CN204840349U - Flavone extraction system - Google Patents
Flavone extraction system Download PDFInfo
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- CN204840349U CN204840349U CN201520486718.6U CN201520486718U CN204840349U CN 204840349 U CN204840349 U CN 204840349U CN 201520486718 U CN201520486718 U CN 201520486718U CN 204840349 U CN204840349 U CN 204840349U
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- extracting
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- heater
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Abstract
The utility model discloses a flavone extraction system, including pretreatment systems, hybrid system, filtration system, extraction system and concentrated drying system, wherein, pretreatment systems is connecting the hybrid system, and filtration system is being connected to the hybrid system, and filtration system is connecting extraction system, and extraction system is connecting concentrated drying system, filtration system includes ceramic membrane filter equipment and the formula of book membrane filter equipment, ceramic membrane filter equipment connects the formula of book membrane filter equipment. The utility model discloses a can effectually keep the activity of natural component, the ratio defective product is high, the efficiency of improving production greatly.
Description
Technical field
This utility model relates to a kind of extraction system, and specifically a kind of extracting flavonoids system, belongs to Extracting Technique of Flavonoids field.
Background technology
Flavonoid substances in Folium Ginkgo is one of principle active component, ginkgetin has the effect of free radical in strong scavenger cell, the oxidative metabolism of cell can be reduced, have obvious and unique curative effect to brain and artery of extremity blood flow a series of cardiovascular and cerebrovascular diseases caused of lacking of proper care.Flavonoid substances content in Folium Ginkgo accounts for 0.8% ~ 3.5% of cured leaf.The problem that mixing arrangement existence is feeded and discharging is loaded down with trivial details and consuming time in conventional extraction system, has a strong impact on the activity of active component; Utilize traditional filtration and separation techniques, filter medium precision is low, and filtrate quality is unstable, and can bring more impurity into, final product rate is low.
Summary of the invention
For above-mentioned prior art Problems existing, this utility model provides a kind of extracting flavonoids system, and effectively can keep the activity of natural constituents, ratio defective product is high, greatly improves the efficiency of production.
To achieve these goals, a kind of extracting flavonoids system that this utility model adopts, comprise pretreatment system, hybrid system, filtration system, extracting system and concentrate drying system, wherein, pretreatment system is connected to hybrid system, hybrid system is connected to filtration system, and filtration system is connected to extracting system, and extracting system is connected to concentrate drying system; Described filtration system comprises ceramic membrane filter device and roll membrane filtering device, and described ceramic membrane filter device connects roll membrane filtering device.
Described hybrid system comprises agitating device, heater and feeding device.
Described agitating device, by puddler, is positioned at the stirring vane of puddler lower end and the servomotor composition for driving puddler to rotate.
Described heater is high-temperature vapour heater.
Described feeding device comprises for reinforced mechanical hand, controls the encoder of manipulator behavior and the servomotor for driving device hands.
Compared with prior art, the beneficial effects of the utility model are: the agitating device in hybrid system, temperature control equipment and feeding device all achieve intellectualized operation, and operation rapidly, fully maintains the activity of effective ingredient; Use ceramic membrane filter system and wound membrane filtration system to substantially increase the extraction ratio of product in filtration system simultaneously.
Accompanying drawing explanation
Fig. 1 is schematic diagram of the present utility model.
Wherein: 1, pretreatment system, 2, hybrid system, 3, filtration system, 4, extracting system, 5, concentrate drying system, 6, ceramic membrane filter device, 7, roll membrane filtering device; 8, agitating device, 9, heater, 10, feeding device.
Detailed description of the invention
Below in conjunction with accompanying drawing, the utility model is described in further detail.
As shown in Figure 1, a kind of extracting flavonoids system, comprise pretreatment system 1, hybrid system 2, filtration system 3, extracting system 4 and concentrate drying system 5, wherein, pretreatment system 1 is connected to hybrid system 2, hybrid system 2 is connected to filtration system 3, and filtration system 3 is connected to extracting system 4, and extracting system 4 is connected to concentrate drying system 5; Filtration system 3 comprises ceramic membrane filter device 6 and roll membrane filtering device 7, and ceramic membrane filter device 6 connects roll membrane filtering device 7.First use ceramic membrane filter device 6 filtering and impurity removing, roll membrane filtering device 7 is for further filtering and impurity removing, and it is extremely low that this defecator has energy consumption, saves the cost filtered, concentration process, without chemical reaction, does not introduce other impurity and the advantage such as the decomposition degeneration causing product.Hybrid system 2 comprises agitating device 8, heater 9 and feeding device 10.Agitating device 8, by puddler, is positioned at the stirring vane of puddler lower end and the servomotor composition for driving puddler to rotate.Described heater 9 is high-temperature vapour heater, utilizes the material of steam to reaction to heat.Feeding device 10 comprises for reinforced mechanical hand, controls the encoder of manipulator behavior and the servomotor for driving device hands.Utilize encoder to set the operating process of mechanical hand, realize the reinforced of automatization, can manpower be saved, reduce production cost.
Above embodiment is only to explanation of the present utility model, and it is not to restriction of the present utility model.When concrete operations, for a person skilled in the art, it still can be modified to technical scheme described in previous embodiment, or carries out equivalent replacement.All in spirit of the present utility model and principle, any amendment done, equivalent replacement, improvement etc., all should be included within protection domain of the present utility model.
Claims (5)
1. an extracting flavonoids system, it is characterized in that, described extraction system comprises pretreatment system (1), hybrid system (2), filtration system (3), extracting system (4) and concentrate drying system (5), wherein, pretreatment system (1) is connected to hybrid system (2), hybrid system (2) is connected to filtration system (3), and filtration system (3) is connected to extracting system (4), and extracting system (4) is connected to concentrate drying system (5); Described filtration system (3) comprises ceramic membrane filter device (6) and roll membrane filtering device (7), and described ceramic membrane filter device (6) connects roll membrane filtering device (7).
2. a kind of extracting flavonoids system according to claim 1, is characterized in that, described hybrid system (2) comprises agitating device (8), heater (9) and feeding device (10).
3. a kind of extracting flavonoids system according to claim 2, is characterized in that, described agitating device (8), by puddler, is positioned at the stirring vane of puddler lower end and the servomotor composition for driving puddler to rotate.
4. a kind of extracting flavonoids system according to claim 2, is characterized in that, described heater (9) is high-temperature vapour heater.
5. a kind of extracting flavonoids system according to claim 2, is characterized in that, described feeding device (10) comprises for reinforced mechanical hand, controls the encoder of manipulator behavior and the servomotor for driving device hands.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520486718.6U CN204840349U (en) | 2015-07-07 | 2015-07-07 | Flavone extraction system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520486718.6U CN204840349U (en) | 2015-07-07 | 2015-07-07 | Flavone extraction system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204840349U true CN204840349U (en) | 2015-12-09 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520486718.6U Expired - Fee Related CN204840349U (en) | 2015-07-07 | 2015-07-07 | Flavone extraction system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204840349U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108578446A (en) * | 2018-04-26 | 2018-09-28 | 太阳树（厦门）生物工程有限公司 | A kind of production method of low lead nettle extract |
-
2015
- 2015-07-07 CN CN201520486718.6U patent/CN204840349U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108578446A (en) * | 2018-04-26 | 2018-09-28 | 太阳树（厦门）生物工程有限公司 | A kind of production method of low lead nettle extract |
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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 |
Granted publication date: 20151209 Termination date: 20190707 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |