CN215741828U - Enrichment facility is used in plant natural product extraction - Google Patents
Enrichment facility is used in plant natural product extraction Download PDFInfo
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- CN215741828U CN215741828U CN202122307546.XU CN202122307546U CN215741828U CN 215741828 U CN215741828 U CN 215741828U CN 202122307546 U CN202122307546 U CN 202122307546U CN 215741828 U CN215741828 U CN 215741828U
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- 238000000605 extraction Methods 0.000 title claims abstract description 26
- 229930014626 natural product Natural products 0.000 title claims abstract description 18
- 238000001704 evaporation Methods 0.000 claims abstract description 103
- 230000008020 evaporation Effects 0.000 claims abstract description 80
- 239000007788 liquid Substances 0.000 claims abstract description 67
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 59
- 239000002904 solvent Substances 0.000 claims abstract description 43
- 238000000935 solvent evaporation Methods 0.000 claims abstract description 28
- 238000001816 cooling Methods 0.000 claims abstract description 24
- 238000011084 recovery Methods 0.000 claims abstract description 9
- 238000005485 electric heating Methods 0.000 claims description 26
- 239000004744 fabric Substances 0.000 claims description 13
- 125000003003 spiro group Chemical group 0.000 claims description 10
- 230000008878 coupling Effects 0.000 claims description 6
- 238000010168 coupling process Methods 0.000 claims description 6
- 238000005859 coupling reaction Methods 0.000 claims description 6
- 239000000284 extract Substances 0.000 abstract description 14
- 238000003756 stirring Methods 0.000 abstract description 5
- 230000005484 gravity Effects 0.000 description 5
- 229910000746 Structural steel Inorganic materials 0.000 description 3
- 238000010586 diagram Methods 0.000 description 3
- 239000002537 cosmetic Substances 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 230000002349 favourable effect Effects 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 239000000419 plant extract Substances 0.000 description 2
- GAMYVSCDDLXAQW-AOIWZFSPSA-N Thermopsosid Natural products O(C)c1c(O)ccc(C=2Oc3c(c(O)cc(O[C@H]4[C@H](O)[C@@H](O)[C@H](O)[C@H](CO)O4)c3)C(=O)C=2)c1 GAMYVSCDDLXAQW-AOIWZFSPSA-N 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 229930013930 alkaloid Natural products 0.000 description 1
- 150000003797 alkaloid derivatives Chemical class 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 229930003944 flavone Natural products 0.000 description 1
- 150000002212 flavone derivatives Chemical class 0.000 description 1
- 235000011949 flavones Nutrition 0.000 description 1
- 150000004676 glycans Chemical class 0.000 description 1
- 229930182470 glycoside Natural products 0.000 description 1
- 150000002338 glycosides Chemical class 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 231100000252 nontoxic Toxicity 0.000 description 1
- 230000003000 nontoxic effect Effects 0.000 description 1
- 150000008442 polyphenolic compounds Chemical class 0.000 description 1
- 235000013824 polyphenols Nutrition 0.000 description 1
- 229920001282 polysaccharide Polymers 0.000 description 1
- 239000005017 polysaccharide Substances 0.000 description 1
- 150000003505 terpenes Chemical class 0.000 description 1
- VHBFFQKBGNRLFZ-UHFFFAOYSA-N vitamin p Natural products O1C2=CC=CC=C2C(=O)C=C1C1=CC=CC=C1 VHBFFQKBGNRLFZ-UHFFFAOYSA-N 0.000 description 1
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- Extraction Or Liquid Replacement (AREA)
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The utility model relates to a plant natural product extraction and concentration device, which comprises an extraction solution box, a solvent evaporation box, a water evaporation box, a solvent vapor cooling tank, a water vapor cooling tank and a solvent recovery tank, wherein the solvent evaporation box is internally provided with a first evaporation plate; the water evaporation box is internally provided with a second evaporation plate, a second liquid distribution pipe is arranged above the second evaporation plate positioned at the top, two sides of the water evaporation box are respectively provided with a water vapor outlet, and the water vapor outlet is communicated with a vapor inlet of the water vapor cooling tank. This enrichment facility not only need not stir, utilizes first evaporating plate and second evaporating plate to make the extract spread out into thin rivers moreover, makes the extract be heated evenly to be convenient for solvent and the evaporation of water in the extract.
Description
Technical Field
The utility model relates to the field of plant natural product extraction equipment, in particular to a concentrating device for extracting a plant natural product.
Background
The plant contains components such as glycoside, acid, polyphenol, polysaccharide, terpenoid, flavone, alkaloid and the like, the plant extract has wide application, particularly, in recent years, the pursuit of cosmetics with natural, environment-friendly and non-toxic side effects is more and more extensive, so that the demand of the plant extract is more and more large, the plant natural product extract contains a large amount of water and solvents, and the concentrated extract obtained by removing the water and the solvents can be applied to the cosmetics. The existing concentration equipment mainly depends on stirring, and the condition that the solvent and water cannot be evaporated due to uneven stirring still exists.
SUMMERY OF THE UTILITY MODEL
The utility model aims to overcome the problems in the prior art and provide a plant natural product extracting and concentrating device.
In order to achieve the technical purpose and achieve the technical effect, the utility model is realized by the following technical scheme:
a plant natural product extraction concentration device comprises an extraction liquid box, a solvent evaporation box with an opening at the top end, a water evaporation box with an opening at the top end, a solvent vapor cooling tank, a water vapor cooling tank and a solvent recovery tank, wherein the water evaporation box, the solvent evaporation box and the extraction liquid box are sequentially stacked from bottom to top; a plurality of inclined first evaporation plates which are alternately arranged from top to bottom are arranged in the solvent evaporation tank, a first liquid distribution pipe arranged at the bottom of the extraction liquid tank is arranged above the first evaporation plate positioned at the top, two sides of the solvent evaporation tank are respectively provided with a solvent vapor outlet, the solvent vapor outlet is communicated with a vapor inlet of the solvent vapor cooling tank through a first exhaust pipe, and a liquid outlet of the solvent vapor cooling tank is communicated with the solvent recovery tank through a water pipe; the water evaporation tank is internally provided with a plurality of inclined second evaporation plates which are alternately arranged from top to bottom, a second liquid distribution pipe arranged at the bottom of the solvent evaporation tank is arranged above the second evaporation plate positioned at the top, two sides of the water evaporation tank are respectively provided with a water vapor outlet, and the water vapor outlet is communicated with a vapor inlet of the water vapor cooling tank through a second exhaust pipe.
The first evaporation plate and the second evaporation plate respectively comprise an electric heating evaporation plate, one side of the electric heating evaporation plate is provided with an upward extending splash guard, the top end of the electric heating evaporation plate is provided with a strip-shaped overflow groove adjacent to the splash guard, the top end of the electric heating evaporation plate is provided with a grid-shaped evaporation groove, the evaporation groove is communicated with the overflow groove, the bottom of the electric heating evaporation plate is embedded with a snake-shaped electric heating pipe, and the bottom end of the electric heating evaporation plate is provided with a protection plate.
Wherein, install temperature sensor on the guard plate.
The electric heating evaporation plate is inclined downwards from one side with the splash guard to one side far away from the splash guard, and the inclination angle is 5 degrees.
Wherein, first cloth liquid pipe and second cloth liquid pipe are T type cloth liquid pipe, T type cloth liquid pipe includes internal thread connector, standpipe, violently manages, end cap, internal thread connector rigid coupling is on the top of standpipe, the bottom of standpipe and the middle part rigid coupling of violently managing, the bottom of violently managing is equipped with a plurality of cloth liquid mouths that reduce step by step to the distance between both ends by the centre, the end cap of both ends difference spiro union of violently managing.
Wherein, the bottom of drawing the liquid case is equipped with first drain pipe, first cloth liquid pipe spiro union is in first drain pipe bottom, the top spiro union of drawing the liquid case has the screw rod coaxial with first drain pipe, the rubber buffer of the inverted cone is installed to the bottom of screw rod.
And the bottom of the solvent evaporation box is provided with a second liquid discharge pipe, and the second liquid distribution pipe is screwed at the bottom of the second liquid discharge pipe.
And a third liquid discharge pipe is arranged at the bottom of the water evaporation tank, and a stop valve is installed on the third liquid discharge pipe.
Wherein, the top of extraction solution case is equipped with the feed liquor pipe, the spiro union has the tube cap on the feed liquor pipe.
The utility model has the beneficial effects that: distributing the extracting solution on first evaporating plates in a solvent evaporating box through a first liquid distribution pipe, enabling the extracting solution to sequentially flow through a plurality of first evaporating plates from top to bottom under the action of gravity, heating the extracting solution to the temperature required by solvent evaporation by the first evaporating plates, enabling the solvent in the extracting solution to form solvent vapor, cooling the solvent vapor in a solvent vapor cooling tank through a first exhaust pipe, and then recovering the solvent vapor into a solvent recovery tank; the extracting solution after solvent evaporation enters a water evaporation box, the extracting solution sequentially flows through a plurality of second evaporation plates from top to bottom under the action of gravity, the second evaporation plates heat the extracting solution to the temperature required by water evaporation, water in the extracting solution forms water vapor, and the water vapor is cooled in a water vapor cooling tank through a second exhaust pipe and then is discharged; this enrichment facility not only need not stir, utilizes first evaporating plate and second evaporating plate to make the extract spread out into thin rivers moreover, makes the extract be heated evenly to be convenient for solvent and the evaporation of water in the extract.
Drawings
The accompanying drawings, which are included to provide a further understanding of the utility model and are incorporated in and constitute a part of this application, illustrate embodiment(s) of the utility model and together with the description serve to explain the utility model without limiting the utility model. In the drawings:
FIG. 1 is a schematic view of a configuration of a concentration apparatus according to an embodiment of the present invention;
FIG. 2 is a schematic view showing a stacked structure of a water evaporation tank, a solvent evaporation tank and an extract tank in the embodiment of the present invention;
FIG. 3 is a schematic view showing the structure of an extraction liquid tank in the embodiment of the present invention;
FIG. 4 is a schematic structural diagram of an embodiment of the utility model after the extraction liquid tank is cut;
FIG. 5 is a schematic view of a solvent evaporation tank from a first perspective in an embodiment of the present invention;
FIG. 6 is a schematic diagram of a second perspective view of a solvent evaporation tank in an embodiment of the present invention;
FIG. 7 is a schematic view of a first perspective of a water evaporation tank according to an embodiment of the present invention;
FIG. 8 is a schematic view of a second perspective of the water evaporation tank in an embodiment of the present invention;
FIG. 9 is a schematic structural view of a first evaporating plate in the embodiment of the present invention;
FIG. 10 is a schematic view showing a disassembled structure of the first evaporating plate in the embodiment of the present invention;
fig. 11 is a schematic structural diagram of the first liquid distribution pipe in the embodiment of the utility model.
Detailed Description
The present invention will be described in detail below with reference to the accompanying drawings in conjunction with embodiments.
As shown in fig. 1 to 11, a plant natural product extraction concentration device comprises an extraction liquid tank 1, a solvent evaporation tank 2 with an opening at the top end, a water evaporation tank 3 with an opening at the top end, a solvent vapor cooling tank 4, a water vapor cooling tank 5 and a solvent recovery tank 6, wherein four corners of the extraction liquid tank 1 are fixedly connected with a first angle iron 7 respectively, four corners of the solvent evaporation tank 2 are fixedly connected with a second angle iron 8 respectively, four corners of the water evaporation tank 3 are fixedly connected with a third angle iron 9 respectively, and the water evaporation tank 3, the solvent evaporation tank 2 and the extraction liquid tank 1 are stacked from bottom to top in sequence; a plurality of inclined first evaporation plates 10 which are alternately arranged from top to bottom are arranged in the solvent evaporation box 2, a first liquid distribution pipe 11 arranged at the bottom of the extraction liquid box 1 is arranged above the first evaporation plate 10 positioned at the top, two sides of the solvent evaporation box 2 are respectively provided with a solvent vapor outlet 12, the solvent vapor outlet 12 is communicated with a vapor inlet of the solvent vapor cooling tank 4 through a first exhaust pipe 13, and a liquid outlet of the solvent vapor cooling tank 4 is communicated with the solvent recovery tank 6 through a water pipe 14; the water evaporation box 3 is internally provided with a plurality of inclined second evaporation plates 15 which are alternately arranged from top to bottom, a second liquid distribution pipe 16 arranged at the bottom of the solvent evaporation box 2 is arranged above the second evaporation plate 15 at the top, two sides of the water evaporation box 3 are respectively provided with a water vapor outlet 17, and the water vapor outlets 17 are communicated with a vapor inlet of the water vapor cooling tank 5 through second exhaust pipes 18.
The first evaporating plate 10 and the second evaporating plate 15 both comprise an electric heating evaporating plate 19, one side of the electric heating evaporating plate 19 is provided with a splash guard 20 extending upwards, the top end of the electric heating evaporating plate 19 is provided with a strip-shaped overflow groove 21 adjacent to the splash guard 20, the electric heating evaporating plate 19 is inclined downwards from one side with the splash guard 20 to one side far away from the splash guard 20, the inclination angle is 5 degrees, and the slow downward flowing of the extracting solution under the action of gravity is facilitated. The top end of the electric heating evaporation plate 19 is provided with a grid-shaped evaporation groove 22, the grid-shaped design is favorable for the free and diffuse flow of the extracting solution in the evaporation groove, the extracting solution is favorably turned over and uniformly heated, the evaporation groove 22 is communicated with the overflow groove 21, the bottom of the electric heating evaporation plate 19 is embedded with a snake-shaped electric heating pipe 23, and the bottom end of the electric heating evaporation plate 19 is provided with a protection plate 24. A temperature sensor 25 is mounted on the guard plate 24 to monitor the temperature on the electrically heated evaporating plate.
The concentration device also comprises a control cabinet, wherein a temperature control switch A, a temperature control switch B and a digital display are arranged in the control cabinet, electric heating pipes in the first evaporation plates are connected in parallel and connected with the output end of the temperature control switch A, and temperature sensors on the first evaporation plates are connected with the signal output end of the temperature control switch A through leads; the electric heating pipes in the second evaporation plates are connected in parallel and connected with the output end of the temperature control switch B, and the temperature sensors on the second evaporation plates are connected with the signal output end of the temperature control switch B through leads.
First cloth liquid pipe 11 and second cloth liquid pipe 16 are T type cloth liquid pipe 26, T type cloth liquid pipe 26 includes internal thread joint 27, standpipe 28, violently manage 29, end cap 30, internal thread joint 27 rigid coupling is on the top of standpipe 28, the bottom of standpipe 28 and the middle part rigid coupling of violently managing 29, the bottom of violently managing 29 is equipped with a plurality ofly by middle cloth liquid mouth 31 that the moment reduces step by step between both ends, it is even to be favorable to making the extract that flows from violently managing when getting into the overflow launder time distribution, end cap 30 of both ends difference spiro union of violently managing 29. The bottom of extraction liquid case 1 is equipped with first drain pipe 32, and first cloth pipe 11 spiro union is in first drain pipe 32 bottom, and the top spiro union of extraction liquid case 1 has the screw rod 33 coaxial with first drain pipe 32, and the rubber buffer 34 of the inverted cone is installed to the bottom of screw rod 33, thereby adjusts the clearance size between rubber buffer and the first drain pipe through the height adjustment rubber buffer of rotating the screw rod to the extract discharge velocity of control first drain pipe. The top of the extracting solution box 1 is provided with a liquid inlet pipe 35, a pipe cover 36 is screwed on the liquid inlet pipe 35, and the liquid inlet pipe is used for adding extracting solution in the phase extracting solution box.
In addition, a second liquid discharge pipe is arranged at the bottom of the solvent evaporation tank 2, and the second liquid distribution pipe 16 is screwed at the bottom of the second liquid discharge pipe. The bottom of the water evaporation tank 3 is provided with a third liquid discharge pipe, and a stop valve 37 is arranged on the third liquid discharge pipe.
The working principle is as follows: distributing the extracting solution on first evaporating plates in a solvent evaporating box through a first liquid distribution pipe, enabling the extracting solution to sequentially flow through a plurality of first evaporating plates from top to bottom under the action of gravity, heating the extracting solution to the temperature required by solvent evaporation by the first evaporating plates, enabling the solvent in the extracting solution to form solvent vapor, cooling the solvent vapor in a solvent vapor cooling tank through a first exhaust pipe, and then recovering the solvent vapor into a solvent recovery tank; the extracting solution after solvent evaporation enters a water evaporation box, the extracting solution sequentially flows through a plurality of second evaporation plates from top to bottom under the action of gravity, the second evaporation plates heat the extracting solution to the temperature required by water evaporation, water in the extracting solution forms water vapor, and the water vapor is cooled in a water vapor cooling tank through a second exhaust pipe and then is discharged; this enrichment facility not only need not stir, utilizes first evaporating plate and second evaporating plate to make the extract spread out into thin rivers moreover, makes the extract be heated evenly to be convenient for solvent and the evaporation of water in the extract.
The foregoing shows and describes the general principles, essential features, and advantages of the utility model. It will be understood by those skilled in the art that the present invention is not limited to the embodiments described above, which are described in the specification and illustrated only to illustrate the principle of the present invention, but that various changes and modifications may be made therein without departing from the spirit and scope of the present invention, which fall within the scope of the utility model as claimed.
Claims (9)
1. A plant is enrichment facility for natural product extraction which characterized in that: the device comprises an extraction solution box, a solvent evaporation box with an opening at the top end, a water evaporation box with an opening at the top end, a solvent vapor cooling tank, a water vapor cooling tank and a solvent recovery tank, wherein the water evaporation box, the solvent evaporation box and the extraction solution box are stacked from bottom to top in sequence; a plurality of inclined first evaporation plates which are alternately arranged from top to bottom are arranged in the solvent evaporation tank, a first liquid distribution pipe arranged at the bottom of the extraction liquid tank is arranged above the first evaporation plate positioned at the top, two sides of the solvent evaporation tank are respectively provided with a solvent vapor outlet, the solvent vapor outlet is communicated with a vapor inlet of the solvent vapor cooling tank through a first exhaust pipe, and a liquid outlet of the solvent vapor cooling tank is communicated with the solvent recovery tank through a water pipe; the water evaporation tank is internally provided with a plurality of inclined second evaporation plates which are alternately arranged from top to bottom, a second liquid distribution pipe arranged at the bottom of the solvent evaporation tank is arranged above the second evaporation plate positioned at the top, two sides of the water evaporation tank are respectively provided with a water vapor outlet, and the water vapor outlet is communicated with a vapor inlet of the water vapor cooling tank through a second exhaust pipe.
2. The device for concentrating plant natural product according to claim 1, wherein: the first evaporation plate and the second evaporation plate both comprise electric heating evaporation plates, one side of each electric heating evaporation plate is provided with an upward extending splash guard, the top end of each electric heating evaporation plate is provided with a strip-shaped overflow groove adjacent to the splash guard, the top end of each electric heating evaporation plate is provided with a grid-shaped evaporation groove, the evaporation grooves are communicated with the overflow grooves, the bottoms of the electric heating evaporation plates are embedded with snake-shaped electric heating pipes, and the bottom ends of the electric heating evaporation plates are provided with protection plates.
3. The device for concentrating plant natural product for extraction according to claim 2, characterized in that: and the protection plate is provided with a temperature sensor.
4. The device for concentrating plant natural product for extraction according to claim 2, characterized in that: the electric heating evaporation plate is inclined downwards from one side with the splash guard to one side far away from the splash guard, and the inclination angle is 5 degrees.
5. The device for concentrating plant natural product according to claim 1, wherein: first liquid distribution pipe and second liquid distribution pipe are T type liquid distribution pipe, T type liquid distribution pipe includes internal thread connector, standpipe, violently manages, end cap, internal thread connector rigid coupling is on the top of standpipe, the bottom of standpipe and the middle part rigid coupling of violently managing, the bottom of violently managing is equipped with a plurality of liquid distribution mouths that reduce step by step to the distance between both ends by the centre, end cap of both ends difference spiro union of violently managing.
6. The device for concentrating plant natural product according to claim 1, wherein: the bottom of drawing the liquid case is equipped with first drain pipe, first cloth liquid pipe spiro union is in first drain pipe bottom, the top spiro union of drawing the liquid case has the screw rod coaxial with first drain pipe, the rubber buffer of the obconic is installed to the bottom of screw rod.
7. The device for concentrating plant natural product according to claim 1, wherein: and a second liquid discharge pipe is arranged at the bottom of the solvent evaporation box, and the second liquid distribution pipe is in screwed connection with the bottom of the second liquid discharge pipe.
8. The device for concentrating plant natural product according to claim 1, wherein: and a third liquid discharge pipe is arranged at the bottom of the water evaporation tank, and a stop valve is installed on the third liquid discharge pipe.
9. The device for concentrating plant natural product according to claim 1, wherein: the top of the extraction liquid box is provided with a liquid inlet pipe, and a pipe cover is screwed on the liquid inlet pipe.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202122307546.XU CN215741828U (en) | 2021-09-23 | 2021-09-23 | Enrichment facility is used in plant natural product extraction |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202122307546.XU CN215741828U (en) | 2021-09-23 | 2021-09-23 | Enrichment facility is used in plant natural product extraction |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN215741828U true CN215741828U (en) | 2022-02-08 |
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ID=80090258
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202122307546.XU Active CN215741828U (en) | 2021-09-23 | 2021-09-23 | Enrichment facility is used in plant natural product extraction |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN215741828U (en) |
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2021
- 2021-09-23 CN CN202122307546.XU patent/CN215741828U/en active Active
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