CN205969404U - Ceramic powder granulator - Google Patents
Ceramic powder granulator Download PDFInfo
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- CN205969404U CN205969404U CN201620521509.5U CN201620521509U CN205969404U CN 205969404 U CN205969404 U CN 205969404U CN 201620521509 U CN201620521509 U CN 201620521509U CN 205969404 U CN205969404 U CN 205969404U
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- colorant
- ceramic powder
- coating agent
- prilling granulator
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Abstract
The utility model discloses a ceramic powder granulator, add device and prilling granulator including feed arrangement, parcel agent, feed arrangement with prilling granulator's feed inlet is connected, parcel agent add the device with a mouthful connection is added in prilling granulator's parcel agent, discharging device with prilling granulator's discharge gate is connected. Ceramic powder granulator is used for the powder dry powder granulation of ceramic trade, sprays the parcel agent toward the ceramic powder in at the granulation in -process under the produced impact effect and gas shock of prilling granulator, the parcel agent is being wrapped up the ceramic powder granule and be the spheroid structure for particle size is fit for on the microcosmic to improved ceramic powder's mobility greatly, ceramic powder distributes evenly in subsequent extrusion, improves the ceramic manufacture quality.
Description
Technical field
The utility model is related to ceramic industry powder powder pelletizing apparatus field, more particularly, to a kind of ceramic powder granulation
Machine.
Background technology
At present, in Production of Ceramics, commonly used extrusion molding makes base substrate, and needs before extrusion molding ceramic powder is entered
Row granulation is granulated using ball mill with improving ceramic powder mobility, tradition, and granulation time is long, consumes ample resources, and in recent years
Carry out gradually popular quick using granulation, the little dry granulating machine processing ceramic powder of resource loss.But current dry granulating machine
Balling ratio is low, and the ceramic powder density after granulation is loose, is easily caused particle damage by external force effect, a granulating qualification rate
Low, poor fluidity, follow-up extrusion molding is susceptible to ceramic powder problem pockety, largely effects on ceramic green
Yield and quality.
Utility model content
The purpose of this utility model is to propose a kind of balling ratio height, the ceramic powder comminutor of finished product good fluidity.
For reaching this purpose, the utility model employs the following technical solutions：
A kind of ceramic powder comminutor, including feed arrangement, coating agent adding set and prilling granulator；
Described feed arrangement is connected with the charging aperture of described prilling granulator, and described coating agent adding set is filled with described granulation
The coating agent put adds mouth and connects.
Preferably, described coating agent adding set includes coating agent storage silo, coating agent jet pipe and coating agent delivery valve, institute
The input stating coating agent jet pipe is connected with the discharging opening of described coating agent storage silo, the output end of described coating agent jet pipe and institute
The coating agent stating prilling granulator adds mouth connection, and described coating agent delivery valve is arranged at the output end of described coating agent jet pipe.
Preferably, also include colorant adding set, described colorant adding set includes colorant storehouse and colorant efferent duct, institute
The input stating colorant efferent duct is connected with the discharging opening in described colorant storehouse, and the output end of described colorant efferent duct passes through three-way pipe
Connect with described coating agent jet pipe.
Preferably, described colorant adding set includes several described colorant storehouses and some colorants export arm, described
The discharging opening in colorant storehouse is passed through corresponding described colorant output arm and is connected with the input of described colorant efferent duct；
Described colorant storehouse includes colorant outlet valve, and described colorant outlet valve is arranged at the discharging opening in described colorant storehouse, described
Colorant efferent duct includes colorant and adds valve, and described colorant adds the output end that valve is arranged at described colorant efferent duct.
Preferably, the coating agent of described coating agent storage silo storage is PVA solution, PVP solution or glue.
Preferably, described feed arrangement includes feed hopper, feed pipe and pusher, described feed hopper and described feed pipe
Input connect, the output end of described feed pipe is connected with the charging aperture of described prilling granulator, and described pusher is arranged at
The inside of described feed pipe.
Preferably, also include drawing mechanism, described drawing mechanism includes discharge nozzle and discharging bin, the input of described discharge nozzle
End is connected with the discharging opening of described prilling granulator, and the output end of described discharge nozzle is connected with the input of described discharging bin.
Preferably, described drawing mechanism also includes discharging dressing sieve, and described discharging dressing sieve is arranged at the output of described discharging bin
End.
Preferably, described prilling granulator is horizontal prilling granulator；Also include leaning device, described leaning device is arranged at institute
State the bottom of prilling granulator, described leaning device drives described prilling granulator to tilt, and angle of inclination is 3 °～10 °.
Preferably, PLC control device, described rabbling mechanism, coating agent output valve, colorant outlet valve, inclination are also included
Mechanism, colorant add valve and pusher is all electrically connected with described PLC control device.
Described ceramic powder comminutor is used for the powder dry powder prilling of ceramic industry, and described ceramic powder comminutor is provided with
Described coating agent adding set, sprays coating agent, micro- by described coating agent jet pipe in granulation process toward in ceramic powder
Being in the sphere structure being suitable for for particle size in sight, thus substantially increasing the mobility of ceramic powder, being squeezed in follow-up
In type, ceramic powder is evenly distributed, and improves Production of Ceramics quality.
Brief description
Accompanying drawing is described further to the utility model, but the content in accompanying drawing is not constituted to any limit of the present utility model
System.
Fig. 1 is the ceramic powder granulator structure schematic diagram of the one of embodiment of the utility model.
Wherein：Feed arrangement 1；Coating agent adding set 2；Prilling granulator 3；Drawing mechanism 4；Rabbling mechanism 31；Coating agent
Storage silo 21；Coating agent jet pipe 22；Coating agent delivery valve 23；Colorant storehouse 51；Colorant efferent duct 52；Colorant exports arm 53；Color
Material outlet valve 511；Colorant adds valve 521；Feed hopper 11；Feed pipe 12；Discharge nozzle 41；Discharging bin 42.
Specific embodiment
Further illustrate the technical solution of the utility model below in conjunction with the accompanying drawings and by specific embodiment.
The ceramic powder comminutor of the present embodiment, as shown in figure 1, including feed arrangement 1, coating agent adding set 2 and making
Grain device 3；Described feed arrangement 1 is connected with the charging aperture of described prilling granulator 3, and described coating agent adding set 2 is made with described
The coating agent of grain device 3 adds mouth and connects.
Preferably, described coating agent adding set 2 includes coating agent storage silo 21, coating agent jet pipe 22 and coating agent output
Valve 23, the input of described coating agent jet pipe 22 is connected with the discharging opening of described coating agent storage silo 21, described coating agent jet pipe
22 output end is added mouth with the coating agent of described prilling granulator 3 and is connected, and described coating agent delivery valve 23 is arranged at described parcel
The output end of agent jet pipe 22.
Described ceramic powder comminutor is used for the powder dry powder prilling of ceramic industry, and ceramic powder is through described feed arrangement 1
Quantitation is conveyed to described prilling granulator 3, while ceramic powder is stirred by described prilling granulator 3 and constantly refinement ceramic powder
Material granularity is required with reaching granulation, and after granulation, ceramic powder is exported to completing follow-up ceramic green by described drawing mechanism 4
Produce operation.Described ceramic powder comminutor is provided with described coating agent adding set 2, described coating agent storage silo 21 storage parcel
Agent, described coating agent delivery valve 23 is used for controlling the addition of coating agent, passes through described prilling granulator 3 in granulation process
Refinement ceramic powder particle, to the particle size being suitable for, sprays parcel by described coating agent jet pipe 22 toward in ceramic powder
Agent, increases the mobility of ceramic powder.Ceramic powder after existing granulator granulation mostly is irregular pyramid on microcosmic
And aspheres, the ceramic powder poor fluidity therefore granulating out, it is susceptible to ceramic powder in follow-up extrusion molding and divide
The uneven problem of cloth, largely effects on Production of Ceramics quality.
And described ceramic powder comminutor sprays coating agent in granulation process toward in ceramic powder, in described prilling granulator
Under effect of impact and gas shock produced by 3, coating agent is wrapped in ceramic powder particle and is in for particle size on microcosmic
Suitable sphere structure, thus substantially increasing the mobility of ceramic powder, ceramic powder distribution in follow-up extrusion molding
Uniformly, improve Production of Ceramics quality.
Preferably, also include colorant adding set 5, described colorant adding set 5 includes colorant storehouse 51 and colorant efferent duct
52, the input of described colorant efferent duct 52 is connected with the discharging opening in described colorant storehouse 51, the output of described colorant efferent duct 52
End is connected with described coating agent jet pipe 22 by three-way pipe.
Described colorant adding set 5 is used for spraying colorant toward in ceramic powder in granulation process, is that ceramic powder is hyperchromic,
Improve the dicoration of ceramic powder.Described colorant storehouse 51 stores colorant, and described colorant is fluent colorant, colorant when need to add colorant
Exported by described colorant efferent duct 52 and mix with the coating agent in described coating agent jet pipe 22, that is, toward ceramic powder when granulating
Material sprays the mixed solution of colorant and coating agent, thus ceramic powder particle surface uniform coloring.Existing comminutor adds
Be solid-state colorant be colorant powder, difficult metering, tack is poor, and during discharging, colorant easily drops from ceramic powder particle surface and glues
The inwall being attached to described discharging bin 42 causes to waste, and the ceramic powder using the coloring of solid-state colorant is easy in extrusion molding
There is layering thus adobe is susceptible to ftracture when firing.And spray toward ceramic powder during described ceramic powder granulator granulation
Colorant and the mixed solution of coating agent, are equivalent to and spray the coloured coating agent of band toward ceramic powder, have for one layer on microcosmic
The coating agent of color is wrapped in ceramic powder particle, and tack is high, occurs without lamination problem during extrusion molding, greatly improves pottery
The tinctorial quality of powder.
Preferably, described colorant adding set 5 includes several described colorant storehouses 51 and some colorants export arm 53,
The discharging opening in described colorant storehouse 51 is passed through corresponding described colorant output arm 53 and is connected with the input of described colorant efferent duct 52
Connect；
Described colorant storehouse 51 includes colorant outlet valve 511, and described colorant outlet valve 511 is arranged at going out of described colorant storehouse 51
Material mouth, described colorant efferent duct 52 includes colorant and adds valve 521, and described colorant adds valve 521 and is arranged at described colorant efferent duct
52 output end.
Described colorant adding set 5 includes several described colorant storehouses 51 and some colorants export arm 53, can store
The colorant of several different colours, and the colorant of different colours can be selected by Production requirement；Correspondence is opened during using certain colorant
The colorant outlet valve 511 in described colorant storehouse 51 and described colorant efferent duct 52 colorant add valve 521, without add color
The colorant closing described colorant efferent duct 52 during material adds valve 521, thus improving production chains, expanding described ceramic powder and making
The scope of application of grain machine.
Preferably, the coating agent of described coating agent storage silo 21 storage is PVA solution, PVP solution or glue.PVA solution
It is poly-vinyl alcohol solution, PVP solution is the water soluble such as polyvinylpyrrolidonesolution solution and glue, and transparent, viscosity is good, become
This is low.
Preferably, described feed arrangement 1 includes feed hopper 11, feed pipe 12 and pusher, described feed hopper 11 and institute
The input stating feed pipe 12 connects, and the output end of described feed pipe 12 is connected with the charging aperture of described prilling granulator 3, described pushes away
Material mechanism is arranged at the inside of described feed pipe 12.Described feed arrangement 1 includes feed hopper 11, feed pipe 12 and pusher,
Ceramic powder stores in described feed hopper 11, and during granulation, ceramic powder is delivered to described prilling granulator 3 by described feed pipe 12,
Described pusher is arranged at the inside of described feed pipe 12, and described pusher is used for controlling the conveying capacity of ceramic powder, real
Now granulate controlledization.
Preferably, also include drawing mechanism 4, described drawing mechanism 4 includes discharge nozzle 41 and discharging bin 42, described discharge nozzle
41 input is connected with the discharging opening of described prilling granulator 3, and the output end of described discharge nozzle 41 is defeated with described discharging bin 42
Enter end to connect.After granulation, ceramic powder is exported by described discharge nozzle 41 and leaves described discharging bin 42 in.
Preferably, described drawing mechanism 4 also includes discharging dressing sieve, and described discharging dressing sieve is arranged at the defeated of described discharging bin 42
Go out end.Described discharging dressing sieve is used for carrying out, to the ceramic powder after granulation, sorting of sieving, the slot size of described discharging dressing sieve and
Granulation require particle size identical, therefore only particle size meet granulation require ceramic powder particle just can by described go out
Feed powder is sieved, thus ensureing that the particle size of the ceramic powder of described ceramic powder comminutor output reaches granulation and requires, greatly
Improve granulation quality.
Preferably, described prilling granulator 3 is horizontal prilling granulator, and powder stirring is more uniformly distributed；Also include leaning device, institute
State the bottom that leaning device is arranged at described prilling granulator 3, described leaning device drives described prilling granulator 3 to tilt, inclination angle
Spend for 3 °～10 °, preferably 6 °.Described leaning device is set and is easy to the discharging of described prilling granulator 3, reduce powder residual quantity.
Preferably, PLC control device, described rabbling mechanism 31, coating agent output valve 23, colorant outlet valve are also included
511st, leaning device, colorant interpolation valve 521 and pusher are all electrically connected with described PLC control device.Described PLC control device
For controlling described ceramic powder comminutor, thus realizing the automation of powder dry powder prilling, improve production efficiency, reduces work
Intensity.
The ceramic powder comminutor of the present embodiment has the advantages that：1. ceramic powder comminutor described in is provided with described
Coating agent adding set 2, coating agent is wrapped in ceramic powder particle and is in the sphere structure being suitable for for particle size on microcosmic,
Thus substantially increasing the mobility of ceramic powder, in follow-up extrusion molding, ceramic powder is evenly distributed, and improves ceramic green
Yield and quality；2. colorant adding set 5 described in is used for spraying toward in ceramic powder colorant in granulation process, and described ceramic powder is made
Spray the mixed solution of colorant and coating agent during grain machine granulation toward ceramic powder, microcosmic is one layer of coloured coating agent parcel
Ceramic powder particle, tack is high, occurs without lamination problem during extrusion molding, greatly improve ceramic powder chromaticness
Amount；3. pusher described in is arranged at the inside of described feed pipe 12, and described pusher is used for controlling the conveying of ceramic powder
Amount, realizes granulation controlledization.
Describe know-why of the present utility model above in association with specific embodiment.These descriptions are intended merely to explain this reality
With new principle, and the restriction to the utility model protection domain can not be construed to by any way.Based on explanation herein,
Those skilled in the art does not need to pay performing creative labour and can associate other specific embodiment of the present utility model,
These modes fall within protection domain of the present utility model.
Claims (9)
1. a kind of ceramic powder comminutor it is characterised in that：Including feed arrangement, coating agent adding set and prilling granulator；
Described feed arrangement is connected with the charging aperture of described prilling granulator, described coating agent adding set and described prilling granulator
Coating agent adds mouth and connects.
2. ceramic powder comminutor according to claim 1 it is characterised in that：Described coating agent adding set includes wrapping up
Agent storage silo, coating agent jet pipe and coating agent delivery valve, the input of described coating agent jet pipe and described coating agent storage silo
Discharging opening connects, and the output end of described coating agent jet pipe is added mouth with the coating agent of described prilling granulator and is connected, described coating agent
Delivery valve is arranged at the output end of described coating agent jet pipe.
3. ceramic powder comminutor according to claim 1 it is characterised in that：Also include colorant adding set, described color
Material adding set includes colorant storehouse and colorant efferent duct, and the input of described colorant efferent duct is connected with the discharging opening in described colorant storehouse
Connect, the output end of described colorant efferent duct is connected with described coating agent jet pipe by three-way pipe.
4. ceramic powder comminutor according to claim 3 it is characterised in that：Described colorant adding set includes several
Described colorant storehouse and some colorants export arms, the discharging opening in described colorant storehouse pass through corresponding described colorant export arm with
The input of described colorant efferent duct connects；
Described colorant storehouse includes colorant outlet valve, and described colorant outlet valve is arranged at the discharging opening in described colorant storehouse, described colorant
Efferent duct includes colorant and adds valve, and described colorant adds the output end that valve is arranged at described colorant efferent duct.
5. ceramic powder comminutor according to claim 1 it is characterised in that：The parcel of described coating agent storage silo storage
Agent is PVA solution, PVP solution or glue.
6. ceramic powder comminutor according to claim 1 it is characterised in that：Described feed arrangement includes feed hopper, enters
Expects pipe and pusher, described feed hopper is connected with the input of described feed pipe, and the output end of described feed pipe is made with described
The charging aperture of grain device connects, and described pusher is arranged at the inside of described feed pipe.
7. ceramic powder comminutor according to claim 1 it is characterised in that：Also include drawing mechanism, described discharging dress
Put including discharge nozzle and discharging bin, the input of described discharge nozzle is connected with the discharging opening of described prilling granulator, described discharge nozzle
Output end be connected with the input of described discharging bin.
8. ceramic powder comminutor according to claim 7 it is characterised in that：Described drawing mechanism also includes feed powder
Sieve, described discharging dressing sieve is arranged at the output end of described discharging bin.
9. ceramic powder comminutor according to claim 1 it is characterised in that：Described prilling granulator is horizontal granulation dress
Put；Also include leaning device, described leaning device is arranged at the bottom of described prilling granulator, make described in described leaning device driving
Grain device tilts, and angle of inclination is 3 °～10 °.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620521509.5U CN205969404U (en) | 2016-05-31 | 2016-05-31 | Ceramic powder granulator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620521509.5U CN205969404U (en) | 2016-05-31 | 2016-05-31 | Ceramic powder granulator |
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| Publication Number | Publication Date |
|---|---|
| CN205969404U true CN205969404U (en) | 2017-02-22 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620521509.5U Active CN205969404U (en) | 2016-05-31 | 2016-05-31 | Ceramic powder granulator |
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| CN (1) | CN205969404U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108751847A (en) * | 2018-06-16 | 2018-11-06 | 山东新大地环保建材有限公司 | Gravity flowing levelling mortar based on slag ball and construction method |
-
2016
- 2016-05-31 CN CN201620521509.5U patent/CN205969404U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108751847A (en) * | 2018-06-16 | 2018-11-06 | 山东新大地环保建材有限公司 | Gravity flowing levelling mortar based on slag ball and construction method |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20170417 Address after: 528031 Chancheng, Foshan District, Jiangwan, No. three, No., layer 8, layer two Co-patentee after: Guangdong Dongpeng Holdings Co., Ltd. Patentee after: Foshan Dongpeng Ceramic Co., Ltd. Co-patentee after: Zibo Kapuer Ceramics Co., Ltd. Co-patentee after: Qingyuan Nafuna Ceramics Co.,Ltd. Address before: 528031 Chancheng, Foshan District, Jiangwan, No. three, No., layer 8, layer two Co-patentee before: Guangdong Dongpeng Holdings Co., Ltd. Patentee before: Foshan Dongpeng Ceramic Co., Ltd. Co-patentee before: Zibo Kapuer Ceramics Co., Ltd. Co-patentee before: Qingyuan Nafuna Ceramics Co.,Ltd. Co-patentee before: Guangdong Dongpeng Ceramic Co., Ltd. |
|
| TR01 | Transfer of patent right |