CN2393612Y - Extractor - Google Patents
Extractor Download PDFInfo
- Publication number
- CN2393612Y CN2393612Y CN 99224988 CN99224988U CN2393612Y CN 2393612 Y CN2393612 Y CN 2393612Y CN 99224988 CN99224988 CN 99224988 CN 99224988 U CN99224988 U CN 99224988U CN 2393612 Y CN2393612 Y CN 2393612Y
- Authority
- CN
- China
- Prior art keywords
- generator
- extractor
- supercriticality
- storage tank
- utility
- 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
- Extraction Or Liquid Replacement (AREA)
Abstract
The utility model relates to an extraction device which belongs to an extraction device without a pump and comprises an extract liquor storage tank, pipelines, a supercritical state generator and an extractor. The utility model is characterized in that the supercritical state generator replaces a high pressure pump in the existing extraction device and is composed of a cylindrical generator shell and a heating water jacket sheathed on the cylindrical generator shell, and the supercritical state generator is respectively connected with the extract liquor storage tank and the extractor through the pipelines. Because the high pressure pump is omitted, the utility model largely reduces production cost and has convenient operation.
Description
The utility model belongs to a kind of no high-pressure pump extraction equipment.
At present domestic under lab has and can realize the above supercritical fluid extraction equipment of 15Mpa.And all having a cover high-pressure delivery to extract the high-pressure pump of fluid in the extraction equipment, general pressure requires about 7-35Mpa.Only about 15Mpa, and investment is big at the qualified products of industrial large-flow high-pressure pump, and fluctuation of service has so just seriously limited industrial supercritical fluid and extracted industrial expansion.
The purpose of this utility model is at the problems referred to above, and a kind of no pump supercritical fluid extraction equipment is provided.
The utility model promptly is made up of extract storage tank, pipeline, supercriticality generator and extractor.Pipeline one end is connected with the extract storage tank and communicates, and the other end is connected with extractor and communicates.The supercriticality generator is serially connected in the pipeline.The supercriticality generator is made of generator body and heater, generator body is made by thermal conductivity good metal material, and heater is a heating jacket, and heating jacket is sleeved on the supercriticality generator body, heating jacket can feed hot water and hot blast, and generator body is heated.After the extract in the extract storage tank enters in the supercriticality generator body through pipeline, in heating jacket, feed the circulating hot water of proper temperature, after reaching supercriticality, extract feeds in the extractor.The target substance that extracts is extracted.
Because the utility model replaces high-pressure pump with generator, not only equipment investment is few, and goes up detective, and is easy to use.
Fig. 1 is a structural representation of the present utility model, and the utility model is described in further detail below in conjunction with accompanying drawing.
Extraction equipment is made up of extract storage tank 1, woven hose 2, supercriticality generator, supercriticality liquid delivery tube 5 and extractor 6.The supercriticality generator is made of cylindrical generator body 3 and heating water jacket 4.Heating water jacket 4 is sleeved on the cylindrical generator body.One end of woven hose 2 is connected with extract storage tank 1, and the other end is connected with cylindrical generator body 3, and an end of supercriticality liquid delivery tube 5 is connected with cylindrical generator body 3, and the other end is connected with extractor.
During use, as liquid CO is housed in extract storage tank 1
2, the target substance that extract is housed in extractor 6.After extract enters supercriticality generator body 3 from storage tank 1,, make CO as long as in the heating water jacket, feed circulating hot water
2After entering supercriticality, and enter in the extractor 6, target substance is extracted get final product.
Claims (2)
1, extraction equipment, form by extract storage tank (1), woven hose (2), supercriticality liquid delivery tube (5), extractor (6) and supercriticality generator, it is characterized in that described supercriticality generator is made of generator body (3) and heating water jacket (4), heating water jacket (4) is sleeved on the generator body (3), generator body (3) is connected with the extract storage tank by woven hose (2), is connected with extractor (6) by supercriticality liquid delivery tube (5).
2, extraction equipment according to claim 1 is characterized in that described generator body (3) is for cylindrical.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 99224988 CN2393612Y (en) | 1999-09-03 | 1999-09-03 | Extractor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 99224988 CN2393612Y (en) | 1999-09-03 | 1999-09-03 | Extractor |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN2393612Y true CN2393612Y (en) | 2000-08-30 |
Family
ID=34014930
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 99224988 Expired - Fee Related CN2393612Y (en) | 1999-09-03 | 1999-09-03 | Extractor |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN2393612Y (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101848665B (en) * | 2007-11-27 | 2012-08-29 | 株式会社太平洋 | Extractor having pottery with a dark brown glaze and the method for extracting using thereof |
| US9132363B2 (en) | 2012-11-20 | 2015-09-15 | Apeks Llc | Extraction system |
| US9908062B2 (en) | 2012-11-20 | 2018-03-06 | Andrew Paul Joseph | Extraction apparatus and method |
-
1999
- 1999-09-03 CN CN 99224988 patent/CN2393612Y/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101848665B (en) * | 2007-11-27 | 2012-08-29 | 株式会社太平洋 | Extractor having pottery with a dark brown glaze and the method for extracting using thereof |
| US9132363B2 (en) | 2012-11-20 | 2015-09-15 | Apeks Llc | Extraction system |
| US9908062B2 (en) | 2012-11-20 | 2018-03-06 | Andrew Paul Joseph | Extraction apparatus and method |
| US9908063B2 (en) | 2012-11-20 | 2018-03-06 | Andrew Paul Joseph | Extraction apparatus |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN2393612Y (en) | Extractor | |
| EP1482255A1 (en) | supplemental water storage tank and service-water heating system including it | |
| CN100484876C (en) | Method and equipment for using condensed water of new steam stripped under high pressure | |
| JPS57159599A (en) | Evaporation-thickener for sewage sludge | |
| CN206119992U (en) | Integrated kitchen with jet -propelled steam ager of quick formula of intelligence | |
| CN207570206U (en) | A kind of drying kettle of alcohol supercritical methanol technology production aeroge | |
| CN208398048U (en) | A kind of energy-saving steam generating device | |
| CN203375422U (en) | High-pressure steam engine | |
| CN205549619U (en) | Pressure boost heat -preservation type spray drying tower | |
| CN204421580U (en) | A kind of food drying process reclaims hot water heat energy and hot water re-use device | |
| CN103322544A (en) | High-pressure steam engine | |
| CN203425554U (en) | Circulating ultrasonic extraction concentration machine set | |
| CN208785814U (en) | The extraction element of active ingredient of natural plant in a kind of cosmetics | |
| CN207562861U (en) | A kind of drying system of alcohol supercritical methanol technology production aeroge | |
| CN218485178U (en) | High-heat-efficiency desolventizing device for BDP | |
| CN1272607A (en) | Equipment for producing high-pressure saturated steam by means of continuous water atomization and heating process | |
| CN206746007U (en) | A kind of waste acid recovery system | |
| CN206459350U (en) | A kind of oily heating tank used in organic fertilizer production | |
| CN211119304U (en) | Exhaust device of boiler feed pump | |
| CN204943428U (en) | Vapour-recovery unit produced by efficient milk | |
| ES8400185A1 (en) | Heat exchanger for operating a boiler installation for superheated steam. | |
| CN208349311U (en) | A kind of carbon dioxide degradation product waste liquid recycling modernization system | |
| CN204421567U (en) | A kind of drying unit with heat recovery function | |
| CN201159449Y (en) | Steam generation device | |
| CN210973882U (en) | Sulfur melting kettle |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C19 | Lapse of patent right due to non-payment of the annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |