CN208887338U - A kind of waste gas residual heat recycling circulation and energy-saving type drying machine - Google Patents
A kind of waste gas residual heat recycling circulation and energy-saving type drying machine Download PDFInfo
- Publication number
- CN208887338U CN208887338U CN201820683848.2U CN201820683848U CN208887338U CN 208887338 U CN208887338 U CN 208887338U CN 201820683848 U CN201820683848 U CN 201820683848U CN 208887338 U CN208887338 U CN 208887338U
- Authority
- CN
- China
- Prior art keywords
- dryer section
- angle box
- grain
- drying machine
- drying
- 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 55
- 238000004064 recycling Methods 0.000 title claims abstract description 20
- 239000002912 waste gas Substances 0.000 title claims abstract description 20
- 235000013339 cereals Nutrition 0.000 claims abstract description 59
- 239000002918 waste heat Substances 0.000 claims abstract description 34
- 235000007164 Oryza sativa Nutrition 0.000 claims abstract description 7
- 235000009566 rice Nutrition 0.000 claims abstract description 7
- 240000007594 Oryza sativa Species 0.000 claims abstract 2
- 239000007789 gas Substances 0.000 claims description 10
- 238000001704 evaporation Methods 0.000 claims description 8
- 230000008020 evaporation Effects 0.000 claims description 8
- 239000000428 dust Substances 0.000 claims description 7
- 238000010438 heat treatment Methods 0.000 claims description 7
- 238000005496 tempering Methods 0.000 claims description 6
- 238000004140 cleaning Methods 0.000 claims description 5
- 239000012535 impurity Substances 0.000 claims description 3
- 239000010903 husk Substances 0.000 claims description 2
- 238000009434 installation Methods 0.000 claims 1
- 238000004062 sedimentation Methods 0.000 claims 1
- 230000000694 effects Effects 0.000 abstract description 4
- 238000005265 energy consumption Methods 0.000 abstract description 3
- 239000000446 fuel Substances 0.000 abstract description 3
- 230000007246 mechanism Effects 0.000 abstract description 3
- 239000000203 mixture Substances 0.000 abstract description 2
- 238000010276 construction Methods 0.000 abstract 1
- 238000004134 energy conservation Methods 0.000 abstract 1
- 230000007613 environmental effect Effects 0.000 abstract 1
- 241000209094 Oryza Species 0.000 description 5
- 238000000034 method Methods 0.000 description 3
- 238000003303 reheating Methods 0.000 description 3
- 238000011084 recovery Methods 0.000 description 2
- 206010013786 Dry skin Diseases 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 125000004122 cyclic group Chemical group 0.000 description 1
- 235000013305 food Nutrition 0.000 description 1
- -1 frame Substances 0.000 description 1
- NJPPVKZQTLUDBO-UHFFFAOYSA-N novaluron Chemical compound C1=C(Cl)C(OC(F)(F)C(OC(F)(F)F)F)=CC=C1NC(=O)NC(=O)C1=C(F)C=CC=C1F NJPPVKZQTLUDBO-UHFFFAOYSA-N 0.000 description 1
- 238000010025 steaming Methods 0.000 description 1
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A40/00—Adaptation technologies in agriculture, forestry, livestock or agroalimentary production
- Y02A40/90—Adaptation technologies in agriculture, forestry, livestock or agroalimentary production in food processing or handling, e.g. food conservation
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P60/00—Technologies relating to agriculture, livestock or agroalimentary industries
- Y02P60/80—Food processing, e.g. use of renewable energies or variable speed drives in handling, conveying or stacking
- Y02P60/85—Food storage or conservation, e.g. cooling or drying
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P70/00—Climate change mitigation technologies in the production process for final industrial or consumer products
- Y02P70/10—Greenhouse gas [GHG] capture, material saving, heat recovery or other energy efficient measures, e.g. motor control, characterised by manufacturing processes, e.g. for rolling metal or metal working
Landscapes
- Drying Of Solid Materials (AREA)
Abstract
The utility model is a kind of waste gas residual heat recycling circulation and energy-saving type drying machine.Its housing construction is by upper flow tube (1), upper delay section (2), waste heat dryer section (3), lower delay section (5), it recycles air compartment (6), dryer section (7), draining crop mechanism (9), downtand (10), base support (13), exhaust outlet (16), suction ventilator (17), the composition such as air inlet (18), waste heat dryer section is continuously dried grain using the waste gas residual heat that dryer section recycles, waste heat utilizes again, heat supply is not increased, improve rice drying rate 0.2%/h or so, energy-saving effect is significant, reduce the unit heat consumption of grain drying, compared with disposable similar model drying machine, energy saving about 20%, it is big to solve ordinary cycle formula drying machine fuel consumption, energy consumption is high, drying is slow, rate of drying is low, the problems such as drying cost is high, realize energy conservation , environmental protection, be widely used in grain and seed drying etc..
Description
Technical field
The utility model relates to a kind of waste gas residual heats of agricultural machinery grain drying to recycle circulation and energy-saving type drying machine.
Background technique
Circulating grain dryer is outside the dryer section exhaust gas direct emission room of bottom or being discharged into dust currently on the market
Expansion chamber, the waste heat of exhaust gas cause fuel consumption big almost without recycling, and rate of drying is slow, and drying cost is high, drying machine
Energy consumption is high.
Summary of the invention
The purpose of the utility model is to overcome disadvantages mentioned above, and it is dry to provide a kind of waste gas residual heat recycling circulation and energy-saving type
The waste gas residual heat of drying machine dryer section is recycled drying grain again, because of the waste gas humidity of circulating drying machine discharge by machine
Small and temperature is applicable in, and waste heat recycling has certain utility value, can play the role of reheating, without will cause increase grain
The problems such as humidity.By drying machine dryer section two sides exclude waste heat exhaust gas, through pipeline back to drying machine middle part to grain again
Secondary heating.Drier structure is by upper flow tube, upper delay section, waste heat dryer section, lower delay section, dryer section, draining crop mechanism, pedestal branch
The compositions such as frame, air inlet, recycling air compartment, dust setting chamber, exhaust outlet, suction ventilator, downtand, motor and electric control gear.Grain
It is flowed from above to below in drying machine, burner ignition work or hot-blast stove heat supply suction ventilator starting simultaneously, in suction ventilator suction
Under effect, hot wind enters dryer section after grain layer by entering the wind angle box, is discharged into recycling air compartment by dryer section exhaust angle box two sides, to
The upper waste heat dryer section back in the middle part of drying machine, enters through waste heat dryer section flow inlet angle box two sides, and waste gas residual heat is then passed through grain
Layer is discharged to after grain heating by exhaust angle box.In usual dry paddy, environment temperature: the north is 10~-25 DEG C or so, south
Side is 5~30 DEG C, and the hot blast temperature of dry paddy is 60~65 DEG C, and the exhaust gas temperature of dryer section discharge is 30~35 DEG C, exhaust gas
Relative humidity is 45~50%, so the waste heat of exhaust gas can be returned directly to the waste heat dryer section of drying machine, reheating is
The grain of tempering cooling is recycled, it is appropriate to accelerate the evaporation of paddy moisture, the unit heat consumption of rice drying is reduced, energy-saving effect is bright
It is aobvious.This way of recycling breaches conventional thought mode and recovery method, and drying machine dryer section waste gas residual heat is recycled, and returns
Debit's formula science, compared with disposable similar model drying machine, energy saving about 20% or so improves rice drying rate
0.2%/h or so, solves that ordinary cycle formula drying machine fuel consumption is big, drying is slow, rate of drying is low, energy consumption is high, is dried into
A series of problems, such as this is high.
The technical scheme adopted by the utility model to solve the technical problem is as follows: in fig. 1 and 2, cold air is heated
For hot-air or it is hot wind, under the rotary action of negative-pressure air-suction machine (17), hot-air enters dryer section (7) through air inlet (18)
In air inlet angle box (8), carry out heat exchange with grain grain when passing through grain layer and improve grain temperature, moisture slow evaporation after grain is heated, steaming
The exhaust gas of hair is discharged into recycling air compartment (6) by dryer section exhaust angle box (19) two sides, returns back up in drying machine along recycling air compartment
The waste heat dryer section (3) in portion enters in machine through waste heat dryer section flow inlet angle box (15) two sides, and waste gas residual heat is then passed through grain layer to grain
After eating heating evaporation grain moisture content, it is discharged through exhaust angle box (4) by suction ventilator (17).Grain is thereby realized in elevator
(14) under castering action, grain constantly from upper flow tube (1) enter circulation dryer, then from downtand (10) be discharged into elevator into
During row one cycle, hot wind from dryer section (7) successively enter drying grain after, be discharged the recovered air compartment of waste gas residual heat
(6) it enters back into waste heat dryer section (3) and reheating drying is carried out to grain, is i.e. grain flows from the top to the bottom in circulating drying machine
During carrying out one cycle, after upper delay section (2) tempering, waste heat dryer section (3) are first passed through using recycling waste gas residual heat pair
It is dry that grain carries out primary heating, then after lower delay section (5) tempering, and the hot wind of drying section (7) carries out two to grain
The every circulation primary of secondary heat drying, i.e. grain is through heat drying twice, and which achieves more quick reasonable heat dryings.
Detailed description of the invention
The present invention will be further described with reference to the accompanying drawings and examples.
Fig. 1 is drying machine main view
Fig. 2 is Fig. 1 left view
Fig. 3 is Fig. 1 top view
Part number explanation in Fig. 1, Fig. 2;
Flow tube on 1., delay section on 2., 3. waste heat dryer sections, 4. exhaust angle boxes, 5. lower delay sections, 6. recycling air compartments, 7.
Dryer section, 8. air inlet angle boxes, 9. draining crop mechanisms, 10. downtands, 11. dust setting chambers, 12. cleaning doors, 13. base supports,
14. elevator, 15. waste heat dryer section flow inlet angle boxes, 16. exhaust outlets, 17. suction ventilator, 18. air inlet, 19. dryer sections are vented angle
Box.
Specific embodiment
The utility model optimum implementation is described with reference to the accompanying drawing.Waste gas residual heat recycles in fig. 1 and 2
Mode is embodied are as follows: hot wind through air inlet (18) enter dryer section (7) in air inlet angle box (8), pass through grain layer when with grain grain
It carries out heat exchange and improves grain temperature, the exhaust gas of moisture slow evaporation after grain is heated, evaporation is vented angle box (19) two sides by dryer section
Be discharged into recycling air compartment (6), along recycling air compartment return back up to the waste heat dryer section (3) in the middle part of drying machine, through waste heat dryer section into
Air horn box (15) two sides enter in machine, and waste gas residual heat is then passed through grain layer to grain heating evaporation grain moisture content, through being vented angle box (4)
It is discharged by suction ventilator (17).Enter the wind angle box (8) and dryer section exhaust angle box (19), waste heat dryer section air inlet angle box (15) and exhaust
Angle box (4) is right-angled intersection arrangement, and air inlet angle box (8) is identical as exhaust angle box (4) size, same layer angle box width and level
Spacing is 100-200mm, with top-bottom cross angle box spacing 120-600mm;Dryer section is vented angle box (19) and waste heat dryer section
Flow inlet angle box (15) size is identical, and same layer angle box width and horizontal space are 80-180mm, with upper and lower alternate angle box spacing
100-550mm.Arrangement and air inlet pattern of the dryer section (7) with waste heat dryer section (3) angle box can be identical mixed flow, fair current or inverse
Flow pattern formula can also be suitable, mixed flow combination pattern.Circulating drying machine hot wind flow mode is that hot wind enters from air inlet (18),
After dryer section (7) and waste heat dryer section (3) twice heat grain, become exhaust gas discharge from exhaust outlet (16), air-heater can
Being mounted on is positive pressure air feed before air inlet (18), and also mountable is negative pressure suction ventilator (17) behind exhaust outlet (16).It is remaining
Low temperature hot wind used in heated drying section (3) is that continuously grain is dried from the waste gas residual heat that dryer section (7) are recycled,
Recovery method is reasonable, and waste heat utilizes again, and energy-saving effect is significant.To guarantee grain quality, waste heat dryer section (3) and dryer section
(7) there are enough tempering spacing between, the minimum tempering spacing of lower delay section (5) should be greater than 2.4m, ensure that increasing in this way
While adding grain drying rate, the percentage of damage and Cracked Rice rate of grain are not increased, circulating drying machine divides into grain and row's grain
Not Cai Yong inclined upper flow tube (1) and downtand (10), without using traditional spiral-poker into row grain, effectively reduce grain
The percentage of damage and Cracked Rice rate of food.During cyclic drying, the dust of recycling air compartment (6) bottom dust setting chamber (11) is fallen into
And the impurity such as rice husk, according to amount of impurities number, it is primary that cleaning door (12) can be opened after completing every batch of grain drying
Cleaning among cleaning or drying process.
Claims (2)
1. a kind of waste gas residual heat recycles circulation and energy-saving type drying machine, it is characterised in that: drying machine is by dryer section and waste heat dryer section
Heating grains twice, the waste gas residual heat that waste heat dryer section continuously utilizes dryer section to recycle, do cereal after tempering
Dry, hot wind enters dryer section after grain layer by entering the wind angle box, is discharged into recycling air compartment by dryer section exhaust angle box two sides, returns upwards
The waste heat dryer section in the middle part of drying machine is returned to, is entered through waste heat dryer section flow inlet angle box two sides, it is right that waste gas residual heat is then passed through grain layer
By exhaust angle box discharge after grain heating.
2. drying machine according to claim 1, it is characterized in that: hot wind through air inlet (18) enter in dryer section (7) into
Wind angle box (8), makes grain heated moisture slow evaporation when across grain layer, the exhaust gas of evaporation is vented angle box (19) two sides by dryer section
Be discharged into recycling air compartment (6), along recycling air compartment return back up to the waste heat dryer section (3) in the middle part of drying machine, through waste heat dryer section into
Air horn box (15) two sides enter in machine, and waste gas residual heat is then passed through grain layer and evaporates grain moisture to heat grain, through being vented angle box (4)
It is discharged by suction ventilator (17), air inlet angle box (8) and dryer section exhaust angle box (19), waste heat dryer section flow inlet angle box (15) and exhaust
Angle box (4) is right-angled intersection arrangement, and air inlet angle box (8) is identical as exhaust angle box (4) size, same layer angle box width and level
Spacing is 100-200mm, with top-bottom cross angle box spacing 120-600mm;Dryer section is vented angle box (19) and waste heat dryer section
Flow inlet angle box (15) size is identical, and same layer angle box width and horizontal space are 80-180mm, with upper and lower alternate angle box spacing
100-550mm, arrangement and air inlet pattern of the dryer section (7) with waste heat dryer section (3) angle box can be identical mixed flow, fair current or inverse
Flow pattern formula can also be suitable, mixed flow combination pattern;Mountable air-heater is positive pressure air feed, or installation before air inlet (18)
Exhaust outlet (16) below be negative pressure suction ventilator (17), drying machine into grain and row grain be respectively adopted inclined upper flow tube (1) and under
Chute (10), drying machine two sides recycling air compartment (6) are arranged below dust setting chamber (11), the impurity such as dust and rice husk of sedimentation,
It is discharged by cleaning door (12).
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201820683848.2U CN208887338U (en) | 2018-04-28 | 2018-04-28 | A kind of waste gas residual heat recycling circulation and energy-saving type drying machine |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201820683848.2U CN208887338U (en) | 2018-04-28 | 2018-04-28 | A kind of waste gas residual heat recycling circulation and energy-saving type drying machine |
Publications (1)
Publication Number | Publication Date |
---|---|
CN208887338U true CN208887338U (en) | 2019-05-21 |
Family
ID=66492866
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201820683848.2U Expired - Fee Related CN208887338U (en) | 2018-04-28 | 2018-04-28 | A kind of waste gas residual heat recycling circulation and energy-saving type drying machine |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN208887338U (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN113465352A (en) * | 2021-07-14 | 2021-10-01 | 安徽正阳机械科技有限公司 | Double-heating type hot air mixed flow adjustable grain drying machine |
CN114543493A (en) * | 2022-04-28 | 2022-05-27 | 江西农业大学 | Integrated hot air drying equipment of many drying modes of granule solid material |
-
2018
- 2018-04-28 CN CN201820683848.2U patent/CN208887338U/en not_active Expired - Fee Related
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN113465352A (en) * | 2021-07-14 | 2021-10-01 | 安徽正阳机械科技有限公司 | Double-heating type hot air mixed flow adjustable grain drying machine |
CN114543493A (en) * | 2022-04-28 | 2022-05-27 | 江西农业大学 | Integrated hot air drying equipment of many drying modes of granule solid material |
CN114543493B (en) * | 2022-04-28 | 2022-07-22 | 江西农业大学 | Integrated hot air drying equipment of many drying modes of granule solid material |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN106369959A (en) | Air energy heat pump agricultural product drying device | |
CN208887338U (en) | A kind of waste gas residual heat recycling circulation and energy-saving type drying machine | |
CN104663875A (en) | Multi-graded concurrent tempering heat pump dehumidification and closed type circulating coarse cereal drying process method | |
CN206094826U (en) | A energy -conserving drying -machine of environment -friendly for solid wood panel is dried | |
CN104273217A (en) | Series heating type counter flow grain dryer | |
CN202340783U (en) | Solar box-type drying device for fruits and vegetables | |
CN110411200A (en) | A kind of waste gas residual heat recycling circulation and energy-saving type drying machine | |
CN202697600U (en) | Fresh Chinese wolfberry dual cycle hot air drying room | |
CN106322968A (en) | Gas drying machine used for tea making | |
CN207163099U (en) | A kind of special air energy drying system of sophora bud | |
CN204259729U (en) | The reverse-flow foodstuff drying device of series connection hot type | |
CN205561502U (en) | Material waste heat recovery drying system | |
CN208139778U (en) | Hot air circulation multilevel belt type drying device | |
CN2088675U (en) | Chain board transmission hot wind circulation drier | |
CN201575676U (en) | Grain dryer provided with semi-angular box | |
CN111288751B (en) | Drying equipment for agricultural and sideline products | |
CN207556095U (en) | A kind of novel integrated heat pump dryer | |
CN203586725U (en) | Fermented forage drying device | |
CN102334544B (en) | Novel low-temperature grain dryer | |
CN107036403A (en) | A kind of air can circulate baking room | |
CN201571454U (en) | Multifunctional foodstuff dryer | |
CN110731393A (en) | Tea leaf superheated steam green removing machine | |
CN216716928U (en) | Energy-saving grain drier | |
CN206724608U (en) | A kind of air can circulate baking room | |
CN205002538U (en) | Integral type waste heat recovery drying device |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
GR01 | Patent grant | ||
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: 20190521 |