CN205461115U - Astaxanthin supercritical fluid extraction device - Google Patents
Astaxanthin supercritical fluid extraction device Download PDFInfo
- Publication number
- CN205461115U CN205461115U CN201620031382.9U CN201620031382U CN205461115U CN 205461115 U CN205461115 U CN 205461115U CN 201620031382 U CN201620031382 U CN 201620031382U CN 205461115 U CN205461115 U CN 205461115U
- Authority
- CN
- China
- Prior art keywords
- astaxanthin
- carbon dioxide
- compressor
- separator
- extraction
- 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
Links
- 235000013793 astaxanthin Nutrition 0.000 title claims abstract description 27
- 239000001168 astaxanthin Substances 0.000 title claims abstract description 26
- 229940022405 astaxanthin Drugs 0.000 title claims abstract description 26
- MQZIGYBFDRPAKN-QISQUURKSA-N 6-hydroxy-3-[(1E,3E,5E,7E,9E,11E,13E,15E,17E)-18-(4-hydroxy-2,6,6-trimethyl-3-oxocyclohexen-1-yl)-3,7,12,16-tetramethyloctadeca-1,3,5,7,9,11,13,15,17-nonaenyl]-2,4,4-trimethylcyclohex-2-en-1-one Chemical compound CC=1C(=O)C(O)CC(C)(C)C=1\C=C\C(\C)=C\C=C\C(\C)=C\C=C\C=C(/C)\C=C\C=C(/C)\C=C\C1=C(C)C(=O)C(O)CC1(C)C MQZIGYBFDRPAKN-QISQUURKSA-N 0.000 title claims abstract description 25
- 238000000194 supercritical-fluid extraction Methods 0.000 title claims abstract description 14
- 238000000605 extraction Methods 0.000 claims abstract description 25
- CURLTUGMZLYLDI-UHFFFAOYSA-N carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 claims abstract description 21
- 229910002092 carbon dioxide Inorganic materials 0.000 claims abstract description 21
- 239000001569 carbon dioxide Substances 0.000 claims abstract description 21
- 238000001035 drying Methods 0.000 claims abstract description 17
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 10
- OKTJSMMVPCPJKN-UHFFFAOYSA-N carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 7
- 239000011148 porous material Substances 0.000 claims description 4
- 239000008187 granular material Substances 0.000 claims description 3
- 239000011347 resin Substances 0.000 claims description 3
- 229920005989 resin Polymers 0.000 claims description 3
- 239000000463 material Substances 0.000 abstract description 6
- 239000000284 extract Substances 0.000 abstract description 4
- 238000000034 method Methods 0.000 abstract description 4
- 239000006185 dispersion Substances 0.000 abstract description 2
- 230000000694 effects Effects 0.000 description 4
- 239000012535 impurity Substances 0.000 description 3
- 229920002456 HOTAIR Polymers 0.000 description 2
- 238000007906 compression Methods 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 description 2
- 241000972773 Aulopiformes Species 0.000 description 1
- 241000238424 Crustacea Species 0.000 description 1
- 241000238557 Decapoda Species 0.000 description 1
- 241000790917 Dioxys <bee> Species 0.000 description 1
- 210000003746 Feathers Anatomy 0.000 description 1
- 241000070023 Phoenicopterus roseus Species 0.000 description 1
- 230000000259 anti-tumor Effects 0.000 description 1
- MQZIGYBFDRPAKN-UWFIBFSHSA-N astaxanthins Chemical class CC(\C=C\C=C(C)\C=C\C1=C(C)C(=O)[C@@H](O)CC1(C)C)=C/C=C/C=C(C)/C=C/C=C(C)/C=C/C1=C(C)C(=O)[C@@H](O)CC1(C)C MQZIGYBFDRPAKN-UWFIBFSHSA-N 0.000 description 1
- 201000011510 cancer Diseases 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 230000002708 enhancing Effects 0.000 description 1
- 230000036039 immunity Effects 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000006011 modification reaction Methods 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 230000004977 physiological function Effects 0.000 description 1
- 230000035790 physiological processes and functions Effects 0.000 description 1
- 230000000069 prophylaxis Effects 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 150000003505 terpenes Chemical class 0.000 description 1
- 235000007586 terpenes Nutrition 0.000 description 1
- 239000004408 titanium dioxide Substances 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
- UZFLPKAIBPNNCA-BQYQJAHWSA-N α-ionone Chemical group CC(=O)\C=C\C1C(C)=CCCC1(C)C UZFLPKAIBPNNCA-BQYQJAHWSA-N 0.000 description 1
Classifications
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/50—Improvements relating to the production of bulk chemicals
- Y02P20/54—Improvements relating to the production of bulk chemicals using solvents, e.g. supercritical solvents or ionic liquids
Abstract
The utility model discloses an astaxanthin supercritical fluid extraction device, carbon dioxide jar and compressor pass through the pipe connection, the compressor is connected with the extraction cauldron, the extraction cauldron is connected with the separator, the separator is connected with the clarifier, drying device is connected with the separator, the fan is connected with air heater, air heater and drying device are connected, clarifier, compressor and carbon dioxide jar connect gradually through the circulating line. Inside at the extraction cauldron is equipped with the multilayer column plate, and is equipped with the cassette on the column plate, can extract the dispersion of astaxanthin material on each column plate, the caking phenomenon that appears when can effectual solution astaxanthin water content higher, handle through the process of the carbon dioxide to extracting clarifier, loop through absorbed layer, adsorbed layer and filter screen for carbon dioxide's purity is higher, and the circulating line is through compressor compressed storage at the carbon dioxide jar, in order to reuse.
Description
Technical field
This utility model belongs to extraction equipment technical field, is specifically related to a kind of astaxanthin supercritical extraction dress
Put.
Background technology
Astaxanthin that is 3,3 '-dihydroxy-4,4 '-diketo-β, β '-carotene, for terpenes not
Saturated compounds, chemical molecular formula is C40H52O4, has two alpha, beta-lonone rings in molecular structure, 11
Individual conjugated double bond.Astaxanthin is widely present in nature, such as most of Crustaceans and salmon fishes body
In, the leaf of plant, flower, really, and the feather of flamingo is medium.Astaxanthin has multiple physiological function,
As non-oxidizability, antitumor, prophylaxis of cancer, enhancing immunity, improve vision etc. in terms of have certain
Effect.Current Astaxanthin extraction substantially uses supercritical extraction unit, and it has comparison excellent
Extract performance, but there is also deficiency.Such as, current astaxanthin supercritical extraction unit is to dioxy
The utilization changing carbon is disposable, compares waste；And when astaxanthin material to be extracted aqueous more time
Materials from bonding caking easily occurs in extraction kettle, and time serious, whole still material can form one piece, does not only reach
Effect of extracting, in some instances it may even be possible to occluding device, furthermore it is exactly the function material not dried, use not
Convenient.
Utility model content
The purpose of this utility model is to provide a kind of astaxanthin supercritical extraction unit, to solve the above-mentioned back of the body
The problem proposed in scape technology.
For achieving the above object, this utility model provides following technical scheme: a kind of astaxanthin supercritical extracts
Fetching is put, including carbon dioxide tank, compressor, regulation tank, drying unit and blower fan, described titanium dioxide
Canister and compressor are connected by pipeline, and described compressor is connected with extraction kettle, described extraction kettle with separate
Device connects, and described separator is connected with depurator, and described drying unit is connected with separator, described blower fan
Being connected with air heater, described air heater is connected with drying unit, described depurator, compressor
It is sequentially connected with by circulating line with carbon dioxide tank.
Preferably, described separator is set to three grades.
Preferably, the inside of described depurator is sequentially provided with drainage screen, adsorption layer and water accepting layer from top to bottom,
The inside of described adsorption layer is filled with activated carbon granule, and the inside of described water accepting layer is filled with water-absorbing resin.
Preferably, the both sides of described drying unit are respectively arranged with discharge pipe, and the surface of described discharge pipe is equal
Even pore is distributed.
Preferably, the inside of described extraction kettle is provided with extraction equipment, and the inside of described extraction equipment is provided with 3-5
Layer column plate, described column plate is provided with filter.
Technique effect of the present utility model and advantage: this astaxanthin supercritical extraction unit, by extraction
The inside of still is provided with multilamellar column plate, and is provided with filter on column plate, astaxanthin material dispersion can be existed
Extract on each column plate, can effectively solve astaxanthin water content higher time occur caking phenomenon；
By stripped carbon dioxide is processed through depurator, pass sequentially through absorbed layer, adsorption layer and
Drainage screen, can effectively remove moisture, particulate matter and other the impurity contained in carbon dioxide,
The purity making carbon dioxide is higher, is stored in carbon dioxide tank by circulating line through compressor compression,
In case again with；By blower fan air input air heater, air heater air is carried out
Heating, then hot-air is delivered to drying unit astaxanthin is dried.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model；
Fig. 2 is depurator structural representation of the present utility model.
In figure: 1 carbon dioxide tank, 2 compressors, 3 extraction kettles, 4 separators, 5 depurators, 6 drying
Device, 7 air heaters, 8 blower fans, 9 extraction equipments, 10 filters, 11 column plates, 12 discharge pipes,
13 pores, 14 drainage screens, 15 adsorption layers, 16 water accepting layers.
Detailed description of the invention
Below in conjunction with the accompanying drawing in this utility model embodiment, to the technology in this utility model embodiment
Scheme is clearly and completely described, it is clear that described embodiment is only this utility model one
Divide embodiment rather than whole embodiments.Based on the embodiment in this utility model, this area is common
The every other embodiment that technical staff is obtained under not making creative work premise, broadly falls into this
The scope of utility model protection.
This utility model provides a kind of astaxanthin supercritical extraction unit as shown in Figure 1-2, including two
Oxidation canister 1, compressor 2, drying unit 6 and blower fan 8, described carbon dioxide tank 1 and compressor 2
Being connected by pipeline, described compressor 2 is connected with extraction kettle 3, and the inside of described extraction kettle 3 is provided with extraction
Fetching puts 9, and the inside of described extraction equipment 9 is provided with 3-5 layer column plate 11, and described column plate 11 was provided with
Filter disc 10, can effectively solve astaxanthin water content higher time occur caking phenomenon, and then improve shrimp
The efficiency of blue or green element extraction and effect；Described extraction kettle 3 is connected with separator 4, and described separator 4 is with clean
Changing device 5 to connect, the inside of described depurator 5 is sequentially provided with drainage screen 14, adsorption layer 15 and from top to bottom
Water accepting layer 16, the inside of described adsorption layer 15 is filled with activated carbon granule, the inside of described water accepting layer 16
Being filled with water-absorbing resin, described separator 4 is set to three grades, and described drying unit 6 is with separator 4 even
Connecing, described blower fan 8 is connected with air heater 7, and described air heater 7 is connected with drying unit 6,
The both sides of described drying unit 6 are respectively arranged with discharge pipe 12, and the surface of described discharge pipe 12 is uniformly distributed
There is pore 13, by 8 air input air heaters 7 of blower fan, air is entered air heater 7
Row heating, then hot-air is delivered to drying unit 6 astaxanthin is uniformly dried, described depurator 5,
Compressor 2 and carbon dioxide tank 1 are sequentially connected with by circulating line, by stripped carbon dioxide
Process through depurator 5, pass sequentially through absorbed layer 16, adsorption layer 15 and drainage screen 14, carry out
Multistage remove impurity and purify can effectively remove carbon dioxide contains moisture, particulate matter and other
Impurity, makes the purity of carbon dioxide again obtained higher, is deposited through compressor 2 compression by circulating line
Store up at carbon dioxide tank 1, in case again with.
Last it is noted that the foregoing is only preferred embodiment of the present utility model, and need not
In limiting this utility model, although this utility model being described in detail with reference to previous embodiment,
For a person skilled in the art, it still can be to the technical scheme described in foregoing embodiments
Modify, or wherein portion of techniques feature carried out equivalent, all in spirit of the present utility model and
Within principle, any modification, equivalent substitution and improvement etc. made, should be included in of the present utility model
Within protection domain.
Claims (5)
1. an astaxanthin supercritical extraction unit, including carbon dioxide tank (1), compressor (2), dries
Equipment for drying (6) and blower fan (8), it is characterised in that: described carbon dioxide tank (1) and compressor (2)
Being connected by pipeline, described compressor (2) is connected with extraction kettle (3), described extraction kettle (3) with point
Connecting from device (4), described separator (4) is connected with depurator (5), described drying unit (6)
Being connected with separator (4), described blower fan (8) is connected with air heater (7), and described air heats
Device (7) is connected with drying unit (6), described depurator (5), compressor (2) and carbon dioxide tank
(1) it is sequentially connected with by circulating line.
A kind of astaxanthin supercritical extraction unit the most according to claim 1, it is characterised in that: institute
State separator (4) and be set to three grades.
A kind of astaxanthin supercritical extraction unit the most according to claim 1, it is characterised in that: institute
The inside stating depurator (5) is sequentially provided with drainage screen (14), adsorption layer (15) and water suction from top to bottom
Layer (16), the inside of described adsorption layer (15) is filled with activated carbon granule, described water accepting layer (16)
Inside is filled with water-absorbing resin.
A kind of astaxanthin supercritical extraction unit the most according to claim 1, it is characterised in that: institute
The both sides stating drying unit (6) are respectively arranged with discharge pipe (12), the surface of described discharge pipe (12)
It is evenly distributed with pore (13).
A kind of astaxanthin supercritical extraction unit the most according to claim 1, it is characterised in that: institute
The inside stating extraction kettle (3) is provided with extraction equipment (9), and the inside of described extraction equipment (9) is provided with 3-5
Layer column plate (11), described column plate (11) is provided with filter (10).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620031382.9U CN205461115U (en) | 2016-01-13 | 2016-01-13 | Astaxanthin supercritical fluid extraction device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620031382.9U CN205461115U (en) | 2016-01-13 | 2016-01-13 | Astaxanthin supercritical fluid extraction device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205461115U true CN205461115U (en) | 2016-08-17 |
Family
ID=56668571
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620031382.9U Expired - Fee Related CN205461115U (en) | 2016-01-13 | 2016-01-13 | Astaxanthin supercritical fluid extraction device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205461115U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110357799A (en) * | 2019-07-29 | 2019-10-22 | 云南钰腾生物科技有限公司 | A kind of extraction element and extraction process of astaxanthin |
-
2016
- 2016-01-13 CN CN201620031382.9U patent/CN205461115U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110357799A (en) * | 2019-07-29 | 2019-10-22 | 云南钰腾生物科技有限公司 | A kind of extraction element and extraction process of astaxanthin |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| 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: 20160817 Termination date: 20180113 |