CN208959360U - A kind of continuous vacuum distillation apparatus being used to prepare arborvitae hydrosol product - Google Patents
A kind of continuous vacuum distillation apparatus being used to prepare arborvitae hydrosol product Download PDFInfo
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- CN208959360U CN208959360U CN201821310426.7U CN201821310426U CN208959360U CN 208959360 U CN208959360 U CN 208959360U CN 201821310426 U CN201821310426 U CN 201821310426U CN 208959360 U CN208959360 U CN 208959360U
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- pipe
- pot body
- tank
- inlet tube
- fluid container
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Abstract
The utility model provides a kind of continuous vacuum distillation apparatus for being used to prepare arborvitae hydrosol product, including pot body, feed liquor mechanism and vacuum pump, and the pot body is equipped with fraction pipe, return pipe and inlet tube；Fraction pipe is controlled to a vacuum pump, and is equipped with condenser, and condenser is connected with condensate tank；The inlet tube is connect with feed liquor mechanism, feed liquor mechanism includes original fluid container and surge tank, surge tank is connected between original fluid container and pot body, the tank mouth of original fluid container is equipped with sealing cover, sealing cover is equipped with and is connected with inside plunger shaft, plunger shaft is equipped with piston boit, and piston boit is equipped with the pressure spring acted between piston boit and plunger shaft；The return pipe is connected with reflux pump and return tank in turn.The continuous still that Thuja extract may be implemented in the vacuum distillation apparatus of the utility model is refined, and can effectively be refined under lower vapo(u)rizing temperature to certain perishable effective components, and oxidation deterioration is prevented.
Description
Technical field
The utility model relates to a kind of continuous vacuum distillation apparatus for being used to prepare arborvitae hydrosol product, belong to plant extract
Equipment technical field.
Background technique
When preparing arborvitae hydrosol product, needs to carry out arborvitae maceration extract distillation and isolate condensate liquid, due to maceration extract
In contain high boiling effective component, when using air-distillation, vapo(u)rizing temperature is excessively high may cause effective component high-temperature oxydation or
It decomposes, thus the hydrosol product of high-quality cannot be obtained.And it is right at a lower temperature to use reduced pressure distillation process to be then able to achieve
Effective component extracts, and obtains grease azeotropic mixture.But between the vacuum distillation apparatus that current plants essential oil refinement is used is mostly
It has a rest distillation, efficiency is lower.
Utility model content
To solve the above-mentioned problems, the utility model provides a kind of continuous decompression steaming for being used to prepare arborvitae hydrosol product
Distillation unit, specific technical solution are:
A kind of continuous vacuum distillation apparatus being used to prepare arborvitae hydrosol product, including pot body, feed liquor mechanism and vacuum pump,
The pot body is equipped with fraction pipe, return pipe and inlet tube；Fraction pipe is controlled to a vacuum pump, and is equipped with condenser, condenser connection
There is condensate tank；The inlet tube is connect with feed liquor mechanism, and feed liquor mechanism includes original fluid container and surge tank, and surge tank is connected to
Between original fluid container and pot body, the tank mouth of original fluid container is equipped with sealing cover, and sealing cover is equipped with and is connected with inside plunger shaft, plunger shaft
Equipped with piston boit, piston boit is equipped with the pressure spring acted between piston boit and plunger shaft；The return pipe is connected with reflux in turn
Pump and return tank.
Further, the pot nside is equipped with vertical interlayer board, and pot nside is separated into two mutually by interlayer board
The distillation chamber of isolation, inlet tube, return pipe and fraction pipe are equipped with branch pipe, are individually connected with two distillation chambers respectively by branch pipe
It is logical, and each branch pipe is equipped with control valve.
Further, the pot body includes shell and top cover, and shell is connected with top cover by flange head, the inlet tube and
Return pipe is set to shell, and the fraction pipe is set to top cover；The interlayer board includes the upper spacer for being respectively arranged at shell and top cover
And lower clapboard；The flange head, upper spacer and lower clapboard are equipped with mutually matched groove and boss.
The beneficial point of the utility model is: the company of Thuja extract may be implemented in the vacuum distillation apparatus of the utility model
Continuous distillation is refined, and can effectively be refined under lower vapo(u)rizing temperature to certain perishable effective components, is prevented
Oxidation deterioration.
Detailed description of the invention
In order to more clearly explain the embodiment of the invention or the technical proposal in the existing technology, to embodiment or will show below
There is attached drawing needed in technical description to be briefly described, it should be apparent that, the accompanying drawings in the following description is only this
Some embodiments of invention without any creative labor, may be used also for those of ordinary skill in the art
To obtain other drawings based on these drawings.
Fig. 1 is the structural schematic diagram of the utility model；
Fig. 2 is the structural schematic diagram of shell in the utility model；
Fig. 3 is the structural schematic diagram of top cover in the utility model.
Specific embodiment
The following will be combined with the drawings in the embodiments of the present invention, carries out the technical scheme in the embodiment of the utility model
Clearly and completely describe, it is clear that the described embodiments are only a part of the embodiments of the utility model, rather than whole
Embodiment.Based on the embodiments of the present invention, those of ordinary skill in the art are without making creative work
Every other embodiment obtained, any modification, equivalent replacement, improvement and so on should be included in the utility model
Within protection scope.
A kind of continuous vacuum distillation apparatus being used to prepare arborvitae hydrosol product as shown in Figs. 1-3, including pot body 1, into
Liquid mechanism and vacuum pump 2, the pot body 1 is equipped with fraction pipe, return pipe and inlet tube, according to the conventional design of the prior art, pot
Body is provided with heating device, and to maintain vapo(u)rizing temperature, conventional electric heating or heating medium for heating is can be used in heating device；Fraction pipe with
Vacuum pump connection, and it is equipped with condenser 3, condenser is connected with condensate tank 4, and condenser 3 is used using conventional water cooler
Condensate liquid is collected in carrying out cooling to fraction；The inlet tube is connect with feed liquor mechanism, and feed liquor mechanism includes original fluid container 5 and buffering
Tank 6, surge tank 6 are connected between original fluid container 5 and pot body 1, and the tank mouth of original fluid container 5 is equipped with sealing cover, sealing cover be equipped with it is interior
The plunger shaft 7 of portion's connection, plunger shaft are equipped with piston boit 8, and piston boit is equipped with the pressure spring 9 acted between piston boit and plunger shaft.
Under the action of vacuum pump, the liquid of original fluid container is pumped to being distilled in pot body, due in continuous vacuum distillation process,
Vacuum degree is larger in pot body, and original fluid container is unable to maintain that vacuum degree in the pot body penetrated through therewith, therefore this according to open type structure
Sealing cover is arranged in original fluid container in scheme, and plunger shaft is arranged on sealing cover, can both maintain vacuum degree in pot body, while can protect
The normal feed flow of original fluid container is demonstrate,proved, surge tank is for stablizing inlet tube flow, and surge tank equally uses sealing structure, and volume should basis
The actual flow of inlet tube determines；The return pipe is connected with reflux pump 10 and return tank 11 in turn, and return pipe is used for distillation
Residual night afterwards is recycled.
As an improvement scheme, vertical interlayer board 16 is equipped with inside the pot body 1, interlayer board separates pot nside
The distillation chamber mutually completely cut off at two, inlet tube 13, return pipe 14 and fraction pipe 15 are equipped with branch pipe, by branch pipe respectively with two
A distillation chamber is individually connected to, and each branch pipe is equipped with control valve 12.The design can utilize in continuous vacuum distillation process
Control valve switches over operation to two distillation chambers, to facilitate the raffinate reflux operation for carrying out boiler.
The specific design of one kind as above-mentioned improvement project, the pot body include shell 1a and top cover 1b, shell and top cover
It is connected by flange head, the inlet tube and return pipe are set to shell, and the fraction pipe is set to top cover；The interlayer board 16 includes
It is respectively arranged at the upper spacer and lower clapboard of shell and top cover；The flange head, upper spacer and lower clapboard are equipped with mutually matched
Groove 17 and boss 18.Boss and groove both can be improved the leakproofness between shell and top cover, at the same can to upper spacer and
Lower clapboard is positioned, and is guaranteed after shell is connected with top cover by flange head, and two distillation chambers mutually completely cut off are constituted.
Claims (3)
1. a kind of continuous vacuum distillation apparatus for being used to prepare arborvitae hydrosol product, including pot body, feed liquor mechanism and vacuum pump,
Be characterized in that: the pot body is equipped with fraction pipe, return pipe and inlet tube；Fraction pipe is controlled to a vacuum pump, and is equipped with condenser, cold
Condenser is connected with condensate tank；The inlet tube is connect with feed liquor mechanism, and feed liquor mechanism includes original fluid container and surge tank, buffering
Tank is connected between original fluid container and pot body, and the tank mouth of original fluid container is equipped with sealing cover, and sealing cover is equipped with and is connected with inside piston
Chamber, plunger shaft are equipped with piston boit, and piston boit is equipped with the pressure spring acted between piston boit and plunger shaft；The return pipe successively connects
It is connected to reflux pump and return tank.
2. the continuous vacuum distillation apparatus according to claim 1 for being used to prepare arborvitae hydrosol product, it is characterised in that: institute
Pot nside is stated equipped with vertical interlayer board, pot nside is separated into two distillation chambers mutually completely cut off by interlayer board, inlet tube,
Return pipe and fraction pipe are equipped with branch pipe, are individually connected to two distillation chambers respectively by branch pipe, and each branch pipe is equipped with control
Valve processed.
3. the continuous vacuum distillation apparatus according to claim 2 for being used to prepare arborvitae hydrosol product, it is characterised in that: institute
Stating pot body includes shell and top cover, and shell is connected with top cover by flange head, and the inlet tube and return pipe are set to shell, described
Fraction pipe is set to top cover；The interlayer board includes the upper spacer and lower clapboard for being respectively arranged at shell and top cover；The flange head,
Upper spacer and lower clapboard are equipped with mutually matched groove and boss.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821310426.7U CN208959360U (en) | 2018-08-15 | 2018-08-15 | A kind of continuous vacuum distillation apparatus being used to prepare arborvitae hydrosol product |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821310426.7U CN208959360U (en) | 2018-08-15 | 2018-08-15 | A kind of continuous vacuum distillation apparatus being used to prepare arborvitae hydrosol product |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN208959360U true CN208959360U (en) | 2019-06-11 |
Family
ID=66753028
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201821310426.7U Expired - Fee Related CN208959360U (en) | 2018-08-15 | 2018-08-15 | A kind of continuous vacuum distillation apparatus being used to prepare arborvitae hydrosol product |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN208959360U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110424967A (en) * | 2019-07-19 | 2019-11-08 | 广东华隧建设集团股份有限公司 | A kind of liquid nitrogen freezer for step freezing |
| CN116041707A (en) * | 2023-03-16 | 2023-05-02 | 福建纳新硅业科技有限公司 | Silicon rubber purification device |
-
2018
- 2018-08-15 CN CN201821310426.7U patent/CN208959360U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110424967A (en) * | 2019-07-19 | 2019-11-08 | 广东华隧建设集团股份有限公司 | A kind of liquid nitrogen freezer for step freezing |
| CN116041707A (en) * | 2023-03-16 | 2023-05-02 | 福建纳新硅业科技有限公司 | Silicon rubber purification device |
| CN116041707B (en) * | 2023-03-16 | 2024-04-05 | 福建纳福硅业有限公司 | Silicon rubber purification device |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20190611 Termination date: 20200815 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |