CN205710524U - A kind of Astaxanthin extraction system - Google Patents
A kind of Astaxanthin extraction system Download PDFInfo
- Publication number
- CN205710524U CN205710524U CN201620550953.XU CN201620550953U CN205710524U CN 205710524 U CN205710524 U CN 205710524U CN 201620550953 U CN201620550953 U CN 201620550953U CN 205710524 U CN205710524 U CN 205710524U
- Authority
- CN
- China
- Prior art keywords
- extraction
- extraction equipment
- astaxanthin
- conveying pipeline
- circulation 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.)
- Active
Links
Landscapes
- Extraction Or Liquid Replacement (AREA)
Abstract
The utility model discloses a kind of Astaxanthin extraction system, it includes the first extraction equipment, the second extraction equipment, conveying pipeline and centrifuge, described first extraction equipment is connected with centrifuge by conveying pipeline, it is positioned at and be provided with circulation pipe on conveying pipeline described between the first extraction equipment and centrifuge, described second extraction equipment is arranged on circulation pipe, and the feed end of circulation pipe and the first extraction equipment connect.The purpose of this utility model is intended to provide that a kind of extract yield is high, extraction time is short, extraction temperature is low, Solvent quantity is few, the content of active ingredient declines to a great extent in extraction slag, and particularly suitable astaxanthin one class has thermal sensitivity, light sensitivity, the Astaxanthin extraction system of oxidisability characteristic material.
Description
Technical field
The utility model belongs to technical field of bioengineering, is specifically related to a kind of Astaxanthin extraction system.
Background technology
Haematococcus pluvialis (Haematococcus pluvialis) is a kind of fresh water monoplast green alga, is subordinate to Chlorophyta, group
Cutleriales, haematococcus section, haematococcus.It accumulates substantial amounts of astaxanthin when being coerced by high light, nitrogen hunger, high salt etc., and content can be high
Reach more than the 6.0% of dry cell weight.Correlative study displays that astaxanthin has extremely strong antioxidation activity, its anti-oxidant work
Property compared with alpha-tocopherol strong thousand times, than vitamin E high nearly a hundred times.The astaxanthin that haematococcus pluvialis produces may be used as anti-oxidant
Agent eliminates intracellular oxygen radical isoreactivity oxygen (ROS).For better profiting from the astaxanthin in haematococcus pluvialis, need to be to it
Carry out extracting processing.
Astaxanthin belongs to carotenoid, in cerise, is a kind of high-quality pigment and super antioxidant, and one has neighbour
The carotenoid of hydroxy-ketone structure, its chemical name is 3,3-dihydroxy-4,4-diketo-β, β '-carrotene, pure astaxanthin
It is reddish dark brown crystal, fusing point 224 DEG C, water insoluble, most of organic solvent can be dissolved in.Astaxanthin has superpower antioxygen
The property changed and the ability removing free radical, clinical and Experiment of Zoology shows that astaxanthin has good anti-inflammatory, antitumor, anti-ageing
Always, protect skin, strengthen immunity of organism, prevent angiocardiopathy, safeguard eye health, the many-side such as reproductive capacity improving animal
Important biological function.In addition, astaxanthin also has a significant tinctorial property, currently mainly as aquatic products, birds, beasts and eggs,
Animal for display cultivation and the colouring agent of livestock products.Therefore astaxanthin is at row such as food, medicine, cosmetics, health products and feeds
Industry has very big application potential, wide market.At present, from haematococcus pluvialis, krill all can extract
Astaxanthin, but from haematococcus pluvialis, extract astaxanthin, and the wall breaking technology of haematococcus pluvialis is very crucial, directly affects shrimp blue or green
The quality of element extraction and purity.
Utility model content
For above-mentioned weak point of the prior art, the purpose of this utility model is intended to provide a kind of extract yield
High, extraction time is short, extraction temperature is low, Solvent quantity is few, the content of active ingredient declines to a great extent in extraction slag, particularly suitable
Astaxanthin one class has thermal sensitivity, light sensitivity, the Astaxanthin extraction system of oxidisability characteristic material.
In order to solve above-mentioned technical problem, the utility model is achieved through the following technical solutions: a kind of astaxanthin carries
Taking system, it includes the first extraction equipment, the second extraction equipment, conveying pipeline and centrifuge, and described first extraction equipment passes through defeated
Material pipe is connected with centrifuge, is positioned at and is provided with circulation pipe on conveying pipeline described between the first extraction equipment and centrifuge, described
Second extraction equipment is arranged on circulation pipe, and the feed end of circulation pipe and the first extraction equipment connect.
Preferably, described first extraction equipment is the first extraction equipment, and described first extraction equipment is provided with charging
Mouth, agitating device, extract inlet pipe, steam inlet tube and draining system, described agitating device working end is positioned at the first extraction equipment
Inside, described extract inlet pipe is provided with first flow controller and the first pneumatic operated valve, and described draining system is arranged at first
The bottom of extraction equipment.
Preferably, described conveying pipeline is provided with delivery pump, the second pneumatic operated valve and second flow controller, described circulation
It is provided with the 3rd pneumatic operated valve on pipe.
Preferably, described centrifuge is provided with leakage fluid dram and slag-drip opening.
Preferably, described second extraction equipment is pipeline mixing shearing extractor.
Operation principle of the present utility model is:
A certain amount of haematococcus pluvialis raw material algae powder to be extracted is added inside the first extraction equipment by charging aperture, starts automatically
Control system program, a certain amount of extractant is controlled automatically by first flow controller, the first pneumatic operated valve on extract inlet pipe
System adds inside the first extraction equipment, and after raw materials finishes, control system starts the agitating device pair on the first extraction equipment
Material within agitating device is stirred mixing, it is ensured that extraction liquid-solid ratio reaches technological requirement, and control system opens steam simultaneously
Inlet pipe, the steam condensate (SC) producing in the chuck of the first extraction equipment is discharged by draining system, it is ensured that extraction temperature reaches technique and wants
Asking, while the first extraction equipment is stirred extraction to materials inside, it is defeated that control system is opened bottom the first extraction equipment
Material pipe, opens the 3rd pneumatic operated valve, closes the second pneumatic operated valve, startup delivery pump, and material is returned by circulation pipe and the second extraction equipment
Carry out outer circulation extraction process in returning the first extraction equipment.When reaching extraction time, materials abstraction process completes, and control system is opened
Open the second pneumatic operated valve, cut out the 3rd pneumatic operated valve is transported to centrifuge the material within the first extraction equipment and carries out solid-liquor separation,
When second flow controller detect in the first extraction equipment material conveying finish after, automatic control system stop delivery pump,
Close the second pneumatic operated valve, steam off inlet pipe, stop agitating device, closedown conveying pipeline, so realize that batch materials first extracts dress
Put stirring extraction serial pipe extraction and extract astaxanthin automatic control process process.
Brief description
Fig. 1 is the utility model structural representation.
Detailed description of the invention
As it is shown in figure 1, a kind of Astaxanthin extraction system, it includes the first extraction equipment the 1st, the second extraction equipment the 3rd, conveying pipeline
8 and centrifuge 2, described first extraction equipment 1 is connected with centrifuge 2 by conveying pipeline 8, be positioned at the first extraction equipment 1 with centrifugal
Being provided with circulation pipe 17 on conveying pipeline 8 described between machine 2, described second extraction equipment 3 is arranged on circulation pipe 17, circulation pipe
Feed end and first extraction equipment 1 of 17 connect；Described first extraction equipment 1 is the first extraction equipment, described first extraction dress
Put and on 1, be provided with charging aperture the 4th, agitating device the 5th, extract inlet pipe the 6th, steam inlet tube 11 and draining system 7, described agitating device 5
It is internal that working end is positioned at the first extraction equipment 1, described extract inlet pipe 6 is provided with first flow controller 10 and first pneumatic
Valve 12, described draining system 7 is arranged at the bottom of the first extraction equipment 1；It is provided with delivery pump the 9th, the second gas on described conveying pipeline 8
Dynamic valve 14 and second flow controller 13, described circulation pipe 17 is provided with the 3rd pneumatic operated valve 18；It is provided with on described centrifuge 2
Leakage fluid dram 15 and slag-drip opening 16；Described second extraction equipment 3 is pipeline mixing shearing extractor.
Claims (5)
1. an Astaxanthin extraction system, it is characterised in that include the first extraction equipment, the second extraction equipment, conveying pipeline and from
Scheming, described first extraction equipment is connected with centrifuge by conveying pipeline, is positioned between the first extraction equipment and centrifuge described
Conveying pipeline on be provided with circulation pipe, described second extraction equipment is arranged on circulation pipe, the feed end of circulation pipe and first extraction
Fetching puts connection.
2. a kind of Astaxanthin extraction system according to claim 1, it is characterised in that described first extraction equipment is first
Extraction equipment, described first extraction equipment is provided with charging aperture, agitating device, extract inlet pipe, steam inlet tube and hydrophobic system
System, described agitating device working end is positioned inside the first extraction equipment, and described extract inlet pipe is provided with first flow control
Instrument and the first pneumatic operated valve, described draining system is arranged at the bottom of the first extraction equipment.
3. a kind of Astaxanthin extraction system according to claim 1, it is characterised in that be provided with conveying on described conveying pipeline
Pump, the second pneumatic operated valve and second flow controller, described circulation pipe is provided with the 3rd pneumatic operated valve.
4. a kind of Astaxanthin extraction system according to claim 1, it is characterised in that be provided with discharge opeing on described centrifuge
Mouth and slag-drip opening.
5. a kind of Astaxanthin extraction system according to claim 1, it is characterised in that described second extraction equipment is pipeline
Mixing shearing extractor.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620550953.XU CN205710524U (en) | 2016-06-08 | 2016-06-08 | A kind of Astaxanthin extraction system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620550953.XU CN205710524U (en) | 2016-06-08 | 2016-06-08 | A kind of Astaxanthin extraction system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205710524U true CN205710524U (en) | 2016-11-23 |
Family
ID=57302684
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620550953.XU Active CN205710524U (en) | 2016-06-08 | 2016-06-08 | A kind of Astaxanthin extraction system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205710524U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111217734A (en) * | 2018-11-27 | 2020-06-02 | 云南爱尔康生物技术有限公司 | Method for extracting astaxanthin from haematococcus pluvialis |
| CN112999686A (en) * | 2021-02-23 | 2021-06-22 | 青岛黄海学院 | Comprehensive astaxanthin broken wall extraction element of haematococcus pluvialis |
| CN113230691A (en) * | 2021-06-09 | 2021-08-10 | 云南爱尔发生物技术股份有限公司 | Extraction system for rapidly preparing astaxanthin monomer |
-
2016
- 2016-06-08 CN CN201620550953.XU patent/CN205710524U/en active Active
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111217734A (en) * | 2018-11-27 | 2020-06-02 | 云南爱尔康生物技术有限公司 | Method for extracting astaxanthin from haematococcus pluvialis |
| CN112999686A (en) * | 2021-02-23 | 2021-06-22 | 青岛黄海学院 | Comprehensive astaxanthin broken wall extraction element of haematococcus pluvialis |
| CN112999686B (en) * | 2021-02-23 | 2022-11-08 | 青岛黄海学院 | Comprehensive astaxanthin broken wall extraction element of haematococcus pluvialis |
| CN113230691A (en) * | 2021-06-09 | 2021-08-10 | 云南爱尔发生物技术股份有限公司 | Extraction system for rapidly preparing astaxanthin monomer |
| CN113230691B (en) * | 2021-06-09 | 2023-08-15 | 云南爱尔发生物技术股份有限公司 | Extraction system for rapidly preparing astaxanthin monomer |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN205710524U (en) | A kind of Astaxanthin extraction system | |
| CN103787941B (en) | A kind of method extracting astaxanthin from Haematocoocus Pluvialls | |
| CN102860996B (en) | Method for preparing lycoypene microcapsule | |
| EP3194607B1 (en) | Method and apparatus for producing astaxanthin | |
| US20180094209A1 (en) | Extraction of Essential Oils | |
| Cheng et al. | Preparation of astaxanthin mask from Phaffia rhodozyma and its evaluation | |
| WO2018071372A1 (en) | Extraction of essential oils | |
| CN110547455A (en) | Microcapsule containing sialic acid and carotenoid and preparation method and application thereof | |
| CN105085598B (en) | K2 compositions and preparation method and application | |
| CN108929256B (en) | Broken wall lactobacillus supercritical CO2The static method for extracting astaxanthin with dynamic cooperation | |
| CN206184037U (en) | A multistage separation device for animal and plant materials | |
| Zakaria et al. | Extraction of antioxidants from Chlorella sp. using subcritical water treatment | |
| CN100408642C (en) | Method for integrated extraction of active substances in Platymonas | |
| CN109431905B (en) | Lithospermum extract and preparation method and application thereof | |
| CN104529851A (en) | New technology for extracting astaxanthin from Haematococcus pluvialis through enzyme method | |
| CN102471795A (en) | Production method for astaxanthin-containing composition | |
| CN106913589A (en) | A kind of haematococcus pluvialis solid dispersions, Preparation Method And The Use | |
| CN104027408B (en) | Oil-in-water type compound apramycin nano-emulsion | |
| CN101609039A (en) | The assay method of sporoderm-broken rate of spore of haematococcus pluvialis | |
| CN202482329U (en) | NSCs (neural stem cell) continuous perfusion and cultivation system | |
| Vatankhah et al. | Astaxanthin extraction—Recent methods, developments and case studies | |
| CN107235881A (en) | The supercritical carbon dioxide extraction method of astaxanthin in transgenic engineering tamato fruit | |
| CN106810483B (en) | A kind of method of active material in extraction spirulina | |
| CN207838366U (en) | A kind of astaxanthin supercritical extraction unit | |
| CN102212024B (en) | Method for synthesizing astaxanthin by using natural lutein |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant |