CN214142386U - Novel extraction, separation and drying integrated equipment - Google Patents
Novel extraction, separation and drying integrated equipment Download PDFInfo
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- CN214142386U CN214142386U CN202022735964.4U CN202022735964U CN214142386U CN 214142386 U CN214142386 U CN 214142386U CN 202022735964 U CN202022735964 U CN 202022735964U CN 214142386 U CN214142386 U CN 214142386U
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- 238000000605 extraction Methods 0.000 title claims abstract description 65
- 238000000926 separation method Methods 0.000 title claims abstract description 30
- 238000001035 drying Methods 0.000 title claims abstract description 15
- 239000007788 liquid Substances 0.000 claims abstract description 77
- 238000004108 freeze drying Methods 0.000 claims abstract description 42
- 238000003756 stirring Methods 0.000 claims abstract description 31
- 102000004190 Enzymes Human genes 0.000 claims abstract description 23
- 108090000790 Enzymes Proteins 0.000 claims abstract description 23
- 230000010354 integration Effects 0.000 claims abstract description 12
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- 238000010168 coupling process Methods 0.000 claims abstract description 8
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 29
- 239000010410 layer Substances 0.000 claims description 16
- 238000002360 preparation method Methods 0.000 claims description 16
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- 239000011229 interlayer Substances 0.000 claims description 6
- 239000011550 stock solution Substances 0.000 claims description 5
- 238000004321 preservation Methods 0.000 claims description 4
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- 238000004804 winding Methods 0.000 claims description 3
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- 238000000034 method Methods 0.000 abstract description 4
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- 238000012544 monitoring process Methods 0.000 abstract 1
- 239000000243 solution Substances 0.000 description 27
- 239000002994 raw material Substances 0.000 description 21
- 229940088598 enzyme Drugs 0.000 description 19
- 238000001914 filtration Methods 0.000 description 10
- 239000008213 purified water Substances 0.000 description 10
- 238000002156 mixing Methods 0.000 description 8
- 108010059892 Cellulase Proteins 0.000 description 7
- 229940106157 cellulase Drugs 0.000 description 7
- 239000012535 impurity Substances 0.000 description 5
- 241000222336 Ganoderma Species 0.000 description 4
- 240000008397 Ganoderma lucidum Species 0.000 description 4
- 235000001637 Ganoderma lucidum Nutrition 0.000 description 4
- 240000000588 Hericium erinaceus Species 0.000 description 4
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- 102000013142 Amylases Human genes 0.000 description 3
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- 102100037486 Reverse transcriptase/ribonuclease H Human genes 0.000 description 3
- 235000019418 amylase Nutrition 0.000 description 3
- 238000009835 boiling Methods 0.000 description 3
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- 101710121765 Endo-1,4-beta-xylanase Proteins 0.000 description 2
- 241000233866 Fungi Species 0.000 description 2
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Abstract
The utility model relates to a novel draw dry integration equipment of separation, include along the feed liquid flow direction in proper order through tube coupling draw jar, liquid storage pot, concentrated jar, freeze-drying jar, draw jar and concentrated jar and be equipped with supersonic generator, draw jar connection storage enzyme ware and inside be equipped with the agitator that two piece at least stirring rakes are constituteed, the thick liquid leaf is located draws the jar interior different vertical position of jar. The special design of the stirring paddle ensures that the feed liquid is fully contacted and collided in the extraction tank, the time is shortened, the yield is improved, and the extraction rate is maximized. Biological enzymolysis, ultrasonic oscillation and optimized extraction are applied to equipment, online monitoring and automatic control can be performed by electrically connecting a PLC automatic control panel, the design is scientific, the structure is reasonable, the modes and parameters of extraction, separation and drying can be flexibly adjusted according to different characteristics of materials, and different components are extracted and separated; the extract or the concentrated solution can be directly frozen and dried on line to form a product, so that one machine with multiple functions and one-step forming are realized, and the method has good market prospect and economic benefit.
Description
Technical Field
The utility model relates to a novel dry integration equipment of extraction and separation relates to edible and medicinal fungus, chinese herbal medicine extraction and separation technical field.
Background
Edible and medicinal fungi and Chinese herbal medicines are valuable resources of human beings and make important contributions to the health of people. The traditional processing mode is not reasonable, the extraction stirring is not sufficient, and the extraction yield is low.
SUMMERY OF THE UTILITY MODEL
In view of the not enough of prior art, the utility model aims to solve the technical problem that a novel dry integration equipment of extraction and separation is provided, not only rational in infrastructure compactness, convenient high efficiency moreover.
In order to solve the technical problem, the technical scheme of the utility model is that: the utility model provides a novel draw dry integration equipment of separation, includes along the feed liquid flow direction through tube coupling's in proper order jar, liquid storage pot, concentrated jar, freeze-drying tank of drawing, draws the inside agitator that is equipped with two piece at least stirring rakes and constitutes of jar, and the paddle leaf of two piece at least stirring rakes is located the vertical position of drawing the inside difference of jar.
Preferably, the quantity of stirring rake is two, and the equal vertical extension of pivot of stirring rake, wherein a pivot top is connected through the rotatory drive sprocket of motor drive, and driven sprocket is connected on another pivot top, and the winding meshing has drive chain between drive sprocket and the driven sprocket.
Preferably, the outer diameter of the drive sprocket is larger than the outer diameter of the driven sprocket.
Preferably, the blades of one stirring paddle are positioned at the inner upper part and the inner lower part of the extraction tank, and the blades of the other stirring paddle are positioned at the middle part of the extraction tank.
Preferably, the top of the extraction tank is provided with a feed port and an enzyme preparation input pipe for connecting an enzyme storage device, and the enzyme preparation input pipe is provided with a first switch valve; the peripheral wall of the extraction tank body is provided with an interlayer, a heat insulation layer is arranged in the interlayer, and an electric heating pipe or a steam generator is arranged in the extraction tank.
Preferably, the bottom of drawing the jar articulates there is the toper tank bottoms that opens and close through the cylinder drive, and tank bottoms inside is equipped with the filter screen, and the pointed end of tank bottoms just is equipped with the liquid outlet down, and this liquid outlet is connected to the inlet at stock solution tank top through first pipeline, and first pipeline is equipped with second switch valve, filter, centrifugal pump along the feed liquid flow direction in proper order.
Preferably, ultrasonic generators are arranged on the body of each of the extracting tank and the concentrating tank.
Preferably, the top of the extraction tank is connected to a condenser through a hot steam pipeline, a liquid outlet of the condenser is connected with an oil-water separator, an oil outlet of the oil-water separator is connected with a collector, and a water outlet of the oil-water separator is connected to the inside of the extraction tank through a return pipe.
Preferably, the liquid outlet of stock solution tank bottom is connected to the three-way valve through the second tube coupling, an exit linkage of three-way valve to the inlet at concentrated tank deck portion, another exit linkage of three-way valve to the entry of freeze-drying jar, the second pipeline is equipped with third switch valve, centrifugal pump along the feed liquid flow direction in proper order, the liquid outlet of concentrated tank bottom is connected to the entry of freeze-drying jar through the third tube coupling, the third pipeline is equipped with fourth switch valve, centrifugal pump along the feed liquid flow direction in proper order.
Preferably, the jar body perisporium of concentrated jar and freeze-drying jar all is equipped with the intermediate layer, has the heat preservation in the intermediate layer of concentrated jar, has the insulating layer in the intermediate layer of freeze-drying jar, and concentrated jar all is connected the vacuum pump with freeze-drying jar, and concentrated jar inside is equipped with electric heating pipe.
Preferably, this novel dry integration equipment of extraction separation still includes control panel, can the adjusting parameter, and control panel is inside to be equipped with control system for the whole extraction separation drying process of jar, liquid storage pot, concentration jar, freeze-drying jar is drawed in the control.
Compared with the prior art, the utility model discloses following beneficial effect has: this novel draw dry integration equipment of separation's is rational in infrastructure, can draw the different composition of separation, still can become the product with extract or the direct online freeze-drying of concentrate, and the special design of stirring rake makes the feed liquid can be in extracting jar interior abundant contact and collision, both shortens the time and improves the yield again, lets the extraction efficiency maximize.
The present invention will be described in further detail with reference to the accompanying drawings and specific embodiments.
Drawings
Fig. 1 is a schematic structural diagram of an embodiment of the present invention.
In the figure: the device comprises an extraction tank 1, a liquid storage tank 2, a concentration tank 3, a freeze-drying tank 4, a paddle 5, a rotating shaft 6, a motor 7, a driving chain wheel 8, a driven chain wheel 9, a chain 10, an enzyme preparation input pipe 11, a first switch valve 12, a heat preservation layer 13, a cylinder 14, a conical tank bottom 15, a filter screen 16, a first pipeline 17, a second switch valve 18, a filter 19, a centrifugal pump 20, an ultrasonic generator 21, a condenser 22, an oil-water separator 23, a collector 24, a second pipeline 25, a three-way valve 26, a third switch valve 27, a third pipeline 28, a fourth switch valve 29, a vacuum pump 30, a feed port 31, an enzyme storage 32, a hot steam pipeline 33 and a return pipe 34.
Detailed Description
In order to make the aforementioned and other features and advantages of the present invention comprehensible, embodiments accompanied with figures are described in detail below.
As shown in fig. 1, a novel draw dry integration equipment of separation, include along feed liquid flow direction in proper order through tube coupling draw jar 1, liquid storage pot 2, concentrated jar 3, freeze-drying jar 4, draw the separation disadvantaged component, and prepare into the chinese herbal medicine extract product with extract or concentrate on line, draw the inside agitator that is equipped with two piece at least stirring rakes and constitute of jar, the thick liquid leaf 5 of two piece at least stirring rakes is located the vertical position of drawing jar inside difference, form the shearing force in the jar, let the feed liquid can be in jar interior abundant contact and collision, both shorten the time and improve the yield again, let the extraction efficiency maximize.
The embodiment of the utility model provides an in, the quantity of stirring rake is two, the equal vertical extension of pivot 6 of stirring rake, and wherein a pivot top is connected through the rotatory drive sprocket 8 of motor 7 drive, and driven sprocket 9 is connected on another pivot top, and the winding meshing has drive chain 10 between drive sprocket and the driven sprocket. However, the present invention is not limited to this, and a driving pulley, a driven pulley, and a transmission belt may be used.
In an embodiment of the present invention, the outer diameter of the driving sprocket is larger than the outer diameter of the driven sprocket. The outer diameter of the driving chain wheel is 2-3 times of the outer diameter of the driven chain wheel, the rotating speeds are different, and the stirring paddle can be set to rotate clockwise or anticlockwise.
In the embodiment of the utility model, the paddle of one of them stirring rake is located the interior upper portion and the interior lower part of drawing the jar, and the paddle of another stirring rake is located the middle part of drawing the jar.
In the embodiment of the utility model, the top of the extraction tank is provided with a feeding port 31 and an enzyme preparation input pipe 11 for connecting an enzyme storage device 32, the enzyme preparation input pipe is provided with a first switch valve 12, so that the enzyme preparation can be conveniently added, and the enzyme preparation is utilized to carry out enzymolysis on tissues which are not beneficial to extraction in the material, so that intracellular active substances can be effectively released; the peripheral wall of the extraction tank body is provided with an interlayer, a heat insulation layer 13 is arranged in the interlayer, and an electric heating pipe or a steam generator is arranged in the extraction tank.
The embodiment of the utility model provides an in, the bottom of drawing the jar articulates there is conical tank bottoms 15 that opens and close through 14 drives of cylinder, and tank bottoms inside is equipped with filter screen 16, and the pointed end of tank bottoms just is equipped with the liquid outlet down, and this liquid outlet is connected to the inlet at liquid storage tank top through first pipeline 17, and first pipeline is equipped with second switch valve 18, filter 19, centrifugal pump 20 along the feed liquid flow direction in proper order. The first pipeline is detachably connected with a liquid outlet at the bottom of the tank.
The embodiment of the utility model provides an in, all be equipped with supersonic generator 21 on the body of drawing jar and concentrated jar, can set for different ultrasonic parameter, ultrasonic vibration effect can promote the enzymolysis, can avoid again to draw the glutinous wall of feed liquid in the jar. The preparation efficiency is higher, and the obtained components are more effective.
In the embodiment of the utility model provides an in, the top of drawing the jar is connected to condenser 22 through hot steam pipeline 33, and oil-water separator 23 is connected to the liquid outlet of condenser, and collector 24 is connected to oil-water separator's oil-out, and oil-water separator's delivery port is connected to inside drawing the jar through back flow 34. The condenser is used for condensing steam generated when feed liquid is heated in the extraction tank, volatile substances in the raw materials are extracted in the cooking process and enter the condenser to be condensed into mixed liquid of the volatile substances and water, the mixed liquid enters the oil-water separator, the separated volatile substances flow out of the oil outlet to the collector, and water liquid flows back to the extraction tank from the return pipe to circulate inside the extraction tank.
The embodiment of the utility model provides an in, the liquid outlet of stock solution tank bottom is connected to three-way valve 26 through second pipeline 25, an exit linkage of three-way valve to the inlet at concentrated tank deck portion, another exit linkage of three-way valve to the entry of freeze-drying jar, the second pipeline is equipped with third switch valve 27, centrifugal pump along the feed liquid flow direction in proper order, the liquid outlet of concentrated tank bottom is connected to the entry of freeze-drying jar through third pipeline 28, the third pipeline is equipped with fourth switch valve 29, centrifugal pump along the feed liquid flow direction in proper order. The flow direction is controlled by a centrifugal pump. The second pipeline and the third pipeline can be detachably connected with each tank body.
The embodiment of the utility model provides an in, the jar body perisporium of concentrated jar and freeze-drying jar all is equipped with the intermediate layer, has the heat preservation in the intermediate layer of concentrated jar, has the insulating layer in the intermediate layer of freeze-drying jar, and vacuum pump 30 is all connected with freeze-drying jar to concentrated jar, and concentrated jar is inside to be equipped with electric heating pipe.
The embodiment of the utility model provides an in, this novel draw dry integration equipment of separation still includes control panel, can the adjusting parameter, and control panel is inside to be equipped with control system for the whole separation drying process that draws of jar, liquid storage pot, concentrated jar, freeze-drying jar is drawn in control. The control of the control system belongs to the prior art.
The embodiment of the utility model provides an in, in principle, this novel dry integration equipment of extraction separation will be biological enzymolysis, ultrasonic oscillation, optimize and draw etc. combination and use in the equipment for preparation efficiency is higher, and the gained composition is more effective. Structurally, the traditional backflow device is omitted, operation is simplified, and cleaning and maintenance difficulty is reduced. And an enzyme storage device is added, and the tissues which are not beneficial to extraction in the materials are subjected to enzymolysis by using an enzyme preparation, so that intracellular active substances are effectively released. The added ultrasonic generator can adjust different ultrasonic parameters, thereby being beneficial to obtaining optimal extraction data; can not only assist enzymolysis to improve yield, but also effectively retain active ingredients, and can prevent feed liquid from sticking to walls.
The specific implementation process comprises the following steps:
example 1: preparation of Hericium Erinaceus extract
Taking hericium erinaceus as a raw material, removing impurities, crushing, and then respectively adding cellulase and protease for enzymolysis.
Firstly, according to the material-liquid ratio of 1: 10 adding purified water, adding cellulase according to 1% of the weight of the raw materials, starting an ultrasonic generator and a stirring paddle after the temperature of a material liquid in an extraction tank reaches 60 ℃, performing enzymolysis for 1 hour, then respectively extracting for 1 hour by rotating in the clockwise direction and the anticlockwise direction, then filtering an extracting solution, then guiding the extracting solution into a liquid storage tank, and then guiding the extracting solution into a freeze-drying tank for freeze-drying to obtain the cellulose enzymolysis hericium erinaceus extract. In the step, the pipeline from the three-way valve to the concentration tank and the concentration tank do not work.
Then, mixing the raw materials according to the material-liquid ratio of 1: 8, adding purified water, adding protease according to 1% of the weight of the raw materials, starting the ultrasonic generator and the stirring paddle again after the temperature of the material liquid in the extraction tank reaches 50 ℃, performing enzymolysis for 1 hour, then respectively extracting for 1 hour according to clockwise and anticlockwise rotation, then filtering the extracting solution, guiding the extracting solution into a liquid storage tank, and then guiding the extracting solution into a freeze-drying tank for freeze drying to obtain the proteolysis hericium erinaceus extract. In the step, the pipeline from the three-way valve to the concentration tank and the concentration tank do not work.
Example 2: preparation of Polygonatum sibiricum extract
Rhizoma polygonati is used as a raw material, and after impurity removal and crushing, high-temperature amylase is added for enzymolysis.
Firstly, according to the material-liquid ratio of 1: 8, adding purified water, adding high-temperature amylase according to 1% of the weight of the raw materials, starting an ultrasonic generator and a stirring paddle after the temperature of the material liquid in the extraction tank reaches 80 ℃, performing enzymolysis for 2 hours, then respectively extracting for 1 hour according to clockwise and anticlockwise rotation, and then filtering the first extracting solution and guiding into a liquid storage tank.
Then, mixing the raw materials according to the material-liquid ratio of 1: 8 adding purified water, adding high-temperature amylase according to 0.8% of the weight of the raw materials, starting the ultrasonic generator and the stirring paddle again after the temperature of the material liquid in the extraction tank reaches 90 ℃, extracting for 0.5 hour respectively by rotating clockwise and anticlockwise after 1 hour of enzymolysis, filtering the second extracting solution and then introducing into a liquid storage tank.
Mixing the two extractive solutions, vacuum concentrating in a concentrating tank until the relative density of the concentrated solution in the concentrating tank reaches 1.05-1.15 (room temperature), and freeze drying in a freeze-drying tank to obtain rhizoma Polygonati extract. In this step, the pipeline from the three-way valve to the freeze-drying tank does not work.
Example 3: preparation of Ganoderma extract
The method comprises the following steps of taking ganoderma lucidum as a raw material, removing impurities, crushing, adding a complex enzyme for enzymolysis, wherein the ratio of cellulase to xylanase in the complex enzyme is 2: 1.
firstly, according to the material-liquid ratio of 1: 10 adding purified water, adding complex enzyme according to 1.5% of the weight of the raw materials, starting an ultrasonic generator and a stirring paddle after the temperature of the material liquid in an extraction tank reaches 60 ℃, carrying out enzymolysis for 2 hours, heating to slightly boil and keeping the slightly boiling state, then respectively extracting for 1 hour by rotating in the clockwise direction and the anticlockwise direction, filtering the extracting solution, and guiding the extracting solution into a liquid storage tank for later use.
Then, mixing the raw materials according to the material-liquid ratio of 1: 8, adding purified water, adding complex enzyme according to 1 percent of the weight of the raw materials, extracting again under the same conditions, filtering the extracting solution, and then guiding the extracting solution into a liquid storage tank.
Mixing the two extractive solutions, vacuum concentrating in a concentrating tank until the relative density of the concentrated solution in the concentrating tank reaches 1.10-1.20 (room temperature), and freeze drying in a freeze-drying tank to obtain Ganoderma extract. In this step, the pipeline from the three-way valve to the freeze-drying tank does not work.
Example 4: preparing volatile oil and extract of folium Artemisiae Argyi
Folium artemisiae argyi is used as a raw material, and after impurity removal and crushing, cellulase is added for enzymolysis.
Firstly, according to the material-liquid ratio of 1: 12 adding purified water, adding cellulase according to 1% of the weight of the raw materials, starting an ultrasonic generator and a stirring paddle after the temperature of the material liquid in an extraction tank reaches 60 ℃, carrying out enzymolysis for 1 hour, heating to slightly boil and keeping the slightly boiling state, starting a condenser and an oil-water separator, then respectively extracting for 1 hour by rotating in the clockwise direction and the anticlockwise direction, closing the condenser and the oil-water separator after the extraction is finished, and collecting the folium artemisiae argyi volatile oil; filtering the extractive solution, and introducing into a liquid storage tank.
Then, mixing the raw materials according to the material-liquid ratio of 1: 8 adding purified water, adding cellulase 0.5 wt% of the raw materials, extracting and separating under the above conditions, collecting folium Artemisiae Argyi volatile oil, filtering the extractive solution, and introducing into a liquid storage tank.
Mixing the two extractive solutions, vacuum concentrating in a concentrating tank until the relative density of the concentrated solution in the concentrating tank reaches 1.15-1.25 (room temperature), and freeze drying in a freeze-drying tank to obtain folium Artemisiae Argyi extract. In this step, the pipeline from the three-way valve to the freeze-drying tank does not work.
Example 5: preparation of Ganoderma spore oil and extract
Taking ganoderma lucidum spore powder as a raw material, removing impurities, physically breaking walls, and adding protease for extraction for the first time; and adding a complex enzyme for extraction for the second time, wherein the ratio of cellulase to xylanase in the complex enzyme is 1: 1.
firstly, according to the material-liquid ratio of 1: 10 adding purified water, adding protease 1% of the weight of the raw materials, starting an ultrasonic generator and a stirring paddle after the temperature of the material liquid in an extraction tank reaches 60 ℃, performing enzymolysis for 2 hours, then respectively extracting for 1 hour by rotating clockwise and anticlockwise, then filtering the extracting solution, guiding the filtered extracting solution into a liquid storage tank, and then guiding the filtered extracting solution into a freeze-drying tank for freeze-drying to obtain the proteolysis ganoderma lucidum spore powder extract. In the step, the pipeline from the three-way valve to the concentration tank and the concentration tank do not work.
Then, mixing the raw materials according to the material-liquid ratio of 1: 8, adding purified water, adding compound enzyme according to 1% of the weight of the raw materials, starting an ultrasonic generator and a stirring paddle after the temperature of the material liquid in an extraction tank reaches 60 ℃, carrying out enzymolysis for 1 hour, heating to slightly boil and keeping the slightly boiling state, starting a condenser and an oil-water separator, respectively extracting for 1 hour by rotating in the clockwise direction and the anticlockwise direction, closing the condenser and the oil-water separator after extraction is finished, and collecting ganoderma spore oil; filtering the extractive solution, and introducing into a liquid storage tank.
And (3) introducing the extracting solution into a concentration tank for vacuum concentration, introducing the concentrated solution into a freeze-drying tank for freeze drying when the relative density of the concentrated solution in the concentration tank reaches 1.05-1.15 (room temperature), and obtaining the compound enzymolysis ganoderma lucidum spore powder extract. In this step, the pipeline from the three-way valve to the freeze-drying tank does not work.
The utility model discloses not limit to above-mentioned best mode, anyone can all draw the novel dry integration equipment of extraction separation of other various forms under the teaching of the utility model. All the equivalent changes and modifications made according to the claims of the present invention shall fall within the scope of the present invention.
Claims (10)
1. The utility model provides a novel draw dry integration equipment of separation which characterized in that: include along feed liquid flow direction through tube coupling's extraction jar, liquid storage pot, concentrated jar, freeze-drying tank in proper order, extract the inside agitator that is equipped with two piece at least stirring rakes and constitute of jar, the paddle of two piece at least stirring rakes is located the different vertical position of extraction jar inside.
2. The novel integrated extraction, separation and drying device as claimed in claim 1, wherein: the quantity of stirring rake is two, and the equal vertical extension of pivot of stirring rake, wherein a pivot top is connected through the rotatory drive sprocket of motor drive, and driven sprocket is connected on another pivot top, and the winding meshing has drive chain between drive sprocket and the driven sprocket.
3. The novel integrated extraction, separation and drying device as claimed in claim 2, wherein: the outer diameter of the driving chain wheel is larger than that of the driven chain wheel; the paddle of one stirring paddle is positioned at the inner upper part and the inner lower part of the extraction tank, and the paddle of the other stirring paddle is positioned at the middle part of the extraction tank.
4. The novel integrated extraction, separation and drying device as claimed in claim 1, wherein: the top of the extraction tank is provided with a feed port and an enzyme preparation input pipe for connecting an enzyme storage device, and the enzyme preparation input pipe is provided with a first switch valve; the peripheral wall of the extraction tank body is provided with an interlayer, a heat insulation layer is arranged in the interlayer, and an electric heating pipe or a steam generator is arranged in the extraction tank.
5. The novel integrated extraction, separation and drying device as claimed in claim 1, wherein: the bottom of drawing the jar articulates there is the toper tank bottoms that opens and close through the cylinder drive, and tank bottoms inside is equipped with the filter screen, and the pointed end of tank bottoms just is equipped with the liquid outlet down, and this liquid outlet is connected to the inlet at stock solution tank deck portion through first pipeline, and first pipeline is equipped with second switch valve, filter, centrifugal pump along the feed liquid flow direction in proper order.
6. The novel integrated extraction, separation and drying device as claimed in claim 1, wherein: ultrasonic generators are arranged on the body of the extracting tank and the body of the concentrating tank.
7. The novel integrated extraction, separation and drying device as claimed in claim 1, wherein: the top of the extraction tank is connected to a condenser through a hot steam pipeline, a liquid outlet of the condenser is connected with an oil-water separator, an oil outlet of the oil-water separator is connected with a collector, and a water outlet of the oil-water separator is connected to the inside of the extraction tank through a return pipe.
8. The novel integrated extraction, separation and drying device as claimed in claim 1, wherein: the liquid outlet of stock solution tank bottom is connected to the three-way valve through the second tube coupling, an exit linkage of three-way valve to the inlet at concentrated tank deck portion, another exit linkage of three-way valve to the entry of freeze-drying jar, and the second pipeline is equipped with third switch valve, centrifugal pump along the feed liquid flow direction in proper order, and the liquid outlet of concentrated tank bottom is connected to the entry of freeze-drying jar through the third tube coupling, and the third pipeline is equipped with fourth switch valve, centrifugal pump along the feed liquid flow direction in proper order.
9. The novel integrated extraction, separation and drying device as claimed in claim 1, wherein: the jar body perisporium of concentrated jar and freeze-drying jar all is equipped with the intermediate layer, has the heat preservation in the intermediate layer of concentrated jar, has the insulating layer in the intermediate layer of freeze-drying jar, and concentrated jar all is connected the vacuum pump with freeze-drying jar, and concentrated jar inside is equipped with electric heating pipe.
10. The novel integrated extraction, separation and drying device as claimed in claim 1, wherein: this novel draw dry integration equipment of separation still includes control panel, can the adjusting parameter, and control panel is inside to be equipped with control system for the whole of control extraction jar, liquid storage pot, concentration jar, freeze-drying jar draws the separation drying process.
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| CN202022735964.4U CN214142386U (en) | 2020-11-24 | 2020-11-24 | Novel extraction, separation and drying integrated equipment |
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| CN202022735964.4U CN214142386U (en) | 2020-11-24 | 2020-11-24 | Novel extraction, separation and drying integrated equipment |
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| CN214142386U true CN214142386U (en) | 2021-09-07 |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113828053A (en) * | 2021-10-21 | 2021-12-24 | 丽江英煌集生物工程有限公司 | Separation and purification preparation device and separation and purification method for maca polysaccharide |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113828053A (en) * | 2021-10-21 | 2021-12-24 | 丽江英煌集生物工程有限公司 | Separation and purification preparation device and separation and purification method for maca polysaccharide |
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