CN205061932U - Extraction element of blueberry anthocyanidin - Google Patents
Extraction element of blueberry anthocyanidin Download PDFInfo
- Publication number
- CN205061932U CN205061932U CN201520676557.7U CN201520676557U CN205061932U CN 205061932 U CN205061932 U CN 205061932U CN 201520676557 U CN201520676557 U CN 201520676557U CN 205061932 U CN205061932 U CN 205061932U
- Authority
- CN
- China
- Prior art keywords
- extractor
- pipeline
- extraction element
- vaccinium oxycoccus
- oxycoccus pigment
- 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
Landscapes
- Treatment Of Liquids With Adsorbents In General (AREA)
Abstract
The utility model provides an extraction element of blueberry anthocyanidin, including extraction system, concentrated system, purification system, wherein, extraction system is including drawing jar, ultrasonic transmitter, one -level filter screen, second grade filter screen, charge door, extract entry, spinning blade, motor, motor shaft, be equipped with ultrasonic transmitter on the lateral surface that draws jar, wherein, concentrated system is including concentrated bottle, vacuum pump, pipeline no. 1, water pump no. 1, the one end of pipeline no. 1 is connected to the bottom of drawing the jar, and the other end is connected to the top of concentrated bottle, wherein, the purification system includes that chromatographic column, eluate store up bottle, water pump no. 2, pipeline no. 2, it has diaion HP220 macroporous absorbent resin to fill in the chromatographic column. The utility model discloses technique and device integration has been carried out with the extraction process of blueberry anthocyanidin, the automation mechanized operation can be realized, it is efficient, easy and simple to handle.
Description
Technical field
The utility model belongs to extraction element field, particularly relates to the extraction element of vaccinium oxycoccus pigment.
Background technology
Vaccinium oxycoccus pigment is the derivative of flavones and flavanone, reddish brown to chocolate powder, bulk or liquid, slightly flavour.Be slightly soluble in water.By thermally labile.It can be applicable to aquatic products processing, livestock product processing, plant egg-products, bakery product etc. painted, be sorrel tinting material; For field of food, skin antioxidant.Its vision enhancing, anti-eye strain; Delay cranial nerve aging; Therapeutic action is had to the microangiopathy caused by diabetes; Strengthen cardio-pulmonary function; Prevention senile dementia.
The extraction of anthocyanidin is a large study hotspot of field of food at present.The extracting method of current employing mainly based on solution extraction, or adopts ultrasonic wave to carry out assisted extraction, to improve its extraction efficiency.At present, the technique that ultrasonic extraction method extracts anthocyanidin is: first the raw material containing anthocyanidin is ground, then with extraction agent, anthocyanidin skin is carried out lixiviate, carry out auxiliary extraction simultaneously with ultrasonic transmitter, to improve the extraction efficiency of anthocyanidin.Do not see the extraction element of vaccinium oxycoccus pigment in prior art, the anthocyanidin extraction element complex structure of other fruit, extraction efficiency is low, and product purity is too low, and cannot realize automatization.
Summary of the invention
The purpose of this utility model is the extraction element providing vaccinium oxycoccus pigment, adopts the means of automatization to complete the leaching process of anthocyanidin, relies on manual operation, inefficient defect to solve existing extracting method.
The utility model solves the problems of the technologies described above adopted scheme:
The extraction element of vaccinium oxycoccus pigment, the extraction element of described vaccinium oxycoccus pigment comprises extraction system, concentration systems, purification system;
Wherein, described extraction system comprises extractor, ultrasonic transmitter, one-level filter screen, secondary screen, charging opening, extracting solution entrance, rotating blade, motor, machine shaft; The outer side of described extractor is provided with ultrasonic transmitter, and the bottom of described extractor is provided with one-level filter screen and secondary screen, and described one-level filter screen is positioned at above secondary screen; The mesh of described one-level filter screen is large compared with the mesh of secondary screen; The bottom of described charging opening and extracting solution entrance is inserted in extractor; Described motor is fixed on the shell of the extraction element of vaccinium oxycoccus pigment, and be positioned at the below of extractor, described machine shaft to be inserted in extractor and to penetrate secondary screen and one-level filter screen, and the end of described machine shaft is equipped with rotating blade, and described rotating blade is positioned at first-level filtering side on the net;
Wherein, described concentration systems comprises concentrated bottle, vacuum pump, pipeline one, water pump one; One end of described pipeline one is connected to the bottom of extractor, and the other end is connected to the top of concentrated bottle, and described pipeline one is provided with water pump one;
Wherein, described purification system comprises chromatographic column, elutriant storage bottle, water pump two, pipeline two; DiaionHP220 macroporous adsorbent resin is filled with in described chromatographic column; The height of described elutriant storage bottle is higher than the exit end of pipeline two, and the bottom of described elutriant storage bottle is provided with circulating tube and connects elutriant storage bottle and pipeline two; One end of described pipeline two is connected to the bottom of valve one, and the other end is switched to the top of chromatographic column, described pipeline two is provided with water pump two and valve one; Described valve one is installed on the initiating terminal of pipeline two.
Preferably, for comprising upper, middle and lower three part hollow cylinder structure in described extractor, the bottom of extractor is ramp structure.
Preferably, the outside middle portion of the hollow circular cylinder of described extractor is provided with ultrasonic transmitter.
Preferably, described one-level filter screen and secondary screen are arranged at the bottom of described extractor hollow circular cylinder.
Preferably, described concentrated bottle is the rectangular shape of hollow, and volume is greater than the volume of described extractor.
Preferably, the exit end of described pipeline two is positioned at directly over chromatographic column.
Preferably, described charging opening and extracting solution entrance are arranged at the top of extractor.
Preferably, described rotating blade is positioned at one-level filter screen vertical direction at least 2 centimeters.
Preferably, described wash-out bottle is provided with elutriant entrance.
Preferably, the circulating tube bottom described elutriant storage bottle is also provided with valve two.
Principle of work of the present utility model is: Blueberry fully contacts with extracting solution after being rubbed by rotating blade, under hyperacoustic effect, anthocyanidin is extracted in extracting solution, extracting solution is pumped to chromatographic column after concentrated, macroporous adsorbent resin specific adsorption anthocyanidin, impurity is flowed out with extracting solution, and anthocyanidin is attracted in chromatographic column, anthocyanidin can elute from chromatographic column by elutriant, thus realizes the extraction and purification of anthocyanidin.
The beneficial effects of the utility model:
(1) extraction process of vaccinium oxycoccus pigment has been carried out technology and device integrated, can realize automated operation, efficiency is high, easy and simple to handle;
(2) Minton dryer has been gathered, can the thick product of direct production vaccinium oxycoccus pigment, be directly anthocyanidin powder by the raw material production containing anthocyanidin, complete machine structure is simple, designs ingenious, is suitable for industrialization manufacture and production.
Accompanying drawing explanation
Fig. 1 is the structural representation of the extraction element of the utility model vaccinium oxycoccus pigment.In figure,
1 extraction system; 101 extractors; 102 ultrasonic transmitters; 103 one-level filter screens; 104 secondary screen; 105 charging openings; 106 extracting solution entrances; 107 electric poles; 108 machine shafts; 109 rotating blades; 2 concentration systems; 201 concentrated bottles; 202 vacuum pumps; 203 pipelines one; 204 water pumps one; 3 purification systems; 301 chromatographic columns; 302 elutriant storage bottles; 303 water pumps two; 304 pipelines two; 305 valves one; 306 valves two; 307 elutriant entrances.
Embodiment
Below in conjunction with the utility model most preferred embodiment, the technical solution of the utility model is further described.
Please refer to Fig. 1, the extraction element of vaccinium oxycoccus pigment, comprising: extraction system 1, concentration systems 2, purification system 3.
Wherein, described extraction system 1, for extracting the anthocyanidin in blueberry, comprising:
For the extractor 101 of splendid attire extracting solution;
For to launching hyperacoustic ultrasonic transmitter 102 in extractor;
For the one-level filter screen 103 of filtering pomace;
For the secondary screen 104 of further filtering pomace;
For blueberry being imported the charging opening 105 in extractor 101;
For extracting solution being imported the extracting solution entrance 106 in extractor 101;
For pulverizing the rotating blade 109 of Blueberry;
Motor 107 and the machine shaft 108 of cutting action is done for driven rotary blade 109.
Wherein, described extractor 101 is the hollow circuit cylinder body structure comprising upper, middle and lower three part, the bottom of extractor 101 is ramp structure, the outside middle portion of the hollow circular cylinder of described extractor 101 is provided with ultrasonic transmitter 102, the bottom of described extractor 101 hollow circular cylinder is provided with one-level filter screen 103 and secondary screen 104, and described one-level filter screen 103 is positioned at above secondary screen 104.
Wherein, described one-level filter screen 103 and secondary screen 104 are reticulated structure, and the mesh of one-level filter screen 103 is large compared with the mesh of secondary screen 104.
Wherein, described charging opening 105 and extracting solution entrance 106 are arranged at the top of extractor 101, and charging opening 105 is inserted in extractor 101 with the bottom of extracting solution entrance 106.
Wherein, described motor 107 is fixed on the shell of the extraction element of vaccinium oxycoccus pigment, and be positioned at the below of extractor 101, described machine shaft 108 to be inserted in extractor 101 and to penetrate in secondary screen 104 and one-level filter screen 103, the end of described machine shaft 108 is equipped with rotating blade 109, and described rotating blade 109 is positioned at one-level filter screen 103 vertical direction at least 2 centimeters.
Wherein, described concentration systems 2, for the anthocyanidin in concentrated blueberry, comprising:
For the concentrated bottle 201 of splendid attire concentrated solution;
For the vacuum pump 202 that concentrated bottle is carried out vacuumizing;
For connecting the pipeline 1 of extraction system and concentration systems;
For the extracting solution in extraction system being pumped into the water pump 1 of concentrated bottle.
Wherein, described concentrated bottle 201 is the rectangular shape of hollow, and volume is greater than the volume of described extractor 101, and described concentrated bottle 201 side is provided with vacuum pump 202.
Wherein, one end of described pipeline 1 is connected to the bottom of extractor 101, and the other end is connected to the top of concentrated bottle 201, and the afterbody of described pipeline 1 is just inserted in described concentrated bottle 201, and described pipeline 1 is provided with water pump 1.
Wherein, described separation system 3, for the anthocyanidin in purification & isolation blueberry, comprising:
For separating of the chromatographic column 301 of anthocyanidin and other impurity;
For the elutriant storage bottle 302 of splendid attire elutriant;
For concentrated solution being extracted from concentrated bottle 201 and being pumped into the water pump 2 303 of chromatographic column;
For being communicated with the pipeline 2 304 of concentration systems 2 and separation system 3;
For controlling the valve 1 of concentrated solution flow velocity;
For controlling the valve 2 306 of eluent flow rate;
For elutriant being poured into the elutriant entrance 307 in elutriant storage bottle 302.
Wherein, described chromatographic column 301 li is filled with DiaionHP220 macroporous adsorbent resin, and the exit end of described pipeline 2 304 is positioned at directly over chromatographic column 301.
Wherein, the height of described elutriant storage bottle 302 is higher than the exit end of pipeline 2 304, and the bottom of described elutriant storage bottle 302 is provided with circulating tube and connects elutriant storage bottle 302 and pipeline 2 304, and described connection is provided with valve 2 306.
Wherein, one end of described pipeline 2 304 is connected to the bottom of valve 1, and the other end is switched to the top of chromatographic column 301, described pipeline 2 304 is provided with water pump 2 303 and valve 1.
Wherein, described valve 1 is installed on the initiating terminal of pipeline 2 304.
The principle of work of described vaccinium oxycoccus pigment extraction element is as follows:
Blueberry fully contacts with extracting solution after being rubbed by rotating blade 109, under hyperacoustic effect, anthocyanidin is extracted in extracting solution, extracting solution is pumped to chromatographic column 301 after concentrated, macroporous adsorbent resin specific adsorption anthocyanidin, impurity is flowed out with extracting solution, and anthocyanidin is attracted in chromatographic column 301, anthocyanidin can elute from chromatographic column 301 by elutriant, thus realizes the extraction and purification of anthocyanidin.
The beneficial effects of the utility model: the extraction process of vaccinium oxycoccus pigment has been carried out technology and device integrated, can realize automated operation, efficiency is high, easy and simple to handle; Gather Minton dryer, can the thick product of direct production vaccinium oxycoccus pigment, be directly anthocyanidin powder by the raw material production containing anthocyanidin, complete machine structure is simple, designs ingenious, is suitable for industrialization manufacture and production.
Claims (10)
1. the extraction element of vaccinium oxycoccus pigment, is characterized in that, the extraction element of described vaccinium oxycoccus pigment comprises extraction system, concentration systems, purification system; Wherein, described extraction system comprises extractor, ultrasonic transmitter, one-level filter screen, secondary screen, charging opening, extracting solution entrance, rotating blade, motor, machine shaft; The outer side of described extractor is provided with ultrasonic transmitter, and the bottom of described extractor is provided with one-level filter screen and secondary screen, and described one-level filter screen is positioned at above secondary screen; The mesh of described one-level filter screen is large compared with the mesh of secondary screen; The bottom of described charging opening and extracting solution entrance is inserted in extractor; Described motor is fixed on the shell of the extraction element of vaccinium oxycoccus pigment, and be positioned at the below of extractor, described machine shaft to be inserted in extractor and to penetrate secondary screen and one-level filter screen, and the end of described machine shaft is equipped with rotating blade, and described rotating blade is positioned at first-level filtering side on the net;
Wherein, described concentration systems comprises concentrated bottle, vacuum pump, pipeline one, water pump one; One end of described pipeline one is connected to the bottom of extractor, and the other end is connected to the top of concentrated bottle, and described pipeline one is provided with water pump one;
Wherein, described purification system comprises chromatographic column, elutriant storage bottle, water pump two, pipeline two; DiaionHP220 macroporous adsorbent resin is filled with in described chromatographic column; The height of described elutriant storage bottle is higher than the exit end of pipeline two, and the bottom of described elutriant storage bottle is provided with circulating tube and connects elutriant storage bottle and pipeline two; One end of described pipeline two is connected to the bottom of valve one, and the other end is switched to the top of chromatographic column, described pipeline two is provided with water pump two and valve one; Described valve one is installed on the initiating terminal of pipeline two.
2. the extraction element of vaccinium oxycoccus pigment as claimed in claim 1, it is characterized in that, described extractor is the hollow circuit cylinder body structure comprising upper, middle and lower three part, and the bottom of extractor is ramp structure.
3. the extraction element of vaccinium oxycoccus pigment as claimed in claim 2, it is characterized in that, the outside middle portion of the hollow circular cylinder of described extractor is provided with ultrasonic transmitter.
4. the extraction element of vaccinium oxycoccus pigment as claimed in claim 2, it is characterized in that, described one-level filter screen and secondary screen are arranged at the bottom of described extractor hollow circular cylinder.
5. the extraction element of vaccinium oxycoccus pigment as claimed in claim 1, it is characterized in that, described concentrated bottle is the rectangular shape of hollow, and volume is greater than the volume of described extractor.
6. the extraction element of vaccinium oxycoccus pigment as claimed in claim 1, it is characterized in that, the exit end of described pipeline two is positioned at directly over chromatographic column.
7. the extraction element of vaccinium oxycoccus pigment as claimed in claim 1, it is characterized in that, described charging opening and extracting solution entrance are arranged at the top of extractor.
8. the extraction element of vaccinium oxycoccus pigment as claimed in claim 1, it is characterized in that, described rotating blade is positioned at one-level filter screen vertical direction at least 2 centimeters.
9. the extraction element of vaccinium oxycoccus pigment as claimed in claim 1, it is characterized in that, described wash-out bottle is provided with elutriant entrance.
10. the extraction element of vaccinium oxycoccus pigment as claimed in claim 1, is characterized in that, the circulating tube bottom described elutriant storage bottle is also provided with valve two.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520676557.7U CN205061932U (en) | 2015-09-03 | 2015-09-03 | Extraction element of blueberry anthocyanidin |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520676557.7U CN205061932U (en) | 2015-09-03 | 2015-09-03 | Extraction element of blueberry anthocyanidin |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205061932U true CN205061932U (en) | 2016-03-02 |
Family
ID=55388512
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520676557.7U Expired - Fee Related CN205061932U (en) | 2015-09-03 | 2015-09-03 | Extraction element of blueberry anthocyanidin |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205061932U (en) |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106947289A (en) * | 2017-04-10 | 2017-07-14 | 广东职业技术学院 | A kind of vegetable colour extraction machine people |
| CN108467814A (en) * | 2018-06-27 | 2018-08-31 | 贵州贵果王实业有限公司 | A kind of pomace of blueberry fruit wine preparation and wine separator |
| CN109400570A (en) * | 2018-12-25 | 2019-03-01 | 江苏哈工药机科技股份有限公司 | A kind of extraction system of anthocyanidin |
| CN111362992A (en) * | 2018-12-25 | 2020-07-03 | 江苏哈工药机科技股份有限公司 | Continuous extraction method of blueberry anthocyanin |
| CN112057893A (en) * | 2020-08-28 | 2020-12-11 | 哈尔滨工大中奥生物工程有限公司 | Purification device and purification method for preparing wild blueberry anthocyanin freeze-dried powder |
| CN113908940A (en) * | 2021-12-14 | 2022-01-11 | 北京熊猫健康管理有限公司 | Industrial production device and method for lycium ruthenicum anthocyanin freeze-dried powder |
-
2015
- 2015-09-03 CN CN201520676557.7U patent/CN205061932U/en not_active Expired - Fee Related
Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106947289A (en) * | 2017-04-10 | 2017-07-14 | 广东职业技术学院 | A kind of vegetable colour extraction machine people |
| CN106947289B (en) * | 2017-04-10 | 2019-11-08 | 广东职业技术学院 | A kind of vegetable colour extraction machine people |
| CN108467814A (en) * | 2018-06-27 | 2018-08-31 | 贵州贵果王实业有限公司 | A kind of pomace of blueberry fruit wine preparation and wine separator |
| CN109400570A (en) * | 2018-12-25 | 2019-03-01 | 江苏哈工药机科技股份有限公司 | A kind of extraction system of anthocyanidin |
| CN111362992A (en) * | 2018-12-25 | 2020-07-03 | 江苏哈工药机科技股份有限公司 | Continuous extraction method of blueberry anthocyanin |
| CN111362992B (en) * | 2018-12-25 | 2023-02-21 | 江苏哈工药机科技股份有限公司 | Continuous extraction method of blueberry anthocyanin |
| CN109400570B (en) * | 2018-12-25 | 2023-12-22 | 江苏哈工药机科技股份有限公司 | Anthocyanin extraction system |
| CN112057893A (en) * | 2020-08-28 | 2020-12-11 | 哈尔滨工大中奥生物工程有限公司 | Purification device and purification method for preparing wild blueberry anthocyanin freeze-dried powder |
| CN112057893B (en) * | 2020-08-28 | 2021-05-04 | 哈尔滨工大中奥生物工程有限公司 | Purification device and purification method for preparing wild blueberry anthocyanin freeze-dried powder |
| CN113908940A (en) * | 2021-12-14 | 2022-01-11 | 北京熊猫健康管理有限公司 | Industrial production device and method for lycium ruthenicum anthocyanin freeze-dried powder |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN205061932U (en) | Extraction element of blueberry anthocyanidin | |
| US12109509B2 (en) | Ultrasonic composite acidic water extraction method for cordyceps polysaccharide and cordycepin in Cordyceps militaris | |
| CN102219866B (en) | Method for extracting and separating ganoderma lucidum polysaccharide from ganoderma lucidum sporocarp | |
| CN209714411U (en) | Filtering equipment is used in a kind of production of plant leaching liquor immersion | |
| CN203976669U (en) | A kind of device that extracts high-purity lycopene from tomato | |
| CN107117338A (en) | A kind of fig juice quantitative filling device | |
| CN112244296A (en) | Preparation method and equipment of acerola cherry extract | |
| CN103864886B (en) | A kind of soybean protein isolate extraction process of high extraction | |
| CN105125600A (en) | Method for efficiently extracting okra flavone | |
| CN204107090U (en) | A kind of extraction element | |
| CN204104742U (en) | A kind of novel sauce installation for fermenting | |
| CN102533446A (en) | New method for removing furocoumarins from citrus essential oil | |
| CN105503981A (en) | Method for extracting and separating anthocyanin from red cabbage | |
| CN205164188U (en) | Continuous extraction device is used to chinese -medicinal material | |
| CN204017434U (en) | A kind of Supercritical Fluid Extraction Enhanced by Ultrasonic device | |
| CN102580348A (en) | Active constituent extractor for natural substance | |
| CN205457982U (en) | Fresh fruit is squeezed juice extrusion formula and is drawed jar | |
| CN104045733B (en) | Method for extracting and separating tricholoma lobayense heim polysaccharide TLH-3 by taking tricholoma lobayense heim as raw material | |
| CN102657271A (en) | Automatic multi-stage countercurrent extraction method of tea infusion | |
| CN202762131U (en) | Multifunctional immature bitter orange Chinese traditional medicine extraction tank | |
| CN209108139U (en) | A kind of ultra micro extraction equipment | |
| CN111869769A (en) | Production process of high-yield high-ester catechin green tea extract | |
| CN203538270U (en) | Device for preparing tea concentrated solution by using fresh tea | |
| CN206391625U (en) | One Plant Extracts extraction equipment | |
| CN206828435U (en) | Sargassum protein extraction system |
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 |
Granted publication date: 20160302 Termination date: 20160903 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |