device
CN105233956A (en) Separation method and device for talc and dolomite
CN104226600A (en) Multifunctional winnower
CN211707116U (en) Cyclone structure particle material rotor-free movable piece airflow classification equipment
CN216756804U (en) Adjustable micro-powder particle separation device
CN2770817Y (en) Five-grade separation combined powder separating machine air intake device
CN203556562U (en) Ternary classification powder selecting machine
CN205308793U (en) Screening plant of high -efficient silicon powder
CN206229684U (en) A kind of air selects powder system and its powder concentrator
CN214916979U (en) Connecting device of coal mill and rotary separator
CN2820347Y (en) Vortex air grader
CN113145234A (en) Grading device with angle for vertical grading wheel blade
CN210022527U (en) Airflow grading device for laboratory
CN105169816A (en) Combined dedusting device used in compound fertilizer production process
CN208146239U (en) A kind of rotational flow sorting device of crushed material grain diameter
CN202427526U (en) Fine smashing system
CN202155250U (en) Special grading machine for superfine powder
CN1236677A (en) Centrifugal wind classifier for bulk materials

Legal Events

Date Code Title Description
GR01 Patent grant
GR01 Patent grant