CN2407826Y - Wetting pellitizer - Google Patents
Wetting pellitizer Download PDFInfo
- Publication number
- CN2407826Y CN2407826Y CN 00204902 CN00204902U CN2407826Y CN 2407826 Y CN2407826 Y CN 2407826Y CN 00204902 CN00204902 CN 00204902 CN 00204902 U CN00204902 U CN 00204902U CN 2407826 Y CN2407826 Y CN 2407826Y
- Authority
- CN
- China
- Prior art keywords
- humidification
- stationary ring
- tower body
- rotating disk
- prilling granulator
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
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- Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
Abstract
The utility model discloses a humidifying granulating device which comprises a powder atomizing device, a humidifying tower body, a humidizer nozzle, a rotary disk and a static ring, wherein, the powder atomizing device is positioned at the upper part of the humidifying tower body in which the humidizer nozzle is positioned; the rotary disc is arranged in the static ring, and rotates regarding the shaft center of the rotary disc and the static ring as a shaft; the rotary disc and the static ring are assembled to form a centrifugal granule strengthening device arranged at the lower part of the humidifying tower body. The utility model has the advantages of simple and reasonable structure, low investment, high granular intensity of products, reasonable grain composition, easy adjustment of granularity and intensity, good fluidity, high production efficiency, and low power consumption and environmental pollution at the time of production.
Description
The utility model relates to a kind of prilling granulator, particularly a kind of humidification prilling granulator.
At present, the preparation of grain products generally adopts wet spray drying-granulating equipment, humidification to stir non-slurry pelletizing equipment, the broken equipment of stone roller (squeezing) crush-cutting, periodicity centrifugal granulating equipment etc.The wet spray drying-granulating, the energy consumption height, investment is big; The product particle intensity that humidification stirs non-slurry pelletizing is low, particle surface is coarse, flowability is poor, dust pollution is serious when producing; The broken grain products flowability of stone roller (squeezing) crush-cutting is poor, production efficiency is low; Periodically centrifugal granulating can not be produced continuously, production capacity is little, production efficiency is low, accommodation is little.
The purpose of this utility model just is to overcome weak point of the prior art, provide a kind of simple and reasonable, energy consumption is low, investment is little, granule strength is high, grain composition is reasonable, the easily adjustment of granularity intensity, good fluidity, production efficiency height, applied widely, can produce continuously, the humidification prilling granulator of non-environmental-pollution.
The purpose of this utility model is to realize like this, it comprises: powder atomising device, humidification tower body, humidizer nozzle, rotating disk, stationary ring, the powder atomising device is positioned at the top of humidification tower body, the humidizer nozzle is positioned at the inside of humidification tower body, rotating disk and stationary ring are with coaxial setting, rotating disk, stationary ring fit together and constitute the bottom that the centrifugal pellet intensifying device is installed in the humidification tower body, and the stationary ring side is provided with discharging opening, and the powder atomising device is provided with feeding mouth.
The purpose of this utility model also can realize by following technical measures, the humidizer nozzle can a plurality ofly be provided with, discharging opening is provided with the discharging opening adjusting device, the powder atomising device is provided with the high-pressure blast inlet, be provided with the spirality air devider in the powder atomising device, the stationary ring bottom is provided with the pressed gas inlet, be provided with the gap between stationary ring and rotating disk, rotating disk top is provided with the horizontal material scraper of radial motion, the stationary ring inwall is provided with the side material scraper, the external side of conditioning Tower is provided with hopper wall vibrator, and side material scraper, rotating disk link to each other with transmission device respectively with hollow shaft by interior axle.
Compared with prior art, the utlity model has following advantage:
1, simple and reasonable, investment is little, energy consumption is low;
2, product particle intensity height, grain composition are rationally, granularity intensity easily adjusts, good fluidity;
3, use a small amount of humidizer can realize granulation.Promptly save humidizer and make evaporation capacity minimizing in the follow-up dry run again;
4, can produce continuously, the production efficiency height, constant product quality, applied widely;
Non-environmental-pollution when 5, producing, and realize control automatically easily.
Accompanying drawing and drawing explanation
Fig. 1 is the utility model humidification prilling granulator structural representation
Fig. 2 is the utility model conditioning Tower structural representation
Fig. 3 is the utility model centrifugal pellet intensifying device structural representation
Fig. 4 is the utility model powder atomising device structural representation front view
Fig. 5 is the utility model powder atomising device structural representation vertical view
Below in conjunction with drawings and Examples in detail the utility model is described in detail, it comprises: powder atomising device 1, humidification tower body 2, humidizer nozzle 3, rotating disk 4, stationary ring 5, powder atomising device 1 is positioned at the top of humidification tower body, humidizer nozzle 3 is positioned at the inside of humidification tower body 2, rotating disk 4 and stationary ring 5 are with coaxial setting, rotating disk 4, stationary ring 5 fits together and constitutes the bottom that the centrifugal pellet intensifying device is installed in humidification tower body 2, stationary ring 5 sides are provided with discharging opening 10, powder atomising device 1 is provided with feeding mouth 14, rotating disk 4 tops are provided with horizontal material scraper 6, stationary ring 5 inwalls are provided with side material scraper 11, stationary ring 5 bottoms are provided with pressed gas inlet 9, side material scraper 11, rotating disk 4 links to each other with transmission device 7 respectively with hollow shaft 8 by interior 18, the powder atomising device is provided with high-pressure blast inlet 13, discharging opening 17, be provided with spirality air devider 16 in the powder atomising device 1, the outside of humidification tower body 2 is provided with hopper wall vibrator 12, humidizer nozzle 3 can be provided with a plurality of, discharging opening 10 is provided with discharging opening adjusting device 15, working mechanism of the present utility model is, the powder of certain fineness enters powder atomising device 1 through feeding mouth 14, high-pressure blast also enters powder atomising device 1 by high-pressure blast inlet 13 simultaneously, powder is spraying with vaporific discharging opening 17 from powder atomising device 1 after spirality air devider 16 quickens to disperse under the high pressure wind action, in humidification tower body 2, form the atomizing powder that vortex falls, the atomizing powder is in humidification tower body 2 inside vortex dropping process, evenly mix and preliminary granulating with the even dispersion humidizer of humidizer nozzle 3 ejections, can guarantee all even granulating rate of humidification from the even dispersion humidizer of humidizer nozzle 3 ejections, the material of humidification and preliminary granulating drops on the rotating disk 4 of centrifugal pellet intensifying device through the outlet of humidification tower body 2, rotating disk 4 rotates with certain speed under the drive of transmission device 7, the powder of humidification and preliminary granulating is under the effect of centrifugal force and frictional force, on the rotating disk 4 and on stationary ring 5 inwalls repeatedly vortex roll, particle is further produced and reinforcement, and grain products constantly overflows from centrifugal pellet intensifying device discharging opening 10.Rotating disk 4 forms seal cavity with stationary ring 5 in the bottom, have certain pressure gas and enter the gap that the back forms by rotating disk 4 and stationary ring 5 from the bottom, be used for the sealing in described gap, prevent that powder from leaking down from the gap, rotating disk 4 is provided with the horizontal material scraper 6 of radial motion, stationary ring 5 inwalls are installed the side material scraper 11 that moves along the inwall circumferencial direction, material sticks to rotating disk 4 or stationary ring 5 after being used to prevent humidification, the rotating speed of rotating disk 4 can be regulated continuously by its transmission device 7, discharging opening 10 on the stationary ring 5 can be adjusted upper-lower position by adjusting device 15, to adapt to the grain products of different material and generation varying strength or granularity, hopper wall vibrator 12 is installed on the humidification granulation tower body 2, the powder that prevents humidification adheres on humidification granulation tower body 2, a plurality of hopper wall vibrators intermittently, alternately vibration, the life-span of improving humidification granulation tower body 2.
Claims (8)
1, a kind of humidification prilling granulator, it comprises: powder atomising device, humidification tower body, humidizer nozzle, rotating disk, stationary ring, it is characterized in that: the powder atomising device is positioned at the top of humidification tower body, the humidizer nozzle is positioned at the inside of humidification tower body, rotating disk and stationary ring are with coaxial setting, rotating disk, stationary ring fit together and constitute the bottom that the centrifugal pellet intensifying device is installed in the humidification tower body, and the stationary ring side is provided with discharging opening, and the powder atomising device is provided with feeding mouth.
2, humidification prilling granulator according to claim 1, it is characterized in that: the humidizer nozzle can be provided with a plurality of.
3, humidification prilling granulator according to claim 1 is characterized in that: the stationary ring bottom is provided with the pressed gas inlet.
4, humidification prilling granulator according to claim 1, it is characterized in that: discharging opening is provided with the discharging opening adjusting device.
5, humidification prilling granulator according to claim 1 is characterized in that: be provided with the spirality air devider in the powder atomising device.
6, humidification prilling granulator according to claim 1 is characterized in that: rotating disk top is provided with the horizontal material scraper of radial motion, and the stationary ring inwall is provided with the side material scraper that moves along the inwall circumferencial direction.
7, humidification prilling granulator according to claim 1 is characterized in that: the external side of conditioning Tower is provided with hopper wall vibrator.
8, humidification prilling granulator according to claim 1 is characterized in that: side material scraper, rotating disk link to each other with transmission device respectively with hollow shaft by interior axle.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 00204902 CN2407826Y (en) | 2000-03-03 | 2000-03-03 | Wetting pellitizer |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 00204902 CN2407826Y (en) | 2000-03-03 | 2000-03-03 | Wetting pellitizer |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN2407826Y true CN2407826Y (en) | 2000-11-29 |
Family
ID=33573170
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 00204902 Expired - Fee Related CN2407826Y (en) | 2000-03-03 | 2000-03-03 | Wetting pellitizer |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN2407826Y (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100345618C (en) * | 2005-04-29 | 2007-10-31 | 尹贵玉 | Continuous powdery humidifying contrifugal granulator and process thereof |
| CN103752213A (en) * | 2014-01-06 | 2014-04-30 | 咸阳陶瓷研究设计院 | Device suitable for humidifying and granulating dry powder |
| CN107930530A (en) * | 2017-12-08 | 2018-04-20 | 咸阳陶瓷研究设计院有限公司 | A kind of ceramic raw material suspension Granulation Equipments |
| CN109603679A (en) * | 2018-12-27 | 2019-04-12 | 咸阳陶瓷研究设计院有限公司 | A kind of ceramic powder humidification Granulation Equipments |
-
2000
- 2000-03-03 CN CN 00204902 patent/CN2407826Y/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100345618C (en) * | 2005-04-29 | 2007-10-31 | 尹贵玉 | Continuous powdery humidifying contrifugal granulator and process thereof |
| CN103752213A (en) * | 2014-01-06 | 2014-04-30 | 咸阳陶瓷研究设计院 | Device suitable for humidifying and granulating dry powder |
| CN107930530A (en) * | 2017-12-08 | 2018-04-20 | 咸阳陶瓷研究设计院有限公司 | A kind of ceramic raw material suspension Granulation Equipments |
| CN109603679A (en) * | 2018-12-27 | 2019-04-12 | 咸阳陶瓷研究设计院有限公司 | A kind of ceramic powder humidification Granulation Equipments |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C19 | Lapse of patent right due to non-payment of the annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |