CN208678403U - A kind of natural borneol high efficiency extraction system - Google Patents
A kind of natural borneol high efficiency extraction system Download PDFInfo
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- CN208678403U CN208678403U CN201820765283.2U CN201820765283U CN208678403U CN 208678403 U CN208678403 U CN 208678403U CN 201820765283 U CN201820765283 U CN 201820765283U CN 208678403 U CN208678403 U CN 208678403U
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- hollow cylinder
- borneol
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Abstract
The utility model discloses a kind of natural borneol high efficiency extraction system, including distilling apparatus and condensing unit, distilling apparatus includes tank body and material frame component, and tank interior is divided into the distillery of top and the steam generating chamber of lower section by net partition；At least one heating coil is equipped in steam generation room；The material frame is inserted into distillery from indentation, there；Condensing unit includes hollow cylinder, scrapes brilliant component and recirculating cooling water system, and scraping brilliant component includes the second motor and scraper plate；Second motor is set to the outer top of hollow cylinder, and the second output shaft of the second motor stretches in the upper plenum of hollow cylinder；The end of second output shaft is connected with one end of scraper plate；Right side at the top of hollow cylinder at the top of steam pipe and tank body by being connected；The position that diaphragm plate corresponds to lower-left cavity is covered with through-hole, is equipped with taper aggregate bin in the cavity of lower-left.The utility model manufacturing cost is low, facilitates the charging of borneol camphor tree branches and leaves in distilling apparatus and reloads, while condensing unit borneol extraction efficiency is high.
Description
Technical field
The utility model relates to active components of plants extractive technique fields, more particularly, to a kind of natural borneol high efficiency extraction
System.
Background technique
Borneol camphor tree is subtropical zone economic tree, and timber, root and branches and leaves are the important source materials for extracting camphor and camphor oil, for doctor
Medicine and perfume industry are used.Borneol also known as piece brain, orange slices, kapur are that the resin of Spore density borneol camphor tree and volatile oil add
The crystallization that work product extract, purifying obtains, is near pure d-Bomeol.Its gas faint scent, bitter, Xin Liang, can be used for leading to all
Key dissipates stagnated fire, swelling and pain relieving, heat reliving and toxin-eliminating, goes screen improving eyesight, closes card coma, for red eye, swell pain, sore throat aphtha, sore swell and ache curative,
It is not held back after bursting.The produced natural borneol in China mainly extracts from the branches and leaves of lauraceae plant borneol camphor tree and by purification
At it is free of the isoborneol being harmful to the human body, and medicinal effects are far superior to synthetic borneol and natural L-Borneol.It is existing natural
Commonly not only economic but also efficient extracting method had been hydrodistillation method, detailed process to borneol are as follows: dragon is placed in distilling apparatus
The fresh branches and leaves of brain camphor tree add boiling to boil or be passed through water vapour, the volatile oil in branches and leaves are steamed, and mixed vapour enters condensing unit,
There is the characteristic of distillation using natural borneol, directly crystallized on condensing unit after condensation, other volatile oil and water enter grease
It is separated in separator.However the existing equipment for extracting natural borneol, not only structure is complicated, and manufacturing cost is high, and is inconvenient to steam
It the charging of borneol camphor tree branches and leaves and reloads in distillation unit, while condensing unit borneol extraction efficiency is low.
Utility model content
The purpose of this utility model is that simple, the manufacturing cost that overcome the deficiencies of the prior art and provide a kind of structure
It is low, facilitate the charging of borneol camphor tree branches and leaves in distilling apparatus and reload, while the natural borneol that condensing unit borneol extraction efficiency is high
High efficiency extraction system.To achieve the goals above, the utility model provides a kind of natural borneol high efficiency extraction system, including steams
Distillation unit and condensing unit, the distilling apparatus include tank body and material frame component, and the tank interior is divided by net partition
The distillery of side and the steam generating chamber of lower section；At least one heating coil is equipped in the steam generation room；The steam hair
Raw room is equipped with water inlet pipe and outlet pipe；The top of the distillery is equipped with safety valve；
The front inner wall and rear side inner wall of the distillery are opposite to be equipped with two guide rails；The right side inner wall of the distillery with lead
Rail flush is equipped with notch；The material frame component includes material frame, transmission parts and pedestal, the transmission parts include rack gear,
Gear and first motor；
The material frame is inserted into distillery from indentation, there, and passes through two guide supportings；The outer right wall of the material frame with
One end of rack gear vertically connects, and the other end of the rack gear is meshed with gear, and the gear is installed on the first of first motor
On output shaft, the first motor is mounted on the base, and the pedestal is located at the outside of tank body；
The distillery is equipped with inclined feed pipe in the top for being located at material frame；Feed pipe is equipped with the first valve
Door.
The condensing unit includes hollow cylinder, scrapes brilliant component and recirculating cooling water system, and described to scrape brilliant component include the
Two motors and scraper plate, the hollow cylinder are separated into upper plenum and lower cavity by diaphragm plate, and the lower cavity is separated by midfeather
At lower-left cavity and bottom right cavity；Second motor is set to the outer top of hollow cylinder, and the second output shaft of the second motor is stretched
Enter to the upper plenum of hollow cylinder；The end of second output shaft is connected with one end of scraper plate, and the scraper plate is in level
The plane of state and bottom fitting diaphragm plate；It the arc-shaped structure of the other end of the scraper plate and is affixed with hollow cylinder circumferential inner wall
It closes；
Right side at the top of the hollow cylinder at the top of steam pipe and tank body by being connected；The left side of the hollow cylinder
Equipped with ejected wash water inlet pipe and ejected wash water inlet pipe is equipped with the second valve；
The position that the diaphragm plate corresponds to lower-left cavity is covered with through-hole, and through-hole penetrates through upper plenum and lower-left cavity；The left side
Taper aggregate bin, the material mouth connection straight tube of the taper aggregate bin and the bottom for extending hollow cylinder are equipped in lower cavity；
Inlet and outlet are respectively equipped with above and below the bottom right cavity；The inlet and outlet difference
It is connected with the cooling water outlet of recirculating cooling water system and room temperature water inlet.
The utility model distilling apparatus is in use, open the first valve on feed pipe, and the fresh branches and leaves of borneol camphor tree are along being in
The feed pipe of heeling condition is fallen into material frame, feeds quite convenient, the first valve of closing after having fed.Pass through steam generating chamber
Water inlet pipe and outlet pipe realize steam generation room in plus water and draining, by heating coil realize water heating with generate steam
Vapour, the steam of generation pass through net partition and enter distillery, steams the volatile oil in the fresh branches and leaves of borneol camphor tree, mixed vapour from
Steam pipe is expelled to condensing unit and carries out condensation-crystallization, and structure is simple, easy to use.The wherein use of safety valve, is effectively ensured
Effective operation of the utility model distilling apparatus is with equipment using safe.
The working principle of the utility model condensing unit is as follows: from the mixed vapour that generates after distilling apparatus distillation from steam
Pipe enters upper plenum, while recirculating cooling water system is passed through cooling water into bottom right cavity, under the action of cooling water, diaphragm plate
Corresponding bottom right re-entrant portion cools down rapidly, so that the quick condensation-crystallization on diaphragm plate of natural borneol in mixed vapour, same with this
The second motor of Shi Qidong, for the rotation of the second output shaft to drive scraper plate circle rotation, scraper plate circle rotation scrapes natural borneol, and day
Right borneol is fallen into from through-hole to the taper aggregate bin of lower-left cavity, and is come out from straight tube, and borneol extraction efficiency is high.
After natural borneol has extracted, the second valve on ejected wash water inlet pipe is opened, water enters in upper plenum, starts simultaneously
Second motor, scraper plate circle rotation to scrape diaphragm plate, gather materials by the taper that the sewage after cleaning is fallen into from through-hole to lower-left cavity
In bucket, and flowed out from straight tube, it is easy to clean and high-efficient.
When the utility model distilling apparatus needs to change borneol camphor tree branches and leaves, starting first motor is rotated forward, and is rotated with band moving gear,
Gear is rotated to drive meshed rack gear to move horizontally, so that the material frame being connected with rack gear be driven to move along guide rail
Dynamic, i.e. rack drives material frame moves right, when rack drives material frame move right the right end to material frame be located at indentation, there when, that is, expect
When frame is pulled out to maximum distance, material frame still passes through tank body and pedestal effectively supports.Distillation is completed in material frame at this time
The borneol camphor tree branches and leaves exposed outside in tank body completely, the borneol camphor tree branches and leaves that distillation is completed in material frame are taken out, restart first
Motor reversal, rack drives material frame are moved to the left material frame and are fully inserted into tank body, open the first valve on feed pipe, dragon
The fresh branches and leaves of brain camphor tree are fallen into along inclined feed pipe to material frame, so complete the replacement of borneol camphor tree branches and leaves,
Replace automation pull-out and propulsion simple and convenient, while that realize material frame, high degree of automation.
The combined use of the utility model net partition and metal mesh, is on the one hand that steam is facilitated to penetrate, and is on the other hand to use
In preventing borneol camphor tree branches and leaves from falling in steam generation room.
The utility model notch is concordant with guide rail to be arranged, and wherein the size of notch and the sectional dimension of material frame are identical, so that
When material frame is inserted into tank body, material frame can close notch.
Further, inlet valve and outlet valve are respectively equipped on the water inlet pipe and outlet pipe.The utility model by into
Water pipe and outlet pipe are realized in steam generation room plus water and draining, when add water or draining close after the completion corresponding inlet valve or
Outlet valve.
Further, high liquid level sensor and low liquid level sensor are equipped in the steam generation room, the high liquid level passes
Sensor and low liquid level sensor pass through conducting wire and are connected with controller, and the controller is connected with inlet valve and outlet valve respectively
It connects.It is used to detect the peak level and lowest water level in steam generation room by high liquid level sensor and low liquid level sensor, and
The information that will test is sent to controller, under the action of controller, the opening and closing of automatic inlet valve.When reaching
When lowest water level, controller controls inlet valve and opens, and water, when being added to peak level, controller are added in previous steam generation room
It controls inlet valve to close, water is added to finish, realize the automation process for adding water.The wherein design of outlet pipe and outlet valve, to need
Depleted of steam occurs to use when the drainage situations such as indoor water or cleaning distilling apparatus.
Further, two blend stops are relatively provided on the tank body inner left wall and right side inner wall, the net partition rides over
On two blend stops.The use of the utility model blend stop facilitates the placement and taking-up and cleaning of net partition.
Further, metal mesh of the material frame by quadro frame and set on quadro frame bottom forms.
Further, the mesh of the net partition is less than the mesh of metal mesh.Practical manufacturing process, net partition and metal mesh
The size of mesh need to guarantee that borneol camphor tree branches and leaves are not fallen out to steam generation room.
Further, between the outer right wall and pedestal of the tank body be equipped with collection material frame, collection material frame be located at rack gear just under
Side, wherein extending the front side outer wall of tank body outside the front of collection material frame.So when replacing the borneol camphor tree branches and leaves in material frame, material frame
When being drawn out to outside tank body under the action of transmission parts, borneol camphor tree branches and leaves are removed and placed from material frame by collection material frame using tool
It is interior.
Further, the heating coil is connected by data line with power connection.To be inserted by power connection
It in seat, realizes and is powered, heating coil realizes water heating.
Further, the diaphragm plate uses copper sheet.Copper sheet heat conduction efficiency is high, so improves the condensation of natural borneol
Crystallization rate.
Further, the hollow cylinder is equipped with insulating layer around corresponding bottom right cavity.I.e. bottom right cavity is not right
It answers and sets insulating layer around diaphragm plate, to guarantee the temperature of cooling water, to improve the condensation-crystallization speed of natural borneol.
It is easy to use the utility model has the beneficial effects that the utility model structure is simple, on tank body it is inclined into
The design of expects pipe facilitates the charging of borneol camphor tree branches and leaves, improves charging rate.Notch and material frame component on the utility model tank body
Matching design, not only facilitate the replacement of borneol camphor tree branches and leaves, while improving the replacement speed of borneol camphor tree branches and leaves, and realize material
The automation of frame is pulled out and is promoted, high degree of automation.The utility model distilling apparatus is effectively ensured in the wherein use of safety valve
Effective operation and equipment using safe.While the utility model realizes the automation in steam generation room and adds water, automatically
Change degree is high.And the utility model structure is simple, manufacturing cost is low, and condensing unit effectively increases the condensation-crystallization speed of borneol
Degree, and borneol extraction efficiency is improved, while condensing unit is easy to clean.
Detailed description of the invention
In order to illustrate the embodiment of the utility model or the technical proposal in the existing technology more clearly, below will be to embodiment
Or attached drawing needed to be used in the description of the prior art is briefly described, it should be apparent that, the accompanying drawings in the following description is only
It is some embodiments of the utility model, for those of ordinary skill in the art, in the premise not made the creative labor
Under, it is also possible to obtain other drawings based on these drawings.
Fig. 1 is the structural schematic diagram of the utility model.
Fig. 2 is the A-A cross-sectional view that distilling apparatus is corresponded in Fig. 1.
Fig. 3 is the B-B cross-sectional view that condensing unit is corresponded in Fig. 1.
Above-mentioned appended drawing reference:
1 tank body, 2 material frames, 3 guide rails, 4 net partitions, 5 blend stops, 6 heating coils, 7 water inlet pipes, 8 outlet pipes, 9 feed pipes, 10
Safety valve, 101 distilleries, 102 steam generating chamber, 11 high liquid level sensors, 12 low liquid level sensors, 13 first valves, 14 teeth
Item, 15 first motors, 16 pedestals, 17 collection material frames, 18 gears, 19 first output shafts, 20 quadro frames, 21 metal meshes, 22 steam
Pipe, 23 hollow cylinders, 230 upper plenums, 231 lower-left cavitys, 232 bottom right cavitys, 24 second motors, 25 second output shafts, 26 scrape
Plate, 27 diaphragm plates, 271 through-holes, 28 midfeathers, 29 taper aggregate bins, 30 straight tubes, 31 recirculating cooling water systems, 32 ejected wash waters into
Pipe.
Specific embodiment
Utility model is further illustrated with reference to the accompanying drawing, but is not intended to limit the scope of the present invention.
As shown in Figure 1-3, a kind of natural borneol high efficiency extraction system provided by the utility model, including distilling apparatus and cold
Solidifying device, the distilling apparatus include tank body 1 and material frame component, are divided into the distillation of top inside the tank body 1 by net partition 4
The steam generating chamber 102 of room 101 and lower section；At least one heating coil 6, the steam are equipped in the steam generating chamber 102
Room 102 occurs and is equipped with water inlet pipe 7 and outlet pipe 8.In actual production process, the number of 6 quantity of heating coil need to consider temperature,
The factors such as steam pressure.
The front inner wall and rear side inner wall of the distillery 101 are opposite to be equipped with two guide rails 3, and guide rail 3 is welded into 1 phase of tank body
One.The right side inner wall of the distillery 101 is equipped with notch with 3 flush of guide rail.
The material frame component includes material frame 2, transmission parts and pedestal 19, and the transmission parts include rack gear 14, gear 18
With first motor 15.
The material frame 2 is inserted into distillery 101 from indentation, there, and is supported by two guide rails 3；The right side of the material frame 2
Outer wall is vertical with one end of rack gear 14 to be connect, and rack gear 14 is welded with 2 phase of material frame.The other end of the rack gear 14 is nibbled with 18 phase of gear
It closes, the gear 18 is installed on the first output shaft 19 of first motor 15, and the first motor 15 is installed on pedestal 16, institute
State the outside that pedestal 16 is located at tank body 1；Wherein first motor 15 is bolted by bolt hole thereon with pedestal 16.
The distillery 101 is equipped with inclined feed pipe 9 in the top for being located at material frame 2；Feed pipe 9 is equipped with the
One valve 13.
The condensing unit includes hollow cylinder 23, scrapes brilliant component and recirculating cooling water system 31, described to scrape brilliant component packet
The second motor 24 and scraper plate 26 are included, the hollow cylinder 23 is separated into upper plenum 230 and lower cavity, the lower sky by diaphragm plate 27
Chamber is separated into lower-left cavity 231 and bottom right cavity 232 by midfeather 28；Second motor 24 is set to outside hollow cylinder 23 and pushes up
Portion, and the second output shaft 25 of the second motor 24 stretches in the upper plenum 230 of hollow cylinder 23；Second output shaft 25
End is connected with one end of scraper plate 26, and the scraper plate 26 is in a horizontal state and the plane of bottom fitting diaphragm plate 27；It is described to scrape
It the arc-shaped structure of the other end of plate 26 and fits with 23 circumferential inner wall of hollow cylinder.Wherein the second output shaft of the second motor 24
25 are connected with scraper plate 26 using key.
The right side at 23 top of hollow cylinder is connected by steam pipe 22 with the top of tank body 1；The hollow cylinder
23 left side is equipped with ejected wash water inlet pipe 32 and ejected wash water inlet pipe 32 is equipped with the second valve.
The position of the corresponding lower-left cavity 231 of the diaphragm plate 27 is covered with through-hole 271, and through-hole 271 penetrates through upper plenum 230 and a left side
Lower cavity 231；Taper aggregate bin 29 is equipped in the lower-left cavity 231, the material mouth of the taper aggregate bin 29 connects straight tube 30
And extend the bottom of hollow cylinder 23.
Inlet and outlet are respectively equipped with above and below the bottom right cavity 232；The inlet and outlet
It is connected respectively with the cooling water outlet of recirculating cooling water system 31 and room temperature water inlet.
Inlet valve and outlet valve are respectively equipped on the water inlet pipe 7 and outlet pipe 8.
Two blend stops 5 are relatively provided in 1 inner left wall of tank body and right side inner wall, blend stop 5 and tank body 1 are welded into one
Body.The net partition 4 rides on two blend stops 5.
Metal mesh 21 of the material frame 2 by quadro frame 20 and set on 20 bottom of quadro frame forms.Metal mesh 21 and four
Square bearer 20 is integrally welded.
The mesh of the net partition 4 is less than the mesh of metal mesh 21.
Collection material frame 17 is equipped between the outer right wall and pedestal of the tank body 1, collection material frame 17 is located at the underface of rack gear 14,
Wherein collect the front side outer wall for extending tank body 1 outside the front of material frame 17.
The heating coil 6 is connected by data line with power connection.It connects power supply to facilitate and is powered.
The utility model recirculating cooling water system 31 directlys adopt the prior art, and it is the technology of existing maturation, so
Cost is researched and developed to reduce.Existing recirculating cooling water system 31 is cooling water heat-exchanging water and through cooling down, and recycled gives water system
System, including open type and closed two types are made of cooling equipment, water pump and pipeline.With open type circulating cooling water system
For system, by following part: cooling tower, heat exchanger, compression system (water circulating pump), other filter system (filter-press), moisturizing
Pond, monitoring system.
The utility model distilling apparatus in use, open feed pipe 9 on the first valve 13, the fresh branches and leaves of borneol camphor tree along
Inclined feed pipe 9 is fallen into material frame 2, feeds quite convenient, the first valve 13 of closing after having fed.Pass through steam
The water inlet pipe 7 and outlet pipe 8 that room 102 occurs realize in steam generating chamber 102 plus water and draining, are realized by heating coil 6
To generate steam, the steam of generation passes through net partition 4 and enters distillery 101 for the heating of water, will be in the fresh branches and leaves of borneol camphor tree
Volatile oil steams, and mixed vapour is expelled to condensing unit from steam pipe 22 and carries out condensation-crystallization, and structure is simple, easy to use.Its
The use of middle safety valve 10 is effectively ensured the effective of the utility model distilling apparatus and runs with equipment using safe.
The working principle of the utility model condensing unit is as follows: from the mixed vapour that generates after distilling apparatus distillation from steam
Pipe 22 enters upper plenum 230, while recirculating cooling water system 31 is passed through cooling water into bottom right cavity 232, in the work of cooling water
Under, corresponding 232 position of bottom right cavity of diaphragm plate 27 is cooled down rapidly, so that natural borneol is quickly in diaphragm plate 27 in mixed vapour
Upper condensation-crystallization, starts the second motor 24 at the same time, and the second output shaft 25 is rotated to drive 26 circle rotation of scraper plate, scraper plate 26
Circle rotation scrapes natural borneol, and natural borneol is fallen into from through-hole 271 to the taper aggregate bin 29 of lower-left cavity 231, and
Come out from straight tube 30, borneol extraction efficiency is high, straight tube 8 can external Material collecting box for harvesting to collect natural borneol.
After natural borneol has extracted, the second valve on ejected wash water inlet pipe 32 is opened, water enters in upper plenum 230, together
The second motor of Shi Qidong 24, to scrape diaphragm plate 27, the sewage after cleaning is fallen into from through-hole 271 to lower-left 26 circle rotation of scraper plate
In the taper aggregate bin 29 of cavity 231, and flowed out from straight tube 30, it is easy to clean and high-efficient.When cleaning, Material collecting box for harvesting is taken away,
Header tank is changed, to collect sewage.
When the utility model distilling apparatus needs to change borneol camphor tree branches and leaves, starting first motor 15 is rotated forward, with band moving gear 18
Rotation, gear 18 are rotated to drive meshed rack gear 14 to move horizontally, to drive the material frame 2 being connected with rack gear 14
It is moved along guide rail 3, i.e., rack gear 14 drives material frame 2 to move right, when rack gear 14 drives material frame 2 to move right to the right side of material frame 2
When end is located at indentation, there, i.e., when material frame 2 is pulled out to maximum distance, material frame 2 is still effectively propped up by tank body 1 and pedestal 16
Support.The borneol camphor tree branches and leaves exposed outside in tank body 1 completely of distillation is completed in material frame 2 at this time, distillation will be completed in material frame 2
Borneol camphor tree branches and leaves take out, restart the reversion of first motor 15, rack gear 14 drives material frame 2 to be moved to the left material frame 2 and be fully inserted into
To tank body 1, the first valve 13 on feed pipe 9 is opened, the fresh branches and leaves of borneol camphor tree are fallen into along inclined feed pipe 9
To material frame 2, the replacement of borneol camphor tree branches and leaves is so completed, replaces automation drawing that is simple and convenient, while realizing material frame 2
Out and promote, high degree of automation.
Embodiment two
On the basis of example 1, high liquid level sensor 11 is equipped in the steam generating chamber 102 and low liquid level senses
Device 12, the high liquid level sensor 11 and low liquid level sensor 12 are connected by conducting wire with controller, the controller point
It is not connected with inlet valve and outlet valve.By high liquid level sensor 11 and low liquid level sensor 12 for detecting steam generating chamber
Peak level and lowest water level in 102, and the information that will test is sent to controller, under the action of controller, automatically
Control the opening and closing of inlet valve.When reaching lowest water level, controller controls inlet valve and opens, previous steam generating chamber
Add water in 102, when being added to peak level, controller controls inlet valve and closes, and adds water to finish, realization plus the automation of water
Journey.The wherein design of outlet pipe 8 and outlet valve, to need depleted of steam that the water in room 102 or cleaning distilling apparatus etc. occurs
It is used when drainage situation.
Basic principles, main features, and advantages of the present invention has been shown and described above.Current row
The technical staff of industry is described in above embodiments and description it should be appreciated that the present utility model is not limited to the above embodiments
Only illustrate the principles of the present invention, the utility model can also on the premise of not departing from the spirit and scope of the utility model
There are various changes and modifications, these various changes and improvements fall within the scope of the claimed invention.The utility model is wanted
Protection scope is asked to be defined by appended claims and its equivalent.
Claims (9)
1. a kind of natural borneol high efficiency extraction system, which is characterized in that including distilling apparatus and condensing unit, the distilling apparatus
Including tank body and material frame component, the tank interior is divided into the distillery of top and the steam generating chamber of lower section by net partition；
At least one heating coil is equipped in the steam generation room；The steam generating chamber is equipped with water inlet pipe and outlet pipe；It is described
The top of distillery is equipped with safety valve；
The front inner wall and rear side inner wall of the distillery are opposite to be equipped with two guide rails；The right side inner wall of the distillery and guide rail phase
Concordant is equipped with notch；The material frame component includes material frame, transmission parts and pedestal, and the transmission parts include rack gear, gear
And first motor；
The material frame is inserted into distillery from indentation, there, and passes through two guide supportings；The outer right wall and rack gear of the material frame
One end vertically connect, the other end of the rack gear is meshed with gear, the gear be installed on first motor first output
On axis, the first motor is mounted on the base, and the pedestal is located at the outside of tank body；
The distillery is equipped with inclined feed pipe in the top for being located at material frame；Feed pipe is equipped with the first valve；
The condensing unit includes hollow cylinder, scrapes brilliant component and recirculating cooling water system, and described to scrape brilliant component include the second electricity
Machine and scraper plate, the hollow cylinder are separated into upper plenum and lower cavity by diaphragm plate, and the lower cavity is separated into a left side by midfeather
Lower cavity and bottom right cavity；Second motor is set to the outer top of hollow cylinder, and the second output shaft of the second motor stretches to
In the upper plenum of hollow cylinder；The end of second output shaft is connected with one end of scraper plate, and the scraper plate is in a horizontal state
And the plane of bottom fitting diaphragm plate；It the arc-shaped structure of the other end of the scraper plate and fits with hollow cylinder circumferential inner wall；
Right side at the top of the hollow cylinder at the top of steam pipe and tank body by being connected；The left side of the hollow cylinder is equipped with
Ejected wash water inlet pipe and ejected wash water inlet pipe are equipped with the second valve；
The position that the diaphragm plate corresponds to lower-left cavity is covered with through-hole, and through-hole penetrates through upper plenum and lower-left cavity；The lower-left is empty
It is intracavitary to be equipped with taper aggregate bin, the material mouth connection straight tube of the taper aggregate bin and the bottom for extending hollow cylinder；
Inlet and outlet are respectively equipped with above and below the bottom right cavity；The inlet and outlet respectively with follow
The cooling water outlet of ring cooling water system is connected with room temperature water inlet.
2. a kind of natural borneol high efficiency extraction system according to claim 1, which is characterized in that the water inlet pipe and water outlet
Inlet valve and outlet valve are respectively equipped on pipe.
3. a kind of natural borneol high efficiency extraction system according to claim 2, which is characterized in that in the steam generation room
Equipped with high liquid level sensor and low liquid level sensor, the high liquid level sensor and low liquid level sensor pass through conducting wire and control
Device is connected, and the controller is connected with inlet valve and outlet valve respectively.
4. a kind of natural borneol high efficiency extraction system according to claim 1, which is characterized in that the tank body inner left wall
With two blend stops are relatively provided on the inner wall of right side, the net partition rides on two blend stops.
5. a kind of natural borneol high efficiency extraction system according to claim 1, which is characterized in that the material frame is by four boxes
Frame and set on quadro frame bottom metal mesh form；The mesh of the net partition is less than the mesh of metal mesh.
6. a kind of natural borneol high efficiency extraction system according to claim 1, which is characterized in that outside the right side of the tank body
Collection material frame is equipped between wall and pedestal, collection material frame is located at the underface of rack gear, wherein extending tank body outside the front of collection material frame
Front side outer wall.
7. a kind of natural borneol high efficiency extraction system according to claim 1, which is characterized in that the heating coil passes through
Data line is connected with power connection.
8. a kind of natural borneol high efficiency extraction system according to claim 1, which is characterized in that the diaphragm plate uses copper
Plate.
9. a kind of natural borneol high efficiency extraction system according to claim 1, which is characterized in that the hollow cylinder is right
It answers and is equipped with insulating layer around the cavity of bottom right.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820765283.2U CN208678403U (en) | 2018-05-22 | 2018-05-22 | A kind of natural borneol high efficiency extraction system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820765283.2U CN208678403U (en) | 2018-05-22 | 2018-05-22 | A kind of natural borneol high efficiency extraction system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN208678403U true CN208678403U (en) | 2019-04-02 |
Family
ID=65877358
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201820765283.2U Expired - Fee Related CN208678403U (en) | 2018-05-22 | 2018-05-22 | A kind of natural borneol high efficiency extraction system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN208678403U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113149815A (en) * | 2021-05-13 | 2021-07-23 | 安徽右旋龙脑生物科技有限公司 | Extraction system and extraction method of high-purity borneol |
-
2018
- 2018-05-22 CN CN201820765283.2U patent/CN208678403U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113149815A (en) * | 2021-05-13 | 2021-07-23 | 安徽右旋龙脑生物科技有限公司 | Extraction system and extraction method of high-purity borneol |
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Granted publication date: 20190402 Termination date: 20200522 |