CN203065434U - Extraction device for extracting linolenic acid from perilla frutescens - Google Patents
Extraction device for extracting linolenic acid from perilla frutescens Download PDFInfo
- Publication number
- CN203065434U CN203065434U CN 201220740088 CN201220740088U CN203065434U CN 203065434 U CN203065434 U CN 203065434U CN 201220740088 CN201220740088 CN 201220740088 CN 201220740088 U CN201220740088 U CN 201220740088U CN 203065434 U CN203065434 U CN 203065434U
- Authority
- CN
- China
- Prior art keywords
- extraction
- mixing tank
- perilla frutescens
- purple perilla
- kettle
- 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
Images
Landscapes
- Extraction Or Liquid Replacement (AREA)
- Fats And Perfumes (AREA)
Abstract
The utility model discloses an extraction device for extracting linolenic acid from perilla frutescens. The extraction device comprises a mixing device, an extraction reactor, a separation chamber and a crystallization reactor which are sequentially connected in series, wherein the mixing device is arranged at a perilla frutescens raw material feed port; the mixing device is connected with a carbon dioxide high-pressure input device; a preheater is arranged between the mixing device and the extraction reactor; and the crystallization reactor comprises a spray crystallization reactor. The extraction device can extract linolenic acid from perilla frutescens and has high efficiency, so that the labor intensity of operators is reduced, and the extraction quality of the perilla frutescens is improved.
Description
Technical field
The utility model relates to a kind of purple perilla extractive technique field, is specifically related to a kind of for extracting linolenic extraction element from purple perilla.
Background technology
Purple perilla is to contain a large amount of greases in a kind of important Chinese medicinal materials, especially the purple perilla seed, and oil yield contains linolenic acid 62.73%, linolic acid 15.43%, oleic acid 12.01% up to 45% in the oil.Protein content accounts for 25% in the seed, includes 18 seed amino acids, wherein relies the content of peace acid, methionine(Met) all to be higher than the high-protein plant amaranth seed powder.Also have thiaminogen, vitamin-E, VITMAIN B1, sterol, phosphatide etc. in addition.
Because linolenic economic worth is than higher in the extract, and adopt traditional linolenic mode of artificial extraction, the labor intensity of operating staff height, efficient is low, and because human factor, extract quality and also can't guarantee, design therefore that a kind of to extract linolenic extraction element from purple perilla necessary.
The utility model content
It is a kind of for extracting linolenic extraction element from purple perilla that the technical problem that the utility model solves is to provide, thereby solve the problem in the above-mentioned background technology.
The technical problem that the utility model solves realizes by the following technical solutions:
A kind of for extracting linolenic extraction element from purple perilla, it is characterized in that, comprise mixing tank, extraction kettle, separate chamber and crystallization kettle, described mixing tank, extraction kettle, separate chamber and crystallization kettle are connected in regular turn, described mixing tank is provided with purple perilla raw material dog-house, and described mixing tank is connected with the CO 2 high pressure input unit, is provided with preheater between described mixing tank and the extraction kettle, and described crystallization kettle comprises the spray crystallization still.
The utility model is at first thrown in the purple perilla raw material to mixing tank from purple perilla raw material dog-house when work, imports carbonic acid gas with pressurization by the CO 2 high pressure input unit in mixing tank again; Material after the reaction is transferred to preheater and is heated; Again material being transferred to extraction kettle extracts; And the material after will extracting is in separate chamber's refrigerated separation, the system that exsomatizes of the carbon dioxide de in the material, and it is fragrant plain to stay purple perilla; Drip perfume base in the fragrant element of purple perilla in the separate chamber, evenly after; Feed the crystallization of crystallization kettle internal spraying again, obtain linolenic acid.
Owing to adopted above structure, the utlity model has following beneficial effect:
The utility model can extract linolenic acid from purple perilla, the efficient height has reduced people's labour intensity, and has improved linolenic extraction quality.
Description of drawings
Fig. 1 is the utility model structural representation;
Among the figure: 1. mixing tank, 2. extraction kettle, 3. separate chamber, 4. crystallization kettle, 5. purple perilla raw material dog-house, 6. CO 2 high pressure input unit, 7. preheater.
Embodiment
For technique means, creation characteristic that the utility model is realized, reach purpose and effect is easy to understand, below in conjunction with concrete diagram, further set forth the utility model.
Referring to Fig. 1, a kind of for extracting linolenic extraction element from purple perilla, it is characterized in that, comprise mixing tank 1, extraction kettle 2, separate chamber 3 and crystallization kettle 4, described mixing tank 1, extraction kettle 2, separate chamber 3 and crystallization kettle 4 are connected in regular turn, and described mixing tank 1 is provided with purple perilla raw material dog-house 5, and described mixing tank 1 is connected with CO 2 high pressure input unit 6, be provided with preheater 7 between described mixing tank 1 and the extraction kettle 2, described crystallization kettle 4 comprises the spray crystallization still.
The utility model is at first thrown in the purple perilla raw material to mixing tank 1 from purple perilla raw material dog-house 5 when work, imports carbonic acid gas with pressurization by CO 2 high pressure input unit 6 in mixing tank 1 again; Material after the reaction is transferred to preheater 7 and is heated; Material being transferred to extraction kettle 2 extracts again; And the material after will extracting in the separate chamber 3 refrigerated separation, the system that exsomatizes of the carbon dioxide de in the material, it is fragrant plain to stay purple perilla; Drip perfume base in the fragrant element of purple perilla in the separate chamber 3, evenly after; Feed crystallization kettle 4 internal spraying crystallizations again, obtain linolenic acid.
More than show and described ultimate principle of the present utility model and principal character and advantage of the present utility model.The technician of the industry should understand; the utility model is not restricted to the described embodiments; that describes in above-described embodiment and the specification sheets just illustrates principle of the present utility model; under the prerequisite that does not break away from the utility model spirit and scope; the utility model also has various changes and modifications, and these changes and improvements all fall in claimed the utility model scope.The claimed scope of the utility model is defined by appending claims and equivalent thereof.
Claims (1)
1. one kind is used for extracting linolenic extraction element from purple perilla, it is characterized in that: comprise mixing tank, extraction kettle, separate chamber and crystallization kettle, described mixing tank, extraction kettle, separate chamber and crystallization kettle are connected in regular turn, described mixing tank is provided with purple perilla raw material dog-house, and described mixing tank is connected with the CO 2 high pressure input unit, be provided with preheater between described mixing tank and the extraction kettle, described crystallization kettle comprises the spray crystallization still.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220740088 CN203065434U (en) | 2012-12-31 | 2012-12-31 | Extraction device for extracting linolenic acid from perilla frutescens |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220740088 CN203065434U (en) | 2012-12-31 | 2012-12-31 | Extraction device for extracting linolenic acid from perilla frutescens |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203065434U true CN203065434U (en) | 2013-07-17 |
Family
ID=48764248
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201220740088 Expired - Fee Related CN203065434U (en) | 2012-12-31 | 2012-12-31 | Extraction device for extracting linolenic acid from perilla frutescens |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203065434U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104046508A (en) * | 2014-06-17 | 2014-09-17 | 李传印 | Purification device and purification process for unsaturated fatty acids in peanuts |
-
2012
- 2012-12-31 CN CN 201220740088 patent/CN203065434U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104046508A (en) * | 2014-06-17 | 2014-09-17 | 李传印 | Purification device and purification process for unsaturated fatty acids in peanuts |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN203065434U (en) | Extraction device for extracting linolenic acid from perilla frutescens | |
| CN101259157B (en) | Chinese medicine kudzu root extract new drying technique method | |
| EP2275526A3 (en) | Device for generating biogas | |
| CN204717191U (en) | A kind of bio-pharmaceuticals pipeline connects clip soon | |
| CN203458833U (en) | Continuous extracting, concentrating and drying production line | |
| CN102757436B (en) | Method for preparing sodium copper chlorophyllin and alkaloids from mugwort leaf as raw material | |
| CN201668729U (en) | Herb decocting pot | |
| CN202377069U (en) | Traditional Chinese medicine blending machine | |
| CN205152181U (en) | A oil -water separator for producing rose hydrosol | |
| CN104782657A (en) | Plant destructive distillation liquid, its preparation and its application in improvement of content of effective components in hairy root of Salvia miltiorrhiza | |
| CN203498288U (en) | Process production line for separating and extracting natural plant effective ingredients from folium isatidis | |
| CN204736469U (en) | Medical ware of pounding medicine in a mortar of chinese herbal medicine | |
| CN207672021U (en) | A kind of essential oil extraction device | |
| CN204865074U (en) | Ultrasonic dispersion extraction element | |
| CN204582602U (en) | Circulation extraction concentration in oral liquid process process | |
| CN203043616U (en) | Percolation tank | |
| CN102603758A (en) | Extraction method of camptothecin and 9-hydroxymethyl camptothecin from tender leaves and twigs of Nothapodytes nimmoniana | |
| CN203043617U (en) | Percolation tank | |
| CN210278321U (en) | Traditional Chinese medicine volatile oil separation device with liquid medicine sprayer | |
| CN207137420U (en) | Flavones supercritical carbon dioxide extracting system | |
| CN103013790A (en) | White-chrysanthemum wine with function of reducing blood fat and brewing method thereof | |
| CN208151357U (en) | A kind of natural extract enrichment facility | |
| CN208641920U (en) | A kind of traditional Chinese medicine extraction slagging-off storage facilities | |
| CN207632758U (en) | A kind of walnut oil extraction system | |
| CN206414793U (en) | A kind of hot percolating extractor of Chinese patent drug |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20130717 Termination date: 20131231 |