CN209485017U - Agalloch eaglewood material negative pressure stirring and drying machine - Google Patents
Agalloch eaglewood material negative pressure stirring and drying machine Download PDFInfo
- Publication number
- CN209485017U CN209485017U CN201822256797.8U CN201822256797U CN209485017U CN 209485017 U CN209485017 U CN 209485017U CN 201822256797 U CN201822256797 U CN 201822256797U CN 209485017 U CN209485017 U CN 209485017U
- Authority
- CN
- China
- Prior art keywords
- drying
- stirring
- liner
- agitating shaft
- agalloch eaglewood
- 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.)
- Active
Links
Landscapes
- Drying Of Solid Materials (AREA)
Abstract
A kind of agalloch eaglewood material negative pressure stirring and drying machine comprising rack and casing, the casing accumbency are mounted on the rack, and cylindrical drying liner is equipped in casing；It is provided with vapor chamber shell between casing and drying liner, is provided with insulating layer between vapor chamber shell and casing；Space between vapor chamber shell and drying liner is vapor chamber；Vapor chamber installs limited valve and intake valve；The top of drying liner is provided with exhaust outlet and feed inlet, and the bottom for drying liner is provided with discharge port；The agitating shaft driven by driving device is installed in drying liner, the stirring plectrum that can convey material to discharge port end stirring is installed on agitating shaft, is also equipped with the screw auger for conveying material to separate discharge port end on agitating shaft；The stirring distance for stirring plectrum is greater than the stirring distance of screw auger；Exhaust outlet is connected with negative pressure receiving tank by condenser.This drying unit material drying is heated evenly, and drying efficiency is high, and can collect the agilawood essential oil ingredient of drying course volatilization.
Description
Technical field
The utility model belongs to the technical field of drying equipment, specifically a kind of agalloch eaglewood material negative pressure stirring and drying machine.
Technical background
Drying (dry) refers to the process of that being passed through hot-air evaporates moisture in material and take away.Traditional drying materials are all
Be by material accumulation in baking room or drying unit, then pass to Hot-blast Heating, improve the temperature of material, make the water in material
Divide vaporization, the vapor being evaporated is drained by dehumidification system and achievees the purpose that material drying.
Agalloch eaglewood is a kind of medicinal material name, belongs to medicine Isolated From Thymelaeaceae Species；Also refer to the timber containing resin of suspension culture of Aquilaria sinensis；Classification system:Aquilariaagallocha(Lour.)Roxb, also known as: honey perfume, stack perfume, lignum aquilariae resinatum, Shen Xiang.Agilawood essential oil is passed through by agalloch eaglewood
It is the essence place of agalloch eaglewood made of being refined after distillation extraction.Agilawood essential oil has multi-efficiency to human body, such as: improve gas
Field, pressure of releiving, sleeping resist strongly fragrant, conditioning body and mind and promotion body metabolism etc..A few drop agalloch eaglewood are instilled in the hot water of bubble foot
Essential oil can achieve the purpose of promoting blood circulation channels and collaterals, moreover it is possible to achieve the effect that remove tinea pedis foot odour.It is non-renewable due to natural agilawood
Property, the linaloe oil after refinement just more seems rare and precious.People usually by agalloch eaglewood after distillation extraction remaining agalloch eaglewood slag
Other purposes are used as after drying.However agalloch eaglewood slag utilizes Hot-blast Heating, makes the drying mode of agalloch eaglewood pulp water point evaporation, agalloch eaglewood slag by
Hot uneven, drying time is longer, and since agalloch eaglewood is after distillation extraction, agalloch eaglewood slag also contain a certain amount of agilawood essential oil at
Point, drying course agilawood essential oil is volatilized at branch, cannot be collected, and very big waste is caused.Therefore a kind of agalloch eaglewood material is needed
It is heated evenly, drying time is short, and can collect the drying unit of agilawood essential oil ingredient.
Summary of the invention
The purpose of this utility model is that in view of the problems of the existing technology, it is ingenious to provide a kind of structure setting, material by
Hot uniformly drying time is short, and drying efficiency is high, and can collect the agalloch eaglewood material negative pressure stirring and drying machine of agilawood essential oil ingredient.
To achieve the goals above, the technical solution adopted in the utility model are as follows:
A kind of agalloch eaglewood material negative pressure stirring and drying machine comprising rack and casing, the casing accumbency are mounted on rack
On, cylindrical drying liner is installed in casing；Be provided with vapor chamber shell between casing and drying liner, vapor chamber shell with
Insulating layer is provided between casing；Space between vapor chamber shell and drying liner is vapor chamber；Vapor chamber installs limited valve
And intake valve；The top of drying liner is provided with exhaust outlet and feed inlet, and the bottom for drying liner is provided with discharge port；In drying
The agitating shaft driven by driving device is installed, being equipped on agitating shaft can be by material stirring to discharge port end stirring conveying in gallbladder
Plectrum is mixed, is also equipped on agitating shaft by material to the screw auger far from discharge port end conveying；It stirs plectrum and agitating shaft hangs down
Histogram to stirring distance be greater than screw auger and agitating shaft vertical direction stirring distance.During agitating shaft rotation,
Stirring plectrum and screw auger follow agitating shaft to rotate together, and stirring plectrum conveys material toward discharge port end, and material is avoided to squeeze
Pressure, screw auger convey partial material toward far from discharge port end, realize conveying stirring back and forth, stir evenly, material is heated
Uniformly.Exhaust outlet and feed inlet are separately positioned on the both ends top of drying liner, and feed inlet is arranged with intake valve identical
One end, pressure limiting valve and exhaust outlet are arranged in the other end.Because when material is just put into, moisture is higher, temperature that when evaporation needs
Higher, steam is passed through from the intake valve of feed inlet end, can accelerate material moisture evaporation, and make the vapor (steam) temperature base in vapor chamber
Originally it is consistent, conducive to being heated evenly for material, is dried while stirring more sufficiently.
The driving device is driven to motor belt formula, motor chain-type or the box transmission device of motor drive.Electricity
Machine belt-type is to be transmitted at agitating shaft using the power of motor output by belt, driving agitating shaft rotation；Motor chain-type
It is to be transmitted at agitating shaft using the power of motor output by chain, driving agitating shaft rotation；Box motor drive is to utilize
The power of motor output after transmission case by being transmitted at agitating shaft, driving agitating shaft rotation.
Exhaust outlet on the drying liner is connected with cooler, and the import of cooler is connect with exhaust outlet；Cooler
Outlet be connected with vacuum receiving tank；Vacuum receiving tank is connect by vacuum tube and vacuum pump with tail gas receiving tank；Cooler
Input end is connected by the top of condensation return pipt and cooling tower；The outlet end of cooler passes through water pump and condensate pipe and cooling
The lower part of tower connects；Condensate pipe provides cooling water for condenser.
The fractionation bucket that the bottom of the vacuum receiving tank is connected with convenient for the essential oil separation for adsorbing drying course.Drying
Process uses the principle of negative-pressure adsorption, and for drying agalloch eaglewood material, the moisture that agalloch eaglewood drying course evaporates is drawn onto condensed system
System, condensed mixing liquid are collected into vacuum receiving tank, and the liquid that vacuum receiving tank is collected passes through fractionation bucket fractionation
Obtained agilawood essential oil and agalloch eaglewood hydrosol.
The drying liner is equipped with relief valve.
The bottom of the vapor chamber is provided with blowdown valve and drain valve.
The vapor chamber is also equipped with pressure gauge.
The drying liner is equipped with thermometer.
The flanged joint lid maintained easily is also equipped on the casing.
Multiple groups stirring plectrum is installed, every group of stirring plectrum is made of 4-8 piece stirring plectrum, and on the agitating shaft
Cloth is on agitating shaft；Every two groups of adjacent 3 piece stirring plectrum is installed in isosceles triangle, and stirs the axis of plectrum mixing surface and agitating shaft
Line is in 8-15 ° of angle, stirs plectrum and is installed on agitating shaft using aforesaid way, is conveyed, matched using material is stirred toward discharge port
It closes screw auger to use, drying efficiency can be improved than stirring plectrum and screw auger exclusive use, drying time shortens half small
When more than.
The application agalloch eaglewood material negative pressure stirring and drying machine is operation instruction: ensuring that staff leaves drying oven before operation
The safe distance of feed inlet, discharge port and holding and rotating device；After ensuring the safe distance of staff, dryer is opened
Motor switch；After the stabilization of speed of machine to be mixed, material drying slowly is put into from feed inlet；Slowly open intake valve, drying
The steam pressure of furnace body will be maintained in defined pressure limit；It successively opens circulating cooling pump switch and opens negative-pressure vacuum
Switch pump；After material will reach the mass dryness fraction of drying, discharges material is needed.30-60 can be shifted to an earlier date according to the difference of material drying
Minute steam off valve allows the intracorporal temperature of dryer that material to be continued to carry out parch；Until drying materials.It is wanted before discharging
First start siccative conveyer belt, simultaneously closes off water circulating pump switch and vacuum pump switch, then open material discharge gate again；To dry
The drained closing drying blender of material drying and feeder switch.
The advantages of the application agalloch eaglewood material negative pressure stirring and drying machine are as follows:
The application agalloch eaglewood material negative pressure stirring and drying machine utilizes the principle of negative-pressure adsorption, receives vacuum first with vacuum pump
Tank vacuumizes, and using the agalloch eaglewood material in the heat drying liner of the steam transmitting in vapor chamber, it is heavy in liner to dry
Perfumery material is constantly stirred back and forth by screw auger and stirring plectrum, and material is heated evenly, will not be even because of uneven heating, and causes
Color after agalloch eaglewood drying materials is bad；The exhaust outlet of the drying unit of the application is connected with cooler, the import of cooler with
Exhaust outlet connection；The outlet of cooler is connected with vacuum receiving tank, and the steam of generation is adsorbed in vacuum receiving tank, drying effect
Rate is high.And the drying unit of transmission, when drying agalloch eaglewood material, the effective component of material can be evaporated together with vapor,
And the negative pressure agitating device of the application, it can be filled recycling is collected with the effective component of moisture evaporation when drying agalloch eaglewood material
Divide and recycles.
Detailed description of the invention
Fig. 1 is the structural schematic diagram of the utility model agalloch eaglewood material negative pressure stirring and drying machine；
The title of serial number in figure are as follows:
1, rack, 2, blowdown valve, 3, drain valve, 4, motor, 5, drying liner, 6, vapor chamber, 7, vapor chamber shell, 8, heat preservation
Layer, 9, casing, 10, relief valve, 11, pressure limiting valve, 12, observation window, 13, screw auger, 14, agitating shaft, 15, exhaust outlet, 16, temperature
Spend table, 17, stirring plectrum, 18, pressure gauge, 19, cooler, 20, condensation return pipt, 21, feed inlet, 22, intake valve, 23, method
Blue connection cover, 24, condensate pipe, 25, vacuum receiving tank, 26, vacuum tube, 27, vacuum pump, 28, tail gas receiving tank, 29, cooling
Tower, 30, water pump, 31, fractionation bucket, 32, discharge port.
Specific embodiment
The utility model is introduced in order to more detailed, below with reference to embodiment and attached drawing, this agalloch eaglewood material negative pressure is stirred
Dryer is mixed to be described further.
Embodiment 1
Agalloch eaglewood material negative pressure stirring and drying machine comprising rack 1 and casing 9,9 accumbency of casing are mounted on rack 1
On, cylindrical drying liner 5 is installed in casing 9；Vapor chamber shell 7, steam are provided between casing 9 and drying liner 5
Insulating layer 8 is provided between chamber shell 7 and casing 9；Space between vapor chamber shell 7 and drying liner 5 is vapor chamber 6；Vapor chamber 6
Limited valve 11 and intake valve 22 are installed；The top of drying liner 5 is provided with exhaust outlet 15 and feed inlet 21, drying liner 5
Bottom is provided with discharge port 32；The agitating shaft 14 driven by driving device is installed in drying liner 5, is equipped on agitating shaft 14
Material can be stirred to the stirring plectrum 17 of conveying to 32 end of discharge port, be also equipped with material on agitating shaft 14 to far from discharge port
The screw auger 13 of 32 ends conveying；The stirring distance for stirring plectrum 17 and agitating shaft vertical direction is greater than screw auger 13 and stirring
The stirring distance of axis vertical direction.During agitating shaft 14 rotates, stirs plectrum 17 and screw auger 13 follows stir together
The rotation of axis 14 is mixed, stirring plectrum 17 conveys material toward 21 end of discharge port, avoids material from squeezing, screw auger 13 is by partial material
It toward far from the conveying of 32 end of discharge port, realizes conveying stirring back and forth, stirs evenly, material is heated also uniform.Exhaust outlet 15 and charging
Mouth 21 is separately positioned on the both ends top of drying liner 5, and feed inlet 21 and intake valve 22 are arranged in identical one end, pressure limiting valve
11 are arranged with exhaust outlet 15 in the other end.Because when material is just put into, moisture is higher, the temperature that when evaporation needs is also higher, steams
Vapour is passed through from the intake valve 22 at 21 end of feed inlet, can accelerate material moisture evaporation, and make the vapor (steam) temperature in vapor chamber 6 basic
It is consistent, conducive to being heated evenly for material, is dried while stirring more sufficiently.
The driving device is driven to the transmission device of 4 transmission case type of 4 belt-type of motor, 4 chain-type of motor or motor.
4 belt-type of motor is to be transmitted at agitating shaft using the power of motor output by belt, driving agitating shaft rotation；4 chain of motor
Formula is to be transmitted at agitating shaft using the power of motor output by chain, and driving agitating shaft rotates；4 transmission case type of motor is
Using the power of motor output by being transmitted at agitating shaft after transmission case, driving agitating shaft rotation.
Exhaust outlet 15 on the drying liner 5 is connected with cooler 19, and the import of cooler 19 and exhaust outlet 15 connect
It connects；The outlet of cooler 19 is connected with vacuum receiving tank 25；Vacuum receiving tank 25 passes through vacuum tube 26 and vacuum pump 27 and tail gas
Receiving tank 28 connects；The input end of cooler 19 is connect by condensation return pipt 20 with the top of cooling tower 29；Cooler 19
Outlet end is connect by condensate pipe 24 and water pump 30 with the lower part of cooling tower 29；Condensate pipe 24 is that cooler 19 provides condensation
Water.
The bottom of the vacuum receiving tank 25 is connected with fractionation bucket 31.Drying course uses the principle of negative-pressure adsorption, with
For drying agalloch eaglewood material, the moisture that agalloch eaglewood drying course evaporates is drawn onto condenser system, condensed mixing liquid is collected into
Vacuum receiving tank 25 is fractionated the liquid that vacuum receiving tank 25 is collected by being fractionated bucket 31, the agilawood essential oil that can be obtained and heavy
Fragrant hydrosol.
The drying liner 5 is equipped with relief valve 10 and observation window 12.
The bottom of the vapor chamber 6 is provided with blowdown valve 2 and drain valve 3.
The vapor chamber 6 is also equipped with pressure gauge 18.
The drying liner 5 is equipped with thermometer 16.
The flanged joint lid 23 maintained easily is also equipped on the casing 9.
Embodiment 2
Agalloch eaglewood material negative pressure stirring and drying machine comprising rack 1 and casing 9,9 accumbency of casing are mounted on rack 1
On, cylindrical drying liner 5 is installed in casing 9；Vapor chamber shell 7, steam are provided between casing 9 and drying liner 5
Insulating layer 8 is provided between chamber shell 7 and casing 9；Space between vapor chamber shell 7 and drying liner 5 is vapor chamber 6；Vapor chamber 6
Limited valve 11 and intake valve 22 are installed；The top of drying liner 5 is provided with exhaust outlet 15 and feed inlet 21, drying liner 5
Bottom is provided with discharge port 32；The agitating shaft 14 driven by driving device is installed in drying liner 5, is equipped on agitating shaft 14
Material can be stirred to the stirring plectrum 17 of conveying to 32 end of discharge port, be also equipped with material on agitating shaft 14 to far from discharge port
The screw auger 13 of 32 ends conveying；The stirring distance for stirring plectrum 17 and agitating shaft vertical direction is greater than screw auger 13 and stirring
The stirring distance of axis vertical direction.During agitating shaft 14 rotates, stirs plectrum 17 and screw auger 13 follows stir together
The rotation of axis 14 is mixed, stirring plectrum 17 conveys material toward 21 end of discharge port, avoids material from squeezing, screw auger 13 is by partial material
It toward far from the conveying of 32 end of discharge port, realizes conveying stirring back and forth, stirs evenly, material is heated also uniform.Exhaust outlet 15 and charging
Mouth 21 is separately positioned on the both ends top of drying liner 5, and feed inlet 21 and intake valve 22 are arranged in identical one end, pressure limiting
Valve 11 and exhaust outlet 15 are arranged in the other end.Because when material is just put into, moisture is higher, the temperature that when evaporation needs is also higher,
Steam is passed through from the intake valve 22 at 21 end of feed inlet, can accelerate material moisture evaporation, and make the vapor (steam) temperature base in vapor chamber 6
Originally it is consistent, conducive to being heated evenly for material, is dried while stirring more sufficiently.
The driving device is driven to the transmission device of 4 transmission case type of 4 belt-type of motor, 4 chain-type of motor or motor.
4 belt-type of motor is to be transmitted at agitating shaft using the power of motor output by belt, driving agitating shaft rotation；4 chain of motor
Formula is to be transmitted at agitating shaft using the power of motor output by chain, and driving agitating shaft rotates；4 transmission case type of motor is
Using the power of motor output by being transmitted at agitating shaft after transmission case, driving agitating shaft rotation.
Exhaust outlet 15 on the drying liner 5 is connected with cooler 19, and the import of cooler 19 and exhaust outlet 15 connect
It connects；The outlet of cooler 19 is connected with vacuum receiving tank 25；Vacuum receiving tank 25 passes through vacuum tube 26 and vacuum pump 27 and tail gas
Receiving tank 28 connects；The input end of cooler 19 is connect by condensation return pipt 20 with the top of cooling tower 29；Cooler 19
Outlet end is connect by condensate pipe 24 and water pump 30 with the lower part of cooling tower 29；Condensate pipe 24 is that cooler 19 provides condensation
Water.
The bottom of the vacuum receiving tank 25 is connected with fractionation bucket 31.Drying course uses the principle of negative-pressure adsorption, with
For drying agalloch eaglewood material, the moisture that agalloch eaglewood drying course evaporates is drawn onto condenser system, condensed mixing liquid is collected into
Vacuum receiving tank 25 is fractionated the liquid that vacuum receiving tank 25 is collected by being fractionated bucket 31, the agilawood essential oil that can be obtained and heavy
Fragrant hydrosol.
The drying liner 5 is equipped with relief valve 10 and observation window 12.
The bottom of the vapor chamber 6 is provided with blowdown valve 2 and drain valve 3.
The vapor chamber 6 is also equipped with pressure gauge 18.
The drying liner 5 is equipped with thermometer 16.
The flanged joint lid 23 maintained easily is also equipped on the casing 9.
Multiple groups stirring plectrum 17 is installed, every group of stirring plectrum 17 stirs plectrum 17 by 4-8 piece on the agitating shaft 14
Composition, and be evenly arranged on agitating shaft 14；Every two groups of adjacent 3 piece stirring plectrum 17 is installed in isosceles triangle, and is stirred plectrum 17 and stirred
The axis of noodles served with soy sauce, sesame butter, etc. and agitating shaft 14 is in 8-15 ° of angle.
Application Example
1, Guangxi Science and Technology Ltd., originally drying 500 kilograms of agalloch eaglewood materials using traditional roller dryer needs
Nearly 5 hours are wanted, wherein agalloch eaglewood material is the remaining agalloch eaglewood slag after the extraction of ultrasonic wave vacuum distillation, the agalloch eaglewood obtained after drying
Material shade deviation is larger, and fails to recycle agilawood essential oil；The agalloch eaglewood material negative pressure stirring and drying machine of the application was used later, together
Sample dries 500 kilograms of agalloch eaglewood materials, and the time-consuming agalloch eaglewood material shade deviation less than 3.5 hours, obtained after drying is little, vision effect
Fruit is good, and can be recovered to nearly 50 grams of agilawood essential oil.
The above description is not intended to limit the present invention, and the utility model is also not limited to examples detailed above, this technology
The those of ordinary skill in field, in the essential scope of the utility model, the variations, modifications, additions or substitutions made should all belong to
In the protection scope of the utility model.
Claims (9)
1. a kind of agalloch eaglewood material negative pressure stirring and drying machine, it is characterised in that: including rack (1) and casing (9), the casing
(9) accumbency is mounted on rack (1), is equipped with cylindrical drying liner (5) in casing (9)；Casing (9) and drying liner
(5) it is provided between vapor chamber shell (7), insulating layer (8) is provided between vapor chamber shell (7) and casing (9)；Vapor chamber shell (7)
Space between drying liner (5) is vapor chamber (6)；Vapor chamber (6) installs limited valve (11) and intake valve (22)；Drying
The top of liner (5) is provided with exhaust outlet (15) and feed inlet (21), and the bottom of drying liner (5) is provided with discharge port (32)；
The agitating shaft (14) driven by driving device is installed, being equipped on agitating shaft (14) can be by material to out in drying liner (5)
The stirring plectrum (17) of conveying is stirred at material mouth (32) end, is also equipped on agitating shaft (14) and holds material to far from discharge port (32)
The screw auger (13) of conveying；Stirring plectrum (17) and the stirring distance of agitating shaft vertical direction are greater than screw auger (13) and stir
Mix the stirring distance of axis vertical direction；Exhaust outlet (15) on the drying liner (5) is connected with cooler (19), cooler
(19) import is connect with exhaust outlet (15)；The outlet of cooler (19) is connected with vacuum receiving tank (25)；Vacuum receiving tank
(25) it is connect by vacuum tube (26) and vacuum pump (27) with tail gas receiving tank (28)；The input end of cooler (19) passes through condensation
Return pipe (20) is connect with the top of cooling tower (29)；The outlet end of cooler (19) passes through condensate pipe (24) and water pump (30)
It is connect with the lower part of cooling tower (29).
2. agalloch eaglewood material negative pressure stirring and drying machine according to claim 1, it is characterised in that: the driving device driving
For the transmission device of motor (4) belt-type, motor (4) chain-type or motor (4) transmission case type.
3. agalloch eaglewood material negative pressure stirring and drying machine according to claim 1, it is characterised in that: the vacuum receiving tank
(25) bottom is connected with fractionation bucket (31).
4. agalloch eaglewood material negative pressure stirring and drying machine according to claim 3, it is characterised in that: the drying liner (5)
Relief valve (10) and observation window (12) are installed.
5. agalloch eaglewood material negative pressure stirring and drying machine according to claim 1, it is characterised in that: the vapor chamber (6)
Bottom is provided with blowdown valve (2) and drain valve (3).
6. agalloch eaglewood material negative pressure stirring and drying machine according to claim 1, it is characterised in that: the vapor chamber (6) is also
Pressure gauge (18) are installed.
7. agalloch eaglewood material negative pressure stirring and drying machine according to claim 1, it is characterised in that: the drying liner (5)
Thermometer (16) are installed.
8. agalloch eaglewood material negative pressure stirring and drying machine according to claim 1, it is characterised in that: on the casing (9) also
The flanged joint lid (23) maintained easily is installed.
9. agalloch eaglewood material negative pressure stirring and drying machine according to claim 1, it is characterised in that: on the agitating shaft (14)
Multiple groups stirring plectrum (17) is installed, every group of stirring plectrum (17) is made of 4-8 piece stirring plectrum (17), and is evenly arranged on agitating shaft
(14) on；Every two groups of adjacent 3 piece stirring plectrum (17) is installed in isosceles triangle, and stirs plectrum (17) mixing surface and agitating shaft
(14) axis is in 8-15 ° of angle.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201822256797.8U CN209485017U (en) | 2018-12-29 | 2018-12-29 | Agalloch eaglewood material negative pressure stirring and drying machine |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201822256797.8U CN209485017U (en) | 2018-12-29 | 2018-12-29 | Agalloch eaglewood material negative pressure stirring and drying machine |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN209485017U true CN209485017U (en) | 2019-10-11 |
Family
ID=68128121
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201822256797.8U Active CN209485017U (en) | 2018-12-29 | 2018-12-29 | Agalloch eaglewood material negative pressure stirring and drying machine |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN209485017U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109612241A (en) * | 2018-12-29 | 2019-04-12 | 广西博能生物质能源科技有限公司 | Agalloch eaglewood material negative pressure stirring and drying device |
| CN111141137A (en) * | 2020-01-19 | 2020-05-12 | 浙江衣拿智能科技股份有限公司 | Conveying system with dryer |
| CN111219974A (en) * | 2020-03-04 | 2020-06-02 | 苏州环川节能设备有限公司 | Low-energy-consumption drying device and drying method thereof |
-
2018
- 2018-12-29 CN CN201822256797.8U patent/CN209485017U/en active Active
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109612241A (en) * | 2018-12-29 | 2019-04-12 | 广西博能生物质能源科技有限公司 | Agalloch eaglewood material negative pressure stirring and drying device |
| CN109612241B (en) * | 2018-12-29 | 2024-02-09 | 广西博能生物质能源科技有限公司 | Negative pressure stirring and drying device for agilawood materials |
| CN111141137A (en) * | 2020-01-19 | 2020-05-12 | 浙江衣拿智能科技股份有限公司 | Conveying system with dryer |
| CN111219974A (en) * | 2020-03-04 | 2020-06-02 | 苏州环川节能设备有限公司 | Low-energy-consumption drying device and drying method thereof |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN209485017U (en) | Agalloch eaglewood material negative pressure stirring and drying machine | |
| CN106382808B (en) | A kind of recycle heat utilizes formula medicinal material high-efficiency drying apparatus | |
| CN206222886U (en) | A kind of kudzu-vine root powder hot-air drying device with dehumidifier apparatus | |
| CN112273437A (en) | Method for preparing composite milk powder | |
| CN108800875A (en) | It is sectional temperature-controlled to control wet continuous agriculture spy flowing water heat pump drying line and furnace drying method | |
| CN206037596U (en) | Dregs of a decoction drying device is used in medicine liqueur production | |
| CN212870455U (en) | Horizontal disc vacuum drying machine system | |
| CN206260791U (en) | A kind of intelligent dryer of saving energy consumption | |
| CN109612241A (en) | Agalloch eaglewood material negative pressure stirring and drying device | |
| CN107668170A (en) | A kind of squid combined drying mechanism | |
| CN208312942U (en) | Rotary drier is used in a kind of manufacture of chemical industry | |
| CN108185492A (en) | A kind of food processing stirring dehydrating integrated machine | |
| CN216080895U (en) | Multilayer combination formula from falling drying equipment | |
| CN206875881U (en) | A kind of chemical industry solid particle material quick drying apparatus | |
| CN105716408A (en) | Low-temperature fodder drier | |
| CN213514681U (en) | Environment-friendly freeze dryer | |
| CN213687628U (en) | Chemical material drying device | |
| CN211170400U (en) | Solid waste drying device | |
| CN208500642U (en) | A kind of photoresist separation system of stripper regeneration technology section | |
| CN106616907A (en) | Thickener preparation system with uniform thermal performance | |
| CN107337707A (en) | A kind of drying enrichment facility of high efficiency extraction Fish protein | |
| CN207556209U (en) | A kind of drying equipment of new medicine pulvis animal-use drug | |
| CN206637984U (en) | One kind is used for grain heat-drying dehydrating unit | |
| CN220669986U (en) | Dryer convenient to refining | |
| CN106766761A (en) | A kind of root of kudzu vine roller drying machine |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant |