CN207085351U - A kind of enrichment facility in tuckahoe extracts technique - Google Patents
A kind of enrichment facility in tuckahoe extracts technique Download PDFInfo
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- CN207085351U CN207085351U CN201720909435.7U CN201720909435U CN207085351U CN 207085351 U CN207085351 U CN 207085351U CN 201720909435 U CN201720909435 U CN 201720909435U CN 207085351 U CN207085351 U CN 207085351U
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- Prior art keywords
- concentration tank
- heating tube
- vacuum
- enrichment facility
- concentration
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- 239000000284 extract Substances 0.000 title claims abstract description 24
- 235000008599 Poria cocos Nutrition 0.000 title claims abstract description 22
- 238000000034 method Methods 0.000 title claims abstract description 19
- 235000001188 Peltandra virginica Nutrition 0.000 title claims abstract description 18
- 240000001754 Peltandra virginica Species 0.000 title claims abstract 10
- 238000010438 heat treatment Methods 0.000 claims abstract description 29
- 239000012530 fluid Substances 0.000 claims abstract description 20
- 238000005086 pumping Methods 0.000 claims abstract description 16
- 230000001105 regulatory Effects 0.000 claims abstract description 9
- 239000000498 cooling water Substances 0.000 claims description 6
- 238000009413 insulation Methods 0.000 claims description 5
- 239000002184 metal Substances 0.000 claims description 4
- 229920002635 polyurethane Polymers 0.000 claims description 4
- 239000004814 polyurethane Substances 0.000 claims description 4
- 230000005611 electricity Effects 0.000 claims 1
- 238000009434 installation Methods 0.000 claims 1
- 239000004575 stone Substances 0.000 claims 1
- 244000197580 Poria cocos Species 0.000 description 12
- 239000002904 solvent Substances 0.000 description 6
- 238000009835 boiling Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 238000001704 evaporation Methods 0.000 description 3
- 230000000259 anti-tumor Effects 0.000 description 2
- 239000012141 concentrate Substances 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 229910052904 quartz Inorganic materials 0.000 description 2
- 239000010453 quartz Substances 0.000 description 2
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N silicon dioxide Inorganic materials O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 2
- 210000002540 Macrophages Anatomy 0.000 description 1
- 241000222341 Polyporaceae Species 0.000 description 1
- 208000004880 Polyuria Diseases 0.000 description 1
- 241000576755 Sclerotia Species 0.000 description 1
- 210000000952 Spleen Anatomy 0.000 description 1
- 210000001744 T-Lymphocytes Anatomy 0.000 description 1
- 239000004480 active ingredient Substances 0.000 description 1
- 210000004027 cells Anatomy 0.000 description 1
- 238000001514 detection method Methods 0.000 description 1
- 201000010099 disease Diseases 0.000 description 1
- 230000035619 diuresis Effects 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 230000002708 enhancing Effects 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 150000004676 glycans Polymers 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000006011 modification reaction Methods 0.000 description 1
- 230000000144 pharmacologic effect Effects 0.000 description 1
- 229920001282 polysaccharide Polymers 0.000 description 1
- 239000005017 polysaccharide Substances 0.000 description 1
- 150000004804 polysaccharides Polymers 0.000 description 1
- 230000025627 positive regulation of urine volume Effects 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
Abstract
The utility model discloses the enrichment facility in a kind of tuckahoe extracts technique, including：Concentration tank, heating tube, lagging casing, thermometer, feed pipe, vacuum-pumping tube, steam pipeline, condenser pipe and fluid reservoir, the top intermediate region of the concentration tank is provided with thermometer, feed pipe is connected with the left of the concentration upper end, vacuum-pumping tube is connected with the right side of the concentration upper end, the vacuum-pumping tube is connected with vacuum extractor, the upper and lower ends of the concentration tank wall have been fixedly connected with retainer ring, heating tube is uniformly installed between the retainer ring, the heating tube circular array distribution, the periphery of heating tube is provided with lagging casing on the concentration tank, temperature regulating switch is installed on the lagging casing, the heating tube is electrically connected with by temperature regulating switch and external power supply, the bottom of the concentration tank is connected with drain pipe.The utility model can be evaporated concentration under low temperature, not destroy the structure of pachymaran, and homogeneous heating.
Description
Technical field
It the utility model is related to the concentration dress in Poria cocos extractive technique field, more particularly to a kind of tuckahoe extracts technique
Put.
Background technology
Poria cocos is the dry sclerotia of On Polyporaceae Poria cocos, is conventional traditional Chinese medicine, has excreting dampness, invigorating the spleen, diuresis
Etc. function.Pachymaran is one of important chemical composition of Poria cocos, and modern age is clinical and pharmacological research shows, pachymaran has very
Good antitumor action, the polysaccharide have the CDCC of enhancing macrophage and T lymphocytes, moreover it is possible to strengthen exempting from for cell
Epidemic disease is reacted and activates immune detection system of the body to tumour, has certain antitumor efficacy.Pachymaran is in extraction process
In need to concentrate extract solution, but traditional condensing mode temperature is too high, can destroy active ingredient, it is difficult to ensure that concentration
Quality.
Utility model content
The purpose of this utility model is reduced using vacuumizing in the enrichment facility in a kind of tuckahoe extracts technique is provided
The boiling point of solvent, concentration can be evaporated at a lower temperature, do not destroy the structure of pachymaran, and homogeneous heating,
Extract solution can be made uniformly to be heated.
According to the enrichment facility in a kind of tuckahoe extracts technique of the utility model embodiment, including：Concentration tank, heating
Pipe, lagging casing, thermometer, feed pipe, vacuum-pumping tube, steam pipeline, condenser pipe and fluid reservoir, the top of the concentration tank
Intermediate region is provided with thermometer, and feed pipe is connected with the left of the concentration upper end, is connected on the right side of the concentration upper end
Vacuum-pumping tube is connected to, the vacuum-pumping tube is connected with vacuum extractor, and the upper and lower ends of the concentration tank wall are fixedly connected with
There is retainer ring, heating tube is uniformly installed between the retainer ring, the heating tube circular array is distributed, on the concentration tank
The periphery of heating tube is provided with lagging casing, and temperature regulating switch is provided with the lagging casing, and the heating tube passes through temperature regulating switch
It is electrically connected with external power supply, the bottom of the concentration tank is connected with drain pipe, on the feed pipe, vacuum-pumping tube and drain pipe
Valve A is mounted on, steam pipeline is connected with above the concentration tank side, the steam pipeline connects with fluid reservoir
Connect, the outer wall of the steam pipeline is fixedly connected with condenser pipe.
Further, the temperature is calculated as flange form bimetallic thermometer and is connected with the top flange of concentration tank.
Further, the vacuum means are set to vavuum pump.
Further, the heating tube is quartz heating-pipe.
Further, the lagging casing includes outer metal plates and internal layer polyurethane thermal insulation board.
Further, the bottom of the concentration tank is fixedly connected with 3-4 leg.
Further, the fluid reservoir is provided with leakage fluid dram, and the leakage fluid dram is provided with valve B.
Further, the condenser pipe is provided with circulating cooling water inlet and circulating cooling water out.
The utility model has an advantageous effect in that compared with prior art：Solvent can be reduced by being vacuumized in concentration tank
Boiling point, it is possible to achieve concentration is evaporated to extract solution under the relatively low environment of temperature, so as to not destroy the knot of pachymaran
Structure, the heating tube of annular array distribution can make extract solution thermally equivalent, avoid local temperature too high, improve the effect of evaporation and concentration
Rate, lagging casing can reduce scattering and disappearing for heat, and the solvent being evaporated, which runs into condenser pipe, can liquefy and flow into fluid reservoir, knot
Structure is simple, easy to use, practical.
Brief description of the drawings
Accompanying drawing is used for providing further understanding to of the present utility model, and a part for constitution instruction, with this practicality
New embodiment is used to explain the utility model together, does not form to limitation of the present utility model.In the accompanying drawings：
Fig. 1 be the utility model proposes a kind of tuckahoe extracts technique in enrichment facility structural representation.
Fig. 2 be the utility model proposes a kind of tuckahoe extracts technique in enrichment facility sectional view.
Fig. 3 be the utility model proposes a kind of tuckahoe extracts technique in the structure of lagging casing of enrichment facility show
It is intended to.
In figure：1- concentration tanks, 2- thermometers, 3- feed pipes, 4- vacuum-pumping tubes, 5- retainer rings, 6- heating tubes, 7- insulations are outer
Shell, 8- temperature regulating switch, 9- drain pipes, 10- steam pipelines, 11- fluid reservoirs, 12- condenser pipes, 13- valve A, 14- leg, 15-
Leakage fluid dram, 16- valve B, 17- outer metal plates, 18- internal layer polyurethane thermal insulation boards.
Embodiment
Below in conjunction with the accompanying drawing in the utility model embodiment, the technical scheme in the embodiment of the utility model is carried out
Clearly and completely describing, it is clear that described embodiment is only the utility model part of the embodiment, rather than whole
Embodiment.Based on the embodiment in the utility model, those of ordinary skill in the art are not under the premise of creative work is made
The every other embodiment obtained, belong to the scope of the utility model protection.
Reference picture 1-3, the enrichment facility in a kind of tuckahoe extracts technique, including：Concentration tank 1, heating tube 6, insulation are outer
Shell 7, thermometer 2, feed pipe 3, vacuum-pumping tube 4, steam pipeline 10, condenser pipe 12 and fluid reservoir 11, in the top of concentration tank 1
Between region thermometer 2 is installed, feed pipe 3 is connected with the left of the top of concentration tank 1, is connected with and takes out on the right side of the top of concentration tank 1
Vacuum tube 4, vacuum-pumping tube 4 are connected with vacuum extractor, and the upper and lower ends of the outer wall of concentration tank 1 have been fixedly connected with retainer ring 5, Gu
Determine heating tube 6 is uniformly installed between ring 5, the circular array of heating tube 6 is distributed, and the periphery of heating tube 6, which is provided with, on concentration tank 1 protects
Warm shell 7, temperature regulating switch 8 is installed, heating tube 6 is electrically connected with by temperature regulating switch 8 and external power supply, dense on lagging casing 7
The bottom of contracting tank 1 is connected with drain pipe 9, and valve A 13, concentration tank 1 are mounted on feed pipe 3, vacuum-pumping tube 4 and drain pipe 9
Steam pipeline 10 is connected with above side, steam pipeline 10 is connected with fluid reservoir 11, and the outer wall of steam pipeline 10 is consolidated
Surely it is connected with condenser pipe 12.
Thermometer 2 is flange form bimetallic thermometer and is connected with the top flange of concentration tank 1, plays monitoring concentration tank 1
The effect of interior temperature；Vacuum means are set to vavuum pump；Heating tube 6 is quartz heating-pipe；Lagging casing 7 includes outer metal plates 17
With internal layer polyurethane thermal insulation board 18；The bottom of concentration tank 1 is fixedly connected with 3-4 leg 14；Fluid reservoir 11 is provided with leakage fluid dram
15, leakage fluid dram 15 is provided with valve B 16；Condenser pipe 12 is provided with circulating cooling water inlet and circulating cooling water out, condenser pipe 12
Heat can be taken away and promote solvent liquefaction；Valve A 13 is magnetic valve.
In use, by feed pipe 3 toward extract solution is added in concentration tank 1, then pass through vacuum-pumping tube 4 again and extract concentration tank
Air in 1, the boiling point that can reduce solvent will be vacuumized in concentration tank 1, it is possible to achieve to carrying under the relatively low environment of temperature
Liquid is taken to be evaporated concentration, so as to not destroy the structure of pachymaran, the heating tube 6 of annular array distribution can make extract solution equal
It is even heated, avoid local temperature too high, improve the efficiency of evaporation and concentration, lagging casing 7 can reduce scattering and disappearing for heat, evaporate
The solvent come can be liquefied and flow into fluid reservoir 11 to the cold, and the concentrate after evaporation is discharged through drain pipe 9.
Part is not described in detail for the utility model, is the known technology of those skilled in the art.
While there has been shown and described that embodiment of the present utility model, for the ordinary skill in the art,
It is appreciated that these embodiments can be carried out with a variety of changes in the case where not departing from principle of the present utility model and spirit, repaiied
Change, replace and modification, the scope of the utility model are defined by the appended claims and the equivalents thereof.
Claims (8)
- A kind of 1. enrichment facility in tuckahoe extracts technique, it is characterised in that including：Concentration tank, heating tube, lagging casing, Thermometer, feed pipe, vacuum-pumping tube, steam pipeline, condenser pipe and fluid reservoir, the top intermediate region installation of the concentration tank There is thermometer, feed pipe be connected with the left of the concentration upper end, vacuum-pumping tube is connected with the right side of the concentration upper end, The vacuum-pumping tube is connected with vacuum extractor, and the upper and lower ends of the concentration tank wall have been fixedly connected with retainer ring, described Heating tube is uniformly installed, the heating tube circular array is distributed, the periphery of heating tube on the concentration tank between retainer ring Provided with lagging casing, temperature regulating switch is installed on the lagging casing, the heating tube passes through temperature regulating switch and external power supply electricity Property connection, the bottom of the concentration tank is connected with drain pipe, valve is mounted on the feed pipe, vacuum-pumping tube and drain pipe A, steam pipeline is connected with above the concentration tank side, the steam pipeline is connected with fluid reservoir, and the steam is defeated The outer wall of pipe is sent to be fixedly connected with condenser pipe.
- 2. the enrichment facility in tuckahoe extracts technique according to claim 1, it is characterised in that：The temperature is calculated as method Blue formula bimetallic thermometer is simultaneously connected with the top flange of concentration tank.
- 3. the enrichment facility in tuckahoe extracts technique according to claim 1, it is characterised in that：The vacuum extractor For vavuum pump.
- 4. the enrichment facility in tuckahoe extracts technique according to claim 1, it is characterised in that：The heating tube is stone English heating tube.
- 5. the enrichment facility in tuckahoe extracts technique according to claim 1, it is characterised in that：The lagging casing bag Include outer metal plates and internal layer polyurethane thermal insulation board.
- 6. the enrichment facility in tuckahoe extracts technique according to claim 1, it is characterised in that：The bottom of the concentration tank Portion is fixedly connected with 3-4 leg.
- 7. the enrichment facility in tuckahoe extracts technique according to claim 1, it is characterised in that：Set on the fluid reservoir There is leakage fluid dram, the leakage fluid dram is provided with valve B.
- 8. the enrichment facility in tuckahoe extracts technique according to claim 1, it is characterised in that：The condenser pipe is provided with Circulating cooling water inlet and circulating cooling water out.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720909435.7U CN207085351U (en) | 2017-07-25 | 2017-07-25 | A kind of enrichment facility in tuckahoe extracts technique |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720909435.7U CN207085351U (en) | 2017-07-25 | 2017-07-25 | A kind of enrichment facility in tuckahoe extracts technique |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207085351U true CN207085351U (en) | 2018-03-13 |
Family
ID=61546067
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720909435.7U Active CN207085351U (en) | 2017-07-25 | 2017-07-25 | A kind of enrichment facility in tuckahoe extracts technique |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN207085351U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110508015A (en) * | 2019-08-12 | 2019-11-29 | 佛山市欧若拉生物科技有限公司 | A kind of plant material evaporation extraction cooling device |
| CN110755864A (en) * | 2019-11-26 | 2020-02-07 | 衡阳旭光锌锗科技有限公司 | A enrichment facility for zinc sulfate solution |
| CN113398608A (en) * | 2021-07-02 | 2021-09-17 | 江苏辰羽堂生物科技有限公司 | Poria cocos extraction and concentration device |
-
2017
- 2017-07-25 CN CN201720909435.7U patent/CN207085351U/en active Active
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110508015A (en) * | 2019-08-12 | 2019-11-29 | 佛山市欧若拉生物科技有限公司 | A kind of plant material evaporation extraction cooling device |
| CN110755864A (en) * | 2019-11-26 | 2020-02-07 | 衡阳旭光锌锗科技有限公司 | A enrichment facility for zinc sulfate solution |
| CN113398608A (en) * | 2021-07-02 | 2021-09-17 | 江苏辰羽堂生物科技有限公司 | Poria cocos extraction and concentration device |
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