CN205199037U - Enrichment facility is drawed in circulation - Google Patents
Enrichment facility is drawed in circulation Download PDFInfo
- Publication number
- CN205199037U CN205199037U CN201521058255.XU CN201521058255U CN205199037U CN 205199037 U CN205199037 U CN 205199037U CN 201521058255 U CN201521058255 U CN 201521058255U CN 205199037 U CN205199037 U CN 205199037U
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- jar
- extractor
- concentrated
- concentration tank
- extraction
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Abstract
The utility model relates to a ring extracts the enrichment facility, the device including extract jar with concentrated jar, extract and jar set up concentrated jar top, pipe connection is passed through with concentrated jar top in the bottom of extracting jar, and is equipped with control valve I on the pipe, steam pipe connection is passed through at concentrated jar top and the top of extracting jar, steam pipe manage with a level of extracting the one end that the jar is connected or vertical pipe on be equipped with condensation circulation mechanism, being equipped with the charge door on drawing the jar, drawing and be equipped with the filter layer in the jar, drawing of filter layer upper portion is equipped with the stirring heating rod in the jar, be equipped with the heating rod in concentrated jar, concentrated tank bottoms portion is equipped with the drain pipe, is equipped with control valve II on the drain pipe, the utility model discloses an extract the combination of jar, concentrated jar and condensation circulation mechanism, realized that cyclic utilization extracts solvent continuous extraction operation, can effectively improve the extraction percentage of natural coloring mattes for the traditional extraction device.
Description
Technical field
The utility model relates to extractive technique field, specifically a kind of circulation extracting concentrating device.
Background technology
The extraction of effective components in plants adopts extractor to carry out usually.Be generally material to be extracted is mixed with extractant be placed in an extractor, after having extracted, carry out the steps such as Purification by filtration again.In practical operation, in order to improve recovery rate, usually material to be extracted is repeatedly obtained extract with extractant extraction, then by extract merging treatment.If use single extractor to complete repeatedly to extract, not only at substantial extractant, and production efficiency is low; If the device using multiple extractor to connect in turn repeatedly extracts simultaneously, although the production efficiency of improve, the cost of device can be rolled up, simultaneously still can the extractant of at substantial.
Water-soluble natural pigment is extensively present in the cell liquid of plant, thus makes plant present the colors such as redness, blueness or purple.Natural colouring matter has certain nutritive value and pharmacological action, can be applicable to food, cosmetics and field of medicaments, is the ideal material of alternative synthetic dyestuff.The process extracting natural colouring matter from plant generally comprises raw material fragmentation, solvent extraction, filtration, purifying and dry run, and wherein solvent extraction affects the topmost step of pigment recovery rate.Current Extraction solvent is generally the mixed solvent of second alcohol and water.Existing extraction element generally enters extractor by after raw material fragmentation from import, mix with the extractant added in extractor and extract, material through extracting processing escapes and enter the further refinement treatment of follow-up filter from outlet, the pigment recovery rate using current extraction element to obtain is lower, and will the Extraction solvent of at substantial by extract mixing after repeatedly extracting, cause waste.
Utility model content
The pigment recovery rate obtained for above-mentioned existing extraction element is lower, and will the Extraction solvent of at substantial by extract mixing after repeatedly extracting, and cause the problems such as waste, the utility model provides a kind of circulation extracting concentrating device.
For solving the problems of the technologies described above, the technical solution adopted in the utility model is:
A kind of circulation extracting concentrating device, this device comprises extractor and concentration tank, extractor is arranged on the top of concentration tank, tubes connection is passed through at the bottom of extractor and the top of concentration tank, and conduit is provided with control valve I, the top of concentration tank is connected by steam lead with the top of extractor, steam lead is provided with condensation cycle mechanism with the horizontal tube or VERTICAL TUBE extracting tank connected one end, described extractor is provided with charge door, filter course is provided with in extractor, agitating heating rod is provided with in the extractor on filter course top, heating rod is provided with in described concentration tank, drain pipe is provided with bottom concentration tank, drain pipe is provided with control valve II,
The liquid outlet of described extractor is provided with filter membrane;
Described condensation cycle organization establishes is in the VERTICAL TUBE of the steam lead with the tank connected one end of extraction;
Described condensation cycle mechanism is condenser pipe;
Described agitating heating rod is for having the stirring rod of heating function, and stirring rod is provided with multiple stirring piece be fixedly connected with stirring rod;
Described stirring piece is connected with stirring rod is vertical.
The beneficial effects of the utility model:
The circulation extracting concentrating device that the utility model provides, by the combination of extractor, concentration tank and condensation cycle mechanism, achieves and recycles Extraction solvent continuous extraction operation, effectively can improve the recovery rate of natural colouring matter relative to traditional extraction element; By the setting of heating arrangements and condensation cycle mechanism, the consumption of Extraction solvent in nature strength process can be reduced, reduce extraction cost; Owing to decreasing the consumption of Extraction solvent, the energy that the transhipment recovery etc. therefore reducing extract consumes, reduce further extraction cost; Final extract can also be concentrated, solvent directly can be stayed extractor Inner eycle and utilize, and simplifies technique, and decreases the consumption of Extraction solvent simultaneously;
The circulation extracting concentrating device that the utility model provides, arranges heating rabbling mechanism in extractor, can carry out agitating heating as required, be conducive to the extraction of natural colouring matter, greatly can improve extraction efficiency to extraction of substance; Filter membrane is set in the exit of extractor, secondary filter can be carried out to extract on the one hand, improve DNA purity, on the other hand, can effectively prevent outflow conduit from blocking.
Accompanying drawing explanation
Fig. 1 the utility model structural representation;
Reference numeral: 1, extractor, 2, agitating heating rod, 3, filter course, 4, control valve I, 5, concentration tank, 6, heating rod, 7, control valve II, 8, condensation cycle mechanism, 9, charge door, 10, filter membrane, 11, steam lead.
Detailed description of the invention
Below in conjunction with detailed description of the invention, the utility model is further elaborated.
As shown in the figure: a kind of circulation extracting concentrating device, this device comprises extractor 1 and concentration tank 5, extractor 1 is arranged on the top of concentration tank 5, tubes connection is passed through at the bottom of extractor 1 and the top of concentration tank 5, and conduit is provided with control valve I 4, the top of concentration tank 5 is connected by steam lead 11 with the top of extractor 1, steam lead 11 is provided with condenser pipe with the VERTICAL TUBE of one end that extractor 1 is connected, described extractor 1 is provided with charge door 9, filter course 3 is provided with in extractor 1, agitating heating rod 2 is provided with in the extractor 1 on filter course 3 top, heating rod 6 is provided with in described concentration tank 5, drain pipe is provided with bottom concentration tank 5, drain pipe is provided with control valve II 7, the liquid outlet of described extractor 1 is provided with filter membrane 10, described agitating heating rod 2 is for having the stirring rod of heating function, and stirring rod is provided with multiple stirring piece of being fixedly connected with vertical with stirring rod.
During use, first closed control valve I 4 and control valve II 7, mixture to be extracted is injected extractor 1 through charge door 9, open agitating heating rod 2, start to stir and extract, after having extracted first, open control valve I 4, extract flows in concentration tank 5 by conduit bottom extractor 1 after filtering layer 3 and filter membrane 10 filter, closed control valve I 4, opening heating rod 6 heats concentrated, add thermogenetic steam to be derived by steam lead 11, and flow back in extractor 1 after condensation cycle mechanism 8 condensation and carry out second extraction, circulation like this is repeatedly extracted, until extracted.
The utility model, by the combination of extractor 1, concentration tank 5 and condensation cycle mechanism 8, achieves and recycles Extraction solvent continuous extraction operation, effectively can improve the recovery rate of natural colouring matter relative to traditional extraction element; By the setting of heating arrangements and condensation cycle mechanism, the consumption of Extraction solvent in nature strength process can be reduced, reduce extraction cost; Owing to decreasing the consumption of Extraction solvent, the energy that the transhipment recovery etc. therefore reducing extract consumes, reduce further extraction cost; Final extract can also be concentrated, solvent directly can be stayed extractor Inner eycle and utilize, and simplifies technique, and decreases the consumption of Extraction solvent simultaneously;
The utility model arranges heating rabbling mechanism in extractor, can carry out agitating heating as required, be conducive to the extraction of natural colouring matter, greatly can improve extraction efficiency to extraction of substance; Filter membrane is set in the exit of extractor, secondary filter can be carried out to extract on the one hand, improve DNA purity, on the other hand, can effectively prevent outflow conduit from blocking.
Claims (6)
1. a circulation extracting concentrating device, it is characterized in that: this device comprises extractor (1) and concentration tank (5), extractor (1) is arranged on the top of concentration tank (5), tubes connection is passed through at the bottom of extractor (1) and the top of concentration tank (5), and conduit is provided with control valve I (4), the top of concentration tank (5) is connected by steam lead (11) with the top of extractor (1), the horizontal tube of one end that steam lead (11) is connected with extractor (1) or VERTICAL TUBE are provided with condensation cycle mechanism (8), described extractor (1) is provided with charge door (9), filter course (3) is provided with in extractor (1), agitating heating rod (2) is provided with in the extractor (1) on filter course (3) top, heating rod (6) is provided with in described concentration tank (5), concentration tank (5) bottom is provided with drain pipe, drain pipe is provided with control valve II (7).
2. circulation extracting concentrating device as claimed in claim 1, is characterized in that: the liquid outlet of described extractor (1) is provided with filter membrane (10).
3. circulation extracting concentrating device as claimed in claim 1, is characterized in that: described condensation cycle mechanism (8) is arranged in the VERTICAL TUBE of the steam lead (11) of the one end be connected with extractor (1).
4. circulation extracting concentrating device as claimed in claim 1, is characterized in that: described condensation cycle mechanism (8) is condenser pipe.
5. circulation extracting concentrating device as claimed in claim 1, is characterized in that: described agitating heating rod (2) is for having the stirring rod of heating function, and stirring rod is provided with multiple stirring piece be fixedly connected with stirring rod.
6. circulation extracting concentrating device as claimed in claim 5, is characterized in that: described stirring piece is connected with stirring rod is vertical.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201521058255.XU CN205199037U (en) | 2015-12-18 | 2015-12-18 | Enrichment facility is drawed in circulation |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201521058255.XU CN205199037U (en) | 2015-12-18 | 2015-12-18 | Enrichment facility is drawed in circulation |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205199037U true CN205199037U (en) | 2016-05-04 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201521058255.XU Expired - Fee Related CN205199037U (en) | 2015-12-18 | 2015-12-18 | Enrichment facility is drawed in circulation |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205199037U (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108771883A (en) * | 2018-06-12 | 2018-11-09 | 合肥丰洁生物科技有限公司 | A kind of traditional Chinese medicine extraction liquid film concentration and separation device |
| CN109045153A (en) * | 2018-11-02 | 2018-12-21 | 朗致集团万荣药业有限公司 | One plant medicinal material extracting solution and preparation method thereof |
| CN113559546A (en) * | 2021-07-15 | 2021-10-29 | 永州德普瑞生物科技股份有限公司 | Extraction, separation and purification system for effective components in polygonum cuspidatum and use method thereof |
| CN114733222A (en) * | 2022-04-19 | 2022-07-12 | 华一鸣 | Ceramic pigment water-soluble substance filter equipment |
-
2015
- 2015-12-18 CN CN201521058255.XU patent/CN205199037U/en not_active Expired - Fee Related
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108771883A (en) * | 2018-06-12 | 2018-11-09 | 合肥丰洁生物科技有限公司 | A kind of traditional Chinese medicine extraction liquid film concentration and separation device |
| CN109045153A (en) * | 2018-11-02 | 2018-12-21 | 朗致集团万荣药业有限公司 | One plant medicinal material extracting solution and preparation method thereof |
| CN113559546A (en) * | 2021-07-15 | 2021-10-29 | 永州德普瑞生物科技股份有限公司 | Extraction, separation and purification system for effective components in polygonum cuspidatum and use method thereof |
| CN113559546B (en) * | 2021-07-15 | 2022-10-18 | 永州德普瑞生物科技股份有限公司 | Extraction, separation and purification system for effective components in polygonum cuspidatum and using method thereof |
| CN114733222A (en) * | 2022-04-19 | 2022-07-12 | 华一鸣 | Ceramic pigment water-soluble substance filter equipment |
| CN114733222B (en) * | 2022-04-19 | 2024-06-28 | 华一鸣 | Ceramic pigment water-soluble substance filter equipment |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CB03 | Change of inventor or designer information |
Inventor after: Huang Yuepu Inventor after: Wang Jing Inventor after: Ping Ping Inventor after: Du Zongming Inventor after: Fan Renxiu Inventor before: Huang Yaopu Inventor before: Wang Jing Inventor before: Ping Ping Inventor before: Du Zongming Inventor before: Fan Renxiu |
|
| COR | Change of bibliographic data | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20160504 Termination date: 20161218 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |