CN205379863U - Be applied to ceramic powder's continuous type granulator - Google Patents
Be applied to ceramic powder's continuous type granulator Download PDFInfo
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- CN205379863U CN205379863U CN201620130905.5U CN201620130905U CN205379863U CN 205379863 U CN205379863 U CN 205379863U CN 201620130905 U CN201620130905 U CN 201620130905U CN 205379863 U CN205379863 U CN 205379863U
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- granulation tank
- shaft
- granulation
- ceramic powder
- comminutor
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Abstract
The utility model relates to a be applied to ceramic powder's continuous type granulator, including the granulation jar, the granulation jar is installed on adjustable base, the upper portion of granulation jar is equipped with the nucleation room, and the indoor (mixing) shaft that is equipped with of nucleation is equipped with a plurality of groups along its axial on and stirs the tooth, still is equipped with atomizing nozzle on the (mixing) shaft, atomizing nozzle and the axial alternate setting of stirring tooth along the (mixing) shaft, atomizing nozzle is connected with the raceway, is equipped with atomizing water control valve on the raceway and prevents stifled device, still include the continuous feed device that links up with the pan feeding mouth of granulation jar, the lower part of granulation jar is equipped with the balling -up room, the indoor slewer that is equipped with of balling -up, and the last gyration dish that is equipped with of slewer is equipped with the discharge gate on the jar body of granulation jar, installing on the inside wall of granulation jar and scraping the flitch, the gyration dish is located between the jar body of scraping flitch and granulation jar. The utility model discloses can realize continuous granulation, it is efficient, the granule moisture content is controllable, and control accuracy is high, the energy consumption is low, compact structure, with low costs.
Description
Technical field
This utility model relates to a kind of continuous way comminutor being applied to ceramic powder.
Background technology
In current ceramic industry, because there is the molding compression ratio problem of the fully dispersed sex chromosome mosaicism of true granule, false granule in non-slurry pelletizing powder-making technique, make powder granule grating prepared by non-slurry pelletizing be difficult to reach the requirement of blank grain composition (20-80 order) of brick machine, and moisture content is difficult to control to.Therefore ceramic industry is generally along with ball milling-spraying wet granulation powder-making technique, and wet granulation powder-making technique exists energy consumption height, cost is expensive, pollute the problems such as big, the energy-saving consumption-reducing policy that significant departure country advocates；Additionally existing granulating disc belongs to interval pelletize, production also has a small amount of application, but interval pelletize exists technique controlling difficulty height, be interrupted production and the deficiencies such as yield can not be greatly improved.Therefore a kind of continuous granulation machine of utility model has become as the inexorable trend of industry development.
Utility model content
Technical problem to be solved in the utility model is to provide that energy consumption is low, cost is low, the convenient granule moisture content that controls, and can continuous prodution, production efficiency is high, produces a kind of continuous way comminutor being applied to ceramic powder that gained granular size is controlled.
In order to solve above-mentioned technical problem, the technical solution of the utility model is: a kind of continuous way comminutor being applied to ceramic powder, and including granulation tank, described granulation tank is installed on the adjustable setting at the inclination angle of the axially opposing horizontal plane that can adjust described granulation tank；The top of described granulation tank is provided with nucleation room, and described nucleation indoor are provided with shaft, and described shaft is connected to the first driving device driving described shaft to rotate；Described shaft is axially arranged with some groups of stirrer gears, the interlaced setting of two adjacent groups stirrer gear along it；Being additionally provided with atomizer on described shaft, described atomizer is connected to water-supply-pipe, and described water-supply-pipe is provided with atomization water control valve and the anti-block apparatus preventing described atomizer from blocking；Described atomizer and described stirrer gear are along the axial alternate setting of described shaft；Also including continuous feeding, described continuous feeding is connected with the feeding mouth being located at described granulation tank top；The bottom of described granulation tank is provided with balling-up room, and described balling-up room connects with described nucleation room, and described balling-up indoor are provided with slewing equipment, and described slewing equipment is connected to the second driving device driving its rotation；Described slewing equipment is provided with rotary disk, and the medial wall of described granulation tank is provided with material scraping plate and adjusts seat, and described material scraping plate adjustment seat is provided with material scraping plate, and described rotary disk is between the tank body of described material scraping plate and described granulation tank；Described granulation tank is provided with discharging opening, and described discharging opening is positioned at the upside of described rotary disk.
As preferred technical scheme, described first driving device includes driving motor, the output shaft of described driving motor is provided with driving gear, described shaft is through and out the upper wall of described granulation tank, described shaft stretches out one end of described granulation tank and is provided with travelling gear, and described travelling gear and described driving gear engage each other.
As preferred technical scheme, described second driving device includes drive motor, described drive motor is connected to adjustable reductor, is provided with shaft coupling between described drive motor and described adjustable reductor, and described slewing equipment is arranged on the output shaft of described adjustable reductor.
As preferred technical scheme, described atomizer is spiral nozzle；Described anti-block apparatus includes air compressor machine, and described air compressor machine connects with the described water-supply-pipe between described atomization water control valve and described atomizer, is provided with pressure-air and controls valve between described air compressor machine and described water-supply-pipe.
As preferred technical scheme, described water-supply-pipe is connected to water pump, and described anti-block apparatus also includes the filter of the outlet of water inlet and the described water pump being arranged at described water pump.
As preferred technical scheme, also include PID controller, described discharging opening is provided with humidity sensor, described continuous feeding is belt conveyor, described belt conveyor is provided with belt conveyer scale, described water-supply-pipe is provided with effusion meter, and described effusion meter, described belt conveyer scale, described humidity sensor, described atomization water control valve and described anti-block apparatus electrically connect with described PID controller.
As preferred technical scheme, described adjustable setting includes the articulated jib and the regulating arm that are oppositely arranged, and one end of described articulated jib is fixed in described granulation tank, and the other end of described articulated jib is with to be arranged on ground hinged seat hinged；Described regulating arm includes fixing seat, is provided with spiral lifting mechanism between described fixing seat and described granulation tank.
As preferred technical scheme, described spiral lifting mechanism includes the drive rod being rotatably installed on described fixing seat, described drive rod is threaded slide block, it is provided with auxiliary rod between described slide block and described granulation tank, described auxiliary rod one end is hinged with described granulation tank, and the other end of described auxiliary rod is fixed on described slide block；One end of described drive rod is fixed with rotary handle by bearing pin.
As preferred technical scheme, the two ends of described material scraping plate are provided with the installation end of cylinder, described material scraping plate adjustment seat is provided with the installation cavity adapted with described installation end profile, the outer wall of described installation cavity is provided with through the locking hole of described outer wall, in described locking hole, is provided with the puller bolt holding out against described installation end.
Operation principle of the present utility model is: powder enters nucleation room through continuous feeding, and the stirrer gear entered on the agitated axle of powder of nucleation room is broken up, and in suspended state, relies on action of gravity, and powder is flow regime；Open atomization water control valve, high-pressure atomization water is uniformly ejected between powder through atomizer, the mutual coagulation granulating of powder body, particle is fallen on rotary disk, under the drive of drive motor, slewing equipment drives rotary disk at the uniform velocity turning round, and contacting with each other between particle and collide in turning course gradually grows up, material time length in rotary disk can be controlled by adjusting the rotating speed of adjustable base and rotary disk, different size of grain products will be obtained.Different according to powders property, control the revolution of rotary disk within the scope of 20r/min-40r/min.
Owing to adopting technique scheme, this utility model has the advantage that
1) this utility model is capable of continuous charging, continuous granulation, improves production capacity, and granulation efficiency is high；
2) changing the inclination angle of granulation tank and control the rotating speed of rotary disk and can control granular size by adjusting adjustable setting, grain composition is controlled；
3) discharging opening of the present utility model is provided with humidity sensor, and PID controller can adjust the amount of water of atomization water control valve automatically according to the data of humidity sensor, belt conveyer scale and effusion meter, and the granule moisture content of production is controlled, and control accuracy is high；
4) this utility model compact conformation floor space is few, and cost is low；Energy consumption is low, noise is little.
Accompanying drawing explanation
In order to be illustrated more clearly that this utility model embodiment or technical scheme of the prior art, the accompanying drawing used required in embodiment or description of the prior art will be briefly described below, apparently, accompanying drawing in the following describes is only embodiments more of the present utility model, for those of ordinary skill in the art, under the premise not paying creative work, it is also possible to obtain other accompanying drawing according to these accompanying drawings.
Fig. 1 is structural representation of the present utility model；
Fig. 2 is the structural representation of adjustment seat in this utility model embodiment；
Fig. 3 is the scheme of installation of material scraping plate in this utility model embodiment；
Fig. 4 is the zoomed-in view of a-quadrant in Fig. 3.
In figure: 1-output shaft；2-slewing equipment；3-rotary disk；4-material scraping plate；5-balling-up room；6-nucleation room；7-water pump；8-filter；9-continuous feeding；10-feeding mouth；11-is atomized water control valve；12-pressure-air controls valve；13-air compressor machine；14-travelling gear；15-driving motor；16-granulation tank；17-shaft；18-atomizer；19-stirrer gear；20-discharging opening；21-drive motor；22-shaft coupling；The adjustable reductor of 23-；24-adjustable setting；25-fixes seat；26-slide block；27-drive rod；28-auxiliary rod；29-hinged seat；30-articulated jib；31-material scraping plate adjusts seat；32-installation cavity；33-locking hole；34-installation end.
Detailed description of the invention
Below in conjunction with the accompanying drawing in this utility model embodiment, the technical scheme in this utility model embodiment is clearly and completely described, it is clear that described embodiment is only a part of embodiment of this utility model, rather than whole embodiments.Based on the embodiment in this utility model, the every other embodiment that those of ordinary skill in the art obtain under not making creative work premise, broadly fall into the scope of this utility model protection.
As it is shown in figure 1, a kind of continuous way comminutor being applied to ceramic powder, including granulation tank 16, described granulation tank 16 includes upper shell and lower house, described upper shell and described lower house and passes through Flange joint.Upper shell and lower house are dismantled and assembled, it is simple to later stage maintenance and maintenance.Described granulation tank 16 is installed on the adjustable setting 24 at the inclination angle of the axially opposing horizontal plane that can adjust described granulation tank 16.As in figure 2 it is shown, described adjustable setting 24 includes the articulated jib 30 and the regulating arm that are oppositely arranged.One end of described articulated jib 30 is fixed in described granulation tank 16, and the other end of described articulated jib 30 is with to be arranged on ground hinged seat 29 hinged.Described regulating arm includes fixing seat 25, is provided with spiral lifting mechanism between described fixing seat 25 and described granulation tank 16.Described spiral lifting mechanism includes the drive rod 27 being rotatably installed on described fixing seat 25, described drive rod 27 is threaded slide block 26, it is provided with auxiliary rod 28 between described slide block 26 and described granulation tank 16, described auxiliary rod 28 one end is hinged with described granulation tank 16, and the other end of described auxiliary rod 28 is fixed on described slide block 26.One end of described drive rod 27 is fixed with rotary handle by bearing pin, it is simple to screw rod 27 is adjusted.By rotating drive rod 27, slide block 26 can axially moving up and down along drive rod 27, owing to articulated jib 30 cannot move up and down, can only rotate, therefore select the inclination angle of axially opposing horizontal plane of drive rod 27 scalable granulation tank 16.Can controlling granule molding time in granulation tank 16 by changing the inclination angle of granulation tank 16, the convenient size controlling granule, grain composition is controlled.
As it is shown in figure 1, the top of described granulation tank 16 is provided with nucleation room 6, being provided with shaft 17 in described nucleation room 6, described shaft 17 is connected to the first driving device driving described shaft 17 to rotate.Described first driving device includes driving motor 15, the output shaft of described driving motor 15 is provided with driving gear, described shaft 17 is through and out the upper wall of described granulation tank 16, described shaft 17 stretches out one end of described granulation tank 16 and is provided with travelling gear 14, and described travelling gear 14 engages each other with described driving gear.Described shaft 17 is axially arranged with some groups of stirrer gears 19, the interlaced setting of two adjacent groups stirrer gear 19 along it.Preferably, described shaft 17 is provided with three groups of stirrer gears 19.Described shaft 17 is additionally provided with atomizer 18, described atomizer 18 and the alternate setting of described stirrer gear 19.Described atomizer 18 is spiral nozzle, and described atomizer 18 is connected to water-supply-pipe, and described water-supply-pipe is provided with effusion meter, atomization water control valve 11 and the anti-block apparatus preventing described atomizer 18 from blocking.Described anti-block apparatus includes air compressor machine 13, and described air compressor machine 13 connects with the described water-supply-pipe between described atomization water control valve 11 and described atomizer 18, is provided with pressure-air and controls valve 12 between described air compressor machine 13 and described water-supply-pipe.Material in nucleation room 6 is caused to the blocking of atomizer 18, then can be interrupted control atomization water control valve 11 and close and open pressure-air control valve 12, temporary impact nozzle, dredging.Additionally atomizer 18 adopts market to commonly use spiral nozzle, has both added atomized water spouting velocity, can effectively prevent again blocking.Described water-supply-pipe is connected to water pump 7, it is preferred that water inlet and outlet at the water pump 7 being connected with water-supply-pipe arrange filter 8, it is ensured that the water needed for atomization reaches requirement.
Also including continuous feeding 9, described continuous feeding 9 is belt conveyor, and described belt conveyor is provided with belt conveyer scale.Described continuous feeding 9 is connected feeding with the feeding mouth 10 being located at described granulation tank 16 top.The bottom of described granulation tank 16 is provided with balling-up room 5, and described balling-up room 5 connects with described nucleation room 6.Being provided with slewing equipment 2 in described balling-up room 5, described slewing equipment 2 is connected to the second driving device driving its rotation.Described second driving device includes drive motor 21, and described drive motor 21 is connected to adjustable reductor 23, is provided with shaft coupling 22 between described drive motor 21 and described adjustable reductor 23.Described slewing equipment 2 is arranged on the output shaft 1 of described adjustable reductor 23.Described slewing equipment 2 is provided with rotary disk 3, and described granulation tank 16 is provided with discharging opening 20, and described discharging opening 20 is positioned at the upside of described rotary disk 3.The medial wall of described granulation tank 16 is provided with material scraping plate and adjusts seat 31, and described material scraping plate adjustment seat 31 is provided with material scraping plate 4, and described rotary disk 3, between described material scraping plate 4 and the tank body of described granulation tank 16, is prevented effectively from shaped granule and sticks on rotary disk 3.As shown in Figure 3 and Figure 4, the two ends of described material scraping plate 4 are provided with the installation end 34 of cylinder, described material scraping plate adjustment seat 31 is provided with the installation cavity 32 adapted with described installation end profile, the outer wall of described installation cavity 32 is provided with through the locking hole 33 of described outer wall, is provided with, in described locking hole 33, the puller bolt holding out against described installation end 34.For the requirement of different technique and granular size, can control in conjunction with the rotating speed of rotary disk 3 and the inclination angle of adjustable setting 24, material scraping plate 4 corner to reach production requirement.
A kind of continuous way comminutor being applied to ceramic powder also includes PID controller; described discharging opening 20 is provided with humidity sensor, and described belt conveyer scale, described humidity sensor, pressure-air control valve 12 and described atomization water control valve 11 electrically connects with described PID controller.Control principle is: PID controller can receive the signal of belt conveyer scale and effusion meter, and whether up to standard adjustment of moisture content feeding back granule automatically according to humidity sensor is atomized water control valve 11 inflow；Meanwhile, PID controller also controls pressure-air and controls valve 12 and the unlatching of atomization water control valve 11, to avoid atomizer to block.
Apply the prilling of above-mentioned a kind of continuous way comminutor being applied to ceramic powder, comprise the following steps:
Step one: starting shaft, the rotating speed of shaft is 50r/min-200r/min；
Step 2: start continuous feeding, continuous feeding is through feeding mouth continuously to granulation tank feed, and stirrer gear stirring powder is fluidized suspension state；
Step 3: open water pump, shaft opens atomization water control valve while rotating, atomizer ejection water smoke, the amount of water of atomization water control valve accounts for powder amount and the 12-14% of amount of water summation；
Step 4: open slewing equipment, the rotating speed controlling rotary disk is 20r/min-40r/min, and molding granule up to standard flows out from discharging opening through rotary disk, and particle diameter is 20 order-80 orders.
This utility model is capable of continuous granulation, improves production capacity, and efficiency is high；Granule moisture content is controlled, and control accuracy is high；Energy consumption is low, noise is little, and compact conformation, floor space are few, and cost is low.
The foregoing is only preferred embodiment of the present utility model; not in order to limit this utility model; all within spirit of the present utility model and principle, any amendment of making, equivalent replacement, improvement etc., should be included within protection domain of the present utility model.
Claims (9)
1. the continuous way comminutor being applied to ceramic powder, it is characterised in that: including granulation tank, described granulation tank is installed on the adjustable setting at the inclination angle of the axially opposing horizontal plane that can adjust described granulation tank；The top of described granulation tank is provided with nucleation room, and described nucleation indoor are provided with shaft, and described shaft is connected to the first driving device driving described shaft to rotate；Described shaft is axially arranged with some groups of stirrer gears, the interlaced setting of two adjacent groups stirrer gear along it；Being additionally provided with atomizer on described shaft, described atomizer is connected to water-supply-pipe, and described water-supply-pipe is provided with atomization water control valve and the anti-block apparatus preventing described atomizer from blocking；Described atomizer and described stirrer gear are along the axial alternate setting of described shaft；Also including continuous feeding, described continuous feeding is connected with the feeding mouth being located at described granulation tank top；The bottom of described granulation tank is provided with balling-up room, and described balling-up room connects with described nucleation room, and described balling-up indoor are provided with slewing equipment, and described slewing equipment is connected to the second driving device driving its rotation；Described slewing equipment is provided with rotary disk, and the medial wall of described granulation tank is provided with material scraping plate and adjusts seat, and described material scraping plate adjustment seat is provided with material scraping plate, and described rotary disk is between the tank body of described material scraping plate and described granulation tank；Described granulation tank is provided with discharging opening, and described discharging opening is positioned at the upside of described rotary disk.
2. a kind of continuous way comminutor being applied to ceramic powder described in claim 1; it is characterized in that: described first driving device includes driving motor; the output shaft of described driving motor is provided with driving gear; described shaft is through and out the upper wall of described granulation tank; described shaft stretches out one end of described granulation tank and is provided with travelling gear, and described travelling gear and described driving gear engage each other.
3. a kind of continuous way comminutor being applied to ceramic powder described in claim 1; it is characterized in that: described second driving device includes drive motor; described drive motor is connected to adjustable reductor; being provided with shaft coupling between described drive motor and described adjustable reductor, described slewing equipment is arranged on the output shaft of described adjustable reductor.
4. a kind of continuous way comminutor being applied to ceramic powder described in claim 1, it is characterised in that: described atomizer is spiral nozzle；Described anti-block apparatus includes air compressor machine, and described air compressor machine connects with the described water-supply-pipe between described atomization water control valve and described atomizer, is provided with pressure-air and controls valve between described air compressor machine and described water-supply-pipe.
5. a kind of continuous way comminutor being applied to ceramic powder described in claim 4, it is characterised in that: described water-supply-pipe is connected to water pump, and described anti-block apparatus also includes the filter of the outlet of water inlet and the described water pump being arranged at described water pump.
6. a kind of continuous way comminutor being applied to ceramic powder described in claim 1; it is characterized in that: also include PID controller; described discharging opening is provided with humidity sensor; described continuous feeding is belt conveyor; described belt conveyor is provided with belt conveyer scale; described water-supply-pipe is provided with effusion meter, and described effusion meter, described belt conveyer scale, described humidity sensor, described atomization water control valve and described anti-block apparatus electrically connect with described PID controller.
7. a kind of continuous way comminutor being applied to ceramic powder described in claim 1; it is characterized in that: described adjustable setting includes the articulated jib and the regulating arm that are oppositely arranged; one end of described articulated jib is fixed in described granulation tank, and the other end of described articulated jib is with to be arranged on ground hinged seat hinged；Described regulating arm includes fixing seat, is provided with spiral lifting mechanism between described fixing seat and described granulation tank.
8. a kind of continuous way comminutor being applied to ceramic powder described in claim 7; it is characterized in that: described spiral lifting mechanism includes the drive rod being rotatably installed on described fixing seat; described drive rod is threaded slide block; it is provided with auxiliary rod between described slide block and described granulation tank; described auxiliary rod one end is hinged with described granulation tank, and the other end of described auxiliary rod is fixed on described slide block；One end of described drive rod is fixed with rotary handle by bearing pin.
9. a kind of continuous way comminutor being applied to ceramic powder described in claim 1; it is characterized in that: the two ends of described material scraping plate are provided with the installation end of cylinder; described material scraping plate adjustment seat is provided with the installation cavity adapted with described installation end profile; the outer wall of described installation cavity is provided with through the locking hole of described outer wall, in described locking hole, is provided with the puller bolt holding out against described installation end.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620130905.5U CN205379863U (en) | 2016-02-20 | 2016-02-20 | Be applied to ceramic powder's continuous type granulator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620130905.5U CN205379863U (en) | 2016-02-20 | 2016-02-20 | Be applied to ceramic powder's continuous type granulator |
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| Publication Number | Publication Date |
|---|---|
| CN205379863U true CN205379863U (en) | 2016-07-13 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620130905.5U Expired - Fee Related CN205379863U (en) | 2016-02-20 | 2016-02-20 | Be applied to ceramic powder's continuous type granulator |
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| CN (1) | CN205379863U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105536644A (en) * | 2016-02-20 | 2016-05-04 | 山东义科节能科技有限公司 | Continuous prilling machine applied to ceramic powder and prilling technology thereof |
| CN110882657A (en) * | 2019-11-29 | 2020-03-17 | 景德镇陶瓷大学 | Spiral type silicon nitride powder dry-wet granulation intelligent device with concave-convex elliptic cylinder combined structure |
-
2016
- 2016-02-20 CN CN201620130905.5U patent/CN205379863U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105536644A (en) * | 2016-02-20 | 2016-05-04 | 山东义科节能科技有限公司 | Continuous prilling machine applied to ceramic powder and prilling technology thereof |
| CN110882657A (en) * | 2019-11-29 | 2020-03-17 | 景德镇陶瓷大学 | Spiral type silicon nitride powder dry-wet granulation intelligent device with concave-convex elliptic cylinder combined structure |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20160713 |
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| CF01 | Termination of patent right due to non-payment of annual fee |