CN206355621U - A kind of peppermint oil, eucalyptus oil natural plant raw material oil processing fractionating device - Google Patents
A kind of peppermint oil, eucalyptus oil natural plant raw material oil processing fractionating device Download PDFInfo
- Publication number
- CN206355621U CN206355621U CN201720016642.XU CN201720016642U CN206355621U CN 206355621 U CN206355621 U CN 206355621U CN 201720016642 U CN201720016642 U CN 201720016642U CN 206355621 U CN206355621 U CN 206355621U
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- China
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- oil
- steam distillation
- distillation kettle
- condenser
- ethanol
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Abstract
The utility model discloses a kind of peppermint oil, eucalyptus oil natural plant raw material oil processing fractionating device, exported including motor and distillate, the motor is arranged on the top of steam distillation kettle, the left hand external of the steam distillation kettle is provided with charging aperture, and the right hand external of steam distillation kettle is provided with steam entry, solid discharge is provided with below the steam distillation kettle, support post is provided with the left of the solid discharge, it is provided with the right side of the steam distillation kettle on the right side of condenser, the condenser and is provided with oil water separator.There is provided rectification under vacuum, reflux ratio can be accurately controlled, make the purity of plant material oil higher, reboiler is provided with rectifying column portion, the higher aromatic hydrocarbon of vegetable oils mid-boiling point by reboiler can be heated rectifying again, the efficiency of rectifying be improved, there is provided ethanol recovery tower and ethanol extractor, the recycling that can be repeated ethanol, saves material.
Description
Technical field
The utility model belongs to vegetable oils processing unit (plant) technical field, and in particular to a kind of peppermint oil, eucalyptus oil are natural
Plant material oil processing fractionating device.
Background technology
Vegetal natural perfume is in preparation and production method, and steam distillation and solvent extraction method are conventional preparations
The method of essential oil and medicinal extract.Water vapour is passed through in the extractor of natural plant raw material by prior art, and volatile ingredient steams with water
Steam distillation comes out, and entering separation in oil water separator by condenser system prepares essential oil.Solvent is added to natural plants former
Extraction, concentration are carried out in the extractor of material and prepares medicinal extract.
The oily process equipment of existing plant material is not only complicated, and the purity of the plants essential oil extracted is low,
The pigment of essential oil is heavier, and fragrance is coarse, and the quality of essential oil is not high, and material can not realize recovery in process, waste compared with
Greatly.
Utility model content
The purpose of this utility model is that providing a kind of peppermint oil, eucalyptus oil natural plant raw material oil processes fractionating device,
It is not only complicated with the oily process equipment of plant material for solving to propose in above-mentioned background technology, and the plant essence extracted
The purity of oil is low, and the pigment of essential oil is heavier, and fragrance is coarse, and the quality of essential oil is not high, and material can not be realized in process
Reclaim, the problem of wasting larger.
To achieve the above object, the utility model provides following technical scheme：A kind of peppermint oil, eucalyptus oil natural plants are former
Material oil processing fractionating device, including motor and distillate outlet, the motor are arranged on the upper of steam distillation kettle
Side, the left hand external of the steam distillation kettle is provided with charging aperture, and the right hand external of steam distillation kettle is provided with water steaming
It is provided with below gas entrance, the steam distillation kettle on the left of solid discharge, the solid discharge and is provided with support post,
It is provided with the right side of the steam distillation kettle on the right side of condenser, the condenser and is provided with oil water separator, the profit point
Ethanol recovery tower is provided with from being provided with below device on the right side of ethanol extractor, the ethanol extractor, the ethanol is reclaimed
It is provided with above tower on the right side of ADSORPTION IN A FIXED BED drier, the ADSORPTION IN A FIXED BED drier and is provided with vacuum rectification tower, institute
The right hand external for stating vacuum rectification tower is provided with return duct, and the right side top of the return duct is provided with rectifying condenser, described
Cooler is provided with below rectifying condenser, the distillate outlet is arranged on the lower section of cooler, the vacuum rectification tower
Right side is provided with above reboiler, the right side of the reboiler close to the lower position that distillate is exported and is provided with heating steam
Condensation-water drain is provided with below entrance, the heating steam inlet, the motor electrically connects with external control panel
Connect.
It is preferred that, the condenser is fixedly connected with oil water separator by connecting pipe.
It is preferred that, the motor is bolted to connection with steam distillation kettle.
It is preferred that, the support post is provided with eight altogether, and eight support posts be separately positioned on steam distillation kettle,
Condenser, reboiler, vacuum rectification tower, the lower section of ethanol recovery tower and ethanol extractor.
It is preferred that, the vacuum rectification tower is cylindrical structural.
Compared with prior art, the beneficial effects of the utility model are：The utility model is scientific and reasonable for structure, uses safety
It is convenient, there is provided rectification under vacuum, can be accurately controlled reflux ratio, make the purity of plant material oil higher, set in rectifying column portion
Reboiler has been put, the higher aromatic hydrocarbon of vegetable oils mid-boiling point by reboiler rectifying can have been heated again, improve rectifying
Efficiency, there is provided ethanol recovery tower and ethanol extractor, the recycling that can be repeated ethanol, save material.
Brief description of the drawings
Fig. 1 is structural representation of the present utility model；
Fig. 2 is top view of the present utility model；
In figure：1- charging apertures, 2- steam distillations kettle, 3- motors, 4- steam entries, 5- condensers, 6- profits
Separator, 7- ADSORPTION IN A FIXED BEDs drier, 8- return ducts, 9- rectifying condensers, 10- coolers, the outlet of 11- distillates, 12- are again
Boil device, 13- heating steam inlets, 14- condensation-water drains, 15- vacuum rectification towers, 16- ethanol recovery tower, 17- ethanol extractor,
18- support posts, 19- solid discharges.
Embodiment
Below in conjunction with the accompanying drawing in the utility model embodiment, the technical scheme in the utility model embodiment is carried out
Clearly and completely describe, it is clear that described embodiment is only a part of embodiment of the utility model, rather than whole
Embodiment.Based on the embodiment in the utility model, those of ordinary skill in the art are not under the premise of creative work is made
The every other embodiment obtained, belongs to the scope of the utility model protection.
Fig. 1 and Fig. 2 are referred to, the utility model provides a kind of technical scheme：A kind of peppermint oil, eucalyptus oil natural plants are former
Material oil processing fractionating device, including motor 3 and distillate outlet 11, motor 3 is arranged on the upper of steam distillation kettle 2
Side, the left hand external of steam distillation kettle 2 is provided with charging aperture 1, and the right hand external of steam distillation kettle 2 is provided with vapor
Entrance 4, the lower section of steam distillation kettle 2 is provided with solid discharge 19, and the left side of solid discharge 19 is provided with support post 18, water
The right side of steam distillation kettle 2 is provided with condenser 5, and the right side of condenser 5 is provided with oil water separator 6, the lower section of oil water separator 6
Ethanol extractor 17 is provided with, the right side of ethanol extractor 17 is provided with ethanol recovery tower 16, and the top of ethanol recovery tower 16 is set
ADSORPTION IN A FIXED BED drier 7 is equipped with, the right side of ADSORPTION IN A FIXED BED drier 7 is provided with vacuum rectification tower 15, vacuum rectification tower 15
Right hand external be provided with return duct 8, be provided with rectifying condenser 9, the lower section of rectifying condenser 9 above the right side of return duct 8
Cooler 10 is provided with, distillate outlet 11 is arranged on the lower section of cooler 10, and the right side of vacuum rectification tower 15 goes out close to distillate
The lower position of mouth 11, which is provided with above reboiler 12, the right side of reboiler 12, is provided with heating steam inlet 13, and heating is steamed
The lower section of vapour entrance 13 is provided with condensation-water drain 14, and motor 3 is electrically connected with external control panel.
In order that stable between condenser 5 and oil water separator 6 connect, in the present embodiment, it is preferred that condenser 5 and oil
Separator 6 is fixedly connected by connecting pipe.
Fixed in order that motor 3 can be stablized, in the present embodiment, it is preferred that motor 3 and steam distillation kettle
2 are bolted to connection.
Fixed in order that the present apparatus can be stablized, in the present embodiment, it is preferred that support post 18 is provided with eight altogether, and
Eight support posts 18 are separately positioned on steam distillation kettle 2, condenser 5, reboiler 12, vacuum rectification tower 15, ethanol and reclaimed
The lower section of tower 16 and ethanol extractor 17.
In order that the rectification effect of vacuum rectification tower 15 is more preferably, in the present embodiment, it is preferred that vacuum rectification tower 15 is cylinder
Shape structure.
Reboiler 12 of the present utility model is liquid is vaporized again.Its structure is similar with condenser, Bu Guoyi
Kind it is that, for cooling, and reboiler is that, for the vaporization that heats up, material diminishes in the even vaporization of reboiler expanded by heating, density, from
And vaporization space is left, smoothly return in tower, return to the gas-liquid two-phase in tower, gas phase is upwardly through tower tray, and liquid phase can be fallen
Fall on bottom of towe.Due to the effect of static pressure difference, bottom of towe will be continuously replenished the part liquid level being evaporated.
Operation principle of the present utility model and use flow：The peppermint oil, the oil processing fractionation of eucalyptus oil natural plant raw material
After device is installed, the normal work of motor 3 is made by external control panel, raw material is added from charging aperture 1, is steamed by water
Steam distillation kettle 2, enters condenser 5 after distillation, enters inside oil water separator 6, passes through after the condensation of condenser 5
Oil water separator 6 is entered inside ADSORPTION IN A FIXED BED drier 7 after separating, and is entered after drying in vacuum rectification tower 15
Portion, volatile aromatic hydrocarbon enters rectifying condenser 9 by top duct, and condensation rear portion lease making crosses return duct 8 and enters decompression
Rectifying is carried out inside rectifying column 15 again, remaining plants essential oil is distillated after being cooled down through subcooler 10 by distillate outlet 11,
The liquid phase plant aromatic hydrocarbon of hardly possible volatilization is entered inside reboiler 12 by pipeline, is heated again by pipeline by reboiler 12
Entering makes the better of rectifying inside vacuum rectification tower 15.
While there has been shown and described that embodiment of the present utility model, for the ordinary skill in the art,
It is appreciated that these embodiments can be carried out in the case where not departing from principle of the present utility model and spirit a variety of changes, repaiies
Change, replace and modification, scope of the present utility model is defined by the appended claims and the equivalents thereof.
Claims (5)
1. a kind of peppermint oil, eucalyptus oil natural plant raw material oil processing fractionating device, including motor（3）With distillate outlet
（11）, it is characterised in that：The motor（3）It is arranged on steam distillation kettle（2）Top, the steam distillation kettle
（2）Left hand external be provided with charging aperture（1）, and steam distillation kettle（2）Right hand external be provided with steam entry（4）,
The steam distillation kettle（2）Lower section be provided with solid discharge（19）, the solid discharge（19）Left side be provided with support
Column（18）, the steam distillation kettle（2）Right side is provided with condenser（5）, the condenser（5）Right side be provided with profit
Separator（6）, the oil water separator（6）Lower section be provided with ethanol extractor（17）, the ethanol extractor（17）The right side
Side is provided with ethanol recovery tower（16）, the ethanol recovery tower（16）Top be provided with ADSORPTION IN A FIXED BED drier（7）, it is described
ADSORPTION IN A FIXED BED drier（7）Right side be provided with vacuum rectification tower（15）, the vacuum rectification tower（15）Right hand external set
It is equipped with return duct（8）, the return duct（8）Right side above be provided with rectifying condenser（9）, the rectifying condenser（9）'s
Lower section is provided with cooler（10）, the distillate outlet（11）It is arranged on cooler（10）Lower section, the vacuum rectification tower
（15）Right side is exported close to distillate（11）Lower position be provided with reboiler（12）, the reboiler（12）Right side on
Side is provided with heating steam inlet（13）, the heating steam inlet（13）Lower section be provided with condensation-water drain（14）, it is described
Motor（3）It is electrically connected with external control panel.
2. a kind of peppermint oil according to claim 1, eucalyptus oil natural plant raw material oil processing fractionating device, its feature exist
In：The condenser（5）With oil water separator（6）It is fixedly connected by connecting pipe.
3. a kind of peppermint oil according to claim 1, eucalyptus oil natural plant raw material oil processing fractionating device, its feature exist
In：The motor（3）With steam distillation kettle（2）It is bolted to connection.
4. a kind of peppermint oil according to claim 1, eucalyptus oil natural plant raw material oil processing fractionating device, its feature exist
In：The support post（18）Eight, and eight support posts are provided with altogether（18）It is separately positioned on steam distillation kettle（2）、
Condenser（5）, reboiler（12）, vacuum rectification tower（15）, ethanol recovery tower（16）With ethanol extractor（17）Lower section.
5. a kind of peppermint oil according to claim 1, eucalyptus oil natural plant raw material oil processing fractionating device, its feature exist
In：The vacuum rectification tower（15）For cylindrical structural.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720016642.XU CN206355621U (en) | 2017-01-07 | 2017-01-07 | A kind of peppermint oil, eucalyptus oil natural plant raw material oil processing fractionating device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720016642.XU CN206355621U (en) | 2017-01-07 | 2017-01-07 | A kind of peppermint oil, eucalyptus oil natural plant raw material oil processing fractionating device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206355621U true CN206355621U (en) | 2017-07-28 |
Family
ID=59380735
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720016642.XU Expired - Fee Related CN206355621U (en) | 2017-01-07 | 2017-01-07 | A kind of peppermint oil, eucalyptus oil natural plant raw material oil processing fractionating device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206355621U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113088398A (en) * | 2021-04-09 | 2021-07-09 | 云南国润香料制造有限公司 | Eucalyptol rectifying device and control system suitable for large-scale production |
-
2017
- 2017-01-07 CN CN201720016642.XU patent/CN206355621U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113088398A (en) * | 2021-04-09 | 2021-07-09 | 云南国润香料制造有限公司 | Eucalyptol rectifying device and control system suitable for large-scale production |
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| GR01 | Patent grant | ||
| 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: 20170728 Termination date: 20210107 |