CN207756100U - A kind of novel eccentric vertical shaft ceramics by dry comminutor - Google Patents
A kind of novel eccentric vertical shaft ceramics by dry comminutor Download PDFInfo
- Publication number
- CN207756100U CN207756100U CN201721766435.2U CN201721766435U CN207756100U CN 207756100 U CN207756100 U CN 207756100U CN 201721766435 U CN201721766435 U CN 201721766435U CN 207756100 U CN207756100 U CN 207756100U
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- China
- Prior art keywords
- vertical shaft
- granulation
- barrel
- ceramics
- eccentric
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Abstract
The utility model discloses a kind of novel eccentric vertical shaft ceramics by dry comminutors, including granulation barrel, the top of granulation barrel is used for the dispatch tube of transferring raw material, the discharge port of granulation barrel is connected to centrifugal sifting machine, the discharge end of centrifugal sifting machine is connected to that the feed bin of the particle screened can be stored, the inner lower of granulation barrel, which vertically runs through, is equipped with eccentric vertical shaft, the top of eccentric vertical shaft is equipped with one group of granulation column being placed in inside granulation barrel, the lower part of the bias vertical shaft is equipped with the granulation motor for driving eccentric vertical shaft and the rotation for being granulated column, and eccentric vertical shaft is arranged in the eccentric position for being granulated bottom of the barrel.The eccentric vertical shaft that the utility model uses obtains better granulation outcome and since the rotation of vertical shaft and revolution is to drive the rotation for being granulated column and revolution to make its granulation efficiency higher.
Description
Technical field
The utility model is related to ceramic processing technique fields, refer specifically to a kind of novel eccentric vertical shaft ceramics by dry granulation
Machine.
Background technology
Currently, in Ceramic manufacturing production, ceramics by dry comminutor is often used, its advantage is that ceramics by dry comminutor
Not only there is energy consumption reduction outstanding to act on relative to wet granulator, largely reduces energy consumption.
But ceramics by dry comminutor the disadvantage is that prepare ceramic powder particle there are following main problems:First is true
The fully dispersed sex chromosome mosaicism of grain；Second is the forming compression ratio problem of false particle.
Utility model content
The utility model is in order to solve the above-mentioned deficiency of the prior art, it is proposed that a kind of novel eccentric vertical shaft ceramics by dry is made
Grain machine.
In order to solve the above-mentioned technical problem, the utility model uses following technical scheme：A kind of novel eccentric vertical shaft ceramics
Dry granulating machine, including granulation barrel, the top of the granulation barrel are used for the dispatch tube of transferring raw material, the discharge port of the granulation barrel
It is connected to centrifugal sifting machine, the discharge end of centrifugal sifting machine is connected to that the feed bin of the particle screened, the granulation can be stored
For the inner lower of bucket vertically through eccentric vertical shaft is equipped with, the top of the bias vertical shaft is equipped with one be placed in inside granulation barrel
Group granulation column, the lower part of the bias vertical shaft are equipped with the granulation motor for driving eccentric vertical shaft and the rotation for being granulated column, and described
Eccentric vertical shaft is arranged in the eccentric position for being granulated bottom of the barrel；The inside of the granulation barrel for heat particle molded in bucket and
The heating plate of inner bucket water point is removed, the top of the granulation barrel is additionally provided with vapor and dust outlet.
Further, belt feeder is installed, the belt feeder, which is equipped with, to be used at the feed inlet of the dispatch tube
It is equipped with the feeding electricity of drive belt feed appliance work in the side of the funnel that raw material is concentrated to blanking, the belt feeder
Machine, the feeding motor are mounted on electric motor stand.
Further, it is also equipped with the heating net of the material powder heat drying dehydration of process in the dispatch tube.
Further, the inside of the centrifugal sifting machine is equipped with the screening of the particle screen selecting separation of different-diameter size
The side of net, the centrifugal sifting machine is equipped with screening motor, and the screening motor is connected with one-stage gear transmission accelerating chamber, described
The output end connection that one-stage gear is driven accelerating chamber drives in the screening net.
Further, the heating plate is connected with computer heating control switch.
Compared with prior art, the eccentric vertical shaft that the utility model uses obtains better granulation outcome and due to vertical shaft
Rotation and revolution to drive the rotation for being granulated column and revolution to make its granulation efficiency higher, total reasonable design,
Compact in design, various devices outfit coordinations are well-balanced, form an entirety, functional, granulation efficiency higher, energy consumption in an orderly manner
Use small, at low cost, easy to spread.
Description of the drawings
Fig. 1 is the structural schematic diagram of the utility model.
Specific implementation mode
Utility model is described in detail with reference to the accompanying drawings and examples.
As shown in Figure 1, the utility model proposes novel eccentric vertical shaft ceramics by dry comminutor, including granulation barrel 8 is granulated
The top of bucket 8 is used for the dispatch tube 5 of transferring raw material, and the discharge port of granulation barrel is connected to centrifugal sifting machine 17, centrifugal sifting machine 17
Discharge end be connected to can to store the feed bin 18 of the particle screened, the inner lower of granulation barrel 8 is vertically through being equipped with partially
Heart vertical shaft 12, the top of eccentric vertical shaft 12 are equipped with one group of granulation column 11 being placed in inside granulation barrel 8, under the bias vertical shaft
Portion is equipped with the granulation motor 13 of drive eccentric vertical shaft and the rotation for being granulated column, and eccentric vertical shaft 12 is arranged in granulation bottom of the barrel
Eccentric position；The inside of granulation barrel 8 is used to heat particle molded in bucket and removes the heating plate 10 of inner bucket water point, the granulation
The top of bucket 8 is additionally provided with vapor and dust outlet 7.Heating plate 10 is connected with computer heating control switch 9.
Belt feeder 4 is installed, belt feeder 4 is equipped with for concentrating raw material at the feed inlet of dispatch tube 5
The side of the funnel 3 of blanking, belt feeder 4 is equipped with the feeding motor 2 that drive belt feed appliance 4 works, and feeding motor 2 is installed
On electric motor stand 1.It is also equipped in dispatch tube 5 by the heating net 6 of the material powder heat drying dehydration of process.
The inside of centrifugal sifting machine 17 is equipped with the screening net 16 of the particle screen selecting separation of different-diameter size, screen centrifuge
The side of machine is selected to be equipped with screening motor 14, screening motor 14 is connected with one-stage gear transmission accelerating chamber 15, and one-stage gear transmission adds
The output end connection of fast case 15 drives in screening net 16.
The operation principle of the utility model is that raw material is dropped down onto from funnel 3 in belt feeder 4, in 4 band of belt feeder
Enter under dynamic in dispatch tube 5 and enter in the granulation barrel 8 of dry method after heating net 6, since eccentric vertical shaft 12 not only has revolution
Also the rotation of itself not only has revolution to also have rotation so that being granulated column 11, to make its granulation efficiency more
Height, largely reduces energy consumption, and heating plate 10 begins to warm up drying and moulding particle, the vapor of generation and a small amount of exhaust gas
It is discharged by steam and dust outlet 7, is controlled by computer heating control switch 9 after the completion of heating process, open heating plate 10, at this time particle
It drops down onto in storage warehouse and enters in centrifugal sifting machine 17, centrifugal sifting machine 17 is driven accelerating chamber in screening motor 14 and one-stage gear
High speed rotation under 15 drive generates centrifugal force, and it is aging to be used that feed bin 18 is entered after particle screen selecting is detached.
The utility model has granulating system, starts feeding motor 2, and power source is transmitted to ribbon feeding by feeding motor 2
Device 4, then belt feeder 4 is in feedstock delivery to dispatch tube 5, by heating net 6, by the material powder heat drying of process
Enter in granulation barrel 8 after dehydration, since eccentric vertical shaft 12 not only has revolution to also have the rotation of itself so that being granulated vertical
Column 11 not only has revolution to also have rotation largely to reduce energy consumption to make its granulation efficiency higher.
2. auxiliary system, the system is by screening motor 14, one-stage gear transmission accelerating chamber 15, screening net 16, centrifugal screening
Machine 17, feed bin 18 form.Centrifugal sifting machine 17 revolves at a high speed in the case where screening motor 14 and one-stage gear are driven the drive of accelerating chamber 15
Turn, generate centrifugal force, it is aging to be used that feed bin 18 is entered after particle screen selecting is detached.
Above-described embodiment only expresses the several embodiments of the utility model, the description thereof is more specific and detailed, but simultaneously
It cannot be therefore understands that for the limitation to the utility model patent range.It should be pointed out that for the ordinary skill people of this field
For member, without departing from the concept of the premise utility, various modifications and improvements can be made, these belong to this reality
With novel protection domain.Therefore, the utility model patent and protection domain should be subject to the appended claims.
Claims (5)
1. a kind of novel eccentric vertical shaft ceramics by dry comminutor, it is characterised in that：Including granulation barrel（8）, the granulation barrel（8）'s
Top is used for the dispatch tube of transferring raw material（5）, the discharge port of the granulation barrel is connected to centrifugal sifting machine（17）, centrifugal sifting machine
（17）Discharge end be connected to that the feed bin of the particle screened can be stored（18）, the granulation barrel（8）Inner lower it is vertical
Through being equipped with eccentric vertical shaft（12）, the bias vertical shaft（12）Top be equipped be placed in granulation barrel（8）Internal one group is made
Grain column（11）, the lower part of the bias vertical shaft is equipped with the granulation motor for driving eccentric vertical shaft and the rotation for being granulated column（13）, and
The bias vertical shaft（12）It is arranged in the eccentric position for being granulated bottom of the barrel；The granulation barrel（8）Inside for heating in bucket
Molding particle and the heating plate for removing inner bucket water point（10）, the granulation barrel（8）Top be additionally provided with vapor and dust outlet
（7）.
2. novel eccentric vertical shaft ceramics by dry comminutor as described in claim 1, it is characterised in that：The dispatch tube（5）'s
Belt feeder is installed at feed inlet（4）, the belt feeder（4）It is equipped with the funnel for raw material to be concentrated to blanking
（3）, the belt feeder（4）Side be equipped with drive belt feed appliance（4）The feeding motor of work（2）, the feeding electricity
Machine（2）Mounted on electric motor stand（1）On.
3. novel eccentric vertical shaft ceramics by dry comminutor as described in claim 1, it is characterised in that：The dispatch tube（5）It is interior
It is also equipped with the heating net of the material powder heat drying dehydration of process（6）.
4. novel eccentric vertical shaft ceramics by dry comminutor as described in claim 1, it is characterised in that：The centrifugal sifting machine
（17）Inside be equipped with the screening net of the particle screen selecting of different-diameter size separation（16）, the side of the centrifugal sifting machine
Equipped with screening motor（14）, the screening motor（14）It is connected with one-stage gear transmission accelerating chamber（15）, the one-stage gear biography
Dynamic accelerating chamber（15）Output end connection drive in the screening net（16）.
5. novel eccentric vertical shaft ceramics by dry comminutor as described in claim 1, it is characterised in that：The heating plate（10）Even
It is connected to computer heating control switch（9）.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721766435.2U CN207756100U (en) | 2017-12-18 | 2017-12-18 | A kind of novel eccentric vertical shaft ceramics by dry comminutor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721766435.2U CN207756100U (en) | 2017-12-18 | 2017-12-18 | A kind of novel eccentric vertical shaft ceramics by dry comminutor |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207756100U true CN207756100U (en) | 2018-08-24 |
Family
ID=63186854
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201721766435.2U Expired - Fee Related CN207756100U (en) | 2017-12-18 | 2017-12-18 | A kind of novel eccentric vertical shaft ceramics by dry comminutor |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN207756100U (en) |
-
2017
- 2017-12-18 CN CN201721766435.2U patent/CN207756100U/en not_active Expired - Fee Related
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20180824 Termination date: 20181218 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |