CN2643967Y - Distilling device of flower essential oil - Google Patents
Distilling device of flower essential oil Download PDFInfo
- Publication number
- CN2643967Y CN2643967Y CN 03253612 CN03253612U CN2643967Y CN 2643967 Y CN2643967 Y CN 2643967Y CN 03253612 CN03253612 CN 03253612 CN 03253612 U CN03253612 U CN 03253612U CN 2643967 Y CN2643967 Y CN 2643967Y
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- Prior art keywords
- still
- pipe
- essential oil
- distillation equipment
- turbine
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- Expired - Fee Related
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- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The utility model discloses a flower aroma essential oil distillation equipment belonging to the aroma essential oil distillation equipment, in particular to the flower plant aroma essential oil distillation equipment. The flower aroma essential oil distillation equipment comprises a still, a distillation tower, a condenser, and an oily water separator which are connected with each other by pipe, one steam input pipe arranged on the side of sill bottom is connected with the annular air pipe horizontally arranged in the still, the air pipe is vertically evenly provided with periphery jet device with jet orifice, another steam input pipe is connected the central jet device arranged at the center of the still and provided with a turbine chamber, the outer wall of the central jet device round pipe is provided with jet orifice, the round pipe is provided with an agitating middle shaft at the center, the bottom end of the middle shaft is provided with vane agitator, the middle shaft in the turbine chamber is provided with a turbine. The utility model has the advantages of easy manufacture, short processing time, even distribution of heat pressure, high distilling efficiency; which is suitable for small processing enterprises.
Description
Affiliated technical field:
The utility model belongs to aromatic oil and extracts equipment, particularly spends class essential oil to extract equipment.
Background technology:
Various aromatics flowers are the important sources of extracting natural perfume material, generally take flower is distilled, and make wherein aromatic oil with steam raising, and condensation separation obtains aromatic oil again.CN8721511U discloses a kind of aromatic oil refining equipment, preferably resolves some problems in the extraction, but heating power flow device internal structure is openly not comprehensive in the distillation still, and it is inhomogeneous to see the still that from file raw material is heated, and can influence oil yield.
Summary of the invention:
It is carrier with the low pressure vapours that the purpose of this utility model provides a kind of, is heated evenly the technical scheme of the novel distillation equipment that oil yield is high in the consersion unit.
The technical solution of the utility model is, a kind of colored class volatile oil distillation equipment, comprise with the interconnective distillation still of pipeline, destilling tower, condenser, oil water separator, in distillation still and the pipeline that destilling tower is connected pressure valve is housed, charging aperture is equipped with at the still top, discharging opening is arranged at the bottom, bottom one side has sewage outlet, the steam inlet Guan Yilu of still lower side is connecting the annular gas pipe of the horizontal setting in the still, annular gas pipe evenly is installed with the peripheral ejector that the 3-8 root has 10-50 jet orifice vertically upward, another road of steam inlet pipe is connecting the central ejector that has turbine room that is positioned at still central authorities, central authorities' ejector circular tube external wall jet orifice that distributing, the pipe center is for stirring axis, blade mixer is equipped with in the axis lower end, on the axis turbine is housed in the turbine room.Thermometer, Pressure gauge are housed on the distillation still.
The beneficial effects of the utility model are, when using the utility model to spend the distillation of class essential oil, raw material is added in the still from charging aperture, feed the low-pressure steam of 70-90Kpa from steam inlet, part steam passes annular gas pipe and leads to peripheral ejector and spray from jet orifice, another road steam enters the minor air cell and promotes turbine rotating band moving vane agitator stirring material, spray the jet orifice of steam around central ejector, material can be uniform like this, be subjected to the head-on collision power of the heat and the steam molecule of steam fully, can take destilling tower to steam being combined in intracytoplasmic volatile aromatic compound, and then, reclaim by oil water separator to condenser condenses.This design has improved thermal pressure steam to the feed distribution degree with to the impulsive force of raw material recipient cell, has accelerated the separating rate of organic aromatic compound and cell organic matter.This device structure simply is easy to make, and technological process is short, extraction efficiency is high, is applicable to that small processing enterprise uses.
Description of drawings:
Accompanying drawing is a structural representation of the present utility model.
Among the figure, 1. charging aperture, 2. thermometer, 3. pressure valve, 4. destilling tower, 5. condenser, 6. oil water separator, 7. Pressure gauge, 8. central ejector, 9. peripheral ejector, 10. distillation still, 11. turbine rooms, 12. annular gas pipe, 13. sewage outlets, 14. agitators, 15. discharging opening, 16. agitator axis, 17. steam inlet pipes.
The specific embodiment:
The specific embodiment of the present utility model is, as shown in the figure:
Embodiment 1, a kind of colored class volatile oil distillation equipment, comprise with the interconnective distillation still 10 of pipeline, destilling tower 4, condenser 5, oil water separator 6, thermometer 2 is housed on the still, Pressure gauge 7, in distillation still and the pipeline that destilling tower is connected pressure valve 3 is housed, charging aperture 1 is equipped with at the still top, discharging opening 15 is arranged at the bottom, bottom one side has sewage outlet 13, the steam inlet pipe 17 one tunnel of still lower side is connecting the annular gas pipe 12 of the horizontal setting in the still, annular gas pipe evenly is installed with 3 peripheral ejectors 9 that have 20 jet orifices vertically upward, another road of steam inlet pipe is connecting the central ejector 8 that has turbine room 11 that is positioned at still central authorities, central authorities' ejector circular tube external wall jet orifice that distributing, the pipe center is for stirring axis 16, blade mixer 14 is equipped with in the axis lower end, on the axis turbine is housed in the turbine room.
Embodiment 2, and basic structure is with embodiment 1 but annular gas pipe evenly is installed with 4 peripheral ejectors 9 that have 30 jet orifices vertically upward.
Embodiment 3, and basic structure is with embodiment 1 but annular gas pipe evenly is installed with 6 peripheral ejectors 9 that have 40 jet orifices vertically upward.
Claims (2)
1. colored class volatile oil distillation equipment, comprise with the interconnective distillation still of pipeline, destilling tower, condenser, oil water separator, it is characterized in that: in distillation still and the pipeline that destilling tower is connected pressure valve is housed, charging aperture is equipped with at the still top, discharging opening is arranged at the bottom, bottom one side has sewage outlet, the steam inlet Guan Yilu of still lower side is connecting the annular gas pipe of the horizontal setting in the still, annular gas pipe evenly is installed with the peripheral ejector that the 3-8 root has 10-50 jet orifice vertically upward, another road of steam inlet pipe is connecting the central ejector that has turbine room that is positioned at still central authorities, central authorities' ejector circular tube external wall jet orifice that distributing, the pipe center is for stirring axis, blade mixer is equipped with in the axis lower end, on the axis turbine is housed in the turbine room.
2. by the determined colored class volatile oil distillation equipment of claim 1, it is characterized in that: thermometer, Pressure gauge are housed on the distillation still.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 03253612 CN2643967Y (en) | 2003-09-23 | 2003-09-23 | Distilling device of flower essential oil |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 03253612 CN2643967Y (en) | 2003-09-23 | 2003-09-23 | Distilling device of flower essential oil |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN2643967Y true CN2643967Y (en) | 2004-09-29 |
Family
ID=34294482
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 03253612 Expired - Fee Related CN2643967Y (en) | 2003-09-23 | 2003-09-23 | Distilling device of flower essential oil |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN2643967Y (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101935590A (en) * | 2010-09-06 | 2011-01-05 | 云南绿宝香精香料股份有限公司 | Low-temperature thin film citronella oil instantaneous distilling device |
| CN102952629A (en) * | 2012-12-06 | 2013-03-06 | 广西京桂香料有限公司 | Technological method for extracting natural cinnamon oil |
| CN102994232A (en) * | 2012-12-24 | 2013-03-27 | 高连波 | Device for extracting plant essential oil |
| CN108434769A (en) * | 2018-04-24 | 2018-08-24 | 安徽春辉仪表线缆集团有限公司 | A kind of energy-efficient Three-effect concentration evaporator |
| CN111139137A (en) * | 2020-01-10 | 2020-05-12 | 昆明理工大学 | Vetiver oil draws economizer system |
-
2003
- 2003-09-23 CN CN 03253612 patent/CN2643967Y/en not_active Expired - Fee Related
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101935590A (en) * | 2010-09-06 | 2011-01-05 | 云南绿宝香精香料股份有限公司 | Low-temperature thin film citronella oil instantaneous distilling device |
| CN101935590B (en) * | 2010-09-06 | 2012-06-27 | 云南绿宝香精香料股份有限公司 | Low-temperature thin film citronella oil instantaneous distilling device |
| CN102952629A (en) * | 2012-12-06 | 2013-03-06 | 广西京桂香料有限公司 | Technological method for extracting natural cinnamon oil |
| CN102952629B (en) * | 2012-12-06 | 2014-04-02 | 广西京桂香料有限公司 | Technological method for extracting natural cinnamon oil |
| CN102994232A (en) * | 2012-12-24 | 2013-03-27 | 高连波 | Device for extracting plant essential oil |
| CN108434769A (en) * | 2018-04-24 | 2018-08-24 | 安徽春辉仪表线缆集团有限公司 | A kind of energy-efficient Three-effect concentration evaporator |
| CN111139137A (en) * | 2020-01-10 | 2020-05-12 | 昆明理工大学 | Vetiver oil draws economizer system |
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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 |