CN106907906A - Multi-level network cylindrical dryer - Google Patents

Multi-level network cylindrical dryer Download PDF

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Publication number
CN106907906A
CN106907906A CN201710267384.7A CN201710267384A CN106907906A CN 106907906 A CN106907906 A CN 106907906A CN 201710267384 A CN201710267384 A CN 201710267384A CN 106907906 A CN106907906 A CN 106907906A
Authority
CN
China
Prior art keywords
drying chamber
heat source
net cylinder
air
source room
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.)
Pending
Application number
CN201710267384.7A
Other languages
Chinese (zh)
Inventor
马仁杰
郭广
马明銮
陈强
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
HUANONG SEED MACHINERY MANUFACTURING Co Ltd SHIHEZI CITY
Original Assignee
HUANONG SEED MACHINERY MANUFACTURING Co Ltd SHIHEZI CITY
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by HUANONG SEED MACHINERY MANUFACTURING Co Ltd SHIHEZI CITY filed Critical HUANONG SEED MACHINERY MANUFACTURING Co Ltd SHIHEZI CITY
Priority to CN201710267384.7A priority Critical patent/CN106907906A/en
Publication of CN106907906A publication Critical patent/CN106907906A/en
Pending legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26DRYING
    • F26BDRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B11/00Machines or apparatus for drying solid materials or objects with movement which is non-progressive
    • F26B11/02Machines or apparatus for drying solid materials or objects with movement which is non-progressive in moving drums or other mainly-closed receptacles
    • F26B11/04Machines or apparatus for drying solid materials or objects with movement which is non-progressive in moving drums or other mainly-closed receptacles rotating about a horizontal or slightly-inclined axis
    • F26B11/0436Machines or apparatus for drying solid materials or objects with movement which is non-progressive in moving drums or other mainly-closed receptacles rotating about a horizontal or slightly-inclined axis comprising multiple stages, e.g. multiple rotating drums subsequently receiving the material to be dried; Provisions for heat recuperation
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26DRYING
    • F26BDRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B21/00Arrangements or duct systems, e.g. in combination with pallet boxes, for supplying and controlling air or gases for drying solid materials or objects
    • F26B21/02Circulating air or gases in closed cycles, e.g. wholly within the drying enclosure
    • F26B21/04Circulating air or gases in closed cycles, e.g. wholly within the drying enclosure partly outside the drying enclosure
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26DRYING
    • F26BDRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B23/00Heating arrangements
    • F26B23/001Heating arrangements using waste heat
    • F26B23/002Heating arrangements using waste heat recovered from dryer exhaust gases
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26DRYING
    • F26BDRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B25/00Details of general application not covered by group F26B21/00 or F26B23/00
    • F26B25/001Handling, e.g. loading or unloading arrangements
    • F26B25/002Handling, e.g. loading or unloading arrangements for bulk goods

Abstract

The application is related to a kind of dryer, more particularly to a kind of multi-level network cylindrical dryer;It includes the heat source room being connected and drying chamber, thermal current in heat source room can be sent into circulating fan, the air -return duct across heat source room and drying chamber, power-equipment, the feed device of drying chamber head end;The two-port of air -return duct is communicated with heat source room and drying chamber tail end respectively;Frame is provided with drying chamber, at least two is provided with frame and is driven by power-equipment and continuous broken line can be constituted along the net of own axis cylinder, the axis of all net cylinders.Due to implementing above-mentioned technical proposal, by Multilayer Network cylinder, material can be acted on the application with thermal current for a long time, uniform drying and it is rapid, quality of finished is high, high working efficiency;Up to more than 90%, reducing energy consumption reduces pollution to heat utilization efficiency;Other the application compact conformation, eliminates conventional air channel long, and floor space is small, is easy to use and promotes.

Description

Multi-level network cylindrical dryer
Technical field
The application is related to a kind of dryer, more particularly to a kind of multi-level network cylindrical dryer.
Background technology
At present, dryer particularly foodstuff drying device, especially high-temperature hot-air tower dryer, use high temperature quick-drying Facture(Temperature is up to 120 DEG C -190 DEG C), drying technology process is that the high-temperature hot-air of following current, adverse current and mixed flow is carried out to grain Drying, the drying of especially aqueous to more than 35% material seed.Although this high-temperature hot-air tower dryer daily output compares Height, but have the following disadvantages:(1)High-temperature hot-air tower dryer equipment is larger, cost is higher, drying is distant, is unfavorable for Peasant household, the use of cooperative society;(2)Combustion of Hot Air Furnace is broken bituminous coal, and calorific value is low, power consumption is big, seriously polluted, is unfavorable for energy-saving ring Protect;(3)Heat exchanger used and exchanged outside tower, and greatly, dead corner cannot be eliminated heat-energy losses, cause drying materials not fill Point, it is uneven;(4)Hot blast is disposable utilization, and its utilization rate only up to reach 60-65%, and waste heat is not used; (5)Material seed is toasted by high-temperature hot-air, and interior free surface moisture cannot balance the rate of drying of dehydration, and starch is made in making material Into gelatinization, surface adustion, materials quality declines after drying, loses the condition of high-end product raw material, reduces the exploitation value of material Value, procurement price reduction, farmers' income is reduced.
Another modular dryer, material is sent into drying chamber and is dehydrated, although drying effect is pretty good, and quality is Improve;But because material is quantitative or with slowly flow velocity into drying chamber, it is necessary to carry out long period drying, work is imitated Rate is relatively low.
The content of the invention
The purpose of the application is to propose a kind of simple structure, and function admirable, good drying effect, reducing energy consumption, lifting is dried Dry efficiency, improves the multi-level network cylindrical dryer of social benefit.
What the application was realized in:Multi-level network cylindrical dryer, it include the heat source room being connected and drying chamber, can be by The thermal current feeding circulating fan of drying chamber head end in heat source room, the air -return duct across heat source room and drying chamber, power-equipment, send Material device;The two-port of air -return duct is communicated with heat source room and drying chamber tail end respectively;Frame is provided with drying chamber, is installed in frame There are at least two to be driven by power-equipment and continuous folding can be constituted along the net of own axis cylinder, the axis of all net cylinders Line, the head end of net cylinder is high, tail end bottom, and the head end of each net cylinder is provided with charging aperture, and the tail end of each net cylinder is provided with discharging opening, highest The charging aperture of the net cylinder of layer is connected with feed device, and the charging aperture of the net cylinder of remainder layer is corresponding with the discharging opening of the net cylinder of last layer It is connected.
Further, feed device includes bidirectional conveyor, measuring chute, grain flowing tube and cooling conveyor;Measuring chute is located at The top of top net cylinder, measuring chute lower end is connected to the charging aperture of top net cylinder by grain flowing tube;Bidirectional conveyor Input is located at the underface of bottom net cylinder discharging opening, and the one of output end of bidirectional conveyor is connected to cooling conveyor Input, the output end of cooling conveyor is connected to measuring chute.
Further, net cylinder two ends are equipped with raceway;Frame is provided with diagonal brace corresponding with net cylinder quantity, the two ends of diagonal brace Can slide up and down respectively and be fixed in frame, be installed with diagonal brace for supporting network cylinder and can by with raceway on net cylinder The cylinder rotation of frictional force drives net support roller, tugboat is electrically connected with power-equipment;Net cylinder base is on corresponding diagonal brace.
Further, fan house is provided between heat source room and drying chamber, the thermal source wind communicated with heat source room is provided with fan house Mouth and at least one drying air port communicated with drying chamber, at least one is provided with fan house can be by drying air port to drying The circulating fan of indoor air-supply;Or/and, the heat source machine and heat exchanger for linking together are provided with heat source room, heat exchanger End is by being provided with the air-introduced machine outside thermal source room through the pipeline at the top of heat source room;Thermal source locular wall is provided with adjustable temperature The cold-air flap of degree.
Further, the discharging opening of net cylinder tail end is connected with material-gathering device;The material-gathering device of the bottom passes through drying chamber bottom Wall is connected with the input of bidirectional conveyor, and the material-gathering device of remainder layer is connected to the next layer of charging aperture of net cylinder.
Further, air -return duct is fixedly mounted on the top of heat source room and drying chamber, and air -return duct is provided with least one set of row Wet mouth or hydrofuge shutter;Measuring chute is fixedly mounted on air -return duct top, and grain flowing tube enters through air -return duct and top net cylinder Material mouth is connected.
Further, warming plate, heat source room, fan house, drying are designed with the inwall of heat source room, fan house, drying chamber Room is equipped with maintenance door.
Further, multi-level network cylindrical dryer also includes Automatic Centering Control;Level detector, blanking are provided with measuring chute Position device, the bottom of measuring chute is connected with seed distributing device;Automatic Centering Control respectively with power-equipment, circulating fan, bidirectional conveyor, Cooling conveyor, cold-air flap, upper level detector, lower level detector, seed distributing device are electrically connected.
Due to implementing above-mentioned technical proposal, the cooperation that the application passes through circulating fan and air -return duct, the hot gas in heat source room Stream returns to heat source room by drying chamber, air channel, forms recycling for energy;Material enters the net cylinder of multilayer from feed device, Under the rotation of net cylinder, material loosening suspends, while dried with sufficient contact of next thermal current is altered, while to net cylinder Tail end is moved and enters next layer of net cylinder, and by Multilayer Network cylinder, material can be acted on thermal current for a long time, be dried equal Even and rapid, quality of finished is high, high working efficiency;Up to more than 90%, reducing energy consumption reduces pollution to heat utilization efficiency;Other this Shen Please compact conformation, eliminate conventional long air channel, floor space is small, is easy to use and promotes.
Brief description of the drawings:The concrete structure of the application is given by following drawings and Examples:
Fig. 1 is the perspective structure schematic diagram of the application most preferred embodiment;
Fig. 2 is the external structure schematic diagram of Fig. 1;
Fig. 3 is the left view structural representation of Fig. 2.
Legend:1. heat source room, 2. drying chamber, 3. circulating fan, 4. air -return duct, 5. frame, 6. net cylinder, 7. charging aperture, 8. Discharging opening, 9. bidirectional conveyor, 10. measuring chute, 11. grain flowing tubes, 12. cooling conveyors, 13. raceways, 14. diagonal braces, 15. supports Wheel, 16. fan houses, 17. thermal source air ports, 18. drying air ports, 19. heat source machines, 20. heat exchangers, 21. cold-air flaps, 22. gather materials Device, 23. hydrofuge shutters, 24. maintenance doors, level detector on 25., 26. times level detectors, 27. seed distributing devices, 28. air-introduced machines, 2. certainly Dynamic control centre.
Specific embodiment:
The application is not limited by following embodiments, can determine specific reality according to the technical scheme of the application and actual conditions Apply mode.
As shown in Figures 1 to 3,6 formula dryers of multi-level network cylinder include the heat source room 1 that is connected and drying chamber 2, can be by heat source room In 1 thermal current feeding the head end of drying chamber 2 circulating fan 3, across heat source room 1 and drying chamber 2 air -return duct 4, power-equipment, give Material device;The two-port of air -return duct 4 is communicated with heat source room 1 and the tail end of drying chamber 2 respectively;Frame 5, frame 5 are provided with drying chamber 2 On be provided with least two and driven by power-equipment and can be along the net of own axis cylinder 6, the axis of all net cylinders 6 composition Continuous broken line, the head end of net cylinder 6 is high, tail end bottom, and the head end of each net cylinder 6 is provided with charging aperture 7, and the tail end of each net cylinder 6 is provided with Discharging opening 8, the charging aperture 7 of top net cylinder 6 is connected with feed device, charging aperture 7 and the last layer of the net cylinder 6 of remainder layer The correspondence of discharging opening 8 of net cylinder 6 is connected.
During work, the heat in heat source room 1 is blowed in drying chamber 2 by circulating fan 3, now the internal pressure urgency of drying chamber 2 Increase severely big, the pressure of heat source room 1 progressively declines, form pressure difference;High-pressure hot wind in drying chamber 2 alters each net cylinder 6 and drying chamber 2 Each corner;Now material enters the net cylinder 6 of multilayer, in the case where net cylinder 6 is rotated and lower high-pressure hot wind is altered, thing from feed device Material is loose to suspend, while dried with sufficient contact of next thermal current is altered, while being moved to the tail end of net cylinder 6 under Gravitative Loads Move and enter next layer net cylinder 6, material by Multilayer Network cylinder 6 after flow out collect, material by continuous broken line path, when long Between contacted with thermal current occurrence dynamics, drying it is rapid and uniform, material forming quality is high;When the hot blast in drying chamber 2 is taken away After material moisture, into air -return duct 4, flow to reheating in negative pressuren zone heat source room 1 and form circulation.
The application compact conformation, heat source room 1, drying chamber 2 and air -return duct 4 are a unitary construction, and heat exchange is carried out inside it, Heat loss is few;Recycle heat is utilized, and is consumed energy less, is polluted small, and drying effect is splendid.Eliminate existing tower dryer " consumption Can high, drying poor quality, seriously polluted " defect, community income is improved, beneficial to peasant household, the application and popularizations of cooperative society.
As shown in Figures 1 to 3, feed device includes bidirectional conveyor 9, measuring chute 10, grain flowing tube 11 and cooling conveyor 12; Measuring chute 10 is located at the top of top net cylinder 6, and the lower end of measuring chute 10 is connected to entering for top net cylinder 6 by grain flowing tube 11 Material mouth 7;The input of bidirectional conveyor 9 is located at the underface of bottom net 6 discharging openings 8 of cylinder, and one of them is defeated for bidirectional conveyor 9 Go out the input that end is connected to cooling conveyor 12, the output end of cooling conveyor 12 is connected to measuring chute 10.
When running into that material particles are big, material type is difficult the situation of drying, the output end of bidirectional conveyor 9 can be gone to On cooling conveyor 12, measuring chute 10 will be again sent back to by the material of first drying, carry out secondary or even repeated drying;Cold But in the transportation of conveyer belt 12, material is cooled down, and is easy to be lifted drying effect next time.When first drying When meeting demand, the output end of bidirectional conveyor 9 is gone into other direction, material can be direct from the discharging opening 8 of bottom net cylinder 6 It is collected.If material moisture is low, it is not necessary to carry out cooling circulation by cooling conveyor 12, this technological process can become For;Cooling conveyor 12 is not used in cooling can become unidirectional as upper ingredient conveyor, bidirectional conveyor 9, be changed to discharging conveying Machine.
As shown in figure 1, the two ends of net cylinder 6 are equipped with raceway 13;Frame 5 is provided with diagonal brace 14 corresponding with the quantity of net cylinder 6, tiltedly The two ends of support 14 can slide up and down be fixed in frame 5 respectively, is installed with diagonal brace 14 for supporting network cylinder 6 and can led to The support roller 15 with the rotation of frictional force drives net cylinder 6 of raceway 13 on net cylinder 6 is crossed, tugboat is electrically connected with power-equipment;6, net cylinder in On corresponding diagonal brace 14.So the rake angle of diagonal brace 14 can be adjusted by the change in fixation at the two ends of diagonal brace 14, so as to change Flow velocity of the material in net cylinder 6, accomplishes that drying efficiency is laid equal stress on drying effect.Support roller 15 contacts friction with raceway 13, by this Frictional force drives each net cylinder 6 to rotate.Net cylinder also can be by sprocket wheel or chain or gear or other existing kinds of drive rotations.
As shown in figure 1, being provided with fan house 16 between heat source room 1 and drying chamber 2, it is provided with fan house 16 and is communicated with heat source room 1 Thermal source air port 17 and at least one drying air port 18 that is communicated with drying chamber 2, being provided with least one in fan house 16 can lead to Drying air port 18 is crossed to the circulating fan 3 blown in drying chamber 2;Or/and, it is provided with the heat source machine for linking together in heat source room 1 19 and heat exchanger 20, the end of heat exchanger 20 is provided with outside heat source room 1 by the pipeline through the top of heat source room 1 Air-introduced machine 28;The wall of heat source room 1 is provided with the cold-air flap 21 of temperature-adjustable.
As shown in figure 1, the discharging opening 8 of the tail end of net cylinder 6 is connected with material-gathering device 22;The material-gathering device 22 of the bottom is passed through and dried The bottom wall of dry chamber 2 is connected with the input of bidirectional conveyor 9, and the material-gathering device 22 of remainder layer is connected to the next layer of charging of net cylinder 6 Mouth 7.
As shown in Figure 1, 2, air -return duct 4 is fixedly mounted on the top of heat source room 1 and drying chamber 2, and air -return duct 4 is provided with least One group of moisture exhausting port or hydrofuge shutter 23;Measuring chute 10 is fixedly mounted on the top of air -return duct 4, grain flowing tube 11 through air -return duct 4 with The charging aperture 7 of top net cylinder 6 is connected.So in cyclic process, pass through when the little hot gas of heat returns to the process of heat source room 1 During air -return duct 4, steam is discharged from the hydrofuge shutter 23 of both sides;Beneficial to raising drying effect.
As shown in Fig. 2 heat source room 1, fan house 16, being designed with warming plate, heat source room 1, fan house on the inwall of drying chamber 2 16th, drying chamber 2 is equipped with maintenance door 24.
As shown in figure 1, multi-level network 6 formula dryers of cylinder also include Automatic Centering Control 29;Material position is provided with measuring chute 10 Device 25, lower level detector 26, the bottom of measuring chute 10 are connected with seed distributing device 27;Automatic Centering Control 29 respectively with power-equipment, follow The electric phase of ring blower fan 3, bidirectional conveyor 9, cooling conveyor 12, cold-air flap 21, upper level detector 25, lower level detector 26, seed distributing device 27 Even.
By upper level detector 25, lower level detector 26 obtain measuring chute 10 in material number so that by adjusting seed distributing device 27 change the flow velocity that material flows out measuring chute 10;Rotating cylinder rotating speed is changed by power-equipment;Heat source room 1 is controlled by cold-air flap 21 Interior temperature;Change the flow velocity of hot blast by circulating fan 3.Automatic Centering Control 29 can compare according to actual conditions with setting value Afterwards, automatic drying control process.
The panel of Automatic Centering Control 29 can displays temperature, metallic numerals thermometer can be housed in frame 5, be easy to remote Temperature conditions in observation drying chamber 2.
Above technical characteristic constitutes the most preferred embodiment of the application, and it has stronger adaptability and optimal implementation effect Really, the need for can according to actual needs increasing and decreasing inessential technical characteristic to meet different situations.

Claims (10)

1. a kind of multi-level network cylindrical dryer, including the heat source room that is connected and drying chamber, thermal current in heat source room can be sent into The circulating fan of drying chamber head end, the air -return duct across heat source room and drying chamber, power-equipment, feed device;The two of air -return duct Port communicates with heat source room and drying chamber tail end respectively;It is characterized in that:Frame is provided with drying chamber, is provided with least in frame Two are driven by power-equipment and can constitute continuous broken line, net cylinder along the net of own axis cylinder, the axis of all net cylinders Head end is high, tail end bottom, the head end of each net cylinder is provided with charging aperture, and the tail end of each net cylinder is provided with discharging opening, top net The charging aperture of cylinder is connected with feed device, and the charging aperture of the net cylinder of remainder layer is corresponding with the discharging opening of the net cylinder of last layer to be connected.
2. multi-level network cylindrical dryer according to claim 1, it is characterised in that:Feed device include bidirectional conveyor, Measuring chute, grain flowing tube and cooling conveyor;Measuring chute is located at the top of top net cylinder, and measuring chute lower end is connected by grain flowing tube To the charging aperture of top net cylinder;The input of bidirectional conveyor is located at the underface of bottom net cylinder discharging opening, two-way defeated The one of output end of machine is sent to be connected to the input of cooling conveyor, the output end of cooling conveyor is connected to measuring chute.
3. multi-level network cylindrical dryer according to claim 1 and 2, it is characterised in that:Net cylinder two ends are equipped with raceway;Machine Frame is provided with diagonal brace corresponding with net cylinder quantity, and the two ends of diagonal brace can slide up and down be fixed in frame respectively, solid on diagonal brace Dingan County is equipped with the support roller for being used for supporting network cylinder and can be rotated by the frictional force drives net cylinder with raceway on net cylinder, tugboat and power Equipment is electrically connected;Net cylinder base is on corresponding diagonal brace.
4. multi-level network cylindrical dryer according to claim 1 and 2, it is characterised in that:It is provided between heat source room and drying chamber Fan house, is provided with the thermal source air port communicated with heat source room and at least one communicated with drying chamber drying air port, wind in fan house Machine indoor location have at least one can by dry air port in drying chamber blow circulating fan;Or/and, it is provided with heat source room The heat source machine and heat exchanger for linking together, the end of heat exchanger are located at by being provided with through the pipeline at the top of heat source room Air-introduced machine outside thermal source room;Thermal source locular wall is provided with the cold-air flap of temperature-adjustable.
5. multi-level network cylindrical dryer according to claim 1 and 2, it is characterised in that:The discharging opening connection of net cylinder tail end There is material-gathering device;The material-gathering device of the bottom is connected through drying chamber bottom wall with the input of bidirectional conveyor, the collection of remainder layer Material device is connected to the next layer of charging aperture of net cylinder.
6. multi-level network cylindrical dryer according to claim 3, it is characterised in that:The discharging opening of net cylinder tail end is connected with collection Material device;The material-gathering device of the bottom is connected through drying chamber bottom wall with the input of bidirectional conveyor, the dress that gathers materials of remainder layer Put the charging aperture for being connected to next layer of net cylinder.
7. multi-level network cylindrical dryer according to claim 1, it is characterised in that:Air -return duct be fixedly mounted on heat source room and The top of drying chamber, air -return duct is provided with least one set of moisture exhausting port or hydrofuge shutter;Measuring chute is fixedly mounted on air -return duct top Portion, grain flowing tube is connected through air -return duct with the charging aperture of top net cylinder.
8. multi-level network cylindrical dryer according to claim 1, it is characterised in that:Heat source room, fan house, drying chamber it is interior Warming plate is designed with wall, heat source room, fan house, drying chamber are equipped with maintenance door.
9. the multi-level network cylindrical dryer according to claim 1 or 2 or 6 or 7 or 8, it is characterised in that:Multi-level network cartridge type is dried Dry machine also includes Automatic Centering Control;Level detector, lower level detector are provided with measuring chute, the bottom of measuring chute is connected with dials seed Device;Automatic Centering Control respectively with power-equipment, circulating fan, bidirectional conveyor, cooling conveyor, cold-air flap, upper level detector, Lower level detector, seed distributing device are electrically connected.
10. the multi-level network cylindrical dryer according to claim 3 or 4 or 5, it is characterised in that:Multi-level network cylindrical dryer Also include Automatic Centering Control;Level detector, lower level detector are provided with measuring chute, the bottom of measuring chute is connected with seed distributing device;From Dynamic control centre respectively with power-equipment, circulating fan, bidirectional conveyor, cooling conveyor, cold-air flap, upper level detector, blanking Position device, seed distributing device are electrically connected.
CN201710267384.7A 2017-04-21 2017-04-21 Multi-level network cylindrical dryer Pending CN106907906A (en)

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Application Number Priority Date Filing Date Title
CN201710267384.7A CN106907906A (en) 2017-04-21 2017-04-21 Multi-level network cylindrical dryer

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Application Number Priority Date Filing Date Title
CN201710267384.7A CN106907906A (en) 2017-04-21 2017-04-21 Multi-level network cylindrical dryer

Publications (1)

Publication Number Publication Date
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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107860185A (en) * 2017-12-13 2018-03-30 甘肃农业大学 Green grass drying device
CN109084566A (en) * 2018-09-20 2018-12-25 郑州长城冶金设备有限公司 Horizontal drying machine
CN111536774A (en) * 2020-05-08 2020-08-14 浙江恒迅环保科技有限公司 Drying machine
CN111536760A (en) * 2020-05-08 2020-08-14 浙江恒迅环保科技有限公司 Dynamic drying treatment method for hermetia illucens

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CH308066A (en) * 1951-03-06 1955-06-30 Lorenz Rudolf Device for roasting bulk material in a rotating drum.
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CN203704581U (en) * 2014-03-07 2014-07-09 甘肃农业大学 Grain drying device
CN203980840U (en) * 2014-07-28 2014-12-03 德清龙溪农业科技有限公司 Rice drying equipment
CN204255006U (en) * 2014-11-26 2015-04-08 重庆市长寿区毛彦宾水果种植场 Double-cylinder type seed drying machine
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CN205897786U (en) * 2016-06-20 2017-01-18 何紫韵 Rice drying device
CN106403565A (en) * 2016-11-18 2017-02-15 郑州中拓知识产权代理有限公司 Cereal drying, cooling and dust removing tower
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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CH186333A (en) * 1936-02-21 1936-09-15 Ammann Maschinenfabrik Aktieng Drying device.
CH308066A (en) * 1951-03-06 1955-06-30 Lorenz Rudolf Device for roasting bulk material in a rotating drum.
JPH0487740U (en) * 1990-11-30 1992-07-30
CN200961988Y (en) * 2006-09-29 2007-10-17 农业部南京农业机械化研究所 After-packing dryer
CN203704581U (en) * 2014-03-07 2014-07-09 甘肃农业大学 Grain drying device
CN203980840U (en) * 2014-07-28 2014-12-03 德清龙溪农业科技有限公司 Rice drying equipment
CN204255006U (en) * 2014-11-26 2015-04-08 重庆市长寿区毛彦宾水果种植场 Double-cylinder type seed drying machine
CN205897786U (en) * 2016-06-20 2017-01-18 何紫韵 Rice drying device
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CN106403565A (en) * 2016-11-18 2017-02-15 郑州中拓知识产权代理有限公司 Cereal drying, cooling and dust removing tower
CN206831968U (en) * 2017-04-21 2018-01-02 石河子市华农种子机械制造有限公司 Multi-level network cylindrical dryer

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107860185A (en) * 2017-12-13 2018-03-30 甘肃农业大学 Green grass drying device
CN107860185B (en) * 2017-12-13 2023-09-15 甘肃农业大学 Grass drier
CN109084566A (en) * 2018-09-20 2018-12-25 郑州长城冶金设备有限公司 Horizontal drying machine
CN111536774A (en) * 2020-05-08 2020-08-14 浙江恒迅环保科技有限公司 Drying machine
CN111536760A (en) * 2020-05-08 2020-08-14 浙江恒迅环保科技有限公司 Dynamic drying treatment method for hermetia illucens

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Application publication date: 20170630