CN205511994U - Continuous drying device of belt corn - Google Patents
Continuous drying device of belt corn Download PDFInfo
- Publication number
- CN205511994U CN205511994U CN201620060465.0U CN201620060465U CN205511994U CN 205511994 U CN205511994 U CN 205511994U CN 201620060465 U CN201620060465 U CN 201620060465U CN 205511994 U CN205511994 U CN 205511994U
- Authority
- CN
- China
- Prior art keywords
- steam
- conveyer belt
- drying baker
- conveying roller
- oryza glutinosa
- 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
Links
- 238000001035 drying Methods 0.000 title claims abstract description 45
- 240000008042 Zea mays Species 0.000 title abstract 3
- 235000005824 Zea mays ssp. parviglumis Nutrition 0.000 title abstract 3
- 235000002017 Zea mays subsp mays Nutrition 0.000 title abstract 3
- 235000005822 corn Nutrition 0.000 title abstract 3
- 238000009826 distribution Methods 0.000 claims abstract description 15
- 235000007164 Oryza sativa Nutrition 0.000 claims description 30
- 240000007594 Oryza sativa Species 0.000 claims description 28
- 238000007599 discharging Methods 0.000 claims description 7
- 239000011148 porous material Substances 0.000 claims description 6
- 238000010438 heat treatment Methods 0.000 abstract description 5
- 235000017166 Bambusa arundinacea Nutrition 0.000 abstract 4
- 235000017491 Bambusa tulda Nutrition 0.000 abstract 4
- 241001330002 Bambuseae Species 0.000 abstract 4
- 235000015334 Phyllostachys viridis Nutrition 0.000 abstract 4
- 239000011425 bamboo Substances 0.000 abstract 4
- 238000009434 installation Methods 0.000 abstract 4
- 238000001914 filtration Methods 0.000 abstract 2
- 235000013339 cereals Nutrition 0.000 description 4
- 238000005265 energy consumption Methods 0.000 description 4
- 241000209094 Oryza Species 0.000 description 2
- 238000007602 hot air drying Methods 0.000 description 2
- 235000009566 rice Nutrition 0.000 description 2
- 239000002918 waste heat Substances 0.000 description 2
- 230000004071 biological effect Effects 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000003306 harvesting Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Landscapes
- Drying Of Solid Materials (AREA)
Abstract
The utility model discloses a continuous drying device of belt corn, including air distribution plate, drying cabinet, conveyer belt, conveying roller, a feeding section of thick bamboo, steam heating device, installation conveyer belt and conveying roller in the drying cabinet, the conveyer belt below sets up the front end top installation feeding section of thick bamboo of air distribution plate, drying cabinet, the lower part installation steam of a feeding section of thick bamboo advances the pipe, and steam advances the pipe to be connected with steam heating device, the top installation feeder hopper and the steam filtration ware of a feeding section of thick bamboo, and steam outlet pipe is connected to the steam filtration ware, and steam outlet pipe is connected to steam heating device. The utility model discloses a continuous drying of corn to adopt steam preheating to improve drying efficiency.
Description
Technical field
This utility model relates to a kind of grain drying device, belongs to drying equipment technical field.
Background technology
Oryza sativa L. is one of main cereal crops of China, is extensively planted in most laboratories.The Oryza glutinosa of new results is difficult to storage because of aqueous higher (25%～30%), and quality deterioration is very fast.According to statistics, the Oryza glutinosa about 2,500,000 tons that China loses because not being dried in time every year, be equivalent to the year consumption figure of 10,000,000 people.Meanwhile, the energy consumption being applied to rice drying accounts for the 64% of Oryza glutinosa production and processing total energy consumption, belongs to the operation of high energy consumption unit.Constantly reduce at cultivated area, grain security and energy crisis the most aobvious prominent today, after rice harvest in time, high-quality, low energy consumption is dried becomes the research topic that grain drying field is important.
The biological property of Oryza glutinosa self determines it and belongs to more difficult dry heat sensitive material.At present, the drying mode of Oryza glutinosa mainly has nature to dry and mechanical drying.Being restricted by economic condition, self-produced Oryza glutinosa is dried by the mode that the many employings of overwhelming majority peasant household of China are dried naturally.This drying mode is subjected to the factor impact such as weather and biology.Particularly south China area, is commonly encountered rainy weather during results Oryza glutinosa, and fresh Oryza glutinosa, because can not get the driest the most mouldy or germinateing, causes foodstuff waste.Naturally mode of drying has been not suitable with the market demand and the requirement of plantation economy benefit raising.Current drying equipment typically uses can not be continuous drying, and work efficiency is relatively low.
Utility model content
The purpose of this utility model is to provide a kind of belt Oryza glutinosa continuous drier, and its drying efficiency is high, can produce continuously.
This utility model uses following technical proposals to realize.A kind of belt Oryza glutinosa continuous drier, including air-intaker, electric heater, blast pipe, air distribution plate, drying baker, conveyer belt, conveying roller, feeding cylinder, steam heater, it is characterized in that: conveyer belt and conveying roller are installed in drying baker, conveyer belt is driven by conveying roller, and conveying roller is driven by motor；Being uniformly distributed pore on described conveyer belt, pore opening is less than Oryza glutinosa size；Below described conveyer belt, air distribution plate is set, it it is inlet air plenum below air distribution plate, inlet air plenum is connected with blast pipe, blast pipe reconnects air-intaker after connecting electric heater, the base plate of drying baker afterbody is provided with discharging opening, discharging opening is installed discharge valve, the top board of drying baker afterbody is provided with pneumatic filter, pneumatic filter connects discharge pipe, the front top of drying baker is installed into barrel, steam inlet tube is installed in the bottom of feeding cylinder, steam inlet tube is connected with steam heater, the top of feeding cylinder is installed into hopper and vapor filter, vapor filter connects steam and goes out pipe, steam goes out pipe and is connected to steam heater.
Described air distribution plate is the flat board of many air vents.
Further, installing striker plate in drying baker, striker plate is positioned at charging aperture side-lower.
Technique effect of the present utility model, uses high-temperature steam preheating Oryza glutinosa in feeding cylinder, and in then Oryza glutinosa enters drying baker, by using hot air drying Oryza glutinosa, and in dry run, Oryza glutinosa carries the most backward, it is achieved continuous drying.High-temperature steam preheating is greatly improved drying efficiency, and steam is reflowable to be reused to steam heater heating, does not waste heat energy.It is continuous drying that this utility model achieves Oryza glutinosa, and rate of drying is fast.
Accompanying drawing explanation
Fig. 1 is schematic diagram of the present utility model.
In figure: 1. air-intaker, 2. electric heater, 3. blast pipe, 4. air distribution plate, 5. drying baker, 6. conveyer belt, 7. conveying roller, 8. discharging opening, 9. discharge valve, 10. pneumatic filter, 11. discharge pipes, 12. feeding cylinders, 13. steam inlet tubes, 14. vapor filters, 15. steam go out pipe, 16. feed hoppers, 17. steam heaters, 18. striker plates.
Detailed description of the invention
As shown in Figure 1, belt Oryza glutinosa continuous drier includes air-intaker 1, electric heater 2, blast pipe 3, air distribution plate 4, drying baker 5, conveyer belt 6, conveying roller 7, feeding cylinder 12, steam heater 17, conveyer belt 6 and conveying roller 7 are installed in drying baker 5, conveyer belt 6 is driven by conveying roller 7, and conveying roller 7 is driven by motor；Being uniformly distributed pore on described conveyer belt 6, pore opening is less than Oryza glutinosa size；Below described conveyer belt 6, air distribution plate 4 is set, it it is inlet air plenum below air distribution plate 4, inlet air plenum is connected with blast pipe 3, for being to make air intake uniform, 6 connected entrances are had between inlet air plenum and blast pipe 3, blast pipe 3 reconnects air-intaker 1 after connecting electric heater 2, the base plate of drying baker 5 afterbody is provided with discharging opening 8, discharging opening 8 is installed discharge valve 9, the top board of drying baker 5 afterbody is provided with pneumatic filter 10, pneumatic filter 10 connects discharge pipe 11, the front top of drying baker 5 is installed into barrel 12, and striker plate 18 is installed in drying baker 5, striker plate 18 is positioned at charging aperture side-lower；Steam inlet tube 13 is installed in the bottom of feeding cylinder 12, and steam inlet tube 13 is connected with steam heater 17, and the top of feeding cylinder 12 is installed into hopper 16 and vapor filter 14, and vapor filter 14 connects steam and goes out pipe 15, and steam goes out pipe 15 and is connected to steam heater 17.
More specifically, described air distribution plate 4 is the flat board of many air vents.
This utility model uses high-temperature steam to preheat Oryza glutinosa in feeding cylinder 12, and in then Oryza glutinosa enters drying baker 5, by using hot air drying Oryza glutinosa, and in dry run, Oryza glutinosa carries the most backward, it is achieved continuous drying.High-temperature steam preheating is greatly improved drying efficiency, and steam is reflowable to be reused to steam heater 17 heating, does not waste heat energy.
Claims (3)
1. a belt Oryza glutinosa continuous drier, including air-intaker, electric heater, blast pipe, air distribution plate, drying baker, conveyer belt, conveying roller, feeding cylinder, steam heater, it is characterized in that: conveyer belt and conveying roller are installed in drying baker, conveyer belt is driven by conveying roller, and conveying roller is driven by motor；Being uniformly distributed pore on described conveyer belt, pore opening is less than Oryza glutinosa size；Below described conveyer belt, air distribution plate is set, it it is inlet air plenum below air distribution plate, inlet air plenum is connected with blast pipe, blast pipe reconnects air-intaker after connecting electric heater, the base plate of drying baker afterbody is provided with discharging opening, installs discharge valve in discharging opening, and the top board of drying baker afterbody is provided with pneumatic filter, pneumatic filter connects discharge pipe, and the front top of drying baker is installed into barrel；Steam inlet tube is installed in the bottom of feeding cylinder, and steam inlet tube is connected with steam heater, and the top of feeding cylinder is installed into hopper and vapor filter, and vapor filter connects steam and goes out pipe, and steam goes out pipe and is connected to steam heater.
Belt Oryza glutinosa continuous drier the most according to claim 1, it is characterised in that: described air distribution plate is the flat board of many air vents.
Belt Oryza glutinosa continuous drier the most according to claim 1, it is characterised in that: installing striker plate in drying baker, striker plate is positioned at charging aperture side-lower.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620060465.0U CN205511994U (en) | 2016-01-22 | 2016-01-22 | Continuous drying device of belt corn |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620060465.0U CN205511994U (en) | 2016-01-22 | 2016-01-22 | Continuous drying device of belt corn |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205511994U true CN205511994U (en) | 2016-08-31 |
Family
ID=56767333
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620060465.0U Expired - Fee Related CN205511994U (en) | 2016-01-22 | 2016-01-22 | Continuous drying device of belt corn |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205511994U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107788113A (en) * | 2017-12-12 | 2018-03-13 | 江西创迪科技有限公司 | A kind of grain drying device |
-
2016
- 2016-01-22 CN CN201620060465.0U patent/CN205511994U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107788113A (en) * | 2017-12-12 | 2018-03-13 | 江西创迪科技有限公司 | A kind of grain drying device |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20160831 Termination date: 20170122 |