CN207734648U - A kind of ergosterol production continuous extraction system - Google Patents
A kind of ergosterol production continuous extraction system Download PDFInfo
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- CN207734648U CN207734648U CN201721808772.3U CN201721808772U CN207734648U CN 207734648 U CN207734648 U CN 207734648U CN 201721808772 U CN201721808772 U CN 201721808772U CN 207734648 U CN207734648 U CN 207734648U
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- sliding rail
- extractor
- extraction
- feed liquid
- continuous extraction
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Abstract
The utility model discloses a kind of ergosterol production continuous extraction systems, including the first extraction cells, the second extraction cells and feed liquid supply unit, first extraction cells include the first sliding rail and several first extractors for being slided along the first sliding rail, second extraction cells include the second sliding rail and several second extractors for being slided along the second sliding rail, the feed liquid supply unit is set in the region between the first sliding rail and the second sliding rail, including setting feed liquid delivery pump and transfer pipeline.When extraction, after the completion of the extraction of first extractor, pipeline connects the feed inlet of the discharge port and the second extractor of the first extractor, infusion pump conveys lower layer's solution, second is carried out in the second extractor to extract, the feed inlet for pipeline being changed again into the second extractor discharge port and the first extractor of connection, again extracts lower layer's solvent delivery to the first extractor, completes continuous extraction repeatedly.
Description
Technical field
The utility model is related to ergosterol process units, especially have with a kind of ergosterol production continuous extraction system
It closes.
Background technology
Ergosterol is most important phytosterol, is present in yeast and certain plants, when it is irradiated by ultraviolet light
It waits, one in molecule in four carbocyclic rings is broken, and becomes calciferol, it is industrial mass manufacture calciferol
Primary raw material.Due to calciferol be humans and animals maintain normal activities with health necessary to organic trace compounds it
One, calciferol can be added in right amount in drug, food and feed is regularly absorbed from the external world to meet human or animal.Dimension
Raw element D2 is about at present 1800 tons in global Year's consumption, wherein 70% or so is used for feed addictive, China year demand
About more than 100 tons of amount, and about 1 ton of the volume of production and marketing of year of China's calciferol, majority needs import, in addition to technical reason, ergot
Sterol starting material is insufficient, and causes the major reason under low output.The enforcement period of the ninth five-year plan, China was once with " fermentation method production dimension life
Plain D2 " sets up emphasis science and technology public relations State Project, and ergosterol is extracted using penicillin waste mycelia, theoretically per ton
Penicillin waste mycelia can extract 4kg ergosterols, but can be with industrial mass production ergot steroid to not yet building up at present
The device of alcohol.
Applicant is at present using the production for having patent ZL2004100409058 progress ergosterols by oneself, technique
Flow is：Saponification again with toluene extracting is carried out after yeast is mixed with alkali, sodium chloride solution, through washing, concentration and refined vacuum
Dry ergosterol finished product.In actual production, repeated washing extracting operation must be carried out after raw material saponification process, thus extracts vehicle
It is interior to be disposed with more extractor, and for pipeline layout and daily maintenance requirement, so that extractor is more disperseed, extraction plant field
Ground effective rate of utilization is relatively low.
Utility model content
The utility model is in view of the above problems, provide a kind of ergosterol production continuous extraction system.By parallel
Two sliding rails at the cooperation of several slidable extractors and feed liquid transfer pipeline that is arranged, the laying for improving extractor is close
Degree avoids the laying of complicated pipeline in workshop, to effectively increase extraction plant place effective rate of utilization.
In order to realize the purpose of this utility model, intend using following technology：
A kind of ergosterol production continuous extraction system, which is characterized in that single including the first extraction cells, the second extraction
Member and feed liquid supply unit, first extraction cells include the first sliding rail and along the first sliding rail slide it is several first extract
Tank, second extraction cells include the second sliding rail and several second extractors for being slided along the second sliding rail, the feed liquid conveying
Unit is set in the region between the first sliding rail and the second sliding rail, including setting feed liquid delivery pump and transfer pipeline, described defeated
It send pipeline one end to be equipped be telescopically connected nozzle, open up towards the first sliding rail, highly matching with the first extractor discharge port, the other end
Towards the second sliding rail opens up, position is matched with the second extractor feed inlet.
Further, the first extractor and the second extractor may be contained on slide unit.
Further, location structure is equipped at slide unit.
Further, transfer pipeline is set up by holder and is fixed.
The utility model has the beneficial effects that：
The utility model is conveyed by several the slidable extractors being arranged at two parallel sliding rails with feed liquid
The cooperation of pipeline improves the layout density of extractor, avoids the laying of complicated pipeline in workshop, to effectively increase extraction
Workshop place effective rate of utilization.
Description of the drawings
Fig. 1 shows the utility model structure diagram.
Specific implementation mode
As shown in Figure 1, a kind of ergosterol production continuous extraction system, including the extraction of the first extraction cells 1, second are single
Member 2 and feed liquid supply unit 3, first extraction cells 1 include the first sliding rail 11 and along several the of the sliding of the first sliding rail 11
One extractor 12, second extraction cells 2 include the second sliding rail 21 and several second extractors along the sliding of the second sliding rail 21
22, the feed liquid supply unit 3 is set in the region between the first sliding rail 11 and the second sliding rail 21, including setting feed liquid conveys
Pump 31 and transfer pipeline 32,32 one end of the transfer pipeline are equipped with and are telescopically connected nozzle 33, opened up towards the first sliding rail 11, height
It is matched with 12 discharge port of the first extractor, the other end opens up towards the second sliding rail 21, position and 22 feed inlet of the second extractor
Match.Transfer pipeline 32 is set up by holder 5 and is fixed.Ensure the stability of transfer pipeline 32.
First extractor 12 and the second extractor 22 may be contained on slide unit 4, and slide unit 4 is slided along sliding rail, and passes through positioning
Structure 41 is fixed on sliding rail specific location.
Illustrate that specific embodiment of the present invention is as follows in conjunction with the embodiments：
Feed liquid after saponification is put into a certain first extractor, after injecting extract liquor, extractor is by its internal configuration
The monitorings such as the temperature monitor, pH detectors, pressure detecting instrument and the agitating paddle motor that are connected with PLC controller and operating mechanism into
Row auto extractive operates, and after extraction, is set to the status display for being equipped at tank wall and being connected with PLC controller output end
The suggestion devices such as lamp, Microspeaker carry out necessary prompt.
First extractor is pushed into along the first sliding rail at feed liquid supply unit 3, a certain second extractor conduct of reselection
Follow-up extraction tank body, is also pushed at feed liquid supply unit 3 along the second sliding rail, makes the feed inlet and transfer pipeline of its top of the tank
Outlet port matches.It will be telescopically connected after nozzle is connected into the first extractor bottom discharge mouth, and open and come out mouth control valve, pass through
External power supply starts feed liquid delivery pump 31, and feed liquid in tank is pumped into the second extractor.It is required according to extraction, it can be in the second extraction
Several groups the utility model is added after taking unit, is used for continuous extraction.
Claims (4)
1. a kind of ergosterol production continuous extraction system, which is characterized in that including the first extraction cells（1）, second extraction
Unit（2）With feed liquid supply unit（3）, first extraction cells（1）Including the first sliding rail（11）With along the first sliding rail（11）
Several first extractors of sliding（12）, second extraction cells（2）Including the second sliding rail（21）With along the second sliding rail（21）
Several second extractors of sliding（22）, the feed liquid supply unit（3）It is set to the first sliding rail（11）With the second sliding rail（21）
Between region in, including setting feed liquid delivery pump（31）And transfer pipeline（32）, the transfer pipeline（32）One end, which is equipped with, stretches
Contracting connection nozzle, the first sliding rail of direction（11）Open up, highly with the first extractor（12）Discharge port matches, other end direction second
Sliding rail（21）It opens up, position and the second extractor（22）Feed inlet matches.
2. continuous extraction system according to claim 1, which is characterized in that the first extractor（12）With the second extractor
（22）It may be contained within slide unit（4）On.
3. continuous extraction system according to claim 2, which is characterized in that slide unit（4）Place is equipped with location structure（41）.
4. continuous extraction system according to claim 1, which is characterized in that transfer pipeline（32）By holder（5）It sets up solid
It is fixed.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721808772.3U CN207734648U (en) | 2017-12-22 | 2017-12-22 | A kind of ergosterol production continuous extraction system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721808772.3U CN207734648U (en) | 2017-12-22 | 2017-12-22 | A kind of ergosterol production continuous extraction system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207734648U true CN207734648U (en) | 2018-08-17 |
Family
ID=63119089
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201721808772.3U Active CN207734648U (en) | 2017-12-22 | 2017-12-22 | A kind of ergosterol production continuous extraction system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN207734648U (en) |
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2017
- 2017-12-22 CN CN201721808772.3U patent/CN207734648U/en active Active
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