CN202359093U - Plant essential oil extraction device - Google Patents
Plant essential oil extraction device Download PDFInfo
- Publication number
- CN202359093U CN202359093U CN2011205088434U CN201120508843U CN202359093U CN 202359093 U CN202359093 U CN 202359093U CN 2011205088434 U CN2011205088434 U CN 2011205088434U CN 201120508843 U CN201120508843 U CN 201120508843U CN 202359093 U CN202359093 U CN 202359093U
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- water
- oil
- essential oil
- still kettle
- condensing surface
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- Expired - Fee Related
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- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The utility model relates to an essential oil extraction device, in particular to a plant essential oil extraction device, which comprises a distillation reactor, a condenser and an oil-water separator and is characterized in that the bottom and the top part of the distillation reactor are provided with large valves, the top part of the distillation reactor is connected with an inlet of the condenser through a guide pipe, a heating device is arranged in the distillation reactor, the condenser is arranged in an inverted way, an outlet of the condenser is connected with the oil-water separator, the upper part of the oil-water separator is connected with a backflow pipe, the middle part of the backflow pipe is connected with a U-shaped pipe, the backflow pipe is connected with the top part of the distillation reactor, the bottom of the oil-water separator is provided with a valve, and the bottom of the oil-water separator is provided with an essential oil collector. By adopting the device, feeding can be performed conveniently and rapidly, oil and water can be separated rapidly, essential oil can be collected easily, the rate of utilization of the device can be improved, the energy consumption can be reduced, and the cost can be decreased.
Description
Technical field
The utility model belongs to steam distillation vegetables oil separation technology field, is specifically related to a kind of plants essential oil high efficiency extraction separating device.
Background technology
Steam distillation is from the most frequently used, the most widely used method of plant extract volatile oil.This method has equipment simple, processing ease, advantage such as treatment capacity is big.But traditional water vapor distillation method solid-to-liquid ratio is very big, and distillation time is long, and energy consumption is big; To the phlegma serious emulsification that some essential oil distills out, the oily water separation difficulty is for oily water separation; Need to leave standstill phlegma 2 ~ 3 days, also need refrigerate the back sometimes and carry out multiple steaming again, owing to heating and extracting for a long time with the supercentrifuge spinning or the water layer after the oily water separation; Some thermo-sensitivity composition in the essential oil can decompose, to the quality generation detrimentally affect of essential oil.
Summary of the invention
The purpose of the utility model is that the defective that traditional steam distillation equipment exists is improved, and provides a kind of energy-efficient essential oil to extract equipment, and it is low that it has energy consumption, and oily water separation is fast, and essential oil is collected easily, the plant factor advantages of higher.
In order to realize above-mentioned target, the utility model is realized through following technical scheme:
Plants essential oil extraction equipment comprises still kettle, condensing surface, water-and-oil separator; It is characterized in that: big valve is arranged at still kettle bottom and top, and the top is connected with the inlet of condensing surface through conduit, and heating unit is installed in the still kettle; Condensing surface is installed for being inverted, and the outlet of condensing surface connects water-and-oil separator, and the top of water-and-oil separator connects return line; The essential oil scoop is arranged at the bottom of water-and-oil separator, has made things convenient for the collection and the follow-up purification operations of essential oil.Connect a U type pipe in the middle of the return line, return line is connected with the top of still kettle, plays to allow liquid to flow into still kettle from water-and-oil separator, hinders the effect that the steam in the still kettle gets into water-and-oil separator.
Described still kettle is enamel still or stainless steel still.
Described heating unit is jacket structured, can use the mode of electrically heated, jacket water (J.W.) steam heating or thermal oil.
Described condensing surface is serpentine condenser or spherical condensation tube.
Described water-and-oil separator is that stainless steel or duraluminum are processed.
The utility model has following advantage:
Still kettle bottom is provided with big flange valve, can conveniently discharge the waste material behind the distillation essential oil, and top also is provided with big valve, and it is convenient and swift to feed.Convenient and swift through the loading and unloading material, improved plant factor.
Condensing surface is that upside-down mounting is installed, and the liquid that condensation is got off meets with the steam that gets into condensing surface, has obtained partial heat energy; Guarantee that phlegma has a suitable temperature, under this temperature,, accelerated the essential oil settling velocity because system viscosity is suitable; Accelerate oily water separation, avoided the formation of milk sap.
Water-and-oil separator top connects return line, can return still kettle through the water layer after the oily water separation, is heated generation steam again and takes essential oil out of, and so circulation has reduced essential oil and extracted water consumption, has reduced energy consumption, has practiced thrift cost.
Description of drawings
Accompanying drawing 1 is the structural representation of the utility model.
Being labeled as in the accompanying drawing: 1-still kettle; The 2-water-and-oil separator; The 3-condensing surface; 4-discharging valve; The 5-return line; 6-charging valve; The 7-heating unit.
Embodiment
Be described in further detail below in conjunction with the embodiment of accompanying drawing the utility model:
Shown in accompanying drawing 1, a kind of plant extract equipment comprises that the top of still kettle 1, still kettle 1 is connected with the import of condensing surface 3 through conduit, and said condensing surface 3 is upside-down mounting; The outlet of condensing surface 3 connects water-and-oil separator 2; The top of water-and-oil separator 2 connects return line 5, and return line 5 is connected with still kettle 1, and heating unit 7 is installed in the still kettle 1; Heating unit is jacket structured, can use the mode of electrically heated, jacket water (J.W.) steam heating or thermal oil.
The example that is extracted as with Oleum Cinnamomi: the cinnamon leaf and a certain proportion of water that dry in the shade after pulverizing join in the still kettle 1 through valve 6; Heating unit 7 (water vapor heating jacket) makes the boiling of still kettle 1 system; Steam is got into the import of condensing surface 3 by the conduit at still kettle 1 top; The steam of process condensation obtains oil, water sepn by the outlet inflow water-and-oil separator 2 of condensing surface 3; The water layer of telling flows back to still kettle 1 through return line 5, and oil reservoir is then collected further purification of back through the bottom conduit of water-and-oil separator 2.Extract certain hour, oil yield stops distillation after reaching certain value, gives off waste material from valve 4.
The utility model is not limited to above embodiment, and the content of mentioning in claim and the specification sheets all can be implemented.
Claims (5)
1. a plants essential oil extracts equipment, and it comprises still kettle, condensing surface and water-and-oil separator, it is characterized in that: big valve is arranged at described still kettle bottom and top; The top is connected with the inlet of condensing surface through conduit, and heating unit is installed in the still kettle, and condensing surface is installed for being inverted; The outlet of condensing surface connects water-and-oil separator; The top of water-and-oil separator connects return line, connects a U type pipe in the middle of the return line, and return line is connected with the top of still kettle; Valve is arranged at the bottom of water-and-oil separator, and the essential oil scoop is arranged at the bottom of water-and-oil separator.
2. plants essential oil according to claim 1 extracts equipment, and it is characterized in that: still kettle is enamel still or stainless steel still.
3. plants essential oil according to claim 1 extracts equipment, and it is characterized in that: heating unit is jacket structured, adopts electrically heated, jacket water (J.W.) steam heating or thermal oil device.
4. plants essential oil according to claim 1 extracts equipment, and it is characterized in that: condensing surface is serpentine condenser or spherical condensation tube.
5. plants essential oil according to claim 1 extracts equipment, and it is characterized in that: water-and-oil separator is that stainless steel or duraluminum are processed.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011205088434U CN202359093U (en) | 2011-12-09 | 2011-12-09 | Plant essential oil extraction device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011205088434U CN202359093U (en) | 2011-12-09 | 2011-12-09 | Plant essential oil extraction device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202359093U true CN202359093U (en) | 2012-08-01 |
Family
ID=46570296
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2011205088434U Expired - Fee Related CN202359093U (en) | 2011-12-09 | 2011-12-09 | Plant essential oil extraction device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202359093U (en) |
Cited By (14)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102978001A (en) * | 2012-12-06 | 2013-03-20 | 广西京桂香料有限公司 | Natural cassia oil condenser |
| CN103041063A (en) * | 2012-09-08 | 2013-04-17 | 新疆新维制药厂 | Closed pressure-reducing refluxing extraction method for general effective components of volatile medicinal materials |
| CN103045368A (en) * | 2012-09-08 | 2013-04-17 | 新疆新维制药厂 | Closed-type vacuum reflux extraction device |
| CN103923748A (en) * | 2014-04-30 | 2014-07-16 | 江西中医药大学 | Volatile oil extracting, collecting and separating device |
| CN105344126A (en) * | 2015-10-10 | 2016-02-24 | 上海应用技术学院 | Simple low-consumption extraction apparatus for solvent in distillation product |
| CN106350230A (en) * | 2016-12-05 | 2017-01-25 | 永州山香香料有限公司 | Litsea cubeba oil distillation separation equipment and technology |
| CN106731015A (en) * | 2017-01-22 | 2017-05-31 | 四川九渊医药科技有限公司 | oil water separator and oil water separator system |
| CN106867673A (en) * | 2017-01-07 | 2017-06-20 | 云南中烟工业有限责任公司 | The apparatus and method that essential oil of tobaccos is extracted in a kind of superheated vapour distillation |
| CN106975236A (en) * | 2017-04-28 | 2017-07-25 | 南宁市青秀区嘉利林化有限公司 | A kind of rosin vacuum distillation apparatus |
| 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 |
| CN108130190A (en) * | 2017-12-11 | 2018-06-08 | 百朗德生物化学(海门)有限公司 | A kind of Chinese torreya essential oil extraction and separation process of novel environment friendly |
| CN108355370A (en) * | 2017-07-01 | 2018-08-03 | 石城县松湖林业化工有限公司 | A kind of turpentine oil processing distilling apparatus |
| CN112500927A (en) * | 2020-12-04 | 2021-03-16 | 佛山德众制药机械有限公司 | Demulsifying aromatic oil recovery device |
-
2011
- 2011-12-09 CN CN2011205088434U patent/CN202359093U/en not_active Expired - Fee Related
Cited By (16)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103041063A (en) * | 2012-09-08 | 2013-04-17 | 新疆新维制药厂 | Closed pressure-reducing refluxing extraction method for general effective components of volatile medicinal materials |
| CN103045368A (en) * | 2012-09-08 | 2013-04-17 | 新疆新维制药厂 | Closed-type vacuum reflux extraction device |
| CN102978001A (en) * | 2012-12-06 | 2013-03-20 | 广西京桂香料有限公司 | Natural cassia oil condenser |
| CN103923748A (en) * | 2014-04-30 | 2014-07-16 | 江西中医药大学 | Volatile oil extracting, collecting and separating device |
| CN103923748B (en) * | 2014-04-30 | 2016-05-11 | 江西中医药大学 | A kind of volatile oil extracts collects separation equipment |
| CN105344126A (en) * | 2015-10-10 | 2016-02-24 | 上海应用技术学院 | Simple low-consumption extraction apparatus for solvent in distillation product |
| CN106350230A (en) * | 2016-12-05 | 2017-01-25 | 永州山香香料有限公司 | Litsea cubeba oil distillation separation equipment and technology |
| CN106867673A (en) * | 2017-01-07 | 2017-06-20 | 云南中烟工业有限责任公司 | The apparatus and method that essential oil of tobaccos is extracted in a kind of superheated vapour distillation |
| CN106731015A (en) * | 2017-01-22 | 2017-05-31 | 四川九渊医药科技有限公司 | oil water separator and oil water separator system |
| 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 |
| CN106975236A (en) * | 2017-04-28 | 2017-07-25 | 南宁市青秀区嘉利林化有限公司 | A kind of rosin vacuum distillation apparatus |
| CN106975236B (en) * | 2017-04-28 | 2019-10-22 | 广西南宁成远科技有限公司 | A kind of rosin vacuum distillation apparatus |
| CN108355370A (en) * | 2017-07-01 | 2018-08-03 | 石城县松湖林业化工有限公司 | A kind of turpentine oil processing distilling apparatus |
| CN108130190A (en) * | 2017-12-11 | 2018-06-08 | 百朗德生物化学(海门)有限公司 | A kind of Chinese torreya essential oil extraction and separation process of novel environment friendly |
| 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 |
| CN112500927A (en) * | 2020-12-04 | 2021-03-16 | 佛山德众制药机械有限公司 | Demulsifying aromatic oil recovery device |
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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: 20120801 Termination date: 20131209 |