CN106753792A - A kind of profit rheology device and essential oil of traditional Chinese medicine extraction system - Google Patents
A kind of profit rheology device and essential oil of traditional Chinese medicine extraction system Download PDFInfo
- Publication number
- CN106753792A CN106753792A CN201710075471.2A CN201710075471A CN106753792A CN 106753792 A CN106753792 A CN 106753792A CN 201710075471 A CN201710075471 A CN 201710075471A CN 106753792 A CN106753792 A CN 106753792A
- Authority
- CN
- China
- Prior art keywords
- tank body
- profit
- sieve plate
- steam
- aqua aromatica
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
- C11B—PRODUCING, e.g. BY PRESSING RAW MATERIALS OR BY EXTRACTION FROM WASTE MATERIALS, REFINING OR PRESERVING FATS, FATTY SUBSTANCES, e.g. LANOLIN, FATTY OILS OR WAXES; ESSENTIAL OILS; PERFUMES
- C11B9/00—Essential oils; Perfumes
- C11B9/0003—Compounds of unspecified constitution defined by the chemical reaction for their preparation
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D11/00—Solvent extraction
- B01D11/02—Solvent extraction of solids
-
- C—CHEMISTRY; METALLURGY
- C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
- C11B—PRODUCING, e.g. BY PRESSING RAW MATERIALS OR BY EXTRACTION FROM WASTE MATERIALS, REFINING OR PRESERVING FATS, FATTY SUBSTANCES, e.g. LANOLIN, FATTY OILS OR WAXES; ESSENTIAL OILS; PERFUMES
- C11B9/00—Essential oils; Perfumes
- C11B9/02—Recovery or refining of essential oils from raw materials
-
- C—CHEMISTRY; METALLURGY
- C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
- C11B—PRODUCING, e.g. BY PRESSING RAW MATERIALS OR BY EXTRACTION FROM WASTE MATERIALS, REFINING OR PRESERVING FATS, FATTY SUBSTANCES, e.g. LANOLIN, FATTY OILS OR WAXES; ESSENTIAL OILS; PERFUMES
- C11B9/00—Essential oils; Perfumes
- C11B9/02—Recovery or refining of essential oils from raw materials
- C11B9/022—Refining
-
- C—CHEMISTRY; METALLURGY
- C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
- C11B—PRODUCING, e.g. BY PRESSING RAW MATERIALS OR BY EXTRACTION FROM WASTE MATERIALS, REFINING OR PRESERVING FATS, FATTY SUBSTANCES, e.g. LANOLIN, FATTY OILS OR WAXES; ESSENTIAL OILS; PERFUMES
- C11B9/00—Essential oils; Perfumes
- C11B9/02—Recovery or refining of essential oils from raw materials
- C11B9/025—Recovery by solvent extraction
-
- C—CHEMISTRY; METALLURGY
- C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
- C11B—PRODUCING, e.g. BY PRESSING RAW MATERIALS OR BY EXTRACTION FROM WASTE MATERIALS, REFINING OR PRESERVING FATS, FATTY SUBSTANCES, e.g. LANOLIN, FATTY OILS OR WAXES; ESSENTIAL OILS; PERFUMES
- C11B9/00—Essential oils; Perfumes
- C11B9/02—Recovery or refining of essential oils from raw materials
- C11B9/027—Recovery of volatiles by distillation or stripping
Abstract
The present invention relates to machinery equipment field, there is provided a kind of profit rheology device, including tank body, steam (vapor) outlet and fragrant water inlet are provided with the top of tank body, the bottom of tank body is provided with cooling liquid outlet, and the bottom of tank body is provided with steam inlet, sieve plate is provided with tank body, sieve plate is provided with multiple through holes, and the edge of sieve plate is connected with the inwall of tank body, and sieve plate is arranged at the top of steam inlet.The profit rheology device can be extracted again to remaining aqua aromatica after extraction of essential oil again, increase the recovery rate of volatility grease, it is to avoid be wasted.Present invention also offers a kind of essential oil of traditional Chinese medicine extraction system, it includes above-mentioned profit rheology device.The essential oil of traditional Chinese medicine extraction system has extraction of essential oil rate higher.
Description
Technical field
The present invention relates to machinery equipment field, in particular to a kind of profit rheology device and essential oil of traditional Chinese medicine extraction system.
Background technology
Essential oil is from the flower of plant, leaf, stem, root or fruit, by steam distillation, extrusion, cold-maceration or molten
Agent extraction method refines the volatility grease of extraction, and essential oil is expensive with great commercial value.Therefore fully extract and plant
Contained volatility grease in thing becomes crucial point.And existing extraction of essential oil equipment is to volatility in plant
The recovery rate of grease is not high, is not reaching to the effect for fully extracting the volatility grease in plant.
The content of the invention
The invention provides a kind of profit rheology device, it is intended to improve that existing Herbivore grease extraction efficiency is not high to ask
Topic.
Present invention also offers a kind of essential oil of traditional Chinese medicine extraction system, only improving existing essential oil of traditional Chinese medicine extraction system essential oil
Recovery rate problem not high.
What the present invention was realized in：
A kind of profit rheology device, including tank body, are provided with steam (vapor) outlet and fragrant water inlet, the bottom of tank body at the top of tank body
Portion is provided with cooling liquid outlet, and the bottom of tank body is provided with steam inlet, and sieve plate is provided with tank body, and sieve plate is provided with multiple logical
Hole, the edge of sieve plate is connected with the inwall of tank body, and sieve plate is arranged at the top of steam inlet.
Further, in preferred embodiments of the present invention, the quantity of sieve plate is at least 5-30, and 5-30 sieve plate is certainly
Set gradually under above.
Further, in preferred embodiments of the present invention, the side of sieve plate is provided with multiple for increasing mass transfer area
Attachment.
Further, in preferred embodiments of the present invention, the top of tank body is in cone shape, and steam (vapor) outlet is arranged at tank
Centre position at the top of body.
Further, in preferred embodiments of the present invention, the bottom of tank body is in inverted cone shape, and cooling liquid outlet is set
In the centre position of tank base.
Further, in preferred embodiments of the present invention, also including circulation separation system, circulation separation system includes collection
Tank, booster pump, circulation pipe and valve, water leg are arranged at the lower section of cooling liquid outlet, and water leg and fragrant water inlet pass through
Circulation pipe is connected, and booster pump and valve are arranged on circulation pipe.
Further, the shunting with aqua aromatica inlet communication is additionally provided with preferred embodiments of the present invention, in tank body
Webmaster, shunting webmaster is made up of multiple interconnected water pipes, and the tube wall of each water pipe is provided with multiple apopores, shunting net
Pipe is in the form of annular discs, and the edge for shunting webmaster is connected with the inwall of tank body.
Further, in preferred embodiments of the present invention, it is provided with and virtue at the outer wall correspondence fragrance water inlet of tank body
The aqua aromatica inlet pipe of perfume inlet communication, water pressure gauge is provided with aqua aromatica inlet pipe；Set at the outer wall correspondence steam inlet of tank body
The steam inlet tube connected with steam inlet is equipped with, air gauge is provided with steam inlet tube.
Further, in preferred embodiments of the present invention, also including the frame for supporting tank body, frame and tank body
Outer wall is connected.
A kind of essential oil of traditional Chinese medicine extraction system, including above-mentioned profit rheology device.
The beneficial effects of the invention are as follows：The profit rheology device that the present invention is obtained by above-mentioned design, when using, steams in tank body
Vapour flows from bottom to top, and aqua aromatica flows from top to bottom, using the high heat of steam, is passed when steam meets with aqua aromatica
Matter diabatic process, the volatility grease that aqua aromatica wherein contains after being heated by steam is taken away by steam, and the process is easy and effective, makes
The volatility grease obtained in aqua aromatica has recovery rate higher；And during aqua aromatica flow down, when it is reached at sieve plate
Can be laid on sieve plate, increase the mass transfer area of aqua aromatica and steam, increase the recovery rate of volatility grease；And due to that can wave
The viscosity of hair property grease is much bigger compared with water, therefore when aqua aromatica is distributed in floor lever of sieve tray, water easily from through hole downstairs, and volatile
Grease is easily attached to floor lever of sieve tray, causes the volatile grease concentration of floor lever of sieve tray higher, is more easy to be taken away by steam.And this hair
The bright essential oil of traditional Chinese medicine extraction system obtained by above-mentioned design, by causing it to institute in Chinese medicine including above-mentioned profit rheology device
The volatility grease for containing has recovery rate higher.
Brief description of the drawings
In order to illustrate more clearly of the technical scheme of embodiment of the present invention, below will be to be used needed for implementation method
Accompanying drawing be briefly described, it will be appreciated that the following drawings illustrate only certain embodiments of the present invention, therefore be not to be seen as
It is the restriction to scope, for those of ordinary skill in the art, on the premise of not paying creative work, can be with root
Other related accompanying drawings are obtained according to these accompanying drawings.
Fig. 1 is the structural representation of the profit rheology device that embodiment of the present invention is provided；
Fig. 2 is the internal structure schematic diagram of tank body in Fig. 1；
Fig. 3 is the schematic cross-section of sieve plate in Fig. 2；
Fig. 4 is the structural representation of shunting webmaster in Fig. 2.
Icon：100- profit rheology devices；110- tank bodies；111- steam (vapor) outlets；112- fragrance water inlets；113- coolants go out
Mouthful；114- steam inlets；115- aqua aromatica inlet pipes；116- water pressure gauges；117- steam inlet tubes；118- air gauges；120- sieve plates；
121- through holes；122- attachments；130- circulation separation systems；131- water legs；132- discharge outlet；133- booster pumps；134- is followed
Endless tube；135- valves；140- shunts webmaster；141- water pipes；142- apopores；143- water inlets；150- frames.
Specific embodiment
To make the purpose, technical scheme and advantage of embodiment of the present invention clearer, implement below in conjunction with the present invention
Accompanying drawing in mode, is clearly and completely described to the technical scheme in embodiment of the present invention, it is clear that described reality
The mode of applying is a part of implementation method of the invention, rather than whole implementation methods.Based on the implementation method in the present invention, ability
The every other implementation method that domain those of ordinary skill is obtained under the premise of creative work is not made, belongs to the present invention
The scope of protection.Therefore, the detailed description of embodiments of the present invention below to providing in the accompanying drawings is not intended to limit and wants
The scope of the present invention of protection is sought, but is merely representative of selected implementation method of the invention.Based on the implementation method in the present invention,
The every other implementation method that those of ordinary skill in the art are obtained under the premise of creative work is not made, belongs to this
Invent the scope of protection.
In the description of the invention, it is to be understood that term " " center ", " on ", D score, " vertical ", " level ",
The orientation or position relationship of the instruction such as " top ", " bottom ", " interior ", " outward " are, based on orientation shown in the drawings or position relationship, to be only
Described with simplified for the ease of the description present invention, must be with specific side rather than the equipment or element for indicating or imply meaning
Position, with specific azimuth configuration and operation, therefore be not considered as limiting the invention.
Additionally, term " first ", " second " are only used for describing purpose, and it is not intended that indicating or implying relative importance
Or the implicit quantity for indicating indicated technical characteristic.Thus, define " first ", the feature of " second " can express or
Implicitly include one or more this feature.In the description of the invention, " multiple " is meant that two or more,
Unless otherwise expressly limited specifically.
In the present invention, unless otherwise clearly defined and limited, term " installation ", " connected ", " connection ", " fixation " etc.
Term should be interpreted broadly, for example, it may be fixedly connected, or be detachably connected, or integrally；Can be that machinery connects
Connect, or electrically connect；Can be joined directly together, it is also possible to be indirectly connected to by intermediary, can be in two elements
The connection in portion or two interaction relationships of element.For the ordinary skill in the art, can be according to specific feelings
Condition understands above-mentioned term concrete meaning in the present invention.
In the present invention, unless otherwise clearly defined and limited, fisrt feature second feature it " on " or D score
The first and second feature directly contacts can be included, it is also possible to including the first and second features be not directly contact but by it
Between other characterisation contact.And, fisrt feature second feature " on ", " top " and " above " include that first is special
Levy directly over second feature and oblique upper, or be merely representative of fisrt feature level height higher than second feature.Fisrt feature exists
Second feature " under ", " lower section " and " below " include fisrt feature immediately below second feature and obliquely downward, or be merely representative of
Fisrt feature level height is less than second feature.
The vapor containing volatile ingredient is after condensation by needing to carry out water-oil separating in plants essential oil extraction process,
At this time most of oil can be separated from water and hold, least a portion of oil can in the form of the small oil droplet with separation after water drain together, this
Plant the water being drained off and be referred to as aqua aromatica.
Refer to shown in Fig. 1, present embodiments provide a kind of profit rheology device 100, it includes tank body 110, tank body 110
Bottom is provided with steam inlet 114, and the top of tank body 110 is provided with steam (vapor) outlet 111；The top of tank body 110 is provided with fragrance
Water inlet 112, the bottom of tank body 110 is provided with cooling liquid outlet 113.Aqua aromatica enters in tank body 110 from fragrant water inlet 112
Portion, steam enters inside tank body 110 from steam inlet 114, and aqua aromatica occurs mass transfer reaction with steam in tank body 110, makes steaming
The volatility grease that vapour is taken away in aqua aromatica is discharged from steam (vapor) outlet 111, loses the aqua aromatica of grease then from cooling liquid outlet 113
Discharge.
Further, the top of tank body 110 is in cone shape, and steam (vapor) outlet 111 is arranged at the interposition at the top of tank body 110
Put.Because steam is up walked, steam (vapor) outlet 111 is arranged at the timely discharge that highest position is conducive to steam.Need explanation
, in other embodiments of the invention, the top of tank body 110 can also be that other have the shape of peak, and steam goes out
Mouth 111 is then arranged at highest position.
Further, the bottom of tank body 110 is in inverted cone shape, and cooling liquid outlet 113 is arranged in the bottom of tank body 110
Between position.Because current walk downward, cooling liquid outlet 113 is arranged at the timely discharge that its lowest position is conducive to coolant.
It should be noted that in other embodiments of the invention, the bottom of tank body 110 can also be that other have the shape of minimum point
Shape, cooling liquid outlet 113 is then arranged at its lowest position.
Refer to shown in Fig. 1 and Fig. 2, sieve plate 120 is provided with tank body 110, the edge of sieve plate 120 is interior with tank body 110
Wall is connected, and sieve plate 120 is to be fixedly connected with the connected mode of tank body 110.And sieve plate 120 is arranged at the top of steam inlet 114,
Sieve plate 120 parallel to horizontal plane, to enable that aqua aromatica uniformly will not be excessive because of gravity influence in the surface distributed of sieve plate 120
It is gathered in position lower.Refer to shown in Fig. 3, multiple through holes 121 are provided with sieve plate 120.When aqua aromatica enters from aqua aromatica
Mouthfuls 112 into flow to sieve plate 120 in tank body 110 when, opened in the Dispersion on surface of sieve plate 120, the steam entered from steam inlet 114 with
Aqua aromatica carries out mass transfer reaction on sieve plate 120 so that effumability grease is taken away by steam in aqua aromatica, and water is from through hole 121
Flow down, simultaneously because the viscosity of volatile grease is much larger compared with the viscosity of water, sieve plate 120 is also oily with volatile is collected
The effect of fat, when aqua aromatica is flow on sieve plate 120, water easily flows out from through hole 121, and volatile grease is then easily attached to sieve
The surface of plate 120, therefore the concentration of the grease on the surface of sieve plate 120 is higher, then easily taken away by steam.
Preferably, the quantity of sieve plate 120 is 5-30, and 5-30 sieve plate 120 from top to bottom sets successively in tank body 110
Put, multiple sieve plates 120 are set and are conducive to increasing mass transfer area of the aqua aromatica with steam and mass transfer time, to volatility in aqua aromatica
The extraction of grease serves positive effect.In general the recovery rate of the quantity of sieve plate 120 more many greases of sauce is higher, but sieve plate 120
When quantity is excessive so that steam reaches the overlong time of steam (vapor) outlet 111, carries out mass transfer reaction with aqua aromatica for a long time, may
The temperature of steam can be made to be down to condensation point and to condense into water discharge, so influence extraction effect, and excessive sieve plate 120 is set on the contrary
Also production cost can be made to be increased.Observed through many experiments, under conditions of comprehensive production cost and grease extraction efficiency, sieve plate 120
Quantity be set to it is best at 5-30.
It is pointed out that in the present embodiment, the quantity of sieve plate 120 is 5, in other embodiments of the invention, root
Needed according to production, the quantity of sieve plate 120 can be with being intended to be adjusted in 5-30.Although it may also be noted that when sieve plate 120
The recovery rate of volatility grease is smaller relative to recovery rate in the present embodiment in aqua aromatica when quantity is less than 5, but its same tool
There is preferable recovery rate, therefore in other embodiments of the invention, the quantity of sieve plate 120 can also adjust in 1-4.
Referring once again to Fig. 3, it is preferable that the side of sieve plate 120 is provided with multiple attachments 122, the shape of attachment 122
It is inverted "L" shaped, the purpose for setting attachment 122 is the bond area in order to increase aqua aromatica and then increases aqua aromatica and steam
Mass transfer area, is conducive to the extraction of volatility grease in aqua aromatica.
It should be noted that in other embodiments of the invention, the shape of attachment can also be del, ladder
The shapes such as shape.
Refer to Fig. 2 and Fig. 4, further, the top of tank body 110 is provided with shunting webmaster 140, shunting webmaster 140 by
The interconnected water pipe 141 of multiple is constituted, and the tube wall of each water pipe 141 is provided with multiple apopores 142, multiple water pipes 141
Include a circular water pipe, the circular water pipe is provided with water inlet 143, and water inlet 143 is connected with fragrant water inlet 112.
The liquid entered from fragrant water inlet 112 is then entered in shunting webmaster 140 by water inlet 143, each in webmaster 140 is shunted
The apopore 142 for being scatter in individual water pipe 141 and being set from water pipe 141 flows out.The effect for setting shunting Dropbox is by fragrance
The aqua aromatica that water inlet 112 is passed through scatter each position uniform flow from the top of sieve plate 120, it is to avoid aqua aromatica from virtue occur
Perfume import 112 directly leaves to sieve plate 120 skewness and causes the insufficient problem of mass transfer.
It is pointed out that in other embodiments of the invention, can also be replaced shunting Dropbox, spray thrower with spray thrower
With aqua aromatica inlet communication, aqua aromatica enters spray thrower from fragrant water inlet, and aqua aromatica is sprayed from each orientation by spray thrower
Go out, can also reach and shunting Dropbox identical effect.
Referring again to Fig. 1, it is preferable that be provided with to enter with aqua aromatica at the outer wall correspondence fragrance water inlet 112 of tank body 110
The aqua aromatica inlet pipes 115 of the connection of mouth 112, the steaming connected with steam inlet 114 is provided with the correspondence steam inlet 114 of tank body 110
Vapour inlet pipe 117.Water pressure gauge 116 is provided with aqua aromatica inlet pipe 115, air gauge 118 is provided with steam inlet tube 117.By setting
The water pressure gauge 116 being placed on aqua aromatica inlet pipe 115 monitors the water inlet flow velocity of aqua aromatica, by being arranged on steam inlet tube 117
Air gauge 118 monitors the induction air flow ratio of steam, by adjusting water inlet flow velocity and induction air flow ratio, makes the water inlet flow velocity of aqua aromatica and steams
The induction air flow ratio of vapour reaches a preferable ratio makes aqua aromatica have a preferable mass-transfer efficiency in tank body 110 with steam.
Preferably, profit rheology device 100 also includes circulation separation system 130, and circulation separation system 130 includes water leg
131st, booster pump 133, circulation pipe 134 and valve 135, water leg 131 is arranged in frame 150, positioned at cooling liquid outlet 113
Lower section, water leg 131 is connected with fragrant water inlet 112 by circulation pipe 134, and booster pump 133 and valve are provided with circulation pipe 134
Door 135.Also, in order to avoid wasting, adopted containing little a part of volatility grease in reacting the cooling water for producing in tank body 110
Cooling water is collected with water leg 131, opens valve 135, by circulation pipe 134 through aqua aromatica in the presence of booster pump 133
Import 112 is delivered in tank body 110 extraction for carrying out volatility grease again.The circulation separation system 130 is simple and convenient, favorably
In the abundant extraction of grease.Further, the bottom of water leg 131 is additionally provided with discharge outlet 132.In water leg 131 is collected in
Condensed water in volatility fat content it is low to being difficult to extract or during without extracting value, then by opening discharge outlet 132, will be cold
Solidifying water discharge.
The course of work of profit rheology device 100 is as follows：Aqua aromatica passes through fragrant water inlet 112 and is passed through in shunting webmaster 140,
Uniformly it is flow on sieve plate 120 from apopore 142 under the shunting action of shunting webmaster 140；At the same time, steam passes through steam
Import 114 enters in tank body 110, and aqua aromatica carries out mass transfer with steam on the multiple sieve plates 120 being uniformly arranged in tank body 110
Reaction, effumability grease is discharged from steam (vapor) outlet 111 during steam then takes away aqua aromatica, and loses the aqua aromatica of volatility grease
Cooling water is formed with the steam of cooling to be discharged from cooling liquid outlet 113；Cooling water after discharge is collected in water leg 131
In, if also needing to proceed grease extraction, the cooling water in water leg 131 is led to again by booster pump 133 by circulation pipe 134
Enter the extraction that volatility grease is carried out in tank body 110.
In sum, steam flows from bottom to top in the tank body of profit rheology device, and aqua aromatica flows from top to bottom, using steaming
, there is mass-and heat-transfer process when steam and aqua aromatica meet in the high heat of vapour, what aqua aromatica wherein contained after being heated by steam
Volatility grease is taken away by steam, and the process is easy and effective so that the volatility grease in aqua aromatica has recovery rate higher；
And during aqua aromatica flow down, it can be laid on sieve plate when reaching at sieve plate, the mass transfer of aqua aromatica and steam is increased
Area, increases the recovery rate of volatility grease；And because the viscosity of volatile grease is much bigger compared with water, therefore when fragrant water distribution
When floor lever of sieve tray, easily from through hole downstairs, and volatile grease is easily attached to floor lever of sieve tray to water, causes waving for floor lever of sieve tray
Hair property grease concentration is higher, is more easy to be taken away by steam；Attachment is set on sieve plate increases the bond area of aqua aromatica and then increase
Big mass transfer area of the steam with aqua aromatica, is conducive to the extraction of volatility grease；And cyclic separation device is set, the letter of its structure
It is single, additionally it is possible to realize extracting the cooling water being unlikely to slattern also containing volatility grease to the circulation of volatility grease.
Present invention also offers a kind of essential oil of traditional Chinese medicine extraction system, it includes above-mentioned profit rheology device, because it includes
Above-mentioned profit rheology device, therefore the essential oil of traditional Chinese medicine extraction system has recovery rate higher to contained volatility grease in Chinese medicine.
The preferred embodiment of the present invention is the foregoing is only, is not intended to limit the invention, for this area
For technical staff, the present invention can have various modifications and variations.It is all within the spirit and principles in the present invention, made it is any
Modification, equivalent, improvement etc., should be included within the scope of the present invention.
Claims (10)
1. a kind of profit rheology device, it is characterised in that including tank body, steam (vapor) outlet and aqua aromatica are provided with the top of the tank body
Import, the bottom of the tank body is provided with cooling liquid outlet, and the bottom of the tank body is provided with steam inlet, is set in the tank body
Sieve plate is equipped with, the sieve plate is provided with multiple through holes, and the edge of the sieve plate is connected with the inwall of the tank body, and the sieve plate
It is arranged at the top of the steam inlet.
2. profit rheology device according to claim 1, it is characterised in that the quantity of the sieve plate is at least 5-30, and
The 5-30 sieve plate sets gradually from top to bottom.
3. profit rheology device according to claim 1, it is characterised in that the side of the sieve plate is provided with multiple for increasing
The attachment of big mass transfer area.
4. profit rheology device according to claim 1, it is characterised in that the top of the tank body is in cone shape, described
Steam (vapor) outlet is arranged at the centre position at the top of the tank body.
5. profit rheology device according to claim 1, it is characterised in that the bottom of the tank body is in inverted cone shape, institute
State the centre position that cooling liquid outlet is arranged at the tank base.
6. profit rheology device according to claim 1, it is characterised in that also including circulation separation system, the circulation point
Include water leg, booster pump, circulation pipe and valve from system, the water leg is arranged at the lower section of the cooling liquid outlet, institute
State water leg to be connected by the circulation pipe with the fragrant water inlet, the booster pump and the valve are arranged at the circulation
Guan Shang.
7. profit rheology device according to claim 1, it is characterised in that be additionally provided with the tank body and the aqua aromatica
The shunting webmaster of inlet communication, the shunting webmaster is made up of multiple interconnected water pipes, and the tube wall of each water pipe is equal
Multiple apopores are provided with, the shunting webmaster is in the form of annular discs, the edge of the shunting webmaster is connected with the inwall of the tank body.
8. profit rheology device according to claim 1, it is characterised in that the outer wall correspondence aqua aromatica of the tank body enters
The aqua aromatica inlet pipe with the aqua aromatica inlet communication is provided with mouthful, water pressure gauge is provided with the aqua aromatica inlet pipe；It is described
The steam inlet tube connected with the steam inlet is provided with the outer wall correspondence steam inlet of tank body, on the steam inlet tube
It is provided with air gauge.
9. profit rheology device according to claim 1, it is characterised in that also including the frame for supporting the tank body,
The frame is connected with the outer wall of the tank body.
10. a kind of essential oil of traditional Chinese medicine extraction system, it is characterised in that including the profit rheology as described in claim any one of 1-9
Device.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710075471.2A CN106753792A (en) | 2017-02-13 | 2017-02-13 | A kind of profit rheology device and essential oil of traditional Chinese medicine extraction system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710075471.2A CN106753792A (en) | 2017-02-13 | 2017-02-13 | A kind of profit rheology device and essential oil of traditional Chinese medicine extraction system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN106753792A true CN106753792A (en) | 2017-05-31 |
Family
ID=58956011
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201710075471.2A Pending CN106753792A (en) | 2017-02-13 | 2017-02-13 | A kind of profit rheology device and essential oil of traditional Chinese medicine extraction system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN106753792A (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108913364A (en) * | 2018-09-25 | 2018-11-30 | 江西中医药大学 | Extract separator and volatile oil preparation system |
| CN108905297A (en) * | 2018-09-25 | 2018-11-30 | 江西中医药大学 | Oil water separator and its component |
| CN112870750A (en) * | 2021-01-21 | 2021-06-01 | 广西六万山生物科技有限公司 | Distillation retort for leaching effective components of plants and application method thereof |
Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101280243A (en) * | 2008-06-04 | 2008-10-08 | 杨利民 | Method for extracting rose essence oil and rose absolute by water vapor water distillation technology |
| 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 |
| CN203033968U (en) * | 2012-12-14 | 2013-07-03 | 茂名市德威圣科技有限责任公司 | Spray type essential oil extractor |
| CN103977587A (en) * | 2014-06-05 | 2014-08-13 | 中国海诚工程科技股份有限公司 | Beancurd blade tower plate continuous distillation method |
| CN203878130U (en) * | 2014-04-29 | 2014-10-15 | 江苏悦禧玫瑰科技有限公司 | Rose essential oil extraction device |
| CN204079937U (en) * | 2014-08-22 | 2015-01-07 | 昆明邦宇制药有限公司 | One ESSENTIAL OIL extraction equipment |
| CN105038992A (en) * | 2015-09-01 | 2015-11-11 | 湖南时代阳光药业股份有限公司 | Multifunctional volatile oil distilling and extracting tank |
| CN105602728A (en) * | 2015-10-22 | 2016-05-25 | 广西新龙制药有限责任公司 | Perfume oil extraction tank |
-
2017
- 2017-02-13 CN CN201710075471.2A patent/CN106753792A/en active Pending
Patent Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101280243A (en) * | 2008-06-04 | 2008-10-08 | 杨利民 | Method for extracting rose essence oil and rose absolute by water vapor water distillation technology |
| 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 |
| CN203033968U (en) * | 2012-12-14 | 2013-07-03 | 茂名市德威圣科技有限责任公司 | Spray type essential oil extractor |
| CN203878130U (en) * | 2014-04-29 | 2014-10-15 | 江苏悦禧玫瑰科技有限公司 | Rose essential oil extraction device |
| CN103977587A (en) * | 2014-06-05 | 2014-08-13 | 中国海诚工程科技股份有限公司 | Beancurd blade tower plate continuous distillation method |
| CN204079937U (en) * | 2014-08-22 | 2015-01-07 | 昆明邦宇制药有限公司 | One ESSENTIAL OIL extraction equipment |
| CN105038992A (en) * | 2015-09-01 | 2015-11-11 | 湖南时代阳光药业股份有限公司 | Multifunctional volatile oil distilling and extracting tank |
| CN105602728A (en) * | 2015-10-22 | 2016-05-25 | 广西新龙制药有限责任公司 | Perfume oil extraction tank |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108913364A (en) * | 2018-09-25 | 2018-11-30 | 江西中医药大学 | Extract separator and volatile oil preparation system |
| CN108905297A (en) * | 2018-09-25 | 2018-11-30 | 江西中医药大学 | Oil water separator and its component |
| CN108905297B (en) * | 2018-09-25 | 2023-08-25 | 江西中医药大学 | Oil-water separator and assembly thereof |
| CN112870750A (en) * | 2021-01-21 | 2021-06-01 | 广西六万山生物科技有限公司 | Distillation retort for leaching effective components of plants and application method thereof |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN202030729U (en) | Plant distillation separating device | |
| CN106753792A (en) | A kind of profit rheology device and essential oil of traditional Chinese medicine extraction system | |
| CN204939435U (en) | A kind of family expenses essential oil distillation extraction device | |
| CN201384866Y (en) | Vertical automatic reflux-withdrawal rectifying device | |
| CN206045456U (en) | A kind of segregation apparatuss that volatile oil is obtained suitable for steam distillation | |
| CN209155159U (en) | Spice oil produces efficient fractionating column | |
| CN209317088U (en) | The extraction of Chinese medicine volatile component and Distallation systm | |
| CN213790038U (en) | Pressure swing rectification device of methyl acetate and methyl alcohol | |
| CN206447856U (en) | A kind of profit rheology device and essential oil of traditional Chinese medicine extraction system | |
| CN206676005U (en) | A kind of use for laboratory small automatic essential oil distilling apparatus | |
| CN206167967U (en) | Be provided with liquid trap, liquid distributor and cooling structure's rectifying column | |
| CN205313497U (en) | Small -size essential oil and pure dew extraction element of easy dismouting | |
| CN208905999U (en) | A kind of steam collection device for Producing medicinal herbs | |
| CN105273845A (en) | Rose oil distillation purification unit | |
| CN206721160U (en) | A kind of filler deodorizing tower for grease post processing | |
| CN212308898U (en) | Fractionating tower and fractionating system for heat conduction oil production | |
| CN108753555A (en) | A kind of wine brewing distillation equipment | |
| CN208844047U (en) | A kind of wine brewing distillation equipment | |
| CN209113846U (en) | A kind of multi-layer efficient essential oil extracting device | |
| CN210855358U (en) | Waste acid distillation still | |
| CN105237358B (en) | Natural borneol extraction system and method capable of increasing yield | |
| CN209260038U (en) | Condensing unit is used in a kind of extraction of tea oil | |
| CN204079946U (en) | Combined type solid-state water distilling apparatus | |
| CN206980150U (en) | A kind of acetic acid rectifying column | |
| CN207627966U (en) | Constant pressure distilling apparatus |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination |