CN201643760U - Vapour extractor - Google Patents
Vapour extractor Download PDFInfo
- Publication number
- CN201643760U CN201643760U CN2010201723043U CN201020172304U CN201643760U CN 201643760 U CN201643760 U CN 201643760U CN 2010201723043 U CN2010201723043 U CN 2010201723043U CN 201020172304 U CN201020172304 U CN 201020172304U CN 201643760 U CN201643760 U CN 201643760U
- Authority
- CN
- China
- Prior art keywords
- top cover
- cylindrical shell
- vapour
- cooling
- barrel body
- 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
- 239000007788 liquid Substances 0.000 claims abstract description 33
- 238000001816 cooling Methods 0.000 claims abstract description 28
- 239000000843 powder Substances 0.000 claims abstract description 24
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 23
- 238000000605 extraction Methods 0.000 claims abstract description 18
- 239000000498 cooling water Substances 0.000 claims abstract description 14
- 238000004821 distillation Methods 0.000 claims abstract description 10
- 239000011229 interlayer Substances 0.000 claims abstract description 10
- 239000010410 layer Substances 0.000 claims abstract description 6
- 230000007246 mechanism Effects 0.000 claims description 15
- 238000001914 filtration Methods 0.000 claims description 9
- 239000002826 coolant Substances 0.000 claims description 5
- 238000007599 discharging Methods 0.000 claims description 5
- 238000007790 scraping Methods 0.000 claims description 5
- 238000009833 condensation Methods 0.000 abstract description 2
- 230000005494 condensation Effects 0.000 abstract description 2
- 239000000284 extract Substances 0.000 description 13
- 239000003921 oil Substances 0.000 description 11
- 241000196324 Embryophyta Species 0.000 description 4
- 241000209094 Oryza Species 0.000 description 3
- 235000007164 Oryza sativa Nutrition 0.000 description 3
- 235000009566 rice Nutrition 0.000 description 3
- 239000007921 spray Substances 0.000 description 3
- 239000000341 volatile oil Substances 0.000 description 3
- NOOLISFMXDJSKH-UTLUCORTSA-N (+)-Neomenthol Chemical compound CC(C)[C@@H]1CC[C@@H](C)C[C@@H]1O NOOLISFMXDJSKH-UTLUCORTSA-N 0.000 description 2
- DTGKSKDOIYIVQL-WEDXCCLWSA-N (+)-borneol Chemical compound C1C[C@@]2(C)[C@@H](O)C[C@@H]1C2(C)C DTGKSKDOIYIVQL-WEDXCCLWSA-N 0.000 description 2
- REPVLJRCJUVQFA-UHFFFAOYSA-N (-)-isopinocampheol Natural products C1C(O)C(C)C2C(C)(C)C1C2 REPVLJRCJUVQFA-UHFFFAOYSA-N 0.000 description 2
- DSSYKIVIOFKYAU-XCBNKYQSSA-N (R)-camphor Chemical compound C1C[C@@]2(C)C(=O)C[C@@H]1C2(C)C DSSYKIVIOFKYAU-XCBNKYQSSA-N 0.000 description 2
- 241000723346 Cinnamomum camphora Species 0.000 description 2
- NOOLISFMXDJSKH-UHFFFAOYSA-N DL-menthol Natural products CC(C)C1CCC(C)CC1O NOOLISFMXDJSKH-UHFFFAOYSA-N 0.000 description 2
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- CKDOCTFBFTVPSN-UHFFFAOYSA-N borneol Natural products C1CC2(C)C(C)CC1C2(C)C CKDOCTFBFTVPSN-UHFFFAOYSA-N 0.000 description 2
- 229940116229 borneol Drugs 0.000 description 2
- 210000004556 brain Anatomy 0.000 description 2
- 229930008380 camphor Natural products 0.000 description 2
- 229960000846 camphor Drugs 0.000 description 2
- DTGKSKDOIYIVQL-UHFFFAOYSA-N dl-isoborneol Natural products C1CC2(C)C(O)CC1C2(C)C DTGKSKDOIYIVQL-UHFFFAOYSA-N 0.000 description 2
- 229940041616 menthol Drugs 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 229910052751 metal Inorganic materials 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 238000011084 recovery Methods 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 239000008247 solid mixture Substances 0.000 description 2
- 238000001256 steam distillation Methods 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000004927 clay Substances 0.000 description 1
- 239000000470 constituent Substances 0.000 description 1
- 235000019628 coolness Nutrition 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000011049 filling Methods 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000002023 wood Substances 0.000 description 1
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- Extraction Or Liquid Replacement (AREA)
Abstract
The utility model relates to a vapour extractor, which comprises a vapour extracting tank which comprises a barrel body, wherein a cooling top cover is arranged on the upper part of the barrel body, a bottom cover is arranged at the lower part of the barrel body, the barrel body is of a double-layer structure, a vapour inlet joint which is connected with the interlayer of the barrel body is arranged at the upper part of the barrel body, a water outlet joint which is connected with the interlayer of the barrel body is arranged at the lower part of the barrel body, a condensate collection trough is arranged at the upper part of the internal layer of the barrel body, and a vapour-liquid outlet which is matched with the condensate collection trough is arranged at one side of the barrel body, and is connected with a condenser through a condensation pipe; a frost wiping board is arranged on the internal surface of the cooling top cover and is driven by a frost wiping board driver which is arranged at the upper part of the cooling top cover, an annular cooling water sprayer is arranged on the external surface of the cooling top cover, and a top cover open and close device which is connected with the cooling top cover is arranged at the outside of the vapour extracting tank; and a distillation inlet is arranged on the bottom cover. The utility model has high extraction efficiency and simple structure, can automatically collect the frost powder of volatile matter by a frost wiper, and is convenient to use.
Description
Technical field
The utility model relates to a kind of vapour extractor, is specifically related to a kind of vapour extractor that the sublimable solid constituent of plant such as borneol, camphor, menthol extract that is used for.
Background technology
The sublimable solid composition of one class is arranged in the plant, as borneol, camphor, menthol, be referred to as in the Chinese pharmacology * * brain, it can be condensed into white powder during with steam distillation, is referred to herein as white powder.The big iron pan of usefulness among the people wood retort clay method is extracted, and is about to a cauldron and puts and claim the ground pot on the kitchen range, and wooden rice steamer is placed in water filling in the pot, and puts into extract in wooden rice steamer, puts a cauldron and claim a day pot on wooden rice steamer, and the white powder that is gone out by steam stripping is condensed in day pot pot face and is scraped and get.Though this method is simple and easy but extraction efficiency is low.The industry extraction of volatile oil is in a metal can in the existing plant, feed steam from the bottom and pass metal can, it makes the contained volatile oil of plant with the top importing condenser of steam by jar, the water that condensation obtains and the mixture of volatile matter enter oil water separator, obtain extractive of volatile oil through separation.But it is inapplicable to the extraction that contains the higher brain class thing of sublimable solid composition.
Summary of the invention
It is high and can collect the condense vapour extractor of the white powder that obtains of solid volatile matter automatically that technical problem to be solved in the utility model provides a kind of extraction efficiency.
For solving the technical problem that the utility model proposed, the technical scheme that is adopted is: a kind of vapour extractor, it is characterized in that: it comprises the steam extraction jar, the steam extraction jar comprises cylindrical shell, the top of cylindrical shell is provided with the cooling top cover, the bottom of cylindrical shell is provided with bottom, cylindrical shell is a double-decker, cylindrical shell top is provided with the Intaking joint that links to each other with the cylindrical shell interlayer, the cylindrical shell bottom is provided with the water out adapter that links to each other with the cylindrical shell interlayer, the top of cylindrical shell internal layer is provided with condensate liquid afflux groove, and a side of cylindrical shell is provided with the vapour-liquid outlet with condensate liquid afflux groove phase configuration, and the vapour-liquid outlet is connected with condenser by condenser pipe; The inner surface of cooling top cover is provided with scrapes white plate, scrapes white plate and is driven by the white sheet drive of scraping that is arranged on cooling top cover top, and the outer surface of cooling top cover is provided with ring-like cool water shower device, and steam extraction jar outside is provided with and cools off the top cover closing device that top cover is connected; Bottom is provided with the distillation vapor inlet.
Press such scheme, described cooling top cover is the dome-type top cover.
Press such scheme, described cooling top cover is provided with cooling water afflux groove outward, and a side of cooling water afflux groove is provided with coolant outlet, is used to collect cooling water.
Press such scheme, described cooling top cover horizontally rotate 90 °～180 ° under be provided with white powder gatherer, the discharging trap is equipped with in white powder gatherer bottom.
Press such scheme, described steam extraction jar outside is provided with the bottom closing device that is connected with bottom.Open bottom, draw off the residue that produces when extract extracts.
Press such scheme, the bottom centre of described bottom is provided with extracting liquid outlet, and it links to each other with the extracting liquid filtering device.Extract is the condensed water that is dissolved with extract, and the extract that obtains is thus made concentration after filtering by the extracting liquid filtering device.
Press such scheme, described top cover closing device is hydraulic pressure cap-opening mechanism or pneumatic cap-opening mechanism.
Press such scheme, described bottom closing device is hydraulic pressure cap-opening mechanism or pneumatic cap-opening mechanism.
Press such scheme, described condenser links to each other with oil water separator.The condensate liquid that enters condenser carries out water-oil separating by oil water separator again, obtains being mixed with the oil phase of a small amount of white powder, thereby improves the recovery rate of white powder.
Described bottom top is provided with orifice plate, and by this orifice plate even uperize in cylindrical shell, in addition, this orifice plate also is used to carry extract.
The beneficial effects of the utility model: (1) extraction efficiency height; (2) simple in structure, volatile matter frost powder can be collected automatically by scraping white device, and is easy to use; (3) the condensate liquid afflux groove on cylindrical shell internal layer top can prevent that condensate liquid from turning back to the white powder that liquid flows wash-out in the extractor, thereby improves the recovery rate of white powder.
Description of drawings
Fig. 1 is the device schematic diagram of vapour extractor.
1 scrapes white sheet drive; 2 annular cooling water spray throwers; 3 cooling top covers; 4 scrape white plate; 5 cooling water afflux grooves; 6 Intaking joints; 7 condensate liquid afflux grooves; The outlet of 8 vapour-liquids; 9 pneumatic cap-opening mechanisms; 10 bottoms; 11 extracting liquid outlets; 12 hydraulic pressure cap-opening mechanisms; 13 condenser pipes; 14 coolant outlets; 15 cylindrical shells; 16 water out adapters; 17 distillation vapor inlets; 18 extracting liquid filtering devices; 19 condensers; 20 oil water separators; 21 white powder gatherers; 22 discharging traps.
The specific embodiment
Below in conjunction with accompanying drawing 1, summary of the invention of the present utility model is further specified, but be not limited only to following examples.
A kind of vapour extractor, it comprises the steam extraction jar, the steam extraction jar comprises cylindrical shell 15, the top of cylindrical shell 15 is provided with cooling top cover 3, the bottom of cylindrical shell is provided with bottom 10, cylindrical shell is a double-decker, cylindrical shell top is provided with the Intaking joint 6 that links to each other with the cylindrical shell interlayer, the bottom of cylindrical shell is provided with the water out adapter 16 that links to each other with the cylindrical shell interlayer, the top of cylindrical shell internal layer is provided with condensate liquid afflux groove 7, one side of cylindrical shell is provided with and the vapour-liquid of condensate liquid afflux groove phase configuration outlet 8, and vapour-liquid outlet 8 is connected with condenser 19 by condenser pipe 13; The inner surface of cooling top cover 3 is provided with scrapes white plate 4, scraping white plate drives by being arranged on the white sheet drive 1 of scraping of cooling top cover top, the outer surface of cooling top cover 3 is provided with ring-like cool water shower device 2, and steam extraction jar outside is provided with and cools off the hydraulic pressure cap-opening mechanism 12 that top cover links to each other; Bottom 10 surfaces are provided with distillation vapor inlet 17.Described cooling top cover 3 is the dome-type top cover; Described cooling top cover is provided with cooling water afflux groove 5 outward, and a side of cooling water afflux groove is provided with coolant outlet 14; Described cooling top cover 3 horizontally rotate 90 °～180 ° under be provided with white powder gatherer 21, discharging trap 22 is equipped with in white powder gatherer 21 bottoms; Described steam extraction jar outside is provided with the air pressure cap-opening mechanism 9 that is connected with bottom; The bottom centre of described bottom is provided with extracting liquid outlet 11, and it links to each other with extracting liquid filtering device 18; Described condenser 19 links to each other with oil water separator 20.
When extracting operation, earlier bottom 10 is closed locking, with hydraulic pressure cap-opening mechanism 12 egg end 3 is risen back and turn-off then, extract when the cylindrical shell mouth is fed into apart from cylindrical shell actinal surface 100mm, is closed top cover 3, locking nut; In the cylindrical shell interlayer, feed heating steam through Intaking joint 6, open the distillation steam at distillation vapor inlet 17 places on the bottom simultaneously, make distillation steam in cylindrical shell, evenly spray distillation steam by orifice plate, when steam to be distilled rises to the top, open the cooling water valve outside the egg end 3, thereby make cooling water through 2 pairs of top cover spray coolings of ring-like cool water shower device, cooling water is through cooling water afflux groove 5, derive by coolant outlet 14, condensed water in the cylindrical shell interlayer is derived by water out adapter 16, volatilizable thing with the steam distillation condenses into white powder at the inner surface of dome-type top cover, contain the condensate liquid afflux groove 7 that is flowed into cylindrical shell top by the condensate liquid of wash-out frost powder, enter condenser 19 by condenser pipe 13, enter oil water separator 20 then and carry out water-oil separating through vapour-liquid outlet 8, isolate oil phase, obtain containing the absolute oil of a small amount of white powder; After finishing, distillation unclamps the clamp nut of top cover, after adopting hydraulic pressure cap-opening mechanism 12 that top cover is risen, it is horizontally rotated 90 °～180 ° tops to white powder gatherer 21, start and scrape white sheet drive 1, the frost powder is then scraped white plate 4 and is scraped, fall into white powder gatherer 21, collect white powder by discharging trap 22 filtering water.Extract (being dissolved with the condensed water of extract) is by the extracting liquid outlet 11 of bottom 10, and by doing concentration after 18 filtrations of extracting liquid filtering device, the residue that produces when extract extracts draws off after opening bottoms by pneumatic cap-opening mechanism 9.
Claims (9)
1. vapour extractor, it is characterized in that: it comprises the steam extraction jar, the steam extraction jar comprises cylindrical shell, the top of cylindrical shell is provided with the cooling top cover, the bottom of cylindrical shell is provided with bottom, cylindrical shell is a double-decker, cylindrical shell top is provided with the Intaking joint that links to each other with the cylindrical shell interlayer, the cylindrical shell bottom is provided with the water out adapter that links to each other with the cylindrical shell interlayer, the top of cylindrical shell internal layer is provided with condensate liquid afflux groove, one side of cylindrical shell is provided with the vapour-liquid outlet with condensate liquid afflux groove phase configuration, and the vapour-liquid outlet is connected with condenser by condenser pipe; The inner surface of cooling top cover is provided with scrapes white plate, scrapes white plate and is driven by the white sheet drive of scraping that is arranged on cooling top cover top, and the outer surface of cooling top cover is provided with ring-like cool water shower device, and steam extraction jar outside is provided with and cools off the top cover closing device that top cover is connected; Bottom is provided with the distillation vapor inlet.
2. vapour extractor according to claim 1 is characterized in that: described cooling top cover is the dome-type top cover.
3. vapour extractor according to claim 1 is characterized in that: described cooling top cover is provided with cooling water afflux groove outward, and a side of cooling water afflux groove is provided with coolant outlet.
4. vapour extractor according to claim 1 is characterized in that: described cooling top cover horizontally rotate 90 °～180 ° under be provided with white powder gatherer, the discharging trap is equipped with in white powder gatherer bottom.
5. vapour extractor according to claim 1 is characterized in that: described steam extraction jar outside is provided with the bottom closing device that is connected with bottom.
6. vapour extractor according to claim 1 is characterized in that: the bottom centre of described bottom is provided with extracting liquid outlet, and it links to each other with the extracting liquid filtering device.
7. vapour extractor according to claim 1 is characterized in that: described top cover closing device is hydraulic pressure cap-opening mechanism or pneumatic cap-opening mechanism.
8. vapour extractor according to claim 1 is characterized in that: described bottom closing device is hydraulic pressure cap-opening mechanism or pneumatic cap-opening mechanism.
9. vapour extractor according to claim 1 is characterized in that: described condenser links to each other with oil water separator.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010201723043U CN201643760U (en) | 2010-04-20 | 2010-04-20 | Vapour extractor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010201723043U CN201643760U (en) | 2010-04-20 | 2010-04-20 | Vapour extractor |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201643760U true CN201643760U (en) | 2010-11-24 |
Family
ID=43108954
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2010201723043U Expired - Fee Related CN201643760U (en) | 2010-04-20 | 2010-04-20 | Vapour extractor |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201643760U (en) |
Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104606909A (en) * | 2015-01-22 | 2015-05-13 | 李而宏 | Distillatory kettle for plant sesame oil |
| WO2015049585A3 (en) * | 2013-10-04 | 2015-11-19 | Natural Extraction Services, Llc | Method and apparatus for extracting botanical oils |
| CN107737462A (en) * | 2017-10-30 | 2018-02-27 | 新中天环保股份有限公司 | Organic solvent recycling and processing device |
| CN110035809A (en) * | 2016-11-10 | 2019-07-19 | 拉米罗·塞尼奥雷特·韦尔杜戈 | Equipment and internal distillation method for extracting volatile oils from organic raw materials by steam distillation |
| CN110986566A (en) * | 2019-11-25 | 2020-04-10 | 耒阳市刘燕酿制生物科技有限公司 | Recovery unit of biological pure water in freeze-dried food production |
| US10617974B2 (en) | 2016-05-02 | 2020-04-14 | Natural Extraction Systems, LLC | Method and apparatus for extracting botanical oils |
| US10974164B1 (en) | 2019-10-10 | 2021-04-13 | Boulder Creek Technologies, LLC | Continuous biomass extraction system and process |
| US11643402B2 (en) | 2018-08-10 | 2023-05-09 | Natural Extraction Systems, LLC | Gas phase methods to decarboxylate cannabinoids |
| US11702397B2 (en) | 2018-08-10 | 2023-07-18 | Natural Extraction Systems, LLC | Methods to purify cannabinoids |
| US12420214B2 (en) | 2018-08-10 | 2025-09-23 | Natural Extraction Systems, LLC | Methods to produce products comprising cannabinoids |
-
2010
- 2010-04-20 CN CN2010201723043U patent/CN201643760U/en not_active Expired - Fee Related
Cited By (18)
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| US10881982B2 (en) | 2013-10-04 | 2021-01-05 | Natural Extraction Systems, LLC | Method and apparatus for extracting botanical oils |
| WO2015049585A3 (en) * | 2013-10-04 | 2015-11-19 | Natural Extraction Services, Llc | Method and apparatus for extracting botanical oils |
| US12064709B2 (en) | 2013-10-04 | 2024-08-20 | Natural Extraction Systems, LLC | Method and apparatus for extracting botanical oils |
| US10159908B2 (en) | 2013-10-04 | 2018-12-25 | Natural Extraction Systems, LLC | Method and apparatus for extracting botanical oils |
| US10456708B2 (en) * | 2013-10-04 | 2019-10-29 | Natural Extraction Systems, LLC | Method and apparatus for extracting botanical oils |
| US11406913B2 (en) | 2013-10-04 | 2022-08-09 | Natural Extraction Systems, LLC | Method and apparatus for extracting botanical oils |
| CN104606909A (en) * | 2015-01-22 | 2015-05-13 | 李而宏 | Distillatory kettle for plant sesame oil |
| US10617974B2 (en) | 2016-05-02 | 2020-04-14 | Natural Extraction Systems, LLC | Method and apparatus for extracting botanical oils |
| CN110035809A (en) * | 2016-11-10 | 2019-07-19 | 拉米罗·塞尼奥雷特·韦尔杜戈 | Equipment and internal distillation method for extracting volatile oils from organic raw materials by steam distillation |
| CN110035809B (en) * | 2016-11-10 | 2022-01-25 | 拉米罗·塞尼奥雷特·韦尔杜戈 | Apparatus for extracting volatile oil from organic raw material by steam distillation and internal distillation method |
| CN107737462A (en) * | 2017-10-30 | 2018-02-27 | 新中天环保股份有限公司 | Organic solvent recycling and processing device |
| US11643402B2 (en) | 2018-08-10 | 2023-05-09 | Natural Extraction Systems, LLC | Gas phase methods to decarboxylate cannabinoids |
| US11702397B2 (en) | 2018-08-10 | 2023-07-18 | Natural Extraction Systems, LLC | Methods to purify cannabinoids |
| US12297181B2 (en) | 2018-08-10 | 2025-05-13 | Natural Extraction Systems, LLC | Methods to chemically modify cannabinoids |
| US12420214B2 (en) | 2018-08-10 | 2025-09-23 | Natural Extraction Systems, LLC | Methods to produce products comprising cannabinoids |
| US10974164B1 (en) | 2019-10-10 | 2021-04-13 | Boulder Creek Technologies, LLC | Continuous biomass extraction system and process |
| US11624038B2 (en) | 2019-10-10 | 2023-04-11 | Boulder Creek Technologies, LLC | Continuous biomass extraction system and process |
| CN110986566A (en) * | 2019-11-25 | 2020-04-10 | 耒阳市刘燕酿制生物科技有限公司 | Recovery unit of biological pure water in freeze-dried food production |
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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: 20101124 Termination date: 20130420 |