CN206011792U - A kind of extractor for producing intensified loquet distillate - Google Patents
A kind of extractor for producing intensified loquet distillate Download PDFInfo
- Publication number
- CN206011792U CN206011792U CN201620957247.7U CN201620957247U CN206011792U CN 206011792 U CN206011792 U CN 206011792U CN 201620957247 U CN201620957247 U CN 201620957247U CN 206011792 U CN206011792 U CN 206011792U
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- China
- Prior art keywords
- tank body
- motor
- control panel
- extractor
- liquid
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Abstract
The utility model discloses a kind of extractor for producing intensified loquet distillate, including tank body, motor, reducing motor, lifting motor, connecting shaft, paddle, dreg-discharging rod, rammer board, control panel, circular rotatable plate, adjust switch, deslagging pneumatic operated valve, slag notch, screen pack, liquid outlet, heat-insulation layer, journal stirrup, backwash interface, steam (vapor) outlet, charge door, temperature indicator, zone of heating and steam inlet, connecting shaft upper end is provided with paddle, the lower end of connecting shaft is provided with dreg-discharging rod and rammer board, deslagging pneumatic operated valve is electrically connected with control panel, the beneficial effect reached by the utility model is:It is easy to be sufficiently stirred for squeezing extraction liquid, reduce liquid waste, install control panel precise control processing temperature, time simultaneously, improve liquid and extract quality, and liquid is flowed out from double-side filtering net, it is to avoid cause residue to block, the utility model is convenient to be managed, extraction efficiency is high, is easy to the extraction of intensified loquet distillate.
Description
Technical field
The utility model is related to a kind of extractor, more particularly to a kind of extractor for producing intensified loquet distillate.
Background technology
Extractor is the leaching that the leaching that commonly uses in medication chemistry is particularly suitable for plant product ingredient
Extract.Structure has tank body, the rotary shaft in tank body outside the spiral propeller or rotating plasma propeller, with tank body of axial location means
Disk connects, and it is characterized in that the continuous reverse flow leaching with one group of horizontally-inclined extracts single tank, and discharging opening is connected with charging aperture each other
One linker of composition is connect, there is charging aperture, bottom there is residual liquid discharge port on the low side top of each single tank body, on tank body is high-end
There is inlet or exhaust outlet, bottom to have discharging opening in portion.The extractor of existing production loquat dew, process of manufacture extract effect
Rate, while substantial amounts of liquid can be contained in residue, cause to waste, and it is poor to filter out liquid effect, easily cause out liquid and block
Liquid residue is more with going out.
Utility model content
The utility model provides a kind of extractor for producing intensified loquet distillate, by installing paddle, dreg-discharging rod, pressure
Plate, control panel and deslagging pneumatic operated valve is squeezed, the extractor for effectively solving existing intensified loquet distillate efficiently cannot be carried
Take and cannot improve the problem that liquid extracts quality.
In order to solve above-mentioned technical problem, the utility model provides following technical scheme:
A kind of extractor for producing intensified loquet distillate of the utility model, including tank body, motor, reducing motor, liter
Drop motor, connecting shaft, paddle, dreg-discharging rod, rammer board, control panel, circular rotatable plate, adjust switch, deslagging pneumatic operated valve, go out
Cinder notch, screen pack, liquid outlet, heat-insulation layer, journal stirrup, backwash interface, steam (vapor) outlet, charge door, temperature indicator, zone of heating and
Steam inlet, the upper end of the tank body are provided with the motor, and the lower end of the motor connects the reducing motor and described
Lifting motor, the lower end of the lifting motor connect the connecting shaft, and the connecting shaft upper end is provided with the paddle, the company
The lower end of spindle is provided with the dreg-discharging rod and the rammer board, and the upper end of the tank body is provided with the control panel, the tank body
Lower end be provided with the circular rotatable plate, and one end connection of the rotor plate described adjusts switch, and the bottom of the tank body
The slag notch is provided with, the side of the slag notch connects the deslagging pneumatic operated valve, the deslagging pneumatic operated valve and the chain of command
Plate is electrically connected with.
As a kind of optimal technical scheme of the present utility model, the screen pack, and institute inside the tank body lower end, is provided with
The one end for stating screen pack connects the liquid outlet, and the bottom of the tank body is provided with the backwash interface.
As a kind of optimal technical scheme of the present utility model, the motor, the reducing motor and lifting electricity
Machine is electrically connected with the control panel.
Used as a kind of optimal technical scheme of the present utility model, the inwall of the tank body is provided with the zone of heating, described plus
Thermosphere is electrically connected with the control panel, and the tank wall is provided with the heat-insulation layer, and the tank wall is provided with institute
State journal stirrup and the temperature indicator.
Used as a kind of optimal technical scheme of the present utility model, the tank body upper end is provided with the steam inlet, the steaming
Vapor outlet and the charge door.
The beneficial effect reached by the utility model is:A kind of extraction for producing intensified loquet distillate of the utility model
Tank, by installing paddle and rammer board, is easy to be sufficiently stirred for squeezing extraction liquid, reduces liquid waste, while installing control
Panel precise control processing temperature, time, improve liquid and extract quality, and liquid is flowed out from double-side filtering net, it is to avoid make
Block into residue, the utility model is convenient to be managed, and extraction efficiency is high, is easy to the extraction of intensified loquet distillate.
Description of the drawings
Accompanying drawing is used for providing further understanding to of the present utility model, and constitutes a part for specification, with this practicality
New embodiment is used for together explaining the utility model, does not constitute to restriction of the present utility model.In the accompanying drawings:
Fig. 1 is structural representation of the present utility model;
Fig. 2 is the structural representation of the utility model circular rotatable plate;
In figure:1st, tank body;2nd, motor;3rd, reducing motor;4th, lifting motor;5th, connecting shaft;6th, paddle;7th, deslagging
Bar;8th, rammer board;9th, control panel;10th, circular rotatable plate;11st, switch is adjusted;12nd, deslagging pneumatic operated valve;13rd, slag notch;14、
Screen pack;15th, liquid outlet;16th, heat-insulation layer;17th, journal stirrup;18th, interface is backwashed;19th, steam (vapor) outlet;20th, charge door;21st, temperature
Degree display;22nd, zone of heating;23rd, steam inlet.
Specific embodiment
Preferred embodiment of the present utility model is illustrated below in conjunction with accompanying drawing, it will be appreciated that described herein excellent
Select embodiment to be merely to illustrate and explain the utility model, be not used to limit the utility model.
Embodiment
As shown in Figure 1-2, a kind of extractor for producing intensified loquet distillate of the utility model, including tank body 1, motor
2nd, reducing motor 3, lifting motor 4, connecting shaft 5, paddle 6, dreg-discharging rod 7, rammer board 8, control panel 9, circular rotatable plate 10,
Adjust switch 11, deslagging pneumatic operated valve 12, slag notch 13, screen pack 14, liquid outlet 15, heat-insulation layer 16, journal stirrup 17, backwash interface
18th, steam (vapor) outlet 19, charge door 20, temperature indicator 21, zone of heating 22 and steam inlet 23, the upper end of tank body 1 are provided with electronic
Machine 2, the lower end connection reducing motor 3 of motor 2 and lifting motor 4, the lower end connection connecting shaft 5 of lifting motor 4, connecting shaft 5
Upper end is provided with paddle 6, and the lower end of connecting shaft 5 is provided with dreg-discharging rod 7 and rammer board 8, and the upper end of tank body 1 is provided with control panel 9, tank
The lower end of body 1 is provided with circular rotatable plate 10, and one end connection of rotor plate 10 adjusts switch 11, and the bottom of tank body 1 is provided with out
Cinder notch 13, the side of slag notch 13 connect deslagging pneumatic operated valve 12, and deslagging pneumatic operated valve 12 is electrically connected with control panel 9.
Screen pack 14, and one end connection liquid outlet 15 of screen pack 14, and the bottom of tank body 1 is provided with inside 1 lower end of tank body
Backwash interface 18 is provided with, screen pack 14 is easy to high efficiency filter, residue and slag liquid inside backwash 18 medicine liquid washing of interface.Electronic
Machine 2, reducing motor 3 and lifting motor 4 are electrically connected with control panel 9, are easy to control processing, facilitate liquid to extract.Tank body 1
Inwall be provided with zone of heating 22, zone of heating 22 is electrically connected with control panel 9, and 1 outer wall of tank body is provided with heat-insulation layer 16, and tank body 1
Outer wall is provided with journal stirrup 17 and temperature indicator 21, and 22 medicine liquid heating of zone of heating extracts liquid, improves liquid outlet quantity.1 upper end of tank body
Steam inlet 23, steam (vapor) outlet 19 and charge door 20 is provided with, steam is used for secondary process.
Specifically, when the utility model is used, related medicinal material is added by charge door 20 first, is opened by control panel 9
Motor 2 is opened, and steam is added by steam inlet 2 and is opened zone of heating 22, paddle 6 is stirred to medicinal material, and
And medicinal material heating-up temperature is controlled by temperature indicator 21, liquid can be flowed out from liquid outlet 15 by screen pack 14;When liquid stream
Going out very slowly, 11 closing circular rotatable plates 10 of switch being adjusted by rotating, and open lifting motor 4, rammer board 8 is to liquid
Enter squeezing, the liquid that medicinal material is contained within fully is extruded;Motor 2 and the circular rotor plate 10 of rotation is again turned on, deslagging is controlled
Pneumatic operated valve 12 is opened, and is carried out cleaning residue by deslagging pneumatic operated valve 12 and dreg-discharging rod 7, is not resulted in blocking;Can finally pass through
Backwash interface 18, to being rinsed inside extractor 1, prevents from reusing, causes drug contamination.
The beneficial effect reached by the utility model is:A kind of extraction for producing intensified loquet distillate of the utility model
Tank, by installing paddle 6 and rammer board 8, is easy to be sufficiently stirred for squeezing extraction liquid, reduces liquid waste, while installing control
9 precise control processing temperature of panel processed, time, improve liquid and extract quality, and liquid is flowed out from double-side filtering net, it is to avoid
Residue is caused to block, the utility model is convenient to be managed, and extraction efficiency is high, is easy to the extraction of intensified loquet distillate.
Finally it should be noted that:Preferred embodiment of the present utility model is the foregoing is only, this is not limited to
Utility model, although being described in detail to the utility model with reference to the foregoing embodiments, for those skilled in the art
For, which still can be modified to the technical scheme described in foregoing embodiments, or to which part technical characteristic
Carry out equivalent.All of the present utility model spirit and principle within, any modification, equivalent substitution and improvements that is made etc.,
Should be included within protection domain of the present utility model.
Claims (5)
1. a kind of extractor for producing intensified loquet distillate, including tank body(1), motor(2), reducing motor(3), lifting electricity
Machine(4), connecting shaft(5), paddle(6), dreg-discharging rod(7), rammer board(8), control panel(9), circular rotatable plate(10), adjust
Switch(11), deslagging pneumatic operated valve(12), slag notch(13), screen pack(14), liquid outlet(15), heat-insulation layer(16), journal stirrup(17)、
Backwash interface(18), steam (vapor) outlet(19), charge door(20), temperature indicator(21), zone of heating(22)And steam inlet
(23), it is characterised in that the tank body(1)Upper end be provided with the motor(2), the motor(2)Lower end connection institute
State reducing motor(3)With the lifting motor(4), the lifting motor(4)Lower end connect the connecting shaft(5), the company
Spindle(5)Upper end is provided with the paddle(6), the connecting shaft(5)Lower end be provided with the dreg-discharging rod(7)With the rammer board
(8), the tank body(1)Upper end be provided with the control panel(9), the tank body(1)Lower end be provided with the circular rotatable plate
(10), and the rotor plate(10)One end connection described adjust switch(11), and the tank body(1)Bottom be provided with described go out
Cinder notch(13), the slag notch(13)Side connect the deslagging pneumatic operated valve(12), the deslagging pneumatic operated valve(12)With described
Control panel(9)It is electrically connected with.
2. a kind of extractor for producing intensified loquet distillate according to claim 1, it is characterised in that the tank body
(1)The screen pack is provided with inside lower end(14), and the screen pack(14)One end connect the liquid outlet(15), and described
Tank body(1)Bottom be provided with the backwash interface(18).
3. a kind of extractor for producing intensified loquet distillate according to claim 1, it is characterised in that the motor
(2), the reducing motor(3)With the lifting motor(4)With the control panel(9)It is electrically connected with.
4. a kind of extractor for producing intensified loquet distillate according to claim 1, it is characterised in that the tank body
(1)Inwall be provided with the zone of heating(22), the zone of heating(22)With the control panel(9)It is electrically connected with, the tank body
(1)Outer wall is provided with the heat-insulation layer(16), and the tank body(1)Outer wall is provided with the journal stirrup(17)With the temperature indicator
(21).
5. a kind of extractor for producing intensified loquet distillate according to claim 1, it is characterised in that the tank body
(1)Upper end is provided with the steam inlet(23), the steam (vapor) outlet(19)With the charge door(20).
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN201620957247.7U CN206011792U (en) | 2016-08-29 | 2016-08-29 | A kind of extractor for producing intensified loquet distillate |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201620957247.7U CN206011792U (en) | 2016-08-29 | 2016-08-29 | A kind of extractor for producing intensified loquet distillate |
Publications (1)
Publication Number | Publication Date |
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CN206011792U true CN206011792U (en) | 2017-03-15 |
Family
ID=58251748
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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CN201620957247.7U Expired - Fee Related CN206011792U (en) | 2016-08-29 | 2016-08-29 | A kind of extractor for producing intensified loquet distillate |
Country Status (1)
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CN (1) | CN206011792U (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN108607236A (en) * | 2018-05-15 | 2018-10-02 | 重庆市洲仨科技发展有限公司 | Plant polyphenol separation and extraction system |
CN114307231A (en) * | 2020-09-27 | 2022-04-12 | 怀化市富源油业有限公司 | Extraction element is used in vegetable oil processing |
CN114534304A (en) * | 2021-12-27 | 2022-05-27 | 桐庐雷泰生物科技有限公司 | Integral type capsaicin draws separator |
-
2016
- 2016-08-29 CN CN201620957247.7U patent/CN206011792U/en not_active Expired - Fee Related
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN108607236A (en) * | 2018-05-15 | 2018-10-02 | 重庆市洲仨科技发展有限公司 | Plant polyphenol separation and extraction system |
CN114307231A (en) * | 2020-09-27 | 2022-04-12 | 怀化市富源油业有限公司 | Extraction element is used in vegetable oil processing |
CN114534304A (en) * | 2021-12-27 | 2022-05-27 | 桐庐雷泰生物科技有限公司 | Integral type capsaicin draws separator |
CN114534304B (en) * | 2021-12-27 | 2024-04-02 | 桐庐雷泰生物科技有限公司 | Integrated capsaicin extracting and separating device |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20170315 Termination date: 20200829 |
|
CF01 | Termination of patent right due to non-payment of annual fee |