CN204285951U - The fluidized bed dryer that a kind of material not easily coheres - Google Patents
The fluidized bed dryer that a kind of material not easily coheres Download PDFInfo
- Publication number
- CN204285951U CN204285951U CN201420729661.3U CN201420729661U CN204285951U CN 204285951 U CN204285951 U CN 204285951U CN 201420729661 U CN201420729661 U CN 201420729661U CN 204285951 U CN204285951 U CN 204285951U
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- house
- boiling
- air intake
- intake plate
- sidewall
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Abstract
The utility model relates to the fluidized bed dryer that a kind of material not easily coheres.It comprises boiling-house, and the top of boiling-house is connected with discharge chamber, and gas outlet is arranged at the top of discharge chamber, and gas outlet is connected by the air inlet of pipeline with a cyclone separator.There is into horizontally disposed air intake plate in the inner chamber of boiling-house, air intake plate is evenly equipped with through hole.A sidewall upper feeding mouth of boiling-house, another boiling-house sidewall relative with this sidewall has material outlet, and material outlet is connected with discharge nozzle, and charging aperture is positioned at the top of air intake plate, and the lower edge of material outlet and the upper face of air intake plate flush.Be positioned on the boiling-house sidewall below air intake plate and have air inlet, be connected with blast pipe outside air inlet, blast pipe be disposed with blower fan, filter and heater.Be characterized in that the upper face of air intake plate is evenly equipped with in the vertical shock post arranged.This fluidized bed dryer, when dried material, can avoid and occur dry incomplete problem because material coheres.
Description
Technical field
The utility model relates to a kind of drying device, is the fluidized bed dryer that a kind of material not easily coheres specifically.
Background technology
Fluid bed dryer is widely used in the industries such as agricultural, chemical industry, biology because of advantages such as its rate of drying is fast, homogeneous temperature, adjustments easy to control.
At present, the fluidized bed dryer used in industry comprises boiling-house, and the top of described boiling-house is connected with discharge chamber, and the inner chamber of discharge chamber communicates with the inner chamber of boiling-house, gas outlet is arranged at the top of discharge chamber, and gas outlet is connected by the air inlet of pipeline with a cyclone separator.There is into horizontally disposed air intake plate in the inner chamber of described boiling-house, in being tightly connected between the surrounding of air intake plate and the madial wall of boiling-house, air intake plate being evenly equipped with through hole.A sidewall upper feeding mouth of described boiling-house, another boiling-house sidewall relative with this sidewall there is material outlet, material outlet is connected with discharge nozzle, and described charging aperture is positioned at the top of air intake plate, and the lower edge of described material outlet and the upper face of air intake plate flush.Be positioned on the boiling-house sidewall below air intake plate and have air inlet, be connected with blast pipe outside air inlet, blast pipe be disposed with blower fan, filter and heater.Traditional fluidized bed dryer only only has fluidized drying function, when occurring that material coheres, can be excessive because of the material particles after cohering, and cause dry incomplete phenomenon.
Utility model content
The technical problems to be solved in the utility model is to provide the fluidized bed dryer that a kind of material not easily coheres, and this fluidized bed dryer, when dried material, can avoid and occur dry incomplete problem because material coheres.
For solving the problem, provide following technical scheme:
The fluidized bed dryer that material of the present utility model not easily coheres, comprise boiling-house, the top of described boiling-house is connected with discharge chamber, and the inner chamber of discharge chamber communicates with the inner chamber of boiling-house, gas outlet is arranged at the top of discharge chamber, and gas outlet is connected by the air inlet of pipeline with a cyclone separator.There is into horizontally disposed air intake plate in the inner chamber of described boiling-house, in being tightly connected between the surrounding of air intake plate and the madial wall of boiling-house, air intake plate being evenly equipped with through hole.A sidewall upper feeding mouth of described boiling-house, another boiling-house sidewall relative with this sidewall there is material outlet, material outlet is connected with discharge nozzle, and described charging aperture is positioned at the top of air intake plate, and the lower edge of described material outlet and the upper face of air intake plate flush.Be positioned on the boiling-house sidewall below air intake plate and have air inlet, be connected with blast pipe outside air inlet, blast pipe be disposed with blower fan, filter and heater.Be characterized in that the upper face of described air intake plate is evenly equipped with in the vertical shock post arranged.
Wherein, the discharging opening of described cyclone separator is connected with described discharge nozzle by pipeline.The advantage of such improvement is the collection being convenient to material.
Adopt above scheme, have the following advantages:
The upper face of the air intake plate of the fluidized bed dryer not easily cohered due to material of the present utility model is evenly equipped with in the vertical shock post arranged.So material is when in boiling-house, fluidisation is advanced, the large granular materials after cohering can collide with shock post, large granular materials is pulverized because of shock, and obtains abundant drying, thus avoid and occur dry incomplete problem because material coheres.
Accompanying drawing explanation
Fig. 1 is the structural representation of the fluidized bed dryer that material of the present utility model not easily coheres.
Detailed description of the invention
Below in conjunction with accompanying drawing, the utility model is described in further detail.
As shown in Figure 1, the fluidized bed dryer that material of the present utility model not easily coheres, comprise boiling-house 1, the top of described boiling-house 1 is connected with discharge chamber 2, the inner chamber of discharge chamber 2 communicates with the inner chamber of boiling-house 1, the top of discharge chamber 2 is processed with gas outlet 3, and gas outlet 3 is connected by the air inlet of pipeline with a cyclone separator 4.Having into horizontally disposed air intake plate 5 in the inner chamber of described boiling-house 1, in being tightly connected between the surrounding of air intake plate 5 and the madial wall of boiling-house 1, air intake plate 5 being evenly equipped with through hole, the upper face of air intake plate 5 is evenly equipped with in the vertical shock post 14 arranged.A sidewall upper feeding mouth 6 of described boiling-house 1, another boiling-house 1 sidewall relative with this sidewall has material outlet 7, material outlet 7 is connected with discharge nozzle 8, the discharging opening of described cyclone separator 4 is connected with this discharge nozzle 8 by pipeline.Described charging aperture 6 is positioned at the top of air intake plate 5, and the lower edge of described material outlet 7 and the upper face of air intake plate 5 flush.Be positioned on boiling-house 1 sidewall below air intake plate 5 and have air inlet 9, be connected with blast pipe 10 outside air inlet 9, blast pipe 10 be disposed with blower fan 11, filter 12 and heater 13.
During use, first material to be dried is joined boiling-house 1 from charging aperture 6, then material fluidisation in boiling-house 1 is advanced, the large granular materials cohered collides with shock post 14 when advancing, large granular materials is pulverized because of shock, material after final drying is discharged to housing from material outlet 7, dust simultaneously in cyclone separator 4 gas of being discharged gas outlet 3 is separated in gas, and deliver to discharge in discharge nozzle 8, the gas after separation is discharged from the gas outlet of cyclone separator 4.
Claims (2)
1. the fluidized bed dryer that not easily coheres of a material, comprise boiling-house (1), the top of described boiling-house (1) is connected with discharge chamber (2), the inner chamber of discharge chamber (2) communicates with the inner chamber of boiling-house (1), gas outlet (3) is arranged at the top of discharge chamber (2), and gas outlet (3) are connected by the air inlet of pipeline with a cyclone separator (4); Have into horizontally disposed air intake plate (5) in the inner chamber of described boiling-house (1), in being tightly connected between the surrounding of air intake plate (5) and the madial wall of boiling-house (1), (5) are evenly equipped with through hole to air intake plate; A sidewall of described boiling-house (1) there is charging aperture (6), another boiling-house (1) sidewall relative with this sidewall there is material outlet (7), material outlet (7) is connected with discharge nozzle (8), described charging aperture (6) is positioned at the top of air intake plate (5), and the lower edge of described material outlet (7) and the upper face of air intake plate (5) flush; Be positioned on boiling-house (1) sidewall below air intake plate (5) and have air inlet (9), air inlet (9) outside is connected with blast pipe (10), blast pipe (10) is disposed with blower fan (11), filter (12) and heater (13); It is characterized in that the upper face of described air intake plate (5) is evenly equipped with in the vertical shock post (14) arranged.
2. the fluidized bed dryer that not easily coheres of material as claimed in claim 1, is characterized in that the discharging opening of described cyclone separator (4) is connected with described discharge nozzle (8) by pipeline.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN201420729661.3U CN204285951U (en) | 2014-11-29 | 2014-11-29 | The fluidized bed dryer that a kind of material not easily coheres |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
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CN201420729661.3U CN204285951U (en) | 2014-11-29 | 2014-11-29 | The fluidized bed dryer that a kind of material not easily coheres |
Publications (1)
Publication Number | Publication Date |
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CN204285951U true CN204285951U (en) | 2015-04-22 |
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Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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CN201420729661.3U Expired - Fee Related CN204285951U (en) | 2014-11-29 | 2014-11-29 | The fluidized bed dryer that a kind of material not easily coheres |
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Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN104941960A (en) * | 2015-06-06 | 2015-09-30 | 安徽瀚洋节能科技有限公司 | Granular-substance cooling and cleaning fluidized bed |
CN106052305A (en) * | 2016-05-31 | 2016-10-26 | 镇江中化聚氨酯工业设备有限公司 | Drying device |
CN107445443A (en) * | 2017-08-31 | 2017-12-08 | 李艺 | A kind of tube furnace and fluidized bed furnace combined drying sludge, excrement material device |
-
2014
- 2014-11-29 CN CN201420729661.3U patent/CN204285951U/en not_active Expired - Fee Related
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN104941960A (en) * | 2015-06-06 | 2015-09-30 | 安徽瀚洋节能科技有限公司 | Granular-substance cooling and cleaning fluidized bed |
CN106052305A (en) * | 2016-05-31 | 2016-10-26 | 镇江中化聚氨酯工业设备有限公司 | Drying device |
CN107445443A (en) * | 2017-08-31 | 2017-12-08 | 李艺 | A kind of tube furnace and fluidized bed furnace combined drying sludge, excrement material device |
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Legal Events
Date | Code | Title | Description |
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GR01 | Patent grant | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20150422 Termination date: 20151129 |