CN204939435U - A kind of family expenses essential oil distillation extraction device - Google Patents
A kind of family expenses essential oil distillation extraction device Download PDFInfo
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- CN204939435U CN204939435U CN201520551607.9U CN201520551607U CN204939435U CN 204939435 U CN204939435 U CN 204939435U CN 201520551607 U CN201520551607 U CN 201520551607U CN 204939435 U CN204939435 U CN 204939435U
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Abstract
The utility model discloses a kind of family expenses essential oil distillation extraction device, comprise still pot, condenser and water-and-oil separator, described still pot is connected with condenser by still tube, described condenser is connected with water-and-oil separator, described still pot is also provided with the heating plate for heating still pot, also comprise return line, described return line one end is connected with water-and-oil separator, the other end communicates with still pot, this extractor adds flow to still pot to the oily liquid physical efficiency of collecting, to implement to repeat distillation, with the quality of the extraction yield and essential oil that improve essential oil.
Description
Technical field
The utility model relates to the extraction element of plants essential oil, particularly relates to a kind of family expenses essential oil distillation extraction device.
Background technology
Essential oil is from the flower of plant, leaf, stem, root or fruit, is refined the volatile flavor of extraction by steam distillation, extrusion process, cold-maceration or solvent-extraction process.Essence oil volatility is very strong, once ingress of air will volatilize very soon, so also known as volatile oil, volatile oil is the general name with wet distillation oily liquids out, plants essential oil not only has vital role on medicine, makeup, applies also very extensive in perfume industry.Distillation method is from plant, extract that volatile oil is the most frequently used, method the most widely, and distillation method has the advantages such as equipment is simple, processing ease, treatment capacity are large.Current family expenses essential oil distillation distillation extraction extraction of essential oil rate is low, and difficult oily water separation, in leaching process, condensation effect is poor.
China Patent No. is separately had to be 201420858113.0, the day for announcing is that 2015.6.17 discloses a kind of essential oil extraction device, comprise still kettle, condenser and water-and-oil separator, it is characterized in that: described still kettle comprises kettle, kettle inside is provided with insulation still pot, be incubated bottom still pot and be provided with far infrared heater between autoclave body bottom internal surface, material basket is hung with in insulation still pot, kettle top is circular arc and is provided with opening for feed and air outlet, air outlet connects condensing reflux pipe by pipeline, condensing reflux pipe connects condenser, condenser is connected with water-and-oil separator by pipeline, water-and-oil separator outlet connects receiving flask, said extracted device oil-water mixture can not be back to still pot and realize repeating distillation, to improve extraction yield and the quality of plants essential oil.
Utility model content
In order to overcome above-mentioned prior art defect, the utility model provides a kind of family expenses essential oil distillation extraction device, and this extractor is back to still pot to the oily liquid physical efficiency of collecting, and realizes repeating distillation, with the quality of the extraction yield and essential oil that improve essential oil.
In order to solve the problems of the technologies described above, the technical solution adopted in the utility model is:
A kind of family expenses extraction of essential oil device, comprise still pot, condenser and water-and-oil separator, described still pot is connected with condenser by still tube, described condenser is connected with water-and-oil separator, described still pot is also provided with the heating plate for heating still pot, it is characterized in that: also comprise return line, described return line one end is connected with water-and-oil separator, and the other end communicates with still pot.
Described return line is connected with still tube, and return line is communicated with still pot by still tube, and the interface of return line and water-and-oil separator is lower than the interface of return line and still tube.
Also comprise air-cooled circulation device, described air-cooled circulation device comprises water tank, water pump and air cooler, water tank is connected with water pump by circulation tube, water pump is connected with the water inlet of condenser by circulation tube, the water outlet of condenser is connected with air cooler by circulation tube, air cooler is connected with water tank by circulation tube, is provided with fan in described air cooler.
The top of described still tube is provided with pressure relief opening, and described pressure relief opening is stamped stopper.
Described water-and-oil separator is provided with bleeding point, and described bleeding point, higher than the interface of return line and still tube, can be used for underpressure distillation, is conducive to carrying out extract at low temperature and fractionation to essential oil.
The utility model has the following advantages:
1, family expenses extraction of essential oil device of the present utility model, comprise still pot, condenser and water-and-oil separator, described still pot is connected with condenser by still tube, described condenser is connected with water-and-oil separator, described still pot is also provided with the heating plate for heating still pot, also comprise return line, described return line one end is connected with water-and-oil separator, the other end communicates with still pot, plant to be extracted is put into still pot and carries out boiling, plant fluid steam to enter in condenser after cooling through still tube, become liquid oil-water mixture and enter water-and-oil separator, be back to still pot by return line after oil-water mixture collection is a certain amount of and continue boiling, after repeatedly boiling, the ratio steaming essential oil in thing (oil-water mixture) could be improved, reach essential oil and separate out object, the extraction yield of more common extracting method essential oil improves more than 30%, after distillation terminates, open the draining valve of water-and-oil separator lower end, water (because the density of water is larger) is first released after water discharges by oil exit pipe, close draining valve, change container collection essential oil.
2, described return line of the present utility model is connected with still tube, return line is communicated with still pot by still tube, and the interface of return line and water-and-oil separator is lower than the interface of return line and still tube, reach withdrawing fluid by difference of altitude and close vapour road, make distillation gas can only arrive condenser by still tube, simultaneous altitude difference provides enough disengaging times for the oily water separation in oil-water mixture.
3, the utility model comprises air-cooled circulation device, described air-cooled circulation device comprises water tank, water pump and air cooler, water tank is connected with water pump by circulation tube, water pump is connected with the water inlet of condenser by circulation tube, the water outlet of condenser is connected with air cooler by circulation tube, air cooler is connected with water tank by circulation tube, is provided with fan in air cooler; Adopt water-cooled and air cooling two kinds of modes to cool, make to steam thing temperature in effective condensation length and be down to below room temperature+10 degree, and achieve circulating cooling, saved and used water.
4, the top of still tube of the present utility model is provided with pressure relief opening, and described pressure relief opening is stamped stopper, prevents still pot air pressure from raising, dangerous accident occurs, utilize pressure relief opening to clean equipment simultaneously.
5, the utility model water-and-oil separator is provided with bleeding point, and described bleeding point, higher than the interface of return line and still tube, can be mixed off-gas pump and carry out underpressure distillation, be conducive to carrying out extract at low temperature and fractionation to essential oil, to improve the efficiency of distillation.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model;
Mark in figure: 1, still pot, 2, still tube, 3, condenser, 4, heating plate, 5, water-and-oil separator, 6, return line, 7, bleeding point, 8, pressure relief opening, 9, stopper, 10, oil exit pipe, 11, draining valve, 12, air cooler, 13, fan, 14, water tank, 15, water pump.
Embodiment
Below in conjunction with accompanying drawing, the utility model is described further:
Embodiment 1
A kind of family expenses essential oil distillation extraction device, comprise still pot 1(and extract the plant of essential oil for boiling), condenser 2 and water-and-oil separator 5, still pot 1 is provided with airtight pot cover, still tube 2 communicates with still pot 1 through pot cover, still tube 2 the other end is connected with condenser 3, described condenser 3 is connected with water-and-oil separator 5, still pot 1 is also provided with the heating plate 4 for heating still pot 1, heating plate 4 is arranged on the bottom of still pot 1, general employing electrically heated or infrared heating mode, the simultaneously power adjustable of this heating plate.
On said structure, also comprise return line 6, described return line 6 one end is connected with water-and-oil separator 5, the other end communicates with still pot 1, here return line 6 still pot 1 communicates, can adopt and be connected with still tube 2 by return line 6, the mode that recycling still tube 2 communicates with still pot 1, the entrance simultaneously connected should meet: the interface of return line 6 and water-and-oil separator 5 is lower than the interface of return line 6 with still tube 2.
In order to improve the cooling performance of family expenses extraction of essential oil device, also be provided with air-cooled circulation device, described air-cooled circulation device comprises water tank 14, water pump 15 and air cooler 12, circulating line is adopted to connect between them, wherein: water tank 14 is connected with water pump 15 by circulation tube, water pump 15 is connected by the water inlet of circulation tube with condenser 3, the water outlet of condenser 3 is connected with air cooler 12 by circulation tube, air cooler 12 is connected with water tank 14 by circulation tube, is provided with fan 13 in described air cooler 12 simultaneously.Adopt water-cooled and air cooling two kinds of modes to cool, make to steam thing temperature in effective condensation length and be down to below room temperature+10 degree, and achieve circulating cooling, saved and used water.
Further, the top of described still tube 2 is provided with pressure relief opening 8, and described pressure relief opening 8 is stamped stopper 9.
Further, described water-and-oil separator 5 is provided with bleeding point 7, and described bleeding point 7 is higher than the interface of return line 6 with still tube 2.Mix off-gas pump and carry out underpressure distillation, be conducive to carrying out extract at low temperature and fractionation to essential oil, to improve the efficiency of distillation.
The working process of above-mentioned family expenses extraction of essential oil device is: plant to be extracted is put into still pot 1 and carry out boiling, plant fluid steam to enter in condenser 3 after cooling through still tube, become liquid oil-water mixture and enter water-and-oil separator 5, be back to still pot by return line 6 after oil-water mixture collection is a certain amount of and continue boiling, after repeatedly boiling, the extraction yield of more common extracting method essential oil improves more than 30%, after distillation terminates, open the draining valve 11 of water-and-oil separator lower end, water (because the density of water is larger) is first released after water discharges by oil exit pipe 10, close draining valve, change container collection essential oil.
Claims (3)
1. a family expenses essential oil distillation extraction device, comprise still pot (1), condenser (3), water-and-oil separator (5) and return line (6), described still pot (1) is connected with condenser (3) by still tube (2), described condenser (3) is connected with water-and-oil separator (5), described still pot (1) is also provided with the heating plate (4) for heating still pot (1), described return line (6) one end is connected with water-and-oil separator (5), the other end communicates with still pot (1), described return line (6) is connected with still tube (2), return line (6) is communicated with still pot (1) by still tube (2), and the interface of return line (6) and water-and-oil separator (5) is lower than the interface of return line (6) with still tube (2), it is characterized in that: also comprise air-cooled circulation device, described air-cooled circulation device comprises water tank (14), water pump (15) and air cooler (12), water tank (14) is connected with water pump (15) by circulation tube, water pump (15) is connected by the water inlet of circulation tube with condenser (3), the water outlet of condenser (3) is connected with air cooler (12) by circulation tube, air cooler (12) is connected with water tank (14) by circulation tube, fan (13) is provided with in described air cooler (12).
2. a kind of family expenses essential oil distillation extraction device according to claim 1, is characterized in that: the top of described still tube (2) is provided with pressure relief opening (8), described pressure relief opening (8) is stamped stopper (9).
3. a kind of family expenses essential oil distillation extraction device according to claim 1, it is characterized in that: described water-and-oil separator (5) is provided with bleeding point (7), described bleeding point (7) is higher than the interface of return line (6) with still tube (2).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520551607.9U CN204939435U (en) | 2015-07-28 | 2015-07-28 | A kind of family expenses essential oil distillation extraction device |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520551607.9U CN204939435U (en) | 2015-07-28 | 2015-07-28 | A kind of family expenses essential oil distillation extraction device |
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| Publication Number | Publication Date |
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| CN204939435U true CN204939435U (en) | 2016-01-06 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520551607.9U Expired - Fee Related CN204939435U (en) | 2015-07-28 | 2015-07-28 | A kind of family expenses essential oil distillation extraction device |
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| CN (1) | CN204939435U (en) |
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107057857A (en) * | 2017-03-29 | 2017-08-18 | 刘文龙 | Agilawood essential oil equipment and process are extracted in a kind of efficiently distillation |
| CN108034500A (en) * | 2017-12-29 | 2018-05-15 | 苏州勃朗科技股份有限公司 | A kind of family expenses plants essential oil fragrance extraction element |
| CN109097195A (en) * | 2018-09-25 | 2018-12-28 | 贵州剑河光能天然植物油农业科技有限公司 | A kind of highly-efficient processing device of valerian oil |
| CN109486555A (en) * | 2018-12-03 | 2019-03-19 | 湖南全望信息科技有限公司 | A kind of agricultural experiment vegetable oil extraction element |
| CN109609281A (en) * | 2019-02-19 | 2019-04-12 | 重庆中烟工业有限责任公司 | Reflow type distilling apparatus for extraction of essential oil |
| CN109609280A (en) * | 2019-02-19 | 2019-04-12 | 重庆中烟工业有限责任公司 | Plants essential oil distills extraction element |
| CN109874950A (en) * | 2019-04-12 | 2019-06-14 | 贵州省果树科学研究所 | A kind of extracting method of passion fruit hydrosol |
| CN113171627A (en) * | 2021-04-14 | 2021-07-27 | 响水中山生物科技有限公司 | Distillation plant in adjustable bentazone production |
-
2015
- 2015-07-28 CN CN201520551607.9U patent/CN204939435U/en not_active Expired - Fee Related
Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107057857A (en) * | 2017-03-29 | 2017-08-18 | 刘文龙 | Agilawood essential oil equipment and process are extracted in a kind of efficiently distillation |
| CN108034500A (en) * | 2017-12-29 | 2018-05-15 | 苏州勃朗科技股份有限公司 | A kind of family expenses plants essential oil fragrance extraction element |
| CN109097195A (en) * | 2018-09-25 | 2018-12-28 | 贵州剑河光能天然植物油农业科技有限公司 | A kind of highly-efficient processing device of valerian oil |
| CN109486555A (en) * | 2018-12-03 | 2019-03-19 | 湖南全望信息科技有限公司 | A kind of agricultural experiment vegetable oil extraction element |
| CN109609281A (en) * | 2019-02-19 | 2019-04-12 | 重庆中烟工业有限责任公司 | Reflow type distilling apparatus for extraction of essential oil |
| CN109609280A (en) * | 2019-02-19 | 2019-04-12 | 重庆中烟工业有限责任公司 | Plants essential oil distills extraction element |
| CN109874950A (en) * | 2019-04-12 | 2019-06-14 | 贵州省果树科学研究所 | A kind of extracting method of passion fruit hydrosol |
| CN113171627A (en) * | 2021-04-14 | 2021-07-27 | 响水中山生物科技有限公司 | Distillation plant in adjustable bentazone production |
| CN113171627B (en) * | 2021-04-14 | 2022-01-18 | 响水中山生物科技有限公司 | Distillation plant in adjustable bentazone production |
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| Date | Code | Title | Description |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20160106 Termination date: 20170728 |