CN207838366U - A kind of astaxanthin supercritical extraction unit - Google Patents

A kind of astaxanthin supercritical extraction unit Download PDF

Info

Publication number
CN207838366U
CN207838366U CN201721867214.4U CN201721867214U CN207838366U CN 207838366 U CN207838366 U CN 207838366U CN 201721867214 U CN201721867214 U CN 201721867214U CN 207838366 U CN207838366 U CN 207838366U
Authority
CN
China
Prior art keywords
extractor
astaxanthin
supercritical extraction
extraction unit
hollow pipe
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
CN201721867214.4U
Other languages
Chinese (zh)
Inventor
成功
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Yunnan Tan Ze Biotechnology Co Ltd
Original Assignee
Yunnan Tan Ze Biotechnology Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Yunnan Tan Ze Biotechnology Co Ltd filed Critical Yunnan Tan Ze Biotechnology Co Ltd
Priority to CN201721867214.4U priority Critical patent/CN207838366U/en
Application granted granted Critical
Publication of CN207838366U publication Critical patent/CN207838366U/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/50Improvements relating to the production of bulk chemicals
    • Y02P20/54Improvements relating to the production of bulk chemicals using solvents, e.g. supercritical solvents or ionic liquids

Landscapes

  • Extraction Or Liquid Replacement (AREA)

Abstract

The utility model discloses a kind of astaxanthin supercritical extraction units, including extractor, agitating device is housed in extractor, extractor upper end is equipped with sealing cover, feed head is housed on sealing cover, it extracts on pot sidewall equipped with observation overflow launder, it observes overflow launder upper end and moveable hollow pipe is connected by seal assembly, moveable hollow pipe upper end connects electric pushrod, moveable hollow pipe upper end is equipped with pipe fitting, extractor lower end is provided with discharge nozzle, discharge nozzle side connects air intake pump, baroceptor is housed in extractor, the utility model structure novel, it is stable, it can realize that carbon dioxide supercritical extraction is processed, carbon dioxide can be realized and be recycled, utilization rate of carbon dioxide is high, it can be left the lifting extraction of extract liquor, it extracts convenient and efficient, meet present requirement.

Description

A kind of astaxanthin supercritical extraction unit
Technical field
The utility model is related to a kind of haematococcus pluvialis processing unit (plant), specifically a kind of astaxanthin supercritical extraction unit.
Background technology
Haematococcus is a kind of fresh water single cell green alga, is subordinate to Chlorophyta, volvocales, haematococcus section, haematococcus.The algae can be big Amount accumulates astaxanthin and red is presented, therefore named haematococcus, also known as haematococcus pluvialis.Haematococcus is current scientific circles' discovery after spiral shell After revolving algae, chlorella, it is rich in the seaweed food of nutritive value and medical value.
In recent years, haematococcus pluvialis is considered as one of production astaxanthin optimum feed stock.Astaxanthin has than carotenoid And the higher antioxidant activity of vitamin E.Studies have shown that its inoxidizability is 10 times of carotenoid, vitamin E 550 Times, it is known as " super antioxidant ".Some external research institutions are it is contemplated that using astaxanthin as the pharmaceutical raw material of high value, protect Health food raw material etc..But extraction astaxanthin generally existing content astaxanthin is low only from aquatic products waste at present, extracts expense High disadvantage.
So extracted in the haematococcus of the usually same artificial breeding of the extraction of astaxanthin now, extracting shrimp blueness When plain, carbon dioxide supercritical extraction usually is carried out to broken wall solution, but this kind of extraction equipment structure is relatively simple now, Carbon dioxide waste is serious, and extract liquor extraction is not easy, and residual is more, cannot meet present requirement.
Utility model content
The purpose of this utility model is to provide a kind of astaxanthin supercritical extraction units, to solve in above-mentioned background technology The problem of proposition.
To achieve the above object, the utility model provides the following technical solutions:
A kind of astaxanthin supercritical extraction unit, including extractor, are equipped with agitating device in the extractor, on extractor End is equipped with sealing cover, and feed head is housed on sealing cover, extracts and passes through equipped with observation overflow launder, observation overflow launder upper end on pot sidewall Seal assembly connects moveable hollow pipe, and moveable hollow pipe upper end connects electric pushrod, and moveable hollow pipe upper end is equipped with pipe fitting, extraction Tank lower end is taken to be provided with discharge nozzle, discharge nozzle side connects air intake pump, baroceptor is housed in extractor.
As further program of the utility model:The agitating device upper end connects driving device.
As further program of the utility model:The observation overflow groove sidewall is provided with transparent panel.
As further program of the utility model:The sealing cover upper end connects air intake pump by recycling air outlet valve.
As further program of the utility model:The air intake pump connects carbon dioxide gas tank by control valve.
As further program of the utility model:The discharge nozzle lower end is provided with discharging control valve.
Compared with prior art, the utility model has the beneficial effects that:The utility model structure novel, stable, energy Enough realize that carbon dioxide supercritical extraction processing, carbon dioxide can realize and recycle that utilization rate of carbon dioxide is high, can remain The lifting of lower extract liquor is extracted, and extraction is convenient and efficient, meets present requirement.
Description of the drawings
Fig. 1 is the structural schematic diagram of astaxanthin supercritical extraction unit.
In figure:1- carbon dioxide gas tanks, 2- control valves, 3- air pumps, 4- extractors, 5- observation overflow launder, 6- electric pushrods, 7- moveable hollows pipe, 8- seal assemblies, 9- pipe fittings, 10- feed heads, 11- cycles air outlet valve, 12- driving devices, 13- air pressures Sensor, 14- agitating devices, 15- discharge nozzles, 16- discharging control valves.
Specific implementation mode
The following will be combined with the drawings in the embodiments of the present invention, carries out the technical scheme in the embodiment of the utility model Clearly and completely describe, it is clear that the described embodiments are only a part of the embodiments of the utility model, rather than whole Embodiment.Based on the embodiments of the present invention, those of ordinary skill in the art are without making creative work The every other embodiment obtained, shall fall within the protection scope of the present invention.
Referring to Fig. 1, in the utility model embodiment, a kind of astaxanthin supercritical extraction unit, including extractor 4, institute It states and agitating device 14 is housed in extractor 4,4 upper end of extractor is equipped with sealing cover, and feed head 10, extractor 4 are housed on sealing cover Moveable hollow pipe 7, moveable hollow pipe 7 are connected by seal assembly equipped with observation overflow launder 5, observation 5 upper end of overflow launder on side wall Upper end connects electric pushrod 6, and 7 upper end of moveable hollow pipe is equipped with pipe fitting 9, and 4 lower end of extractor is provided with discharge nozzle 15, discharge nozzle 15 sides connect air intake pump 3, and baroceptor 13 is housed in extractor 4, and 14 upper end of agitating device connects driving device 12, observation 5 side wall of overflow launder is provided with transparent panel, and sealing cover upper end connects air intake pump 3 by recycling air outlet valve 11, and air intake pump 3 passes through control Valve 2 connects carbon dioxide gas tank 1, and 15 lower end of discharge nozzle is provided with discharging control valve 16.
The utility model structure novel, it is stable, it can realize that carbon dioxide supercritical extraction is processed, carbon dioxide energy Enough realize recycles, and utilization rate of carbon dioxide is high, can be left the lifting extraction of extract liquor, extraction is convenient and efficient, meets Present requirement.
In the description of the present invention, it should be understood that term "center", " longitudinal direction ", " transverse direction ", "upper", "lower", The orientation or positional relationship of the instructions such as "front", "rear", "left", "right", "vertical", "horizontal", "top", "bottom", "inner", "outside" is It is based on the orientation or positional relationship shown in the drawings, is merely for convenience of describing the present invention and simplifying the description, rather than indicate Or imply that signified device or element must have a particular orientation, with specific azimuth configuration and operation, therefore cannot understand For limitations of the present invention.In addition, term " first ", " second " etc. are used for description purposes only, and should not be understood as indicating Or it implies relative importance or implicitly indicates the quantity of indicated technical characteristic." first ", " second " etc. are defined as a result, Feature can explicitly or implicitly include one or more this feature.It is in the description of the present invention, unless another It is described, the meaning of " plurality " is two or more.
In the description of the present invention, it should be noted that unless otherwise clearly defined and limited, term " is pacified Dress ", " connected ", " connection " shall be understood in a broad sense, for example, it may be being fixedly connected, may be a detachable connection, or integrally Connection;It can be mechanical connection, can also be electrical connection;Can be directly connected, can also indirectly connected through an intermediary, It can be the connection inside two elements.For the ordinary skill in the art, on being understood by concrete condition State the concrete meaning of term in the present invention.
It is obvious to a person skilled in the art that the present invention is not limited to the details of the above exemplary embodiments, and And without departing substantially from the spirit or essential attributes of the utility model, it can realize that this practicality is new in other specific forms Type.Therefore, in all respects, the present embodiments are to be considered as illustrative and not restrictive, this practicality is new The range of type is indicated by the appended claims rather than the foregoing description, it is intended that containing in the equivalent requirements of the claims will be fallen All changes in justice and range are embraced therein.Any reference numeral in claim should not be considered as limitation Involved claim.
In addition, it should be understood that although this specification is described in terms of embodiments, but not each embodiment is only wrapped Containing an independent technical solution, this description of the specification is merely for the sake of clarity, and those skilled in the art should It considers the specification as a whole, the technical solutions in the various embodiments may also be suitably combined, forms those skilled in the art The other embodiment being appreciated that.

Claims (6)

1. a kind of astaxanthin supercritical extraction unit, including extractor (4), which is characterized in that be equipped with and stir in the extractor (4) Device (14) is mixed, extractor (4) upper end is equipped with sealing cover, feed head (10) is housed on sealing cover, is equipped on extractor (4) side wall Overflow launder (5) is observed, observation overflow launder (5) upper end connects moveable hollow pipe (7) by seal assembly, on moveable hollow pipe (7) End connection electric pushrod (6), moveable hollow pipe (7) upper end are equipped with pipe fitting (9), and extractor (4) lower end is provided with discharge nozzle (15), discharge nozzle (15) side connection air intake pump (3), extractor (4) is interior to be equipped with baroceptor (13).
2. astaxanthin supercritical extraction unit according to claim 1, which is characterized in that agitating device (14) upper end Connect driving device (12).
3. astaxanthin supercritical extraction unit according to claim 1, which is characterized in that observation overflow launder (5) side Wall is provided with transparent panel.
4. astaxanthin supercritical extraction unit according to claim 1, which is characterized in that the sealing cover upper end is by following Ring air outlet valve (11) connects air intake pump (3).
5. astaxanthin supercritical extraction unit according to claim 1, which is characterized in that the air intake pump (3) passes through control Valve (2) connection carbon dioxide gas tank (1) processed.
6. astaxanthin supercritical extraction unit according to claim 1, which is characterized in that discharge nozzle (15) lower end is set It is equipped with discharging control valve (16).
CN201721867214.4U 2017-12-27 2017-12-27 A kind of astaxanthin supercritical extraction unit Expired - Fee Related CN207838366U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201721867214.4U CN207838366U (en) 2017-12-27 2017-12-27 A kind of astaxanthin supercritical extraction unit

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201721867214.4U CN207838366U (en) 2017-12-27 2017-12-27 A kind of astaxanthin supercritical extraction unit

Publications (1)

Publication Number Publication Date
CN207838366U true CN207838366U (en) 2018-09-11

Family

ID=63419276

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201721867214.4U Expired - Fee Related CN207838366U (en) 2017-12-27 2017-12-27 A kind of astaxanthin supercritical extraction unit

Country Status (1)

Country Link
CN (1) CN207838366U (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111701276A (en) * 2020-08-19 2020-09-25 东营正大金属制品有限公司 Supercritical carbon dioxide extraction kettle

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111701276A (en) * 2020-08-19 2020-09-25 东营正大金属制品有限公司 Supercritical carbon dioxide extraction kettle
CN111701276B (en) * 2020-08-19 2021-01-05 白婷婷 Supercritical carbon dioxide extraction kettle

Similar Documents

Publication Publication Date Title
CN204417501U (en) A kind of propelling stirring-type backflow anaerobic fermentation tank
CN210901243U (en) Plant protein extraction device
CN207838366U (en) A kind of astaxanthin supercritical extraction unit
CN106749734A (en) sweet lily polysaccharide extracting method
CN207845647U (en) A kind of haematococcus pluvialis means for breaking walls
CN108929256B (en) Broken wall lactobacillus supercritical CO2The static method for extracting astaxanthin with dynamic cooperation
CN104397641A (en) Pickled pepper vacuum suction pool fishing method and suction machine
CN209193936U (en) Edible mature vinegar drenches vinegar device
CN207845646U (en) A kind of Astaxanthin extraction device
CN207845643U (en) A kind of bioreactor of scale haematococcus production astaxanthin
CN207838333U (en) A kind of Low-temperature concentration device
CN207845631U (en) A kind of algae culture case
CN204356326U (en) A kind of Novel angle recirculate mixing stirring-type anaerobic fermentation tank
CN207845525U (en) A kind of solvent flashing recovery system
CN203886234U (en) Ultrasonic extractor
CN205214153U (en) Continuous production energy -saving control device is peeld to walnut -meat
CN204342781U (en) A kind of Novel angle recirculate mixing stirs and filtering type fermentor tank
CN209338424U (en) Sodium lactate filter plant
CN107858174A (en) A kind of special Embryo Culture mineral oil in vitro fertilization and preparation method thereof
CN207845623U (en) A kind of haematococcus pluvialis dehydration device
CN207980449U (en) A kind of haematococcus pluvialis drying device
CN109395428A (en) Extraction and separation device and system and extraction and separation method thereof
CN203841065U (en) Red jujube continuous crushing equipment system for red jujube juice production
CN209456428U (en) A kind of filter device of raspberry health preserving wine
CN203833853U (en) Improved equipment for extracting seaweed polysaccharide with assistance of ultrasonic waves

Legal Events

Date Code Title Description
GR01 Patent grant
GR01 Patent grant
CF01 Termination of patent right due to non-payment of annual fee
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20180911

Termination date: 20211227