CN200946143Y - Gas-electric dual-using aromatic oil distiller - Google Patents
Gas-electric dual-using aromatic oil distiller Download PDFInfo
- Publication number
- CN200946143Y CN200946143Y CN 200620009819 CN200620009819U CN200946143Y CN 200946143 Y CN200946143 Y CN 200946143Y CN 200620009819 CN200620009819 CN 200620009819 CN 200620009819 U CN200620009819 U CN 200620009819U CN 200946143 Y CN200946143 Y CN 200946143Y
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- Prior art keywords
- steam
- electric
- retort
- heating
- distiller
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- Expired - Fee Related
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- Fats And Perfumes (AREA)
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The utility model discloses a gas-electric dual-using aromatic oil distiller belonging to aromatic oil distiller, in particular to flower plants aromatic oil distiller. The gas-electric dual-using aromatic oil distiller comprises a distilling pot, a distilling tower, a condenser, an oil-water separator, a charging port, a discharging port and a sewage draining outlet, being characterized in that the distilling pot and the distilling tower are vertical serial connected, the distilling pot is inside provided with a clapboard, wherein the lower of the clapboard is a heating area, and the upper is a charging area, and the heating area is provided with a steam heating device and an electric heater. The distiller provided by the utility model is provided with steam heating and electric heating in the heating device to fulfill dual using of steam heating and electric heating, avoiding the defect in prior distiller that mass steam enters into the pot and influences the oil yield, and the automatic controlling can be achieved according to the arranged parameter during electric heating. The fillings in the distilling tower can be washed to remove sewage, thereby reducing labor intensity and saving repairing time of equipment to improve efficiency.
Description
Technical field
The utility model belongs to the aromatic vegetable oil distillation plant, particularly spends class essential oil distillation plant.
Background technology
The flower of all kinds of aromatics plants, leaf, stem are the important sources of extracting natural perfume, and general the employing waits raw material to distill to flower, make wherein perfume oil with steam raising again condensation separation obtain perfume oil.ZL8721511 discloses a kind of perfume oil refining equipment and has preferably resolved some problems in the extraction, but heating power flow-through appt internal structure exists in still-process and utilizes steamer when beginning heat heat-up rate slow in the still kettle, when temperature in the kettle reaches 100 when spending, need frequent control quantity of steam and vapor pressure in order to avoid cross conference because of quantity of steam and perfume oil is caused to decompose loss or influence the vapour-liquid condensation separation reduce oil yield, operate shortcomings such as control techniques complexity.
The utility model content
The purpose of this utility model provides a kind ofly both can use steam heating, also can use electrically heated, the technical scheme of the simple novel aromatic oil of operation control water distilling apparatus.
The technical solution of the utility model is, a kind of steam-electric dual purpose perfume oil distillation plant, comprise retort, distillation tower, condenser, water-and-oil separator, opening for feed, discharge port, sewage draining exit, it is characterized in that: retort is vertical with distillation tower to be installed in series, dividing plate is housed in the retort, dividing plate for the heating zone, is loading area on the dividing plate down, and steam heater and electric heater are equipped with in the heating zone.
Described steam heater comprises that the annular coil pipe that the taper steam sparging device is housed by the end that links to each other with steam inlet tube forms with the spiral steam duct two-way diffuser that the end that links to each other with the insulation steam inlet tube is equipped with the regulating the qi flowing in the channels valve.
On described retort and the water-and-oil separator retort thermopair and the water-and-oil separator thermopair that links to each other with housing is housed respectively.
The recoil sewage disposal unit is equipped with at described distillation tower top.
Steam heating and electrically heated have been installed in the heating unit in the two-way diffuser perfume oil distillation plant that the utility model provides have realized that the dual-purpose steam supply area undesired or that do not have steam to supply with that is particularly suitable for of steam and electrically heated uses; in steam heater, adopted the taper steam sparging device can improve intensification degree speed, the spiral steam duct that is provided with the insulation sealing and circulating simultaneously only need regulate Air-regulating valves just can keep the temperature of needs to avoid in the existing water distilling apparatus in a large number again steam enter the shortcoming that influences oil yield in the jar.When using electrically heated,, thermopair and housing can realize control automatically according to the parameter of setting owing to being installed.At the distillation tower top recoil sewage disposal unit has been installed in addition, can wash the removing dirt to the filler in the distillation tower as required, having solved needs in the prior art to take out the loaded down with trivial details technology that filler cleans, and not only reduces labour intensity but also save the maintenance of the equipment time and raise the efficiency.
Description of drawings
Accompanying drawing 1 is a structural representation of the present utility model,
Among the figure, 1. sewage draining exit, 2. regulating the qi flowing in the channels valve, 3. taper steam sparging device, 4. electric heater, 5. dividing plate, 6. discharge port, 7. retort, 8. opening for feed, 9. distillation tower, 10. recoil sewage disposal unit, 11. condensers, 12. water-and-oil separator, 13. water-and-oil separator thermopairs, 14. housings, 15. the retort thermopair, 16. steam inlet tubes, 17. insulation steam inlet tubes.
Embodiment
Embodiment of the present utility model is, as shown in the figure:
Claims (4)
1. steam-electric dual purpose perfume oil distillation plant, comprise retort, distillation tower, condenser, water-and-oil separator, opening for feed, discharge port, sewage draining exit, it is characterized in that: retort is vertical with distillation tower to be installed in series, dividing plate is housed in the retort, dividing plate is the heating zone down, be loading area on the dividing plate, steam heater and electric heater are equipped with in the heating zone.
2. according to the determined steam-electric dual purpose perfume oil of claim 1 distillation plant, it is characterized in that: described steam heater is equipped with the taper steam sparging device by the end that links to each other with steam inlet tube annular coil pipe is formed with the spiral steam duct two-way diffuser that the end that links to each other with the insulation steam inlet tube is equipped with the regulating the qi flowing in the channels valve.
3. according to the determined steam-electric dual purpose perfume oil of claim 1 distillation plant, it is characterized in that: on described retort and the water-and-oil separator retort thermopair and the water-and-oil separator thermopair that links to each other with housing is housed respectively.
4. according to the determined steam-electric dual purpose perfume oil of claim 1 distillation plant, it is characterized in that: the recoil sewage disposal unit is equipped with at described distillation tower top.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200620009819 CN200946143Y (en) | 2006-09-15 | 2006-09-15 | Gas-electric dual-using aromatic oil distiller |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200620009819 CN200946143Y (en) | 2006-09-15 | 2006-09-15 | Gas-electric dual-using aromatic oil distiller |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN200946143Y true CN200946143Y (en) | 2007-09-12 |
Family
ID=38733206
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 200620009819 Expired - Fee Related CN200946143Y (en) | 2006-09-15 | 2006-09-15 | Gas-electric dual-using aromatic oil distiller |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN200946143Y (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104046514A (en) * | 2013-03-15 | 2014-09-17 | 什邡市恒源油脂有限责任公司 | Garlic essential oil extraction method |
| CN105368567A (en) * | 2015-11-25 | 2016-03-02 | 四川麻辣空间食品有限公司 | Chinese prickly ash oil production device and production method |
-
2006
- 2006-09-15 CN CN 200620009819 patent/CN200946143Y/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104046514A (en) * | 2013-03-15 | 2014-09-17 | 什邡市恒源油脂有限责任公司 | Garlic essential oil extraction method |
| CN104046514B (en) * | 2013-03-15 | 2016-08-03 | 什邡市恒源油脂有限责任公司 | A kind of Bulbus Allii quintessence oil extracting method |
| CN105368567A (en) * | 2015-11-25 | 2016-03-02 | 四川麻辣空间食品有限公司 | Chinese prickly ash oil production device and production method |
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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: 20070912 Termination date: 20091015 |