CN206391625U - One Plant Extracts extraction equipment - Google Patents
One Plant Extracts extraction equipment Download PDFInfo
- Publication number
- CN206391625U CN206391625U CN201720037079.4U CN201720037079U CN206391625U CN 206391625 U CN206391625 U CN 206391625U CN 201720037079 U CN201720037079 U CN 201720037079U CN 206391625 U CN206391625 U CN 206391625U
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- Prior art keywords
- pipe
- magnetic valve
- layer
- dissolving
- solution
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Abstract
The Plant Extracts extraction equipment of the utility model one, including tank body, control cabinet and feed pipe one are respectively equipped with the top of the tank body, the control cabinet is located at the side of feed pipe one, the control box cavity is provided with PLC and stepper motor, the tank body side is sequentially provided with feed pipe two from top to bottom, bleed pipe, the bleed pipe is provided with magnetic valve one, the tank body opposite side is provided with feed back pipe, by the way that organic solvent and material liquid are sufficiently mixed into dissolving provided with dissolving layer and cooling layer, heating plate improves the temperature of solution, the course of dissolution of common aggravation solute, by provided with magnetic valve, solution is carried out secondary agitation filtering by compression pump with feed back pipe, improve the utilization rate of equipment, also increase the intelligent of device, by being filtered provided with filter to solution, separate out corresponding impurity and moisture, by setting temperature-constant plate the temperature of solution is first reduced a part, help to enter the separation that separator carries out next step by discharge nozzle.
Description
Technical field
The utility model is related to a Plant Extracts extraction equipment, more particularly to a Plant Extracts extraction equipment.
Background technology
Plant extracts be using plant as raw material, according to the purposes to the final products of extraction the need for, by physico
Learn and extract separation process, a certain kind or plurality of active ingredients in orientation acquisition and concentration plant, without changing its active ingredient
Product formed by structure, at present, the product concept of plant extracts are more wide in range, different according to the composition for extracting plant, shape
It is different according to the character of final products into glucoside, acid, polyphenol, polysaccharide, terpene, flavones, alkaloid etc., vegetable oil, leaching can be divided into
Cream, powder, crystalline lens etc., plant extract industry are to grow up for nearest 20 years, belong to an emerging industry, plant at this stage
The most complex manufacturing of extract solution extraction equipment, cost is higher, and the utilization rate to equipment is relatively low, and current extraction equipment intelligence
Degree can be changed relatively low, result in that extraction efficiency is relatively low, and might have in extraction process the phenomenon of impurity residual.
Utility model content
The utility model proposes a Plant Extracts extraction equipment, complex manufacturing, equipment in the prior art are solved
Cost is higher and utilization rate of equipment and installations is relatively low, and caused extraction efficiency is low, in extraction process it is possible that impurity residual lacks
Point；By the way that organic solvent and material liquid are sufficiently mixed into dissolving provided with dissolving layer and cooling layer, by provided with stepper motor to molten
Liquid is stirred, and heating plate improves the temperature of solution, the course of dissolution of common aggravation solute, by provided with magnetic valve, pressure
Solution is carried out secondary agitation filtering by pump with feed back pipe, is improved the utilization rate of equipment, the intelligent of device is also increased, by setting
There is filter to filter solution, corresponding impurity and moisture are separated out, by setting temperature-constant plate the temperature of solution is first dropped
A low part, helps to enter the separation that separator carries out next step by discharge nozzle.
In order to solve the above-mentioned technical problem, the utility model provides following technical scheme：
The Plant Extracts extraction equipment of the utility model one, including tank body, the tank body are sequentially provided with control from top to bottom
Case processed, dissolving layer and cooling layer, the control cabinet include PLC and stepper motor, the upper end binder of the dissolving layer
One end of pipe one and feed pipe two, the lower end connection bleed pipe of the dissolving layer, the bleed pipe is provided with magnetic valve one, described
Filter is provided between dissolving layer and bleed pipe, the dissolving layer bottom is heating plate, between the dissolving layer and cooling layer
Connected by charge tube, magnetic valve two is provided with the charge tube, the cooling layer bottom is provided with temperature-constant plate, the cooling layer
Bottom connects separator by discharge nozzle, and the separator connects collection device（21）, electromagnetism is set on the discharge nozzle
Valve three, the cooling layer is connected by feed back pipe and sets compression pump on dissolving layer, the feed back pipe, and the PLC is electrical
Connect the stepper motor, the compression pump, the magnetic valve one, the magnetic valve two and the magnetic valve three.
Preferably, the stepper motor includes rotary shaft and agitation blades.
Preferably, the filter is semi-transparent membrane module.
Preferably, the temperature-constant plate is PTC thermostatic elements.
The beneficial effect that the utility model is reached is：The utility model is simple in construction, practical, by provided with dissolving
Organic solvent and material liquid are sufficiently mixed dissolving by layer with cooling layer, by being stirred provided with stepper motor to solution, heating
Plate improves the temperature of solution, the course of dissolution of common aggravation solute, by provided with magnetic valve, compression pump and feed back pipe by solution
Carry out secondary agitation filtering, improve equipment utilization rate, also increase the intelligent of device, by provided with filter to solution
Filtered, separate out corresponding impurity and moisture, by setting temperature-constant plate to make the temperature of solution first reduce a part, help to lead to
Cross the separation that discharge nozzle carries out next step into separator.
Brief 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 to explain the utility model together, does not constitute to limitation of the present utility model.In the accompanying drawings：
Fig. 1 is structure chart of the present utility model；
Fig. 2 is electric connection figure of the present utility model.
In figure：1st, tank body；2nd, control cabinet；3rd, feed pipe one；4th, PLC；5th, stepper motor；6th, feed pipe two；7、
Bleed pipe；8th, magnetic valve one；9th, feed back pipe；10th, compression pump；11st, dissolving layer；12nd, cooling layer；13rd, filter；14th, heat
Plate；15th, charge tube；16th, magnetic valve two；17th, temperature-constant plate；18th, discharge nozzle；19th, magnetic valve three；20th, separator；21st, collect
Device.
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 1
As shown in Figure 1-2, the utility model provides a Plant Extracts extraction equipment, including tank body 1, and tank body 1 is from upper
Control cabinet 2, dissolving layer 11 and cooling layer 12 are sequentially provided with, control cabinet 2 includes PLC 4 and stepper motor 5, dissolving
Set on the upper end connection expects pipe 1 of layer 11 and one end of feed pipe 26, the lower end connection bleed pipe 7 of dissolving layer 11, bleed pipe 7
There is magnetic valve 1, filter 13 is provided between dissolving layer 11 and bleed pipe 7, the bottom of dissolving layer 11 is heating plate 14, dissolving layer
Connected between 11 and cooling layer 12 by charge tube 15, magnetic valve 2 16 is provided with charge tube 15, the bottom of cooling layer 12 is provided with
Temperature-constant plate 17, the bottom of cooling layer 12 connects separator 20, the connection collection device 21 of separator 20, discharging by discharge nozzle 18
Magnetic valve 3 19 is set on pipe 18, and cooling layer 12 is connected by feed back pipe 9 and compression pump 10 is set on dissolving layer 11, feed back pipe 9,
PLC 4 is electrically connected with stepper motor 5, compression pump 10, magnetic valve 1, magnetic valve 2 16 and magnetic valve 3 19.
Stepper motor 5 includes rotary shaft and agitation blades, and driving blade to stir solution by stepper motor 5 makes it fully mix
Close.
Filter 13 is semi-transparent membrane module, effectively filters out water and other impurities.
The side of feed back pipe 9 connects dissolving layer 11, and the opposite side of feed back pipe 9 connects cooling layer 12, and compression pump 10 is close to dissolving layer
11, compression pump 10 draws back water to dissolving layer 11 from cooling layer 12, and then carries out secondary dissolving.
Temperature-constant plate 17 is PTC thermostatic elements, and PTC thermostatic elements can keep certain temperature, solution temperature is obtained just
Step reduction.
Specifically, in use, adding material liquid from feed pipe 1, feed pipe 26 adds organic solvent, in dissolving layer 11
Material liquid is mixed with organic solvent, and stepper motor 5 drives flabellum agitation mixed solution, is begun to warm up while heating plate 14 is powered,
So that the dissolving of solute is more abundant, the now control of PLC 4 opens magnetic valve 1 and opens bleed pipe 7, filter 13
Water and its contaminant filter in solution is fallen, after a period of time, PLC 4 closes magnetic valve 1, and electromagnetism is opened in control
Valve 2 16, opens the passage of charge tube 15 so that solution enters cooling layer 12, is then shut off magnetic valve 2 16, PLC 4 is controlled
Magnetic valve 3 19 processed opens feed back pipe 9, while opening compression pump 10, solution is drawn back to dissolving layer 11 again and carries out secondary dissolving,
Then the processing of next step is carried out by separator 20, finally extract is obtained in collection device 21, in PLC 4
Repeatedly aforesaid operations improve the utilization ratio of equipment under effect so that impurity content is minimized, and technique is simple, operation side
Just.
It is molten by being sufficiently mixed organic solvent and material liquid provided with dissolving layer 11 and cooling layer 12 by the utility model
Solution, by being stirred provided with stepper motor 5 to solution, heating plate 14 improves the temperature of solution, the dissolving of common aggravation solute
Process, by provided with three magnetic valves, compression pump 10 and feed back pipe 9 solution is subjected to secondary agitation filtering, improve equipment
Utilization rate, also increases the intelligent of device, by being filtered provided with filter 13 to solution, separate out corresponding impurity and
Moisture, by setting temperature-constant plate 17 to make the temperature of solution first reduce a part, helps to enter separator by discharge nozzle 18
20 carry out the separation of next step, and the utility model is simple in construction, practical.
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 the utility model is described in detail with reference to the foregoing embodiments, for those skilled in the art
For, it can still modify to the technical scheme described in foregoing embodiments, or to which part technical characteristic
Equivalent substitution is carried out, all within spirit of the present utility model and principle, any modification, equivalent substitution and improvements made etc.,
It should be included within protection domain of the present utility model.
Claims (4)
1. a Plant Extracts extraction equipment, including tank body（1）, it is characterised in that the tank body（1）Set successively from top to bottom
There is control cabinet（2）, dissolving layer（11）And cooling layer（12）, the control cabinet（2）Including PLC（4）With stepper motor
（5）, the dissolving layer（11）Upper end connection expects pipe one（3）With feed pipe two（6）One end, the dissolving layer（11）Lower end
Connect bleed pipe（7）, the bleed pipe（7）It is provided with magnetic valve one（8）, the dissolving layer（11）With bleed pipe（7）Between set
There is filter（13）, the dissolving layer（11）Bottom is heating plate（14）, the dissolving layer（11）With cooling layer（12）Between
Pass through charge tube（15）Connection, the charge tube（15）On be provided with magnetic valve two（16）, the cooling layer（12）Bottom is provided with
Temperature-constant plate（17）, the cooling layer（12）Bottom passes through discharge nozzle（18）Connect separator（20）, the separator（20）
Connect collection device（21）, the discharge nozzle（18）Upper setting magnetic valve three（19）, the cooling layer（12）Pass through feed back pipe（9）
Connect dissolving layer（11）, the feed back pipe（9）Upper setting compression pump（10）, the PLC（4）It is electrically connected with the stepping
Motor（5）, the compression pump（10）, the magnetic valve one（8）, the magnetic valve two（16）With the magnetic valve three（19）.
2. Plant Extracts extraction equipment according to claim 1, it is characterised in that the stepper motor（5）Bag
Include rotary shaft and agitation blades.
3. Plant Extracts extraction equipment according to claim 1, it is characterised in that the filter（13）For
Semi-transparent membrane module.
4. Plant Extracts extraction equipment according to claim 1, it is characterised in that the temperature-constant plate（17）For
PTC thermostatic elements.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720037079.4U CN206391625U (en) | 2017-01-13 | 2017-01-13 | One Plant Extracts extraction equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720037079.4U CN206391625U (en) | 2017-01-13 | 2017-01-13 | One Plant Extracts extraction equipment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206391625U true CN206391625U (en) | 2017-08-11 |
Family
ID=59512816
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720037079.4U Expired - Fee Related CN206391625U (en) | 2017-01-13 | 2017-01-13 | One Plant Extracts extraction equipment |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206391625U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112535986A (en) * | 2020-11-11 | 2021-03-23 | 吴立章 | Pretreatment device and pretreatment method for processing high-performance fiber composite material |
-
2017
- 2017-01-13 CN CN201720037079.4U patent/CN206391625U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112535986A (en) * | 2020-11-11 | 2021-03-23 | 吴立章 | Pretreatment device and pretreatment method for processing high-performance fiber composite material |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20170811 Termination date: 20190113 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |